tuberías en polipropileno (ppr) y polietileno (pe) - abn

Catálogo de producto

"The healthiest choicefor your installation"

Product Catalogue

PIPE SYSTEMSPIPE SYSTEMS

System in PPR-CT-RP + FV for water-sanitary installationswith B-s1, d0 classification

//////////////////////////////////ABN INSTAL CT FASER RD

B-s1,d0

01 Introduction

02 Characteristics of the system2.1. Characteristics of the system2.2. Fields of application2.3. Distinguishing characteristics2.4. Technical characteristics2.5. Regression curves2.6. Working pressures2.7. Study of the microbial load and legionella evolution

2.7.1. Study of the microbial load evolution2.7.2. Study of the of legionella evolution

03 Resistance to the chemical and thermal disinfection

04 Sizing4.1. Water quality4.2. Minimum supply conditions 4.3. Calculation volume. DIN 1988 standard. Formula and tables 4.4. Diameter equivalence4.5. Thermal insulation

05 Pressure loss5.1. Equivalences5.2. ABN//INSTAL CT FASER RD pipes series 3,2 /SDR 7,55.3. ABN//INSTAL CT FASER RD pipesseries 5 /SDR 115.4. ABN//INSTAL CT FASER RD pipes series 8 / SDR 175.5. Fittings pressure loss

06 Installation criteria6.1. General conditions6.2. Protections6.3. Support 6.4. Thermal expansion6.5. Transition with pipes and metallic fittings

07 Joint systems7.1. Introduction 7.2. Welding by thermo-fusion to socket7.3. Welding by electro-fusion7.4. Butt-welding7.5. Weld in saddles7.6. Use of pipe repair

/////////////////// www.abnpipesystems.comCatalogue valid from May 2015Subject to technical modifications

08 Pressure tests8.1. Preparation and cleaning8.2. Tests and operating

09 Transport, handling and collecting9.1. Transport9.2. Handling9.3. Stock piling

10 Range of products10.1. Pipes10.2. Socket welding fittings10.3. Welding-threading combined fittings10.4. Socket-welding valves10.5. Electro-welding fittings10.6. Butt-welding fittings

11 Quality11.1. Quality control11.2. Internal quality control of the product11.3. Regulations11.4. Certificates11.5. Warranty

12 Information and safety advice

13 Bibliography

ANNEX - Chemical Resistance

///////////////////www.abnpipesystems.comCatalogue valid from May 2015

Subject to technical modifications

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MORE THAN 25 YEARS OF SERVICETO OUR CUSTOMERS

After more than 25 years, the ABN Group started his activity with the commitment to be specialist in sales and distribution of pipe systems for civil work. Its field of activity focused in the Galician market, in which they achieved to be a referent in customer service and solutions with their product range.

Over the past years, noval systems of canalization for the sector of edification were been introduced which suppose that the field of activity has expanded to the whole national territory and Portugal. In 2001 they have created a specific company, ABN PIPE Systems, with the objective to fulfill all this new activity.

Since 1988 we wanted to facilitate the work of our customers, providing innovative solutions that were pioneers in the sector.

With the beginning of the production plant of Medina del Campo in 2008, our philosophy of work changed completely, moving from sales to produce our own pipe systems.

This new sphere of activity means an interesting challenge, in which we will define us as we would like to be in the future, and which proposals we would like to offer to the market.

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ABN INSTAL CT Faser RD - Page 01-08//

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2001 ABN PIPE Systems started business as distributor of products for edification for the national market. Also importing the newest pipe systems for Austria, Germany and Italy.

In 2006 the ABN Group started the building works of their own production plant, dedicated to the production of pipe systems fabricated with thermoplastic materials.

The production plant from ABN PIPE Systems has a surface of 100.000m². Its facilities are divided in two productions areas highly automated, development department, Laboratory and Quality, area of loading and disloading, also with an automated warehouse with a capacity of 18.000 palets.

It is located in the town of Medina del Campo, with a excellent geographic situation near Madrid and Valladolid, with good road and rail communication network.

Actually it's the first production plant in Spain, specialist in production of multilayer pipes fabricated with thermoplastic materials.

Is fitted with the top European technology of:

- Ultimate extrusion machines for the production of pipe systems with 5 layers and up to diameter 500mm,

- injector for the production of fittings,

- automated systems for the storage,

- own laboratory of R&D for the realization of tests and analyses.

ABN Pipe Systems is certificated according to ISO 9001:2008 for the production of pipe systems and thermoplastic compounds in Medina del Campo.

ABN Pipe Systems

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01 Compound areaThis area is designated for the formulation and production of the raw materials. This section is equipped with ultimate machines, in order to realize all kind of formulations. We work with different raw materials, mineral loads and additives in order to make our own products or the products of our clients in accordance to the requirements.

02 Extrusion areaThis area has 3 extrusion lines allowing the production of multilayer until diameter 500mm with polypropylene and polyethylene with mineral charge or without it. This system is connected with the Silos. This automated system allows the automatic change of the dimensions of the material, in order to advantage total the raw material. In addition this area has also, a spread machine for the displacement of the pipes. Three marking machines for the identification, socket machine for the socket of the pipe and a roll up machine for the flexible pipe.

03 Injection areaThis area is for the injection of the fittings. There are available diferent moulds for the injection of bends, muff and derivation for sewage, drainage and networks of pressure.

04 R&D and Laboratory areaWe have a complete laboratory where new materials, new technical of production and new designs for better solutions are investigated, in order to develop products with better properties.

05 WharehouseThe warehouse has an automated system with 3 stacker crane of 15 meter working horizontal and vertical. An intelligent systems how optimized its occupation. This systems is synchronized with other storage system and with the logistic department through the software.

The production plant has five different areas:compound area, extrusion area, inyection area, Laboratory and storage.


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Business division

The market

01 ConstructionThe construction area, both public and private, are our core business. We work for important public public organisms and also we are present in building works, both in national and international markets.

02 Civil worksWe are behind important civil projects, incorporating our products to create a sustainable system.

03 IndustryWe have specific products for industry: minery, agriculture, fishing industry, chemical, automotive, etc., contributing with solutions adapted to the specific needs.

In the last years we have

develop new pipe systems for

construction, civil works and

industry. //////////////////

ABN NSTAL CT Faser RD - Page 01-11//I

/////////////////////////////////////////////////////Internacional presence

Our international presence is based in the opening of new international markets and the consolidating in current key markets. In the process, our greatest strength is to boost the development of our own-branded products. With the use of the pioneering raw materials like polyethylene CT and polyethylene PE-RC gives us a special position in the international market especially in Latin America.

In Europe, we are present in the Portuguese market through important distributors. This has enabled us to operate in other countries in the North of Africa such as Angola, Algeria, Cape Town, Marruecos and Mozambique.

We export also to Austria, Czech Republic, Great Britain and Germany, through the division of compound and also through our division of canalization.

In Latin America, we have strategic partners and also specific distributors which have allowed us to get closer to important sectors that have enabled us to conclude important agreements with public and private companies.

We are present with our products in important projects of different sectors in Chile, Colombia, Ecuador, Guatemala, Peru and Uruguay.

In Latin America we are present in Chile, Colombia, Ecuador, Guatemala, Peru and Uruguay. In Europe, in Austria, Cezch Republic, Great Britain, Germany and Portugal.In Africa, we work in Angola, Argelia, Cape Town, Marruecos and Mozambique. / / / / / / / / / / / / /

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Characteristics of the system2.1. Characteristics of the system2.2. Fields of application2.3. Distinguishing characteristics2.4. Technical characteristics2.5. Regression curves2.6. Working pressures2.7. Study of microbial load and Legionella evolution

// 02

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PIPE SYSTEMS ABN INSTAL CT FASER RD

Characteristics of the system

////////////////////////////////////////////2.1.

ABN//INSTAL CT Faser RD is a system of pipes and fittings, specially developed for water installations. It is made up of state-of-the-art multilayer polypropylene (PP RCT RP + FV).

ABN//INSTAL CT Faser RD stands out for incorporating a new additive to its internal layer, which is resistant to the processes of disinfection and disinfectants providing a high resistance to cracks with an excellent long-term result. An antimicrobial additive that prevents from bacteria and fungi spreading inside the pipe walls, and it also contributes to prevent and control legionella.

A protection UV has been added to ABN//INSTAL CT Faser RD, which minimizes the degradation provoked by solar exhibition.

It has a wide range of pipes and fittings, from 20 to 500 mm diameter, which guarantee any constructive proposal for water conduction, contributing to a comprehensive solution for installing a finished ecological network.

System in PP RCT RP resistant to disinfection procesess


ABN INSTAL CT FASER RD

231

Three-layer ABN//INSTAL CT FASER RD pipe systems:

1.PPR CT RP grey external layer RAL 9006 with white strips.The additives with antioxidants that are used for the external layer minimized the degradation of sun exposure.

2.PP R CT grey middle layer RAL 7042 with micro-fibre anti-expansion.Ensures high mechanical strength resistance and impact resistance with a less thick wall of the pipe, allowing the installation of lesser diameters in comparison to traditional PP R.

3. White internal layer RAL 9003 with additive resistant to the disinfection, anti-incrustation and anti-microbial.With a high resistance to the disinfection process, anti-microbial protection, anti-incrustation, also provides a 100% protection against the legionella, according to the microbial analysis performed by AQM laboratories.

B-s1,d0

100%EFICAZ CONTRA LA LEGIONELLA100% RECYCLABLE B-s1,d0 FOOD USE

UVPROTECTIÓN UV

HFHALOGEN FREEECOLOGICAL

RESISTANCE TO DESINFECTION FIRE NETWORKS

ABN//INSTAL FASER RD is a pipe system in PPR CT RP resistant to disinfection processes and with antimicrobial protection, it is classified B,s1-d0

CT

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Fields of application2.2.

The system ABN//INSTAL CT Faser RD is ideal for assembling installations in residential buildings, non-residential and industrial applications. Water-sanitary installationsThe system ABN//INSTAL CT Faser RD, is designed for hot and cold water installations inside the structure of the buildings, for drinking water pipelines, going from the general service of the building, through the columns, up to the last tap.

Heating and air conditioningThanks to its high temperature resistance and its low heat conductivity, the ABN//INSTAL CT Faser RD system is ideal for heating, air conditioning and refrigeration installations. There is an increase in the water flow conveyed by reducing the pipe wall thickness, which provides a great temperature stability.

Industry and agricultureThanks to its high chemical resistance, the ABN//INSTAL CT Faser RD system adapts itself to different types of installation allowing the conduction of different chemical agents with excellent results.To define its possibility of use it is recommended to observe the table of attached chemical resistances. In the case of food industries, the ABN//INSTAL CT Faser RD system meets the requirements regarding the contact with food according to the main regulations.

Compressed air installationsThe ABN//INSTAL CT Faser RD system allows the transport of compressed air and gases compatible with the chemical resistance of the material.

Special usesIn every work which demands the use of pipelines with a high resistance to pressure, entire safety in the joins, an easy and economic installation and a high chemical resistance, ABN //INSTAL CT Faser RD is recommended.

ABN//INSTAL CT FASER RD is a pipe system in PPR CT RP with antimicrobial protection.


Resistant to the disinfection procedures

The disinfection process carried out in the facilities, as the regulations require, is leading to a premature aging in the pipe systems.

The combination of high temperatures and high concentrations of disinfectants, provoke an intensive degradation and diminish the useful life of the installation. ABN//INSTAL CT Faser RD is designed to comply with all the technical requirements for the new disinfection systems of drinking water, which are of forced application in most of the countries. Its internal layer has a material that possesses an improved resistance against the disinfectants and provides an excellent long-term resistance to cracks.

Anti-expansion micro-fibres

The piping systems made of plastics materials have high degrees of expansion due to the temperature changes of the fluid.

The micro-fibre incorporation reduces the expansion coefficient by up to 75 %.

The disposition of the micro-fibres in mesh and the incorporation of a compatibilizing additive allow to improve the mechanical resistance of the system.

UV Protection

The standard polypropylenes get damaged if they remain outdoors for a long time, due mainly to the ultraviolet component of the solar light and are not protected against these radiations. That is why they are not indicated for the installation outdoors without a protection. ABN//INSTAL CT Faser RD is given an additive with antirust that minimizes the degradation produced by the solar exhibition.

Anti-fouling protection

The inner pipe roughness, the quality and velocity of the fluid are elements which promote the incrustations.

An increase of incrustations is conducive to reduce the pipe length, an increase in pressure loss and a higher energy consumption.

ABN//INTAL CT FASER RD includes an anti-fouling additive that provides an ultra- smooth effect, generating an anti-fouling protection.

The smoothness of a pipe is directly associated with its porosity and, therefore, with its aptitude to avoid the incrustations or calcareous deposits.

ABN//INSTAL CT Faser RD pipes are completely smooth and their length is not reduce in the course of time which guarantees the invariability of the roughness coefficient of the pipes.

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Distinguishing characteristics2.3.


Anti-microbial protection

The pipes used for the distribution of drinking water must not contaminate or worsen the quality of the transported water with germs or substances that could mean a potential danger for the consumers' health. The metallic pipes used nowadays in many systems can add oxides to the water which help the proliferation of pathogenic agents giving origin to a bio layer inside the pipe walls.

This increasing worry for the water quality in distribution systems has introduced a substantial progress on having incorporated a novel antimicrobial additive that works effectively against the bacteria and fungi proliferation inside the pipe walls. Thus, the installation of ABN//INSTAL CT Faser RD pipes assures a pipeline free from incrustations and bacteria helping to maintain the water quality. (Further information in paragraph 2.6. Study of microbial load evolution).

High impact resistance

The elasticity of this product provides a high impact resistance much higher than that of metal pipes. This will preserve the pipes both in its use (water hammers) and in the transport, storage and handling in work.

Resistance to corrosion

The pipe corrosion depends mainly on the environment where they are placed, on the manufacturing material and on the operating mode they are subject to, being the exterior protection of the pipes what should be more carefully studied, because the surrounding environment is more aggressive than the water circulating inside.

The properties of ABN//INSTAL CT Faser RD pipes do not turn out to be altered because of limes, plasters and cement mortars. This means that no application of superficial protection is necessary. They do not present problems of rottenness, rust, appearance of mould or oxidation, nor turn out to be affected due to the seaweed, bacteria or fungi.

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A• N S TE I-N INOI CC RA UT SS TU AR CC ION NI-I ET S N •AR• E SN ISÓI TS EO NR TR E O AC LA AL CA O E RT RN OE ST IÓSI NSE • R

A • LTO AT RCA EP SIM SI TL EA N CAI IAC N AE LT IS MI S PE ACR TA OT • L A

ABN INSTAL CT Faser RD - Página 02-05//

////////////////////////////////////////////Resistance to the chemical agents

Since ABN//INSTAL CT, Faser RD pipes are polyolefin of high molecular weight, present a non-polar structure, which provides an excellent resistance to chemical agents.

Thanks to its chemical inertness, they are resistant to inorganic acids (hydrochloric, sulphuric, etc.), alkalis, detergents, mineral oils or fermentation products.

They do not suffer any alteration caused by sea water, saline or acidic soils, nor by urban or industrial discharges.

ABN//INSTAL CT Faser RD has higher resistance to the possible aggression of hard waters and they support chemical substances with a PH between 1 and 14, what it includes acidic and alkaline substances, as well as chlorine, fluorine or iron present in water.

Abrasion resistance

The high abrasion resistance of ABN//INSTAL CT Faser RD pipes allows the water circulation at a high velocity without any risk of erosion.

Lowest noise level in the installation

The sound absorption and the elasticity of ABN//INSTAL CT Faser RD system avoid noise propagation, the vibrations when water is running and the water hammers, reaching thus a very high degree of sound isolation.

In this way, the transmission of noises is much lower compared to the metallic pipes, allowing the water to run faster.

Healthiness

ABN//INSTAL CT Faser RD pipes are inert, odourless, tasteless, stainless, insoluble and innocuous. All these are ideal qualities for drinking water conveyance, among other applications. ABN//INSTAL CT Faser RD preserves the organoleptic properties of drinking water intact without modifying its colour, smell and flavour.

The excellent quality of ABN//INSTAL CT Faser RD system keeps the full qualities of the transported water during its entire useful life.

Safe joints

The molecular fusion of the pipe material and fittings (thermo-fusion) makes the joints disappear giving place to continuous pipelines, which guarantees the highest security degree regarding, cold and warm water installations and other applications.

R• E SA IC SI TM EÍ NU CQ I AAI QC UN ÍE MT IS CI AS E • R

GICÓ OL O C •E E • C O L ÓO GCI ICG OÓ L O •C E

% 0 SE0 G1 UN RÓ AI N • U U • N IA ÓR NU 1G 0E 0S %

% S0 E0 G1 UN RÓI AN • UIOC SN OE •L SI IS L• E NOS CIO OI C SON E •L I SS I L• EO NS COI


Reducing installation times

The joining systems of ABN//INSTAL CT Faser RD pipes is based on the thermo-fusion, either by means of poly-fusion, electro-fusion or butt welding.

Thermo-fusion implies reducing installation times offering the entire guarantee of the final system due to the complete molecular structure of the polypropylene.

Likewise, the time necessary for loading and operation immediately after the welding is considerably reduced compared to other materials.

Thinner wall pipes

The excellent physical and mechanical characteristics of PP RCT RP and its ideal behaviour exposed to high and low temperatures manage to reduce the pipe thickness in order to improve their services. The thinner pipes allow to transport much more water flow in equal diameters, or to maintain it using smaller pipes.

Environmentally compatible

The ABN //INSTAL CT Faser RD material is sustainable, ecological and recyclable.

The nature of the materials makes the recovery easy at a qualitative level necessary for recycling in the production. This process does not need energy and chemical resources, simply a mechanical process.

Any consumption generates a residue. The plastic residues are a valuable resource to get rid of them without making use of them like source of matter (recycling) or energy source (energy valuation).

As soon as its useful life was concluded, the polypropylene tubes can be mechanically recycled by means of a grinding process turning into a new raw material that in turn can serve for the manufacture of other products, giving this way to the material a new useful life. B-s1, d0 classified and halogen Free

ABN//INSTAL CT Faser RD is free from halogens, a striking security feature in case of reaction against fire. It does not produce poisonous gasses, because any dioxin comes out in case of fire.

Also has a cassification of fireproof B-s1, d0.

////////////////////////////////////////////OSTC EO J A • B B • A J OE CT OS SO TC EO J A • B

0 1 2 3 4 5 6 7

0

0 4 8 1/128

0 1 2 3 4 5 6 7 8 9 0 1/20

1 2

8

SPE ESR OO RN E • MM • E NR OO RS E EP SS PE E SR OO RN E •M



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MaterialDensityMelt mass flow rate (230ºC/2,16kg)Hydrostatic (hoop) stress (20ºC–1h) a 15 MpaHydrostatic (95º-22h) a 4.2 MpaHydrostatic (95ºC–165h) a 4.0 MpaHydrostatic (95ºC–1000h) a 3.8 MpaThermal stability (110ºC–8760 h) a 2.6 MpaLongitudinal retraction (135ºC)Tensile ModulusTensile strain at yieldEsfuerzo de tracción en el punto de fluenciaLineal thermal expansionThermal conductivity coefficientOpacityImpact resistance determination(ball drop method)Roughness k

(hoop) stress (hoop) stress (hoop) stress

PPR CT RP + FV>0.930.25

No faultNo faultNo faultNo faultNo fault

<2>950>12>30

<0.040.24

SI

H50≥1m (s3,2) H50≥0.7m (s4 - s5 - s6,3- s8)

0,003

-g/cm3g/10'

-----

%Mpa

%Mpa

mm/mºCW/m ºC

-m

mm

-ISO 1183ISO 1133ISO 1167ISO 1167ISO 1167ISO 1167ISO 1167ISO 2505ISO 527ISO 527ISO 527

-DIN 52612ISO 7686EN 1411

-

Properties Values Units Standards

TECHNICAL CHARACTERISTICS

Technical characteristics2.4.

PP RCT FASER RP PROPYLENE PIPE

ABN//INSTAL CT Faser RD Pipe,B,s1-d0 classification of fireproof, halogen free, fabricated in PPR CT RP multilayer, for cold water, A.C.S., heating and air-conditioning, with disinfection resistance, anti-microbial additive, anti-incrustation resistance, anti-expansion resistance and UV protection. Series---, SDR ---, from external diameter – mm and thickness -- mm, white inner layer (RAL 9003) and grew external layer (RAL 9006) with white strips, installed in accordance to UNE ENV 12108.


//////////////////////////////////////////////////////////////////////////////////////// Regression curves

2.5.

Determination of the long-term hydrostatic strengthISO 9080:2003 - Evaluation of the ABN//INSTAL CT FASER RD pipes.

1

1,5

2

2,5

3

4

5

6789

10

15

20

25

30

40

50

0,1 1 10 10² 10³ 10 10 1054 6

1 5 10 25 50 100

10 ºC

20 ºC

30 ºC40 ºC50 ºC

60 ºC

70 ºC

80 ºC

95 ºC

years

breaking time (h)

Hydr

osta

tic e

ffor

t (M

Pa)

Standard Method: ISO 9080:2003, 4-parameteraccording to DIN 8078:2008:PP-RCT

Working pressure supported by the pipes for pressurized water. The maximum work pressures according to the resistance equation to the internal pressure in accordance with DIN 8078, bearing in mind a security factor SF.

Where : p - Admisible work pressureσ- Hydrostatic effort at MPaS - Pipes series SF - Security factor

p = x10σ

SxSF

Tests carried out by EXOVA Materials Technology



////////////////////////////////////////////The tables of Permissive Working Pressure represent the expected operating of pipes under pressure and temperature conditions, indicated in every series. The resultant information does not include alterations the installations go through, such as high concentration of chemical agents and anomalies regarding control of pressure and temperature, etc.

The allowable pressures resulted from the specific conditions to wich pipe system components in the drinking water domestic installations are exposed to.

Permissive working pressure2.6.


Permissive working pressure

1bar = 14.5 psiCalculation performedwith a safety factor = 1.25

bar39.2038.2037.5736.7536.5035.9534.1533.0532.7732.0031.7031.15

29.8029.0028.4527.9027.6227.0526.0525.2024.6524.3723.8223.5223.0522.1721.6021.3020.7520.4519.3718.8018.5017.9217.7016.5515.6715.4015.1014.9013.8213.2212.9212.7010.7510.15

psi568.52554.04544.90533.01529.38521.41

495.30479.34474.70464.12459.76451.79432.21420.60412.63404.65400.59392.32377.82365.49357.51353.45345.47341.12334.31321.54313.28308.93300.95296.60280.93372.67268.31259.90256.71240.03227.27223.35219.00216.10

200.44191.73187.38184.19155.91147.21

bar25.0824.4024.0423.5223.3623.0021.8521.1520.9720.4820.3019.9319.0818.5618.2017.8517.6817.3116.6716.1215.7715.6015.2415.0514.7514.1913.8213.6313.2013.0012.4012.0311.8411.4711.3010.5910.009.859.669.508.848.468.278.106.886.49

psi363.75353.89348.67341.12

338.80333.58316.90306.75304.14297.03294.42289.06276.73269.19263.96258.89256.42251.06241.77233.80228.72226.25221.03218.28213.93205.80200.44197.78191.44188.54179.84174.48171.72166.35163.89153.59145.03142.86140.10137.78128.21122.70119.94117.4899.7894.12

bar15.6815.2815.0314.7014.6014.3813.6613.2213.11

12.8012.6812.4611.9311.6011.3811.1611.0510.8210.4210.089.869.759.539.419.228.878.648.528.308.187.757.527.407.177.066.626.276.166.045.935.535.295.175.064.304.06

psi227.42221.61217.99213.20211.75

208.56198.12191.74190.14185.64183.90180.71173.03168.24165.05161.86160.26156.93151.12146.19143.00141.41138.22136.48133.72128.64125.31123.57120.38118.64112.40109.06107.32103.99102.3996.0190.9389.3487.6086.0080.2076.7274.9873.3862.3658.88

Temperature ABN//INSTAL CT FASER RDSeries 3,2-SDR 7,4

ABN//INSTAL CT FASER RDSeries 5-SDR 11

ABN INSTAL// CT FASER RDSeries 8-SDR 17years of service

15102550100

15102550100

15102550100

15102550100

15102550100

151025501510255015102515

20 ºC

30 ºC

40 ºC

50 ºC

60 ºC

70 ºC

80 ºC

95 ºC

10 ºC

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The present study is realized by AQM Laboratories, collaborating company with the Environment Ministry and accredited by ENAC.(www. aqmlaboratorios.com)

Antimicrobial additives

Pipes destined to drinking water supply should not contaminate or worsen the conveyed water quality with germs or substances that could mean a potential danger for the consumer's health. The metallic pipes used nowadays in multiple systems add highly polluting elements to water like copper, iron, or lead which promote proliferation of pathogenic agents due to a bio-film present inside the pipe walls. There is not any corrosion inside PPR-CT RP pipes, therefore nutrient contribution or scale formation does not take place where bacteria could reside and multiply. There is not any harm in drinking water quality that runs inside them either.

The growing concern on water quality inside the supply systems has led ABN Pipe Systems to introduce a substantial progress in ABN// INSTAL CT Faser RD pipes, that incorporate a novel antimicrobial additive which acts effectively against of bacteria and fungi proliferation inside the pipe walls.

Study of microbial load evolution

Adding antimicrobial agents to ABN//INSTAL CT Faser RD pipes the virtual disappearance of microorganisms developing inside the pipes walls has been achieved.

These assertions derive from the results issued by the “Study of microbial load evolution” prepared by AQM Laboratories (entity accredited by ENAC) for pipes made by ABN Pipe Systems for pressurized hot and cold water installations.

24 hours after the inoculation of different microorganisms at 30ºC (peak of growth) the additive makes virtually disappear most of the potential hazards for potable water, such as aerobic mesophylls and coliform organisms, just as the graphs show, effectively reducing the mentioned micro-organisms to 99% just 24 hours after the network starts up.

The novel antimicrobial additive incorporated to these systems becomes an effective microorganism reducer just 24 hours after the network starts up.

//////////////////////////////////////////// Study of microbial load and Legionella evolution

2.7.


////////////////////////////////////////////Prevention and control of Legionella

One of the most dangerous bacteria for human beings growing in drinking water distribution networks is the Legionella. High temperature (between 20-40ºC), nutrients, and a substratum (bio-film) capable of protecting it against the bactericide disinfection agents are the ideal conditions helping it growth and multiply. Corrosion process that takes place inside the metallic pipes promotes the development of these nutrients, and they contribute to the development of the Legionella. These conditions usually happen mainly in producer or tank water like cooling towers, condensers, systems of air conditioning, etc.

Study of the legionella evolution

The effectiveness of the antimicrobial agents to prevent the expansion of the legionella has been proved in the “Study of legionella evolution” carried out by AQM Laboratories, in pipes made by ABN Pipe Systems for conduction of pressurized drinking water.

The test has demonstrated that 72 hours after the inoculation of the bacterium in pipes treated with and without additive (peak of growth of the strain at this point) the Legionella pneumophila has been reduced to 56 % in pipes with additive.

The ABN//INSTAL CT Faser RD systems have an antimicrobial internal layer that contributes to the prevention and control of Legionella.

With additiveWithout additive

Fungi proliferation in sample with and without additive


////////////////////////////////////////////Study of the evolution of different microorganisms inoculated in pipes treated with specific antimicrobial.

The analysed samples correspond to materials made of PPR-CT RP + FV in three-layer configuration. One of them without the antimicrobial agent, henceforth PIPE WITHOUT ADDITIVES; and the other one, an antimicrobial agent has been added in its production process, henceforth PIPE WITH ADDITIVES.

PROCEDURE

The pipes have been inoculated with four strains of different microorganisms suspended in 1 litre of sterile potable water. The inoculated microorganisms are the following ones:

Escherichia coli Citrobacter freundii Pseudomonas aeruginosa Saccharomyces cerevisiae

Subsequently, the pipes with the seeds (inóculos) have been incubated for 24 hours at 30ºC of temperature.

The microbial load of the seeds (inóculos) has been analyzed at different incubation times in every one of four equal test tubes, of every one of two samples to be studied: initially, at 12 a. m. and at 12 p. m.

The test results have been the following ones:

Aerobic microorganisms count at 30ºC (PNT-M-AL-003) Coliform bacteria count (PNT-M-AL-009) Yeast count (PNT-M-AL-008)

2.7.1. Study of microbial load evolution


RESULTS

Next, the results obtained for both samples are listed on the table below. The count of every microorganism is identified separately at every incubation time, as well as the logarithm of ufc/ml, a usual measure unit of the microbiology growth (or culture).

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Initial concentracion

Test pipe 0

Test pipe 1

Test pipe 2

Initial concentracion

Test pipe 0

Test pipe 1

Test pipe 2

64

500000

41000000

60

430

16000

1.81

5.70

7.61

1.78

2.63

4.20

26

26

26

15

18

20

1.41

1.41

1.41

1.18

1.26

1.30

37

230000

31000000

46

200

6200

1.57

5.36

7.49

1.66

2.30

3.79

Pipe without additive

Pipe with additive

0

12

24

0

12

24

RESULTS

ufc/ml logufc/ml ufc/ml log

ufc/ml ufc/ml logufc/ml

Mesophylls aerobic(PNT-M-AL-003)

Yeasts(PNT-M-AL-008)

Yeasts(PNT-M-AL-009)

Incubationtime

(hours)Test pipes

The following graphs exemplify the decreases of each of the micro-organisms in two samples analysed for the inoculated initial concentration and the analyses practised 12 and 24 hours after the inoculation.

ufc/ml: forming colony unit per millilitre


////////////////////////////////////////////

COUN

T AE

ROBI

C M

ESOP

HILI

C(u

fc/m

l)-3000000

60430

64

2500

Without additivesWith additives

0 Hours12 Hours 24 Hours

1600

42000000

37000000

32000000

27000000

22000000

17000000

12000000

7000000

2000000

Aerobic Mesophilic

500000

41000000

0

2500

40

35

30

25

20

15

10

5

Sacchararomyces crevisiae

262626

15 18 20

COUN

T C

OLIF

ORM

ES(u

fc/m

l)

046

200

37

6200

230000

35000000

30000000

25000000

20000000

15000000

10000000

5000000

31000000

Escherichia coli

Chart 1: Recount in plate of mesophylls aerobic microorganisms at 30ºC (PNT-M-AL-003) – Mesophylls Aerobic

Chart 2: Recount in plate of yeasts (PNT-M-AL-008) - Saccharomyces cerevisiae

Chart 3: Recount in plate of coliform bacteria (PNT-M-AL-009) – Escherichia coli


COUN

T AE

ROBI

C M

ESOP

HILI

C(u

fc/m

l)





////////////////////////////////////////////CONCLUSIONS

24 hours after the inoculation of each of the microorganisms the following conclusions have been drawn:

ŸResults of TOTAL AEROBIC MESOPHYLLS: The antimicrobial additive has reduced the content of aerobic mesophylls in the PIPE WITH ADDITIVES to 99.96%. ŸResults of YEASTS: The PIPE WITH ADDITIVES presents a 23.08% descent in the content of yeasts compared with the pipe without any antimicrobial additive. Ÿ Results of COLIFORMS: The addition of antimicrobial agent has eliminated 99.98% of the present coliform bacteria in the pipe WITHOUT ADDITIVES.

In short, having added appropriate antimicrobial agents in ABN//INSTAL CT Faser RD polypropylene pipes helps the inoculated and growing microorganisms at 30ºC totally disappear (so that temperature has worked in favour of growth). Coliform bacteria and total aerobic mesophylls represent most of the potential threats being present in potable water and its percentage diminishes over 99%, as the counts have shown.


////////////////////////////////////////////Study of the evolution of Legionella pneumophila inoculated in pipes treated with specific antimicrobial additives.

The ABN //INSTAL CT Faser RD (PPR-CT RP+FV) samples have been classified into two groups and each of them presents different characteristics regarding composition. Pipes WITHOUT anti-microbial ADDITIVES and Pipes WITH anti-microbial ADDITIVES.

PROCEDURE

The pipes have been inoculated with the Legionella pneumophila strain suspended in 1 litre of sterile potable water. Later on, the pipes containing the seeds, have been incubated during 6 days (144h hours) at 37ºC ± 1ºC.

The microbial load of the seeds has been analysed at different incubation times: initially and up to 96 hours of inoculation (4 days). The Legionella pneumophila strain develops a maximum growth in 3 days, later on the seeds ' death would be taking place if the culture (growth) is not re-established or if a new strain is not introduced.

The tests carried out are the following ones: Legionella pneumophila count at 37ºC (PNT-M-AQ - 004)

RESULTS

The results obtained for ABN// INSTAL CT Faser RD material for the samples with and without bacteriostatic agent at different incubation times, are shown below.

Initial concentration

Test pipe 0

Test tube1

Test pipe 2

Test pipe 3

Test pipe 4

Initial concentration

Test pipe 0

Test tube1

Test pipe 2

Test pipe 3

Test pipe 4

500

1470

2200

2570

2500

500

2500

4100

4780

4900

2.70

3.17

3.34

3.41

3.40

2.70

3.40

3.61

3.68

3.69

Pipe with additives

Pipe without additives

0

24

48

72

96

0

24

48

72

96

RESULTS

ufc/ml log (ufc/ml)

Legionella pneumophila count

(PNT-M-AQ-004)

Incubation time

(hours)Test pipe

2.7.2. Study of Legionella evolution


COUN

T LE

GION

ELA

(ufc

/ml)

5000

4500

4000

3500

3000

2500

2000

1500

1000

500

0

500

1470

2200 25702500

500

2500

4100

4780

0 Horurs 24 Hours 48 Hours 72 Hours 96 Hours

Legionela pneumophila

4900

Tiempo de Cultivo (Horas)

////////////////////////////////////////////CHART 4: RECOUNT OF Legionella pneumophila (PNT-M-AQ-004)

CONCLUSIONS

After 96 hours (4 days) from the inoculation of Legionella and having the strain reached the maximum growth at this point, the difference between the pipe without additive (standard pipe) and the pipe with additive is a descent to 49% in the pipe with antimicrobial agent.



////////////////////////////////////////////

Resistance to chemical and thermal disinfection (R.D. 865/2003)

// 03

////////////////////////////////////////////


////////////////////////////////////////////

Interior sanitary cold and warm water installations

The design of sanitary and cold hot water systems for human consumption should guarantee:

a) That there is not stagnations (this is solved by opening the faucets periodically to help water renewal).

b) An appropriate thermal isolation. c) A correct water circulation.

With regard to the materials of the installations, these should resist the established methods of disinfection (high disinfectant concentration or high temperature). The ECO-SIS CT Faser RD pipe systems support successfully both disinfection methods.

Maintenance of the interior ACS installations and cold water of human consumption

The prevention measurements will be aimed to avoid the micro-organism growth inside the interior installations. The most important preventive measurements are a good design and maintenance of the installations, temperature control and a continuous disinfection.

That is why it is necessary to follow the periodic review instructions of these installations as the Royal decree 865/2003 establishes in its Annex 3.

In accordance with the above mentioned Royal Decree, it is established that the sanitary cold and warm water installations should be cleaned and disinfected at least once a year, the first time they start to operate, after more than a month stop and after a repair or structural modification. The cleanliness and disinfection will be more rigorous in case of legionella outbreak.

//////////////////////////////////////////// Resistance to chemical and thermal disinfection (Royal Decree 865/2003)

3.

Inadequate treatment

The execution of the disinfection treatment should be done correctly following the parameters (chlorine concentration, temperature, time) established by the Royal decree RD 865/2003, otherwise, an inadequate treatment, can provoke the oxidative degradation of the different elements of the system.


////////////////////////////////////////////Review of hot and cold water installations

A disinfection process will not be effective if it is not followed by an exhaustive cleanliness. Suitable systems of treatment and products fit for human consumption water should be used.

The methods of cleanliness and disinfection referred to in the RD 865/2003 are:

a) thermal disinfection b) chemical disinfection with chlorine

Thermal disinfection

The thermal disinfection consists in raising the temperature networks up to the levels adapted to the treatment selected:

Disinfection treatment

•In case of having water tanks: Empty the system, if they are accessible, clean thoroughly the walls of the accumulation deposits, otherwise, a purge should be done. Do the necessary repairs in the deposits and rinse them with clean water.

•Fill the deposit and raise the temperature of the water up to 70 ºC and maintain for 2 hours.

•Later on, open all the faucets and showers by sectors, during 5 minutes, in a sequential way.

•Confirm the temperature in such a way that in all the terminal points of the network a temperature of 60ºC should be reached.

•Empty the accumulation deposits and to fill them again, restoring this way its routine operation.

Treatment in case of legionella outbreak:

• In case of having water tanks: Empty the system, clean thoroughly the walls of the deposits and the batteries, do the necessary repairs and rinse with clean water.

• Fill the storage tank and raise the temperature of water up to 70ºC or more for at least 4 hours. Later on, open all the faucets and showers during 10 minutes in a sequential way. Verify the temperature so that in all the terminal points of the network the temperature reaches 60ºC. Empty the storage tanks and fill them again.

•The sustained water treatment will be applied for 3 months so that 1-2mg/l of residual free chlorine for cold water is detected in the terminal points of the network and that the service temperature for hot water in such points stabilizes between 55 and 60ºC.

The methods of cleanliness and disinfection referred to in the RD 865/2003 are:

a) thermal disinfection b) chemical disinfection with chlorine


Disinfection with chlorine

The chlorine and its compounds are appropriate for chemical disinfection because they are capable to destroy pathogens very quickly

Usage of Chlorine, as disinfectant of these installations, is much extended for being an effective, easily measured and an economic product. But we must bear in mind that its usage presents two important disadvantages: its high oxidizing power, which can give place to corrosive effects in the installations and that it is necessary to keep the pH is below 8, otherwise its bactericidal action is much reduced. According to the type of treatment, it is possible to do it as it is laid out in the Royal Decree RD 865/2003:

Chemical treatment for disinfection with chlorine

•In case of having a water tanks, chlorinate the water inside with 20-30 mg/l of free residual chlorine, maintaining the water below 30 ºC and with a pH of 7-8, making come 1-2 mg/l of chlorine to every terminal points of the network. A period of 3-2 hours will be kept respectively.

•If there are no water tanks, it is understood that the system must be chlorinated to obtain 1-2 mg/l in consumption points without being necessary to reach 20-30 mg/l.

•As an alternative, the tank can chlorinated with 4-5 mg/l, maintaining these levels for 12 hours.

•Neutralize the quantity of free residual chlorine and empty the water of the system.

•In systems with storage water tanks clean thoroughly the walls. If these are not easily accessible, practise a purge. Do the necessary repairs in the systems and rinse them with clean water.

•Fill again with water and restore the normal use conditions. If a re-chlorination is necessary, it will be carried out by means of automatic dispensers.

Treatment in case of legionella outbreak

•Chlorinate with 15 mg/l of free residual chlorine, maintaining the water below 30ºC and at 7-8 pH. These values will be kept during a period of 4 hours.

•As an alternative, the system can be chlorinated with 20 or 30 mg/l of free residual chlorine, maintaining these levels for 3 or 2 hours respectively.

•Neutralize the quantity of residual free chlorine and remove the water from the system. Clean the walls of the deposits thoroughly, do the necessary repairs in the systems, rinse and fill them with clean water.

•Re-chlorinate with 4-5 mg/l of residual free chlorine and maintain for 12 hours. This chlorination should be done sequentially, distributing the disinfectant in an orderly way from the beginning to the end of network. Open all the faucets and showers, by sectors during 5 minutes, check out in a sequential way, that the concentration in terminal points is 1-2 mg/l.

•Empty the storage tanks and fill them again.

•It is necessary to renew all those elements of the network in which some anomaly is observed, especially those affected by the corrosion or the incrustation.

////////////////////////////////////////////

Water temperature

< 30ºC

Water PH7-8


////////////////////////////////////////////

Sizing4.1. Water quality4.2. Minimum supply conditions 4.3. Calculation volume. DIN 1988 standard. Formula and tables 4.4. Diameter equivalence4.4.1. Diameter equivalence of Cooper pipes-ABN//INSTAL CT Faser RD 4.4.2. Diameter equivalence of Steel pipes-ABN//INSTAL CT Faser RD.Diamtres 20 to 634.4.3. Diameter equivalence of Steel pipes-ABN//INSTAL CT Faser RD.Diametres 75 to 200

4.5. Thermal insulation

// 04

////////////////////////////////////////////


Water quality

////////////////////////////////////////////4.1.

The water of the installation must comply with provisions of existing legislation on water for human consumption.

The materials used in the installation, as regards its effects on the water supplied, must conform to the following requirements:

• the materials used for the pipes and fittings should not produce concentrations of harmful substances that exceed the values allowed by the RD 140/2003 by which the sanitary criteria of the water quality of human consumption are establish, and the RD 865/2003 by which the hygienic-sanitary criteria are established, that should be born in mind, in order to prevent and control of legionella. • they should not modify either the drinking quality, the smell, the colour nor the taste of the water; • they must be resistant to the interior corrosion; • they must be capable of working efficiently in the provided operating conditions; •they must not show any electrochemical incompatibility between themselves; •they must be compatible with the supplied water and must not allow the migration of substances from the materials in quantities that put the healthiness and cleanliness of the water for human consumption at a risk.•their aging, fatigue, durability and the remaining mechanical, physical or chemical characteristics, must not diminish the provided useful life of the installation.

To comply with the previous conditions revetments, systems of protection or systems of water treatment can be used.

The water supply installation must have characteristics adapted to avoid the development of pathogenic germs and not to favour the development of the biolayer (biofilm).

Protection from returns:

Non-return systems will be provided to avoid reverse flow direction in the points listed below, as well as in any other that turns out to be necessary:

•next the meters; • in the base of the uplinks; •before the equipment of water treatment; •in the feeding pipes not destined for domestic uses; •before the refrigeration or air conditioning devices.

The water supply installations will not be connected directly neither to installations of evacuation nor to installations of water supply from another origin than the public network.

The water will reach the devices and equipments of the installation in such a way that returns o refluxes will not take place.

The non-returns will be placed alternatively with emptying faucets in such a way that it is always possible to empty any stretch of the network.


The installation must supply the devices and hygienic equipments with the volumes that appear in the table.

In the consumption points the minimal pressure must be:

• 100 kPa (1 bar) for common faucets; • 150 kPa (1,5 bar) for fluxors and heaters.

The pressure in any consumption point must not overcome 500 kPa. (5 bar)

The ACS temperature in the consumption points must be comprised between 50ºC and 65ºC except in the installations located in buildings destined to exclusive use of housing provided that they do not affect the exterior appearance of the mentioned buildings.

////////////////////////////////////////////Minimum supply conditions 4.2.

WashbasinToiletShowerBath pipe 1.40m or moreBath pipe less than 1.40mBidetToilet bowl with cisternToilet bowl with fluxorUrinals with timer-tapUrinals with cisternDomestic sinkNon domestic sinkDomestic dishwashers Industrial dishwashers (20 services)LaundryDomestic washing machineIndustrial washing machine (8kg)Isolated tapGarage tapDump

0.050.100.200.300.200.100.101.250.150.040.200.300.150.250.200.200.600.150.200.20

0.030.0650.100.200.15

0.065----

0.100.200.100.200.100.150.400.10

--

MINIMUM INSTANT VOLUME FOR EACH TYPE OF DEVICE

Type of device Minimum instant volumeof cold water

(dm3/s)

Minimum instant volumeof A.C.S(dm3/s)

Separations regarding other installations

The cold water piping must be done in such a way that it is not affected by the heat sources and consequently they must always run along separated from the canalizations of hot water (ACS or heating) placed at least, 4 cm distant. When both pipes are in the same vertical plane, the pipe of cold water must always be placed below that of hot water. The pipes must be arranged below any canalization or element that contains electrical or electronic devices, as well as of any telecommunication network, keeping a distance in parallel of at least 30 cm.With regard to the gas conductions a minimum distance of 3 cm should be maintained.


According to (CTE) Spanish regulation, the installation must supply the sanitary devices with the following volumes:

Dimensioning of the distribution networks

The calculation will be done with a first dimensioning by selecting the most unfavourable pipe stretch and being obtained a few previous diameters that later on it will be necessary to verify according to the load loss that is obtained with them.

This dimensioning will be done bearing always in mind the peculiarities of every installation and the diameters obtained will be the minimums that turn out compatible both its proper functioning and economy.

Dimensioning of the stretches

The network dimensioning will be done from the dimensioning of every stretch, and for this purpose it will start from the circuit considered as the more unfavourable which it will be the one provided with the greatest loss of pressure due both to the friction and to its geometric height. The dimensioning of the stretches will be done in accordance with the following procedure:

• the maximum water flow of every stretch will be equal to the sum of flows running at the consumption points fed by the first one according to the table of instantaneous flow. • allocation of simultaneity coefficients of every stretch according to a suitable criterion.

•assessment of the calculation flow in every stretch as the result of the maximum flow by the corresponding simultaneity coefficient.

• selection of a calculation velocity estimated within the following intervals:

▫ metallic pipes: between 0,50 and 2,00 m/s ▫ thermo-plastic and multi-layer pipes: between 0.50 and 3.50 m/s

•Achievement of the diameter corresponding to every stretch according to the flow and the velocity.

////////////////////////////////////////////


Checking the pressure

It will be verified that the available pressure in the most unfavourable consumption point overcomes the stated minimal values and that in all the consumption points the maximum value is not overcome according to the following:

• determine the loss of pressure of the circuit adding the total losses of pressure of every stretch. The localized losses of load can be estimated in 20% to 30% of the produced load on the actual length of the stretch or be evaluated from the elements of the installation.

• verify the adequacy of the available pressure: once obtained the values of the pressure looses of the circuit, it is proved whether they are perceptibly equal to the available pressure that remains after deducting, the geometric and residual height of the more unfavourable consumption point from the total pressure. In case the available pressure in the consumption point was lower than the minimum demanded pressure the installation of a pressure generator would be necessary.

Dimensioning of the ACS networks

Dimensioning of the ACS networks of impulsion

For the networks of impulsion or return of ACS the same calculation method as for networks of cold water will be used. Dimensioning of the return networks of ACS

To determine the flow that will circulate through the return circuit it is estimated, that at the farthest tap there will be a maximum temperature loss of 3°C from the tank exit or heat exchanger in its case.

In any case, if the installation answers to this scheme, about 250 l/h will be re-circulating in every column, to be able to carry out a suitable hydraulic balancing.

The return flow can be estimated according to empirical rules in the following way: •Consider that 10 % of the feeding water as a minimum, is re-circulated.

////////////////////////////////////////////

Diameter of the pipesABN//INSTA CT Faser RD

(mm)

20

25

32

40

50

63

Re-circulated flow(l/h)

140

300

600

1.100

1.800

3.300

Relation between the diameter of the pipes and the re-circulated flow of A. C. S.


////////////////////////////////////////////Calculation flow. DIN 1988 Standard. Formula and table4.3.

A good solution for determining the calculation flow in a plumbing installation, bearing in mind the simultaneity, is provided by the DIN 1988-T2 Standard (Practice Codes for drinking water installations).

Calculation or simultaneity flow

DIN 1988 Standar

Q = Total flow InstalledQc = Calculation flow (quantity) (simultaneous) Qmin = Minimal instantaneous flow (quantity)

RESIDENCE

OFFICESSTATIONSAIRPORTS

HOTELESDISCOTEQUESMUSEUMS

HOSPITALS

COMMERCIAL CENTERS

SCHOOLSSPORT CENTERS

BUILDINGS Q>20Q≤20

Qmin≥0,5

0,21 1,70 x (Q) - 0,70

0,540,40 x (Q) + 0,48

0,501,08 x (Q) - 1,83

0,650,25 x (Q) + 1,25

0,274,3 x (Q) - 6,65

-0,50-22,5 x (Q) + 11,5

0,450,682 x (Q) - 0,14

0,500,698 x (Q) - 0,12

0,274,4 x (Q) - 3,41

0,366(Q)

Q≤1 Algún Q>1Qmin<0,5

0,21 1,70 x (Q) - 0,70

Q

l/s

Qc(l/s)

For other special constructions (barracks, jails, seminars, industries) it is necessary to establish special considerations on the simultaneity.

Total flow installed, Q

It is the sum of the minimal instantaneous flows of all the devices installed.

Calculation flow or simultaneous flow, Qc

This is the flow that takes place due to the simultaneous logical functioning of consumption devices or supply units.

Minimum instantaneous flow, Qmin

It is an instantaneous flow necessary to supply each sanitary devices regardless of the operation state.


<0.5>=0.5<0.5>=0.5<0.5>=0.5<0.5>=0.5<0.5>=0.5<0.5>=0.5<0.5>=0.5<0.5>=0.5<0.5>=0.5<0.5>=0.5<0.5>=0.5<0.5>=0.5<0.5>=0.5<0.5>=0.5<0.5>=0.5<0.5>=0.5<0.5>=0.5<0.5>=0.5<0.5>=0.5<0.5>=0.5

0.581.000.871.291.091.491.281.661.441.801.591.931.732.041.852.141.972.232.092.322.202.412.302.482.402.562.492.632.582.692.672.762.762.822.842.882.922.943.002.99

////////////////////////////////////////////

1.0

2.0

3.0

4.0

5.0

6.0

7.0

8.0

9.0

10.0

11.0

12.0

13.0

14.0

15.0

16.0

17.0

18.0

19.0

20.0

0.541.000.791.270.981.441.131.571.271.681.371.781.501.861.601.931.692.001.782.061.872.111.952.162.022.212.102.262.172.302.232.342.302.382.362.422.432.452.492.49

0.541.000.791.270.981.441.131.571.271.681.371.781.501.861.601.931.692.001.782.061.872.111.952.162.022.212.102.262.172.302.232.342.302.382.362.422.432.452.492.49

0.581.000.871.291.091.491.281.661.441.801.591.931.732.041.852.141.972.232.092.322.202.412.302.482.402.562.492.632.582.692.672.762.762.822.842.882.922.943.002.99

0.581.000.871.291.091.491.281.661.441.801.591.931.732.041.852.141.972.232.092.322.202.412.302.482.402.562.492.632.582.692.672.762.762.822.842.882.922.943.002.99

0.990.991.901.902.512.512.992.993.383.383.733.734.034.034.304.304.554.554.784.785.005.005.205.205.385.385.565.565.735.735.895.896.056.056.196.196.336.336.476.47

Q Qmin RESI

DEBN

CE

OFFI

CES

HOTE

LES

HOSP

ITAL

S

COM

ERCI

AL

CEN

TERS

SPOR

T CE

NTE

RS3.123.243.353.463.573.683.783.883.994.094.184.284.374.474.564.654.744.834.915.005.095.175.255.335.415.495.575.655.735.815.885.966.036.116.186.256.326.406.476.54

2.552.602.652.712.752.802.852.902.942.993.043.083.123.173.213.253.293.333.373.413.453.493.533.573.603.643.683.723.753.793.823.863.893.933.964.004.034.064.104.13

3.063.113.173.223.283.333.383.433.483.533.583.633.683.723.773.823.863.913.954.004.044.094.134.184.224.264.304.354.394.434.474.514.554.594.634.674.714.754.794.83

3.133.263.383.493.603.713.823.924.024.124.224.314.404.494.584.674.754.834.914.995.075.155.225.305.375.445.515.585.655.715.785.855.915.976.046.106.166.226.286.34

6.596.706.816.917.007.097.177.257.327.397.467.527.587.647.707.757.807.857.907.947.998.038.078.118.158.188.228.258.298.328.358.388.418.448.478.498.528.558.578.60

Q

21.022.023.024.025.026.027.028.029.030.031.032.033.034.035.036.037.038.039.040.041.042.043.044.045.046.047.048.049.050.051.052.053.054.055.056.057.058.059.060.0

2.522.552.582.612.642.672.702.722.752.772.802.822.842.862.892.912.932.952.972.993.013.033.053.063.083.103.123.133.153.173.183.203.213.233.243.263.273.293.303.32


RESI

DEBN

CE

OFFI

CES

HOTE

LES

HOSP

ITAL

S

COM

ERCI

AL

CEN

TERS

SPOR

T CE

NTE

RS

0,10

0,20

0,30

0,40

0,50

0,60

0,70

0,80

0,90

1,00

3,50

volu

men

l/s

0,5 1,0 1,5 2,0 2,5 3,0 3,5 Velocity m/s

1,50

2,00

2,50

3,00

4,00

Max

imum

vel

ocity

for p

last

ic p

ipes

Max

imum

vel

ocity

for m

etal

lic p

ipes

CT Faser RD Ø 40

CT Faser RD Ø 50

Cu Ø10/12

Cu Ø13/15

Cu Ø16/18

Cu Ø20/22

Cu Ø26/28

Cu Ø33/35

Cu Ø40/42

4.4.1. DIAMETER EQUIVALENCES OF COOPER TUBES – ABN//INSTALL CT FASER RD

Diameter equivalence

////////////////////////////////////////////4.4.

Cu pipe Diameter

(mm)

121518

22

28

35

42

ABN//INSTAL CT Faser RDDiameter

(mm)

20

25

32

40

50

QUICK EQUIVALENCE TABLE

CT Faser RD Ø 32

CT Faser RD Ø 25

CT Faser RD Ø 20


4.4.2.DIAMETER EQUIVALENCES OF STEEL TUBES – ABN//ISNTALL CT FASER RD Diameters 20 to 63.

Volu

men

l/s

1,0

Velocity m/s

1,00

0,5 1,5 2,0 2,5 3,0 3,5

2,00

3,00

4,00

5,00

10,00

ECO SIS CT Ø25

CT Faser RDØ32

CT Faser RD Ø40

ECO SIS CT Ø20

CT Faser RD Ø50

CT Faser RD Ø63

DIN 2440 - 1 1/4 "

DIN 2440 - 2 "

DIN 2440 - 3/8 "

DIN 2440 - 1 "

DIN 2440 - 1 1/2 "

DIN 2440 - 3/4 "

DIN 2440 - 1/2 "

////////////////////////////////////////////

QUICK EQUIVALENCE TABLE

Steel Tube DIN 2440Diameter

(”)

3/8"

1/2"

3/4"

1"

1 1/4"

1 1/2"

2"

2 1/2"

3"

4"

5"

6"

ABN//INSTAL CT Faser RD

Diameter(mm)

20

25

32

40

50

63

75

90

110

140

160


Max

imum

vel

ocity

for p

last

ic p

ipes

Max

imum

vel

ocity

for m

etal

lic p

ipes

Volu

men

l l/s

1,0

Velocity m/s

1,00

0,5 1,5 2,0 2,5 3,0 3,5

2,00

3,00

4,00

5,00

10,00

15,00

20,00

25,00

30,00

35,00

40,00

45,00

50,00

55,00

60,00

65,00

70,00

CT Faser RD Ø75

CT Faser RD Ø90

CT Faser RD Ø110

CT Faser RD Ø125

CT Faser RD Ø140

CT Faser RD Ø160

CT Faser RD Ø180

CT Faser RD Ø200

DIN 2440 - 6"

DIN 2440 - 5"

DIN 2440 - 4"

DIN 2440 - 3"

DIN 2440 - 2 1/2"

////////////////////////////////////////////


4.4.3.DIAMETER EQUIVALENCES OF STEEL TUBES – ABN//ISNTALL CT FASER RD Diameters 75 to 200.

Max

imum

vel

ocity

for p

last

ic p

ipes

Max

imum

vel

ocity

for m

etal

lic p

ipes

Thermal insulation4.5.

////////////////////////////////////////////The thickness of the isolation layers of the conductions, both in the feed and return flow, will be dimensioned under the Regulation of Thermal Installations in Buildings (RITE = RTIB), approved in the Royal decree 1027/2007, of July 2nd and updated in April 2013 in its technical instruction TI 1. 2. 4. 2. 1, the conditions under which the network pipes should be isolated in cold and warm water installations.

TI 1.2.4.2.1.1

All the pipes and fittings, as well as equipments, devices and deposits of thermal installations will have a thermal isolation when they contain:

• fluids refreshed at a temperature lower than the room temperature of the place they run through.

• fluids with temperature higher than 40 ºC when they are installed in unheated places.

Simplified procedure TI 1. 2. 4. 2. 1. 2

The simplified procedure establishes the minimum thicknesses of thermal isolation, in mm, for an isolation material of reference to 10ºC of 0.040 W / (m.K) they must be indicated in the following tables:

> 60 ... 1002530304040

40 ... 602530303035

Maximum fluid temperature ºC

WARM fluids INSIDE the buildings

> 60 ... 1003540405050

> 100 ... 1804050506060

40 ... 603540404045


WARM fluids OUTSIDE the buildings

External diameter(mm) D≤ 35

35<D ≤6060<D ≤9090<D ≤140

140< D

> 0...102530304040

>-10...03040405050


COLD fluids INSIDE the buildings

> 0...104550506060

> 104040505050

>-10...05060607070


COLD fluids OUTSIDE the buildings


35<D ≤6060<D ≤9090<D ≤140

140< D

> 100 ... 1803040405050

> 102020303030


35<D ≤6060<D ≤9090<D ≤140

140< D


35<D ≤6060<D ≤9090<D ≤140

140< D

External diameter

(mm)D≤ 13

13<D<1626<D<3535<D<90

D>90

Internal buildings

(mm)1

15203040

Minimum isolation thicknesses (mm) of refrigerating circuits for air

conditioning*depending on the pipe route.

* Excluded the processes of industrial cold If the exterior pipe route is longer than 25 m, these thicknesses will have to be increased up to the immediately top commercial thickness, and in no case should this increase be lower than 5 mm.

The tables are of informative nature, extracted directly from the Regulation of Thermal Installations (RTE)

External buildings

(mm)1520254050


////////////////////////////////////////////

Pressure loss

5.1. General issues5.2. Pressure loss in the ABN//INSTAL CT FASER RD pipes series 3,2 /SDR 7,55.3. Pressure loss in the ABN//INSTAL CT FASER RD pipes series 5 /SDR 115.4. Pressure loss in the ABN//INSTAL CT FASER RD pipes series 8 / SDR 175.5. Fittings pressure loss

// 05

////////////////////////////////////////////


General issues

////////////////////////////////////////////5.1.

Diameter

2025324050637590110125160200250315400500

series 3,2 SDR 7,4

0.1630.2540.423

-------------

series 5 SDR 11

- - -

0.8351.3072.0752.9614.2546.3628.20313.43621.02132.87852.19884.187

-

series 8 SDR 17

- - - - - -

3.4214.9277.3599.53815.61524.38438.15260.52497.646

152.468

Capacity (litres of water per meter)


Example for selecting the diameter of a pipeline

METRIC

ATMOSPHERE

AVOIRDUPOIS (U.S.A.)

WATER

Megapascal (Mpa) 0,1

Bar 1

kgf/cm2 1,02

Kilopascal (kPa) 100

Hectopascal (hPa) 1000

Milibar (mbar) 1000

kgf/m2 10197,16

Pascal (Pa) 100000

Physical atmosphere 0,99

Technical atmosphere 1,02

Kilopound per square inch (ksi) 0,01

Pound force per square inch (psi) 14,5

Pound per square foot (psf) 2088,54

Water meter 10,2

Water inch 401,47

Water centimeter 1019,4

Equivalence units to 1 bar

324.423.23.330.763.700.804.090.854.500.904.920.956.051.067.281.188.621.30

10.061.4211.601.5413.241.66

14.981.7716.811.8918.752.01

20.782.1322.192.2525.132.37

29.862.60

34.982.8440.473.08

46.343.31

52.583.55

202.8

14.432.861.96

36.622.09

40.562.21

44.692.33

49.002.46

60.592.7673.323.0787.193.38

102.183.68

External Diameter (mm)Thickness (mm)Internal diameter (mm)Loss of load “R” (mbar/m)Velocity “V” (m/s)

RVRVRVRVRVRVRVRVRVRVRVRVRVRVRVRVRVRVRVRVRV

253.5

18.011.211.2612.481.34

13.801.4115.191.49

16.641.57

20.511.77

24.761.96

29.382.16

34.352.36

39.692.55

45.382.7551.432.9557.843.14

64.603.3471.713.54

Flow(l/s)

0.32

0.34

0.36

0.38

0.40

0.45

0.50

0.55

0.60

0.65

0.70

0.75

0.80

0.85

0.90

0.95

1.00

1.10

1.20

1.30

1.40

1.50

step

3

Step

1

step2

5.2. ABN//INSTAL CT FASER RD pipes series 3,2 /SDR 7,4 pressure loss

////////////////////////////////////////////5.2.

324.423.2

0.100.090.150.120.200.140.250.170.320.190.380.210.460.240.540.260.620.280.710.310.810.330.910.351.010.381.12

0.401.240.431.360.451.480.471.740.522.020.572.320.622.640.662.980.71

202.8

14.40.100.6

0.300.120.580.180.930.251.340.311.820.372.360.432.950.493.610.554.320.615.080.685.900.746.770.807.700.868.670.929.700.9810.781.0411.911.11

13.091.17

14.321.2316.931.3519.731.47

22.731.60

25.921.72

29.291.84

Flow(l/s)

0.01

0.02

0.03

0.04

0.05

0.06

0.07

0.08

0.09

0.10

0.11

0.12

0.13

0.14

0.15

0.16

0.17

0.18

0.19

0.20

0.22

0.24

0.26

0.28

0.30

External Diameter (mm)Thickness (mm)Internal diameter (mm)Pressure loss “R” (mbar/m)Velocity “V” (m/s)

RVRVRVRVRVRVRVRVRVRVRVRVRVRVRVRVRVRVRVRVRVRVRVRV

253.5

18.00.090.120.11

0.080.210.120.330.160.470.200.640.240.830.281.040.311.260.351.51

0.391.770.432.050.472.350.512.670.553.000.593.360.633.730.674.110.714.510.754.930.795.820.866.770.947.791.028.871.10

10.011.18

324.423.23.330.763.700.804.090.854.500.904.920.956.051.067.281.188.621.30

10.061.4211.601.5413.241.66

14.981.7716.811.8918.752.01

20.782.1322.192.2525.132.37

29.862.60

34.982.8440.473.08

46.343.31

52.583.55

202.8

14.432.861.96

36.622.09

40.562.21

44.692.33

49.002.46

60.592.7673.323.0787.193.38

102.183.68


RVRVRVRVRVRVRVRVRVRVRVRVRVRVRVRVRVRVRVRVRV

253.5

18.011.211.2612.481.34

13.801.4115.191.49

16.641.57

20.511.77

24.761.96

29.382.16

34.352.36

39.692.55

45.382.7551.432.9557.843.14

64.603.3471.713.54

Flow(l/s)

0.32

0.34

0.36

0.38

0.40

0.45

0.50

0.55

0.60

0.65

0.70

0.75

0.80

0.85

0.90

0.95

1.00

1.10

1.20

1.30

1.40

1.50


Unit loss of load in the ABN//INSTAL CT FASER RD pipes series 5 /SDR 11

////////////////////////////////////////////5.3.

635.851.40.090.12

0.230.290.300.340.370.390.460.430.550.480.650.530.760.580.870.630.990.671.12

0.721.250.771.390.821.540.871.700.921.860.962.201.062.581.162.971.253.391.353.841.45

756.861.4

0.200.300.240.340.280.370.320.410.370.440.420.470.480.510.540.540.600.570.660.610.720.640.790.680.940.741.100.811.260.881.440.951.631.01

908.2

73.6

0.160.310.180.330.200.350.230.380.250.400.280.420.301.450.330.470.390.520.460.560.530.610.600.660.680.71

11010

90.0

0.120.300.130.310.150.350.180.380.200.410.230.440.260.47

12511.4

102.2

0.110.320.130.340.140.37

16014.6

130.8

20018.2

163.6

25022.7

204.6

31528.6257.8

40036.3327.4

403.7

32.60.090.120.300.240.590.360.970.481.430.601.970.722.580.843.270.964.021.084.851.205.741.326.711.447.751.568.841.6810.011.8011.241.9212.542.0413.912.16

15.342.2816.842.40

20.022.6423.472.8827.173.1131.133.35

35.343.59

Flow(l/s)

0.10

0.20

0.30

0.40

0.50

0.60

0.70

0.80

0.90

1.00

1.10

1.20

1.30

1.40

1.50

1.60

1.70

1.80

1.90

2.00

2.20

2.40

2.60

2.80

3.00



504.6

40.80.090.120.100.150.210.230.340.310.490.380.680.460.880.541.120.611.370.691.650.761.950.842.280.922.630.993.001.073.391.153.801.224.231.304.691.385.171.455.671.356.721.687.871.849.091.99

10.402.1411.792.29


////////////////////////////////////////////635.851.44.321.544.811.645.341.735.891.836.461.938.002.179.702.4111.552.6513.542.8915.693.1317.993.37

20.433.61

756.861.41.831.082.041.152.261.222.491.282.731.353.371.524.081.694.851.865.692.036.582.207.532.368.552.539.622.7010.752.8711.953.0413.203.2114.513.3815.883.55

908.2

73.60.770.750.850.800.940.851.040.891.14

0.941.411.061.701.182.021.292.361.412.731.533.121.653.531.763.971.884.442.004.932.125.442.235.972.356.532.477.11

2.597.722.708.352.829.002.949.683.0610.373.1711.103.29

11010

90.00290.500.330.530.360.570.400.600.430.630.530.710.640.790.760.860.890.941.031.021.181.101.331.181.501.261.671.341.851.412.041.492.241.572.451.652.671.732.891.813.131.893.371.963.622.043.882.124.142.20

12511.4

102.20.16

1.582.091.652.231.71

0.390.180.410.200.440.220.460.240.490.290.550.350.610.410.670.480.730.560.790.640.850.720.910.810.980.901.041.001.101.101.161.211.221.321.281.441.341.561.401.691.461.821.521.95

16014.6

130.8

0.090.330.110.370.130.410.150.450.170.480.200.520.220.560.250.600.280.630.310.670.340.710.370.740.400.780.440.820.470.860.510.890.550.930.590.970.631.000.671.04

20018.2

163.6

0.070.330.080.360.080.380.090.400.100.430.11

0.450.130.480.140.500.150.520.160.550.170.570.190.590.200.620.220.640.230.67

25022.7

204.6

0.050.320.050.330.060.350.060.360.060.380.070.400.070.410.080.43

31528.6257.8

40036.3327.4

403.7

32.6

Flow(l/s)

3.20

3.40

3.60

3.80

4.00

4.50

5.00

5.50

6.00

6.50

7.00

7.50

8.00

8.50

9.00

9.50

10.00

10.50

11.00

11.50

12.00

12.50

13.00

13.50

14.00



504.6

40.813.262.4514.812.6016.442.7518.152.91

19.943.0624.773.44

30.083.82


////////////////////////////////////////////635.851.4

756.861.4

908.2

73.611.843.4112.613.53

11010

90.04.422.284.702.364.992.445.292.525.602.595.922.676.242.756.582.836.922.917.272.997.633.077.993.148.373.228.753.309.143.389.543.469.943.54

12511.4

102.22.38

3.056.713.116.963.177.21

1.772.531.83

3.23

2.691.892.851.953.012.013.182.073.352.133.532.193.712.263.902.324.092.384.292.444.492.504.692.564.902.625.11

2.685.332.745.552.805.772.866.002.936.232.996.47

16014.6

130.80.721.080.761.120.811.150.861.190.911.230.961.271.011.301.061.341.121.381.171.411.231.451.291.491.351.531.411.561.471.601.531.641.601.671.661.711.731.751.801.791.871.821.941.862.011.902.081.932.151.97

20018.2

163.60.240.690.260.710.280.740.290.760.310.780.330.810.340.830.360.860.380.880.400.900.420.930.440.950.460.980.481.000.501.020.521.050.541.070.561.090.581.120.611.140.631.170.651.190.681.210.701.240.731.26

25022.7

204.60.080.440.090.460.090.470.100.490.11

0.500.110.520.120.530.120.550.130.560.140.580.140.590.150.610.160.620.160.640.170.650.180.670.180.680.190.700.200.710.210.730.210.750.220.760.230.780.240.790.250.81

31528.6257.8

0.030.300.030.310.030.320.040.330.040.340.040.340.040.350.040.360.050.370.050.380.050.390.050.400.060.410.060.420.060.430.060.440.070.450.070.460.070.470.070.480.080.490.080.500.080.51

40036.3327.4

0.020.300.020.300.020.310.030.31

403.7

32.6

Flow(l/s)

14.50

15.00

15.50

16.00

16.50

17.00

17.50

18.00

18.50

19.00

19.50

20.00

20.50

21.00

21.50

22.00

22.50

23.00

23.50

24.00

24.50

25.00

25.50

26.00

26.50



504.6

40.8


////////////////////////////////////////////635.851.4

756.861.4

908.2

73.6

11010

90.0

12511.4

102.27.463.297.723.357.983.418.253.478.523.54

16014.6

130.82.232.012.312.052.382.082.462.122.542.162.622.202.712.232.792.272.872.312.962.343.052.383.132.423.222.463.312.493.412.533.502.573.592.603.692.643.792.683.882.723.982.754.082.794.182.834.292.874.392.90

20018.2

163.60.751.280.781.310.801.330.831.360.861.380.881.400.911.430.941.450.971.470.991.501.021.521.051.551.081.571.11

1.591.141.621.17

1.641.211.661.241.691.271.711.301.741.331.761.371.781.401.811.441.831.471.86

25022.7

204.60.250.870.260.840.270.850.280.870.290.880.300.900.310.910.320.930.330.940.340.960.350.970.360.990.371.000.381.020.391.030.401.050.411.060.421.080.431.090.441.110.451.130.461.140.471.160.481.170.501.19

31528.6257.80.080.520.090.530.090.540.090.550.100.560.100.570.100.570.100.580.110.590.11

0.600.110.610.120.620.120.630.120.640.130.650.130.660.130.670.140.680.140.690.140.700.150.710.150.720.150.730.160.740.160.75

40036.3327.40.030.320.030.330.030.330.030.340.030.340.030.350.030.360.030.36

0.050.450.050.450.050.460.050.46

0.030.370.030.370.040.380.040.390.040.390.040.400.040.400.040.410.040.420.040.420.040.430.050.430.050.44

403.7

32.6

Flow(l/s)

27.00

27.50

28.00

28.50

29.00

29.50

30.00

30.50

31.00

31.50

32.00

32.50

33.00

33.50

34.00

34.50

35.00

35.50

36.00

36.50

37.00

37.50

38.00

38.50

39.00



504.6

40.8


////////////////////////////////////////////635.851.4

756.861.4

908.2

73.6

11010

90.0

12511.4

102.2

16014.6

130.84.502.944.602.984.713.014.823.054.933.095.043.135.153.165.263.205.383.245.493.275.613.315.733.355.853.395.973.426.093.466.213.50

20018.2

163.61.501.881.541.901.581.931.611.951.651.971.682.001.722.021.762.051.802.071.832.091.872.121.912.141.952.161.992.192.032.212.072.242.11

2.262.152.282.192.312.242.332.282.352.322.382.362.402.412.432.452.45

25022.7

204.60.511.200.521.220.531.230.541.250.561.260.571.280.581.290.591.310.601.320.621.340.631.350.641.370.661.380.671.400.681.410.701.430.711.440.721.460.741.480.751.490.771.510.781.520.791.540.811.550.821.57

31528.6257.80.170.760.170.770.170.780.180.790.180.800.190.800.190.810.190.820.200.830.200.840.210.850.210.860.210.870.220.880.220.890.230.900.230.910.240.920.240.930.250.940.250.950.250.960.260.970.260.980.270.99

40036.3327.40.050.470.050.480.050.480.060.490.060.490.060.500.060.500.060.51

0.080.590.080.600.080.610.080.61

0.060.520.060.520.070.530.070.530.070.540.070.550.070.550.070.560.070.560.070.570.080.580.080.580.080.59

403.7

32.6

Flow(l/s)

39.50

40.00

40.50

41.00

41.50

42.00

42.50

43.00

43.50

44.00

44.50

45.00

45.50

46.00

46.50

47.00

47.50

48.00

48.50

49.00

49.50

50.00

50.50

51.00

51.50



504.6

40.8


////////////////////////////////////////////635.851.4

756.861.4

908.2

73.6

11010

90.0

12511.4

102.2

16014.6

130.8

20018.2

163.62.502.472.542.502.592.522.632.552.682.572.722.592.772.622.822.642.862.662.912.692.962.713.012.743.062.763.102.783.152.813.202.833.252.853.302.883.352.903.412.933.462.953.512.973.563.003.613.023.673.04

25022.7

204.60.841.580.851.600.871.610.881.630.901.640.911.660.931.670.941.690.961.700.981.720.991.731.011.751.021.761.041.781.061.791.071.811.091.821.11

1.841.121.861.141.871.161.891.17

1.901.191.921.211.931.231.95

31528.6257.80.271.000.281.010.281.020.291.020.291.030.301.040.301.050.311.060.311.070.321.080.321.090.331.100.331.11

0.341.120.341.130.351.140.351.150.361.160.371.170.371.180.381.190.381.200.391.210.391.220.401.23

40036.3327.40.090.620.090.620.090.630.090.640.090.640.090.650.100.650.100.66

0.120.740.120.750.120.750.130.76

0.100.670.100.670.100.680.100.680.100.690.11

0.690.110.700.110.710.110.710.110.720.110.720.120.730.120.74

403.7

32.6

Flow(l/s)

52.00

52.50

53.00

53.50

54.00

54.50

55.00

55.50

56.00

56.50

57.00

57.50

58.00

58.50

59.00

59.50

60.00

60.50

61.00

61.50

62.00

62.50

63.00

63.50

64.00



504.6

40.8


////////////////////////////////////////////635.851.4

756.861.4

908.2

73.6

11010

90.0

12511.4

102.2

16014.6

130.8

20018.2

163.63.723.073.773.093.833.123.883.143.943.163.993.194.053.214.113.234.163.264.223.284.283.314.333.334.393.354.453.384.513.404.573.434.633.454.693.474.753.50

25022.7

204.61.241.961.261.981.281.991.302.011.322.021.332.041.352.051.372.071.392.081.412.101.432.111.452.131.472.141.492.161.502.171.522.191.542.211.562.221.582.241.602.251.622.271.642.281.662.301.682.311.702.33

31528.6257.80.401.240.411.250.421.250.421.260.431.270.431.280.441.290.451.300.451.310.461.320.461.330.471.340.481.350.481.360.491.370.491.380.501.390.511.400.511.410.521.420.531.430.531.440.541.450.551.460.551.47

40036.3327.40.130.770.130.770.130.780.130.780.130.790.140.800.140.800.140.810.140.81

0.170.900.170.91

0.140.820.150.830.150.830.150.840.150.840.150.850.160.860.160.860.160.870.160.870.160.880.170.880.170.890.170.90

403.7

32.6



504.6

40.8

Flow(l/s)

64.50

65.00

65.50

66.00

66.50

67.00

67.50

68.00

68.50

69.00

69.50

70.00

70.50

71.00

71.50

72.00

72.50

73.00

73.50

74.00

74.50

75.00

75.50

76.00

76.50


////////////////////////////////////////////635.851.4

756.861.4

908.2

73.6

11010

90.0

12511.4

102.2

16014.6

130.8

20018.2

163.6

25022.7

204.61.732.341.752.361.772.371.792.391.812.401.832.421.852.431.872.451.892.461.922.481.942.491.962.511.982.522.032.552.052.572.072.592.302.742.552.892.803.043.353.353.943.65

31528.6257.80.561.480.571.480.571.490.581.500.591.510.591.520.601.530.611.540.611.550.621.560.631.570.631.580.641.590.651.600.661.610.661.620.671.630.741.720.821.820.901.971.082.111.262.301.472.491.682.681.912.87

40036.3327.40.180.910.180.920.180.930.180.930.180.940.190.940.190.950.190.960.190.96

0.521.660.591.78

0.190.970.200.970.200.980.200.990.200.990.211.000.211.000.211.010.231.070.261.130.281.190.341.310.391.430.461.54

403.7

32.6



504.6

40.8

Flow(l/s)

77.00

77.50

78.00

78.50

79.00

79.50

80.00

80.50

81.00

81.50

82.00

82.50

83.00

83.50

84.00

84.50

85.00

90.00

95.00

100.00

110.00

120.00

130.00

140.00

150.00


////////////////////////////////////////////635.851.4

756.861.4

908.2

73.6

11010

90.0

12511.4

102.2

16014.6

130.8

20018.2

163.6

25022.7

204.6

31528.6257.82.163.072.423.262.693.452.983.64

40036.3327.40.671.900.752.020.832.140.922.261.012.381.11

2.491.212.611.312.731.422.851.532.971.653.091.773.211.893.332.023.442.153.56

403.7

32.6


RVRVRVRVRVRVRVRVRVRVRVRVRVRV

504.6

40.8

Flow(l/s)

160.00

170.00

180.00

190.00

200.00

210.00

220.00

230.00

240.00

250.00

260.00

270.00

280.00.

290.00

300.00


Unit loss of load in the ABN//INSTAL CT FASER RD pipes series 8 / SDR 17

////////////////////////////////////////////5.4.

1106.6

96.80.090.12

0.110.300.120.330.140.350.160.380.180.410.210.430.230.460.250.490.280.520.310.540.380.610.450.680.540.750.630.820.730.88

1257.4

110.2

0.100.310.11

0.340.120.360.140.380.150.400.160.420.200.470.240.520.290.580.340.630.390.68

1609.5

141.0

0.100.380.120.42

20011.9

176.2

25014.8

220.4

31518.7

277.6

40023.7

352.6

50029.7

440.6

754.5

66.00.200.320.230.350.260.380.300.410.340.440.380.470.420.500.470.530.510.560.560.580.660.640.770.700.890.761.020.821.15

0.881.290.941.440.991.591.051.761.111.931.172.381.322.881.463.241.614.001.754.631.90

Flow(l/s)

1.10

1.20

1.30

1.40

1.50

1.60

1.70

1.80

1.90

2.00

2.20

2.40

2.60

2.80

3.00

3.20

3.40

3.60

3.80

4.00

4.50

5.00

5.50

6.00

6.50



905.4

79.20.090.12

0.140.300.160.320.180.350.200.370.220.390.240.410.280.450.320.490.370.530.430.570.480.610.540.650.600.690.660.730.730.770.800.810.990.911.191.011.411.121.651.221.911.32


////////////////////////////////////////////

1257.4

110.20.440.730.500.790.560.840.630.890.700.940.771.000.841.050.921.101.001.151.081.211.171.261.261.311.351.361.451.421.551.471.651.521.751.571.861.631.971.682.091.732.201.782.321.832.451.892.571.942.701.99

1609.5

141.00.140.450.150.480.170.510.190.540.210.580.230.610.260.640.280.670.300.700.330.740.360.770.380.800.410.830.440.860.470.900.500.930.530.960.560.990.601.020.631.060.671.090.701.120.741.150.781.180.821.22

25014.8

220.4

0.040.310.040.330.050.340.050.350.050.370.060.380.060.390.070.410.070.420.070.430.080.450.080.460.090.470.090.480.090.50

31518.7

277.6

40023.7

352.6

50029.7

440.6

754.5

66.03.502.056.012.196.762.347.552.488.392.639.262.7810.182.9211.143.0712.143.2213.183.3614.263.51

Flow(l/s)

7.00

7.50

8.00

8.50

9.00

9.50

10.00

10.50

11.00

11.50

12.00

12.50

13.00

13.50

14.00

14.50

15.00

15.50

16.00

16.50

17.00

17.50

18.00

18.50

19.00

External diameter (mm)Thickness (mm)Internal diameter (mm)Pressure loss ”R”(mbar/m)

Velocity “V” (m/sg)RVRVRVRVRVRVRVRVRVRVRVRVRVRVRVRVRVRVRVRVRVRVRVRV

905.4

79.22.181.422.481.522.781.623.111.733.451.833.801.934.182.034.572.134.972.235.392.335.832.446.292.546.762.647.242.747.742.848.262.948.793.049.343.159.913.2510.493.3511.093.4511.703.55

1106.6

96.80.830.950.941.021.051.091.181.151.301.221.441.291.581.361.721.431.871.492.031.562.191.632.361.702.541.772.721.832.911.903.101.973.302.043.502.113.712.173.922.244.152.314.372.384.602.454.842.515.092.58

20011.9

176.2

0.100.430.100.450.110.470.120.490.130.510.140.530.150.550.160.570.170.590.180.620.190.64

0.230.700.240.720.250.740.260.760.280.78

0.200.660.220.68


////////////////////////////////////////////

1257.4

110.22.832.042.972.103.102.153.242.203.392.253.532.313.682.363.832.413.992.464.152.524.312.574.472.624.642.674.812.734.982.785.152.835.332.885.512.945.702.995.883.046.073.096.263.156.463.206.663.256.863.30

1609.5

141.00.851.250.901.280.941.310.981.341.021.381.061.411.11

1.441.151.471.201.511.251.541.291.571.341.601.391.631.441.671.491.701.551.731.601.761.651.791.711.831.761.861.821.891.881.921.931.951.991.992.052.02

25014.8

220.40.100.510.100.520.11

0.540.110.550.120.560.120.580.130.590.130.600.140.620.140.630.150.640.150.660.160.670.170.680.170.690.180.710.180.720.190.730.200.750.200.760.210.770.220.790.220.800.230.810.230.83

31518.7

277.60.030.320.030.330.040.340.040.350.040.360.040.360.040.370.040.380.050.390.050.400.050.400.050.410.050.420.050.430.060.440.060.450.060.450.060.460.060.470.070.480.070.490.070.500.070.500.080.510.080.52

40023.7

352.6

0.020.300.020.300.020.310.020.310.020.320.020.32

50029.7

440.6

754.5

66.0

Flow(l/s)

19.50

20.00

20.50

21.00

21.50

22.00

22.50

23.00

23.50

24.00

24.50

25.00

25.50

26.00

26.50

27.00

27.50

2800

28.50

29.00

29.50

30.00

30.50

31.00

31.50



905.4

79.2

1106.6

96.85.342.655.592.725.852.796.122.856.392.926.672.996.953.067.243.137.533.197.833.268.143.338.453.408.763.469.093.53

20011.9

176.20.290.800.300.820.320.840.330.860.350.880.360.900.380.920.390.940.410.960.420.980.441.000.461.030.471.050.491.070.511.090.521.11

0.541.130.561.15

0.621.210.631.230.651.250.671.270.691.29

0.581.170.601.19


////////////////////////////////////////////

1257.4

110.27.063.367.273.417.483.467.693.51

1609.5

141.02.11

2.052.172.082.232.112.302.152.362.182.422.212.492.242.552.272.622.312.692.342.762.372.832.402.902.432.972.473.042.503.112.533.182.563.262.593.332.633.412.663.482.693.562.723.642.753.722.793.802.82

25014.8

220.40.240.840.250.850.260.860.260.880.270.890.280.900.280.920.290.930.300.940.310.960.310.970.320.980.331.000.341.010.351.020.351.040.361.050.371.060.381.070.391.090.401.100.401.110.411.130.421.140.431.15

31518.7

277.60.080.530.080.540.080.550.090.550.090.560.090.570.090.580.100.590.100.590.100.600.100.610.11

0.620.11

0.630.11

0.640.11

0.640.120.650.120.660.120.670.120.680.130.690.130.690.130.700.140.710.140.720.140.73

40023.7

352.60.030.330.030.330.030.340.030.340.030.350.030.350.030.360.030.360.030.370.030.370.030.380.030.380.030.390.040.390.040.400.040.400.040.410.040.410.040.420.040.430.040.430.040.440.040.440.040.450.040.45

50029.7

440.6

754.5

66.0

Flow(l/s)

32.00

32.50

33.00

33.50

34.00

34.50

35.00

35.50

36.00

36.50

37.00

37.50

38.00

38.50

39.00

39.50

40.00

40.50

41.00

41.50

42.00

42.50

43.00

43.50

44.00

External diameter (mm)Thickness (mm)Internal diameter (mm)Pressure loss ”R”(mbar/m)

Velocity “V” (m/sg)RVRVRVRVRVRVRVRVRVRVRVRVRVRVRVRVRVRVRVRVRVRVRVRV

905.4

79.2

1106.6

96.8

20011.9

176.20.711.310.731.330.761.350.781.370.801.390.821.410.841.440.861.460.881.480.911.500.931.520.951.540.981.561.001.581.021.601.051.621.071.641.101.66

1.171.721.201.741.221.761.251.781.281.80

1.121.681.151.70


////////////////////////////////////////////

1257.4

110.2

1609.5

141.03.882.853.962.884.042.914.122.954.212.984.293.014.383.044.463.074.553.114.643.144.733.174.813.204.993.275.183.335.373.395.563.465.753.525.943.59

25014.8

220.40.441.170.451.180.461.190.471.210.481.220.491.230.491.250.501.260.511.270.521.280.531.300.541.310.561.340.581.360.601.390.631.420.651.440.671.470.691.490.711.520.741.550.761.570.781.600.811.630.831.64

31518.7

277.60.140.740.150.740.150.750.150.760.160.770.160.780.160.780.170.790.170.800.170.810.170.820.180.830.180.840.190.860.200.880.200.890.210.910.220.930.230.940.230.960.240.970.250.990.261.010.261.020.271.04

40023.7

352.60.050.460.050.460.050.470.050.470.050.480.050.480.050.490.050.490.050.500.050.500.060.510.060.510.060.520.060.530.060.540.060.550.070.560.070.570.070.580.070.590.080.600.080.610.080.620.080.630.090.65

50029.7

440.6

0.020.300.020.300.020.300.020.300.020.310.020.310.020.310.020.320.020.320.020.320.020.330.020.330.020.340.020.350.020.350.020.360.020.370.020.370.030.380.030.390.030.390.030.400.030.410.030.41

754.5

66.0

Flow(l/s)

44.50

45.00

45.50

46.00

46.50

47.00

47.50

48.00

48.50

49.00

49.50

50.00

51.00

52.00

53.00

54.00

55.00

56.00

57.00

58.00

59.00

60.00

61.00

62.00

63.00



905.4

79.2

1106.6

96.8

20011.9

176.21.301.821.331.851.361.871.391.891.411.911.441.931.471.951.501.971.531.991.562.011.592.031.622.051.682.091.742.131.802.171.862.211.932.261.992.30

2.192.422.262.462.332.502.402.542.472.58

2.062.342.122.38


////////////////////////////////////////////

1257.4

110.2

1609.5

141.0

25014.8

220.40.851.680.881.700.901.730.931.760.951.780.981.811.011.831.031.861.061.891.091.911.11

1.941.141.971.171.991.202.021.232.041.262.071.292.101.322.121.352.151.382.181.41

2.201.442.231.472.251.502.281.532.31

31518.7

277.60.281.060.291.070.291.090.301.110.311.120.321.140.331.160.341.170.341.190.351.210.361.220.371.240.381.260.391.270.401.290.411.310.421.320.431.340.441.350.451.370.461.390.471.400.481.420.491.440.501.45

40023.7

352.60.090.660.090.670.090.680.100.690.100.700.100.710.100.720.110.730.110.740.110.750.110.760.120.770.120.780.120.790.130.800.130.810.130.820.130.830.140.840.140.850.140.860.150.870.150.880.150.890.160.90

50029.7

440.60.030.420.030.430.030.430.030.440.030.450.030.450.040.460.040.470.040.470.040.480.040.490.040.490.040.500.040.510.040.510.040.520.040.520.050.530.050.540.050.540.050.550.050.560.050.560.050.570.050.58

754.5

66.0

Flow(l/s)

64.00

65.00

66.00

67.00

68.00

69.00

70.00

71.00

72.00

73.00

74.00

75.00

76.00

77.00

78.00

79.00

80.00

81.00

82.00

83.00

84.00

85.00

86.00

87.00

88.00

905.4

79.2

1106.6

96.8

20011.9

176.22.552.622.622.672.702.712.772.752.852.792.932.833.012.873.092.913.182.953.252.993.343.033.423.083.513.123.593.163.683.203.773.243.863.283.953.32

4.223.444.323.494.413.534.513.57

4.043.364.133.40




////////////////////////////////////////////

1257.4

110.2

1609.5

141.0

25014.8

220.41.572.331.602.361.632.391.672.411.702.441.732.461.772.491.802.521.842.541.872.571.912.591.942.622.322.882.733.153.173.413.643.67

31518.7

277.60.511.470.521.490.531.500.541.520.551.540.561.550.571.570.581.590.601.600.611.620.621.640.631.650.751.820.881.981.022.151.172.311.332.481.502.641.682.811.872.972.073.142.273.302.493.47

40023.7

352.60.160.910.160.920.170.930.170.940.170.950.180.960.180.970.180.980.190.990.191.000.191.010.201.020.231.130.271.230.321.330.361.430.411.540.471.640.521.740.581.840.641.950.702.050.772.150.842.250.912.36

50029.7

440.60.050.580.060.590.060.600.060.600.060.610.060.620.060.620.060.630.060.640.060.640.070.650.070.660.080.720.090.790.11

0.850.120.920.140.980.161.050.181.11

0.201.180.221.250.241.310.261.380.281.440.311.51

754.5

66.0

Flow(l/s)

89.00

90.00

91.00

92.00

93.00

94.00

95.00

96.00

97.00

98.00

99.00

100.00

110.00

120.00

130.00

140.00

150.00

160.00

170.00

180.00

190.00

200.00

210.00

220.00

230.00



905.4

79.2

1106.6

96.8

20011.9

176.2


////////////////////////////////////////////

1257.4

110.2

1609.5

141.0

25014.8

220.4

31518.7

277.6

40023.7

352.60.992.461.062.561.14

2.661.232.771.312.871.402.971.503.071.593.171.693.281.793.381.893.482.003.58

50029.7

440.60.331.570.361.640.381.710.411.770.441.840.471.900.501.970.532.030.562.100.602.160.632.230.672.300.702.360.742.430.782.490.862.620.902.690.942.750.982.821.022.891.072.951.11

3.021.16

3.081.203.151.253.21

754.5

66.0

Flow(l/s)

240.00

250.00

260.00

270.00

280.00

290.00

300.00

310.00

320.00

330.00

340.00

350.00

360.00

370.00

380.00

390.00

400.00

410.00

420.00

430.00

440.00

450.00

460.00

470.00

480.00

905.4

79.2

1106.6

96.8

20011.9

176.2




////////////////////////////////////////////

1257.4

110.2

1609.5

141.0

25014.8

220.4

31518.7

277.6

40023.7

352.6

50029.7

440.61.253.211.303.281.353.341.403.411.453.481.503.54

754.5

66.0

Flow(l/s)

490.00

500.00

510.00

520.00

530.00

540.00


RVRVRVRVRV

905.4

79.2

1106.6

96.8

20011.9

176.2


T in derivation 1.30

T of reduced infux 0.90

T in reduced derivation 0.30

T of infux 0.60

T of central infux with reduced input 3.00

Elbow 1.13

Conic expansion ß=10º 0.20ß=20º 0.45ß=30º 0.60ß=40º 0.75

Expansion with free unload 1.00

Reducer 1 diameter 0.402 diameters 0.503 diameters 0.604 diameters 0.705 diameters 0.806 diameters 0.90

Designation Graphic symbol φ

Single resistors

////////////////////////////////////////////5.5.


Screw down valve DN 20 8.5DN 25 7.0DN 32 6.0DN 40 aDN 100 5.0

Angle seat valve DN 20 2.5DN 25 a DN 50 2.0DN 65 0.7

Ball valve DN 20 a DN 25 1.5DN 32 a DN 50 1DN 65 a DN 80 0.7hasta DN 100 0.6

Angle valve DN 20 a DN 40 3.5DN 50 a DN 100 2.0

Gate valve DN 20 a DN 25 0.5DN 32 0.3

Chek valve DN 25 a DN 40 2.5DN 50 1.9

Ball valves with built-in check valves DN 20 4.6

DN 25 a DN 50 3.6

Flap valve DN 50 1.5DN 100 1.2DN 200 1.0

Check valve withanti-water hammer DN 20 15

DN 25 a DN 50 13

+

+

Fitting Symbol φ

////////////////////////////////////////////


////////////////////////////////////////////

Installation

6.1. General conditions6.2. Protections6.3. Support6.4. Thermal expansion6.5. Transition with pipes and metallic fittings

// 06

////////////////////////////////////////////


6.1. General issues

The execution of pipe networks will be carried out in such a way that the objectives foreseen in the project are achieved without damaging or spoiling the rest of the building, avoiding annoying noises, preserving the drinking characteristics of the water of supply, as well as the best conditions for its maintenance and conservation.

The hidden or embedded tubes will run preferably through vertical conduits or factory chambers done or prefabricated for this purpose, over roofs or along technical soils, walls curtain or technical dividing walls. If this was not possible, due to outer walls of suitable thickness, its embedding is not allowed in dividing walls made of simple hollow brick. When the pipes run through these conduits they will be ventilated properly and they will be provided with a suitable emptying system.

The piping layout will be carried out in a clean and tidy way. If they were exposed to any deterioration for blows or fortuitous shocks they should be protected appropriately.

////////////////////////////////////////////


Protections

Protection against corrosion

Any exterior and outdoor water pipe system will be protected in the same way. When pipes run through soil channels it has to be guaranteed that these are impermeable or that they are provided with a suitable ventilation and drainage.

Protection against mechanical efforts

When tubes have to cross any outer wall (ornament) of the building or any other type of constructive element that could transmit harmful efforts of mechanical type, they will do it inside a case, also of circular section, with a larger diameter and sufficiently resistant. When, the installations had to run in a vertical sense, the tube case will protrude at least 3 centimetres on the side where occasional blows could take place, in order to protect the pipe. Likewise, if there is a change of sense, the tube case will protrude at least a length equal to the diameter of the pipe plus 1 centimetre.

When the tube network crosses, an expansion joint of the building, in surface or in embedded form, an element or dilated device will be placed, so that the possible structural movements do not transmit efforts of mechanical type to it.

The sum of water hammers and of the stand still pressure must not exceed the over pressure of admissible service. The magnitude of the positive water hammer in valves and devices operating, measured immediately before these, must not exceed 2 bar; the negative water hammer must not descend below 50 % of the pressure of service

Protection against noise

The following are general norms to be adopted:

•both horizontal and vertical hollows or conduits, through where piping run, will be placed in common areas; •flexible connectors should be installed at the water pump outlet to attenuate noise and vibration transmission along the distribution network.

The above mentioned connectors will be appropriate to the type of pipe and to the place of its installation.

Tube bushings

Tube bushings

6.2.////////////////////////////////////////////


(70 ºC)708095-------------

Support

SupportsSupports shall be provided so that the weight of the tubes rests on these and never on the proper pipes or their unions.

They will not be able to be attached in any element of structural type, unless in certain occasions another solution is not possible, for which the necessary preventive measurements will be adopted.

The embedding length will be such that guarantees a perfect fixation of the network without possible detachments.

The same as for the staples and clamps a flexible element will be put in the same cases, even when it is a question of supports that group several pipes.

Brackets

The use of isophonic brackets (clamps) is recommended.

The brackets laying for attaching the pipes to the facings (outer walls) shall be done in such a way that the pipes remain perfectly aligned with the mentioned facings, keep the demanded distances and do not transmit noises and/or vibrations to the building.

The type of clamp will always be of easy assembly and dismantling, as well as an electrical insulator.

(20 ºC)90105120

-------------

Diámetro exterior

(mm)2025324050637590110125160200250315400500

Distancia entre abrazaderas horizontales L (cm)

6.3.////////////////////////////////////////////

(50 ºC)8595110-------------

Relación de distancia entre abrazaderas

Temperatura en ºC

(70 ºC)---

100120135140145150155160170175185195

-

(20 ºC)---

125145165175185200205210220225230250

-

(50 ºC)---

115135155160170170175180190200205220

-

(70 ºC)------

125130135140145155160170180205

(20 ºC)------

170175180185190200205210230255

(50 ºC)------

155160165170175180190200210235

ECO SIS CT Faser RDSerie 3,2 SDR 7,4

ECO SIS CT Faser RDSerie 5 SDR 11

ECO SIS CT Faser RDSerie 8 SDR 17

L L

ABRAZADERA ISOFÓNICA

(70 ºC)708095-------------

(20 ºC)90105120

-------------

External diameter

(mm)2025324050637590110125160200250315400500

Distance between horizontal brackets L (cm)

(50 ºC)8595110-------------

Relación de distancia entre abrazaderas

Temperature in ºC

(70 ºC)---

100120135140145150155160170175185195

-

(20 ºC)---

125145165175185200205210220225230250

-

(50 ºC)---

115135155160170170175180190200205220

-

(70 ºC)------

125130135140145155160170180205

(20 ºC)------

170175180185190200205210230255

(50 ºC)------

155160165170175180190200210235

ABN//INSTAL CT Faser RDSerie 3,2 SDR 7,4

ABN//INSTAL CT Faser RDSerie 5 SDR 11

ABN//INSTAL CT Faser RDSerie 8 SDR 17

* For vertical installations the mentioned distances can increase in 30%


Thermal expansion

The main precaution that should be borne in mind is the design of ABN//INSTAL CT FASER RD air piping which is related to the possible longitudinal expansion because of the thermal changes.

The change in the piping length submitted to a difference of temperature is given by the expression:

ABN//ISTALL CT FASER RD Coefficient of thermal expansion: 0.04 mm/m. ºC

ΔL = L x λ x Δt

donde:

ΔL= Total thermal expansion of the studied stretch (mm)L= Length of the stretch between two fixed pointsλ = Coefficient of the thermal expansion of the material (mm/m. ºC)Δt= Temperature difference (ºC) between highest fluid temperature

and environmental temperature

6.4.////////////////////////////////////////////

It is a high value which indicates that, the installations that go through important changes in the room temperature will be affected by important elongations, although the flexibility of the material makes it capable of absorbing them without valuable tensions appearing along the conduction. On the other hand, ABN//INSTAL CT FASER RD pipes (like almost all the plastic ones) has a good capacity of thermal isolation. In particular, the coefficient of thermal conductivity is 0.24 W / m · ºC. This good thermal isolation reduces the risk of fragile break in case of frosts.

Effectively, the water from the inside of a of PPR CT RP, pipe freezes the increase in volume would result in an increase in diameter, without getting to break the piping, recovering the original diameter after the thaw.

When the temperature variation is positive, the pipe elongates, whereas if the temperature variation is negative, piping will be shortened


Ø110Ø125

Ø160

Ø200

Ø250

150

10 30 50 70 90 110 150 200

200

130 160 170 180 19014012010020 40 60 80

300

400

500

600

700

800

900

1000

1200

1300

1400

1500

1600

1700

1800

1900

2000

2100

2200

2300

2400

2500

2600

2700

2800

2900

3000

LEN

GHT

OF

BEN

DIN

G SI

DE (m

m)

LINEAR EXPANSION DL in mm

Ø25

Ø32

Ø40

Ø50

Ø63

Ø75

Ø90

UNE ENV 12108

////////////////////////////////////////////

1100

LENGHT OF BENDING SIDE


////////////////////////////////////////////

1.100

1.200

1.300

1.400

1.500

Ø315

Ø400

Ø500

10 20 30 40 50 60 70 80 90 100 110 120 130 140 150 160 170 180 190 200

2.000

2.500

3.000

3.500

4.000

4.500

5.000

5.500

LINEAR EXPANSION DL EN mm

LEN

GHT

OF

BEN

DIN

G SI

DE (m

m)

LENGHT OF BENDING SIDE


Anchorage point

Anchorage point is that which prevents the movement of the pipe for effect of

BracketMuff

The anchoring points are placed to keep a direction and to limit the spread of the thermal expansion.

Anchor points can be placed in such a way that the length variations due to temperature can be distributed in different directions.

////////////////////////////////////////////

BracketMuff


Systems of compensation of expansion

To compensate the dilations produced in ABN//INSTAL CT FASER RD pipes for effect of the temperature variation, different methods can be used. If the layout of the piping is completely straight, it will be necessary to insert elements capable of absorbing such expansions, as, for example, lire or expansion compensator.

Nevertheless, the thermal dilation can be absorbed during the changes of direction, being unnecessary to appeal to the previous components. In particular, there are two most frequent possible dispositions to compensate the expansion thanks to the breaks in the piping: in "L", or in "U". All of them are based in arranging a series of fixed and mobile anchoring in such a way that they allow the pipe conduction to expand enough for effect of the temperature to prevent from seeming excessive tensions.

The dimensions that must be respected in every case are those indicated in the following paragraphs:

////////////////////////////////////////////

+∆L-∆L

L

L b

Anchorage point

Guiding bracket

Compensation system “L” shaped

It consists in arranging a 90º-break in the pipeline. It must remain completely anchored to two points fixed and joined by a third clamp that allows the axial displacements (mobile point), so that for effect of temperature variations it is able to move freely as it schematically is represented in the figure.


L

L2

L 1

+∆L-∆L -∆L+∆L

Compensation system “U” shaped

The last possible solution to absorb the thermal expansions occurred in ABN//INSTAL CT FASER RD pipe would be to arrange four 90º-breaks in the pipe "U" shaped. In this case, the pipeline must remain completely anchored to three fixed points and joined by another two brackets that help the axial displacements (mobile points), so that for effect of the temperature variations it could be easily moved.

Known the position of one of the fixed points, the location of the other ones and of the mobile points must be calculated according to the same expressions used in the previous case.

////////////////////////////////////////////

Expansion joints of the buildings

Any building or building material, due to seismic or thermal effects, turns out to be submitted to contractions or expansions. Therefore to control these movements we must execute together that allow the free movement of the materials with the only end of avoiding cracks or fissures in the same ones.

A problem that is common to all the tubes either plastic or not, deals with the water running through the expansion joints. In the case of ABN//INSTAL CT Faser RD tubes the simplest method to avoid these problems consists in sheathing the tubes with a corrugated pipe of the electrical type (approximately 30 cm) to prevent the pipe from stretching only from a point. This method makes the pipe stretch along the length of the corrugated pipe, which helps to eliminate any problem derived from the stretching caused by the expansion joints.

Expansion joints Protection tube


Anchorage point

Guiding bracket

Vertical mains with derivations in plant

It should be borne in mind that the pipe derivation has the enough elasticity according to the expansion of vertical piping.This can be achieved as it is indicated in the figures:

Figure A - the installation is in the exact point, the vertical piping is rigid and the length of the line of the branching is correct.

Figure B - when the vertical piping is not rigid and can suffer an expansion, a tube bushing is done being 1,5 times the outside diameter of the derivation. Figure C - when the vertical piping is not rigid and goes through an expansion, it is necessary to do a bending arm by means of one stretch of pipe and an elbow to 90 º in order to absorb any possible expansion.

In general lines it is possible to assemble a rigid vertical piping can, i.e., without expansion compensators. In this way, the expansion is absorbed between the fixed points..

Figure A

Figure B

Figure C

////////////////////////////////////////////

The distance of vertical brackets is obtained increasing 30 % the distances indicated in the tables of horizontal brackets.


////////////////////////////////////////////Vertical installation that does not allow longitudinal expansion

Sometimes and for special situations, the piping between anchorage points is necessary. In this case the force is transmitted through the supports to the structure of the building due to the expansion and thermal contraction

In the installation of vertical tubes the first thing to do is the immobilization or fixation of the derivations. Once this carried out, and having the anchorage points close to derivation “Ts”, verify that the distance between the above mentioned points does not overcome 3 m. It is also important to install the necessary sliding brackets, between the fixed points to avoid buckling, according to the table of distances which regulates the separation between brackets following the pipe diameter and the temperature of the fluid. The above mentioned distances will be increased in 30 % for vertical installations.

Anchorage point


Vertical installations that allow the length variati

The disposition of the anchorage points works as a guide to give a direction and to limit the proportion of the thermal expansion. The anchorage points can be placed so that the length variations by effect of temperature could be distributed in different directions.

When the tubes stretches are very long, without derivations, we might sectorize the installation maintaining the following concepts:

•Fixed point at the beginning of the vertical mains •Intermediate stretches with expansion lyres •Top stretch with expanding arm

////////////////////////////////////////////

Anchorage point

Anchorage point

Anchorage point

Anchorage point


The transition will be mainly done with mixed fittings of PP and brass (alloy of cooper + zinc).

The combined fittings allow to connect tube systems of different materials between themselves.

The screwed fittings are manufactured to be compatible with the standards:

• UNE-EN 10226-1: Pipe threads where pressure tight joints are made on the threads. Part 1: Taper external threads and parellel internal threads. Dimensions, tolerances and designation.

• UNE-EN ISO 228: Pipe threads where pressure-tight joints are not made on the threads - Part 1: Dimensions, tolerances and designation

Copper-PP

The copper is a catalyst that contributes to the oxidation process of polypropylene. Specifically: the free copper ions. After the start of the oxidation process, and due to a high level of chlorine, used for the treatment of secondary water, the copper ions have a catalyst effect on the oxidation process. The increase in the quantity of copper free from ions, is followed by an increase in the catalytic effect. The quantity of ions of copper depends on the specific system of tubes used, the exposed surface of copper and the water quality (pH). This process hastens at temperatures over 70°C. To assure a long-term uninterrupted use of copper/PP combined circulation systems in hot water, it is advisable to respect the limitations indicated in the square.

//////////////////////////////////////////// Transition with pipe lines and metallic fittings

6.5.

The brass is an alloy of copper and zinc. Due to the low copper content, the risk of oxidation of the brass is reduced. The additives are added to the resin of PP to compensate the minimum influence of the free ions from copper in the brass.

Precauciones en las instalaciones de agua caliente de cobre/PPmixtas

Temperatura máxima del agua

70ºC

Presión máxima de servicio Velocidad máxima del

agua

1,50 m/s

SDR 7,4

14 bar

SDR 11

9 bar

SDR 17

5bar

Specific conditions as high concentration of disinfectants with chlorine in combination with water at low levels of PH or high places of ORP (level of bacterial activity), they affect to the long-term properties of the PP.

ABN//INSTAL CT FASER RD incorporates additives that reduce the risk of pipe deterioration caused by metallic ions.


////////////////////////////////////////////

// 07

////////////////////////////////////////////

Joint systems

7.1. Introduction7.2. Welding by thermo-fusion to socket7.3. Welding by electro-fusion7.4. Butt welding7.5. Use of bypass grafts7.6. Use of reparair plugs


Introduction

There is no joint between a ABN//INSTAL CT Faser RD pipe and a fitting, there is thermo-fusion. This means that pipe and connection fuse together molecularly, giving place to a continuous pipeline, which guarantees the highest degree of security in water systems.

Thermo-fusion: a simple, but sure and inalterable process

The thermo-fusion, in contrast to the extrusion welding, remains inalterable by passing of time. It also turns out to be easy-doing by the use of precise and practical tools that simplify execution and eliminate the problems of work arising from human error. Its simplicity and rapidity, is translated into a significant saving of time and cost of installation.

The thermo-fusion process is very simple. During a few seconds pipe and connection are submitted to a temperature of 260/270 °C. Having completed the time of warming, which varies according to the different diameters, between 6 and 40 seconds, pipe and connection are joined by interposition of its ends, fusing, melting in only one piece.

The unions between pipes and fittings of the ABN//INSTAL CT Faser RD systems is carried out by means in different of types of welding: - Welding for thermo-fusion using a polyfusor (polisystem) - Welding for electro-fusion using muffs electro-welded. - Butt welding

////////////////////////////////////////////7.1.

ABN//INSTAL CT Faser RD Page 07-02//

Heating plate

Male heating mould

Female heating mould

Correct assembly

Incorrect assembly

Socket welder (Polyfusor)

Step 1

Place the moulds in the polyfusor in the corresponding holes of the warming plate.

Step 2

The welding moulds must be clean and free from impurities before being assembled. They must be clean, if necessary, with absorbent fibre less and lint-free paper, and if necessary, with alcohol.

Step 3

The moulds for welding must always be assembled in such a way that their surface does not exceed the rim of the heating plate. Those bigger than 40 mm in diameter shall always be connected to the rear part of the plate.

Step 4

Start on the device. The indicating lights of the thermostat and of control have to be illuminated. Verify that the temperature of the thermostat is at 260 ºC. The warming process of the heating plate lasts between 10 and 30 minutes depending on the temperature ambience.

Step 5

Fasten the warming matrixes with an Allen key. To avoid damages in the Teflon layer of the mould (matrixes) do not use cutting elements.

Step 6

For the good functioning of the polyfusor the matrixes must be protected against the impurities. Burned and stuck particles can drive to a deficient fusion. The matrixes must remain always clean.

////////////////////////////////////////////7.2.

Thermo-fusion welding to socket


////////////////////////////////////////////

The welding

Step 1

When the tubes are of a small diameter cut them with a tube-cutter scissor, or with a swaying saw if they are of a big diameter. The cut has to be always perpendicular. Mark on the pipe with a pencil or felt pen the depth which is to be introduced in the matrix.

Step 2

The parts to be welded must be clean and free from impurities. Introduce tubes and accessory at the same time, applying a necessary pressure so that pipe and fittings get into the matrixes; the pressure applied has to be proportional to diameter that is being welded, the greater the diameter the greater the thrust pressure. The time used to introduce pipe and fittings into the matrix has to be progressive, appearing a homogeneous drawstring round the tubes as it gets into the matrix. They will be introduced without twist or turn.

Step 3

When the mark is reached the tubes will be withdrawn 1 mm from itself outside, so as not to reduce the passage in the end of the pipes. The time that pipe and fitting should remain in the thermo-fusor shall be the indicated one in table of “Times of warming”. There is also a time indicated in this table, to withdraw the pipes and fittings of the thermo-fusor and to proceed joining both pieces.

Step 4

Joning will be done immediately, applying the maximum possible pressure in this step without twisting or turning, verifying that a uniform drawstring shows up in the tubes and in the fitting.

Step 5

Having reached this step, there are a few seconds for verifying and rectifying the linearity of pipes and fittings, always maintaining pressure on both pieces until the set cools down.

Step 6

After waiting for the time of cooling indicated in the table, the welded piece can be manipulated and the following welding can be done to continue with the installation. This welding process is valid in ABN//INSTAL CT Faser RD system even up to 125 mm diameters. From this on, welding of the type “A testa” or with accessories “Electro-weldable“ will be done.

Fitting

Male mould Female mould

Pipe

Polyfusor

Heating

Connection finished

90º

Mark and cut


////////////////////////////////////////////

Ø

en mm

Exterior of the pipe

2025324050637590110125

Joint timein seconds

446668881010

Fixed(seconds)

6101020203030405060

Table of temperatures and times of thermo-fusion (DVS 2207-11)

SDR 7,4- SDR 11

67812182430405060

Heating time(seconds)

SDR 17

15223035

Cooling time

Total(minutes)

2244466688

b

L

≈15º

D

Ø Exterior of the pipe “D”

(mm)

2025324050637590110125

Beveling “b”

(mm)

222223333

Welding depth “L”

(mm)

14161820232731354146

Beveling and insertion of the pipes (DVS 2207-11)


////////////////////////////////////////////7.3.

Electro-fusion welding

Generalities and control

The pipe surface has to be clean and without defects. It is necessary to cut the defective ends of the pipe and to avoid the electro-weldable socket getting dirty.

Be sure that the pipe and the temperatures sensor of the welder are in the same temperature range, within the admissible temperature range to weld. For example the solar radiation or an inadequate storage, produce so big temperature difference that it leads to incorrect welding.

Preparation

1- CutCut the pipe perpendicularly with a suitable pipe cutter. The cut has to be perfectly perpendicular in order to assure the perfect distribution of cold and warm areas during the electro-fusion process.

Mark the welding length with a pencil. The length corresponds to depth of the fitting up to the stop.

2- ScratchingRemove the surface of the pipe uniformly with the rotary tangential scraper to eliminate completely the superficial oxide layer provoked by atmospheric impurities catalyzing and to obtain a smooth surface.

The scratching excludes the use of abrasive elements remains for the pipe (radial, saw blade. . . ).

3. - Cleanliness Clean the terminal and the inner part of the scratched pipe with a clean cloth. Do not use synthetic fibre fabrics, paper, dirty cloth or detergent-like substances.

4. - Union Introduce the end of the clean pipe inside the electro-weldable accessory up to the special line and block the pipes in the aligner avoiding this way that the resistances are uncovered.

The alignment is fundamental to prevent flux material leakage and to assure that the resistances of the accessory should not put themselves in contact provoking a short circuit.

5. - Electric welding Connect the two terminals of the electrical welder to the connectors of accessory. Turn on the machine and follow the indications of the screen. Once finished, let the piece electro-welded cool down without moving it during the time indicated in the bar code.

90º

Scratched and clean stretch

Mechanized area;

Insertion

Connection surface

Joint plane


////////////////////////////////////////////Possible causes of electro-fusion failures

The welding does not take place •The machine does not have the same tension as the fitting. •Erroneous welding time. •Temperature ambience out of range. •The elements to be joined have dirt or impurities (fat, water. . . ). •It has passed too much time between the preparation of the joint and the moment to carry out the welding (condensation between the elements to be joined). •The connectors do not make a good contact or they are dirty.

Leakage through an area of the joint •Inadequate welding time. •Movement of the joint before fulfilling the cooling time. •Too much separation between fitting and pipe: excessive scratching, the pipe is not aligned, the pipe is not completely introduced.

The machine stops welding before the time is over •Resistance break, because the accessory was forcibly introduced weakening the resistance. •The connectors do not do good contact or they are dirty. •Unstable electric current.

There is a leakage in the joint •The tension is not the correct one. •Too much fusion time or it was welded more than once. •The resistance does not touch another part to be joined in any point: excessive scratching, insufficient introduction of the pipe, the pipes are not aligned.

The joint emits smoke •The tension is not the correct one •The resistance is uncovered: excessive scratching, insufficient introduction of the pipe, the pipes are not aligned, it can cause deflagration. Leakage through the reference electro-weldable •The resistance does not touch another part to be joined in this point: excessive curettage, the pipes are not aligned.

The pipes made of similar materials and wall thicknesses can be joined by butt welding or electro-fusion. The pipes made of similar materials but different wall thicknesses can only be joined by electro-fusion.

Cleanliness is fundamental to do a trustworthy welding and of a high quality.


TerminalWireIdicator

Pipe Pipe

1. Tube placed inside the solder-sleeve before warming the wire

2. Wire getting hot.

////////////////////////////////////////////

3. The material round the wire starts melting.

4. The melted surface spreads towards the tube surface.

5. Heat is transmitted to the tube walls and it starts melting.

6. The melted material hardens at the beginning of the cold areas sealing the melted area. In a later phase the warming increases the pressure of the melted area.

////////////////////////////////////////////

7.The pressure of the mixture reaches its ideal point at the end of the merger (fusion) cycle. The welding reference indicates that the process has ended.

Cycle of the electro-fusion process

The welding surface must be free from tensions.


////////////////////////////////////////////7.4.

The butt welding procedure for thermo-fusion ”butt welding” consists basically on the component joining by means of the surface merging in contact. The merger conditions is achieved thanks the heat contribution through a heating element that gets in contact with the surfaces to be welded.

StandardsFor doing this type of welding the application processes are sustained on the basis of the standards issued by the Institute by the institute Deutscher Verband für Schweißen und verwandte Verfahren (DVS), codes extensively adopted recognized in the field of the thermoplastic welding. In particular, as far as the butt welding of the polypropylene, the norm that it applies is DVS 2207-11 (PP).

Finally, the inspection of the executed welding is done on the basis on guidelines of the Standard DVS 202-1.

Machinery and tools This type of welding has to be done by means of the use of machines and tools in accordance with the requisites of the standard DVS 2208-1. The basic components of a pipe welding machine are the following ones:

•A work surface bench on which clamping jaws slide and hold the elements to be welded tightly. One of the jaws is fixed, while other one is a sliding piece.

•A facing element formed by a double disc provided with cutting blades, that allow the surfaces to be welded are perfectly flat and parallel between themselves.

•An electrical heating element that allows to lead the surfaces to welding to its merger temperature, equipped with a control thermostat. The above mentioned heating element is covered in teflon to avoid any adhesion.

•A drive system of the mobile clamp to exercise pressure between the elements to be welded, mechanically or hydraulically operated.

Surface cleanliness Before warming the heating element, the surfaces will be cleaned with methyl alcohol. Between welding surfaces, the internal and external parts (influence area in the welding) of both pipes will be cleaned with methyl alcohol. The heating element too will be cleaned with a dry cloth.

Butt weld


////////////////////////////////////////////

External diameter

(mm)

≤355400...<630630...<800

800...≤1000>1000

Separation(mm)

0.5

1.0

1.3

1.5

2.0

Maximum separation of the pipes prepared to be

welded

Facing of surfaces

Once clean, the ends of the pipes will undergo a facing. This procedure will insure bonding surfaces perfectly smooth, as well as the parallelism between both surfaces. To ensure the necessary chip start-up, facing will be done by applying a light pressure with the hydraulic until flat and parallel surfaces are obtained.

Once practised facing, the ends of the pipes will be joined to verify its parallelism.

It is important not to touch with the hands the faced surfaces to prevent from contaminating them with the fat of the hands.

Environmental conditions Environmental conditions may affect the efficiency of the welding carried out. The main parameters that can have an impact on the welding process are as follows:

•A room temperature below 5 ° C causes a rapid cooling of the heating element, complicating the regulation of temperature as well as the uniformity of the temperature in the element itself.

•Prolonged exposure to the sun of the areas to be welded (tube end/fittings) can provoke high temperature differences in the mentioned areas.

•The action of the wind may have double consequence. On the one hand, it can encourage a cooling of the heating element. On the other hand, it is possible that the cooling process is not natural.It is advisable, as far as possible, to avoid any of these extreme conditions.

Preparation of the welding

Prior to the completion of the welding it is necessary to prepare the machinery and surfaces to be welded to obtain the optimum results. Such actions are defined in the following sections.


////////////////////////////////////////////Welding process

The butt welding process develops in accordance with a cycle of temperature and pressure represented in the attached graph.

The different phases of the cycle are:

•The temperature cord shows up with pressure (t1)

•Warming temperature without pressure (t2)

•Extraction of the heating element (t3)

•Pressure Increase (t4)

•Cooling pressure without temperature (t5)

Pres

sure

Timet1 t2 t3 t4 t5

P1

P2

P1

Parameters of butt welding according to DVS 2207-11

Heating time

t2 (seconds)

135135-175175-245245-330330-400400-485485-560

Time for removing the plate

t3 (seconds)

55-66-77-99-1111-1414-17

Time for reaching pressure

t4 (seconds)

66-77-1111-1717-2222-3232-43

Cooling time

t5 (seconds)

66-12

12-2020-3030-4040-5555-70

Protruding of the initial

welding cord *h(mm)

0.50.51.01.01.52.02.5

Pipe thickness(mm)

hasta 4,54.5-77-1212-1919-2626-3737-50


////////////////////////////////////////////Assembly of pipes / fittings on the machine and alignment

The operations to be followed prior to the proper welding are defined by the following steps:

•Choose the clamping jaws adequate to the diameter of the pipe •Cut the pipes to-measure and clamp them •Place rollers on the floor to support the pipe and to facilitate its dragging (in case of long stretches) •Verify the axial alignment of the elements on the machine •Verify the alignment between the pipe sections. It cannot overcome 10% of the of the pipe thickness (or accessory) •As soon as the pipes are clamped, and in case of long stretches, the pipe stretch on the floor will be dragged slowly with the hydraulic system to determine the necessary pulling power. The corresponding pressure he will read in the manometer.

Temperature setting

Prior to preparing the parts to be welded, the first action to be performed is the setting of the temperature of the heating element. The object of this first action is to perform other operations during the time it takes the heating element in reaching its working temperature, which is usually relatively long.

Working temperature depends on the material and thickness of the tube. The final adjustment with respect to the thickness will be held later. The following data will be used for a first adjustment:

PP 210ºC ±10ºC

The temperature is set with the thermostat, in addition, a check with a surface thermometer is advisable. The temperature will fit with the thermostat, also, one is advisable cross-check with a surface thermometer.


////////////////////////////////////////////


In this first stage pressure and heat are applied jointly to assure a perfect alignment between both ends, as well as the uniform warming of the junction areas.

Time t1 will be the necessary one until obtaining a rough edge (slivers) of a certain protuberance.

The values of pressure, protuberance of rough edge and temperature are given in the table

corresponding to the machine with which the welding is executed.

Pres

sure

Timet1 t2 t3 t4 t5

P1

P2

P1

x

T1 = Showing up of the welding cord

During this stage the surfaces to be welded should be kept in contact with the heating element, without pressure application. Pressure should be applied only to prevent the pipes from separating.

The warming time t2 depends on the thickness of the pipe.

The value of temperature is reflected on the table corresponding to the machine used.

Pres

sure

Timet1 t2 t3 t4 t5

P1

P2

P1

x

T2 = Heating

X

X X

X

////////////////////////////////////////////


Pres

sure

Timet1 t2 t3 t4 t5

P1

P2

P1

T3 = Removing the heating element

X

X X

X

The removing of the heating element should be done as soon as possible. Otherwise, the temperature of the junction area drops too much and, in addition to this, a possible oxidation of the heated surfaces can take place.

The time t3 is not reflected in tables, it will attempt to make it as short as possible.

Pres

sure

Timet1 t2 t3 t4 t5

P1

P2

P1

T4 = Pressure increase

0

presión

During this stage the surfaces joined by pressure will be maintained, allowing the natural cooling. Together with annealing, this phase is of great importance.

The pressure which the tubes are kept will be reflected in the corresponding table plus the dragging pressure.

Time t4 will be the required one for, once removed the heating element, joining the ends of the pipe, so that at the moment of the contact the dragging velocity is practically nil.

The value of t4 will not be reflected in the tables.

Pres

sure

Timet1 t2 t3 t4 t5

P1

P2

P1

T5 = Cooling

////////////////////////////////////////////The cooling time t5 depends on the thickness of the pipe, in this point the it is necessary to maintain the pressure of one pipe against the other. It is the longest welding process.

The value of the temperature is reflected in the corresponding table..

The value of the temperature is reflected in the corresponding table.

Visual inspection

As soon as the welding was executed, it is necessary to proceed to a visual inspection.

The only possible non-destructive testing related to materials welded by using this procedure is visual inspection. This test is sufficient provided that the welding is performed by a qualified welder according to DVS 2212-1 code.

The following table details types of the most common defects in performing butt welding, as well as its causes and the acceptance or not (evaluation criteria) of such defects.

k


////////////////////////////////////////////

Cracks in transverse or parallel direction to the welding. They can appear in: - the welding - the basic material - area affected by heating

Local or continued notches parallel to the welding, with root in core material. Caused by: - pressure of insufficient adjustment - very short annealing time - very short cooling time

Notches close to the welding, in transverse or parallel direction to the welding. Caused by: - clamping jaws- incorrect transport - defective superficial preparation

Surfaces welded displaced one with respect the other one

Angular deviation of the welded pipes. Caused by: - machine failure- failure in assembling the pipes

Welding cord sharpened partially or totally. Caused for: - Incorrect welding parameters (excessive setting pressure)

Very narrow or very wide welding cord, present partly or in the whole welding. Caused for: - incorrect annealing time - incorrect mirror temperature - incorrect setting pressure

Not uniform welding with irregular welding cord partly or the totality of the welding. Caused by: - defective superficial preparation - defective machine

Incomplete fusion partly or the whole of the welding. Caused by: - contaminated or rusty surfaces - very long time of position change- very low reference temperature - very high reference temperature

Hollow between surfaces. Caused by: - insufficient cooling pressure- insufficient cooling time

Isolated, pores or inclusions dispersed or locally concentrated. Caused by: - steam formation during the welding - contaminated (reference) mirror

Not allowed

Not allowed

Allowed only∆s ≤ 0,5 mm

Allowed only if e≤2 mm

Allowed only if e ≤1 mm

Not allowed

Allowed values are defined in the

table below

Allowed only if b1 ≥0,7 b2

Not allowed

Not allowed

Allowed isolated pores only if ∆s≤ 0,05s

Not allowed

Not allowed

Allowed only ∆s ≤ 1,0 mm



Not allowed


table below

Allowed only if b1 ≥0,6 b2

Not allowed

Not allowed


Not allowed

Not allowed

Allowed only∆s ≤ 2,0 mm



Not allowed


table below

Allowed only ifb1 ≥0,5 b2

Not allowed

Not allowed


DEFECT DESCRIPTIONLEVEL I LEVEL II LEVEL III

EVALUATION

s

∆s

1

2

3

4

5

6

7

8

9

10

11


////////////////////////////////////////////The attached graphic shows a welding cordon width admitted after the welding, depending on the pipe thickness of the (corresponds to point 7)As it is possible to appreciate, this cordon width will remain inside the range defined for every thickness. Such range is determined between two straight lines (values limit), according to the required inspection level.

0 5 10 15 20 25 30 35 40 45 50 55

Pipe thickness (mm)

0

5

10

15

20

25

30

35

40

45

50

55

60

65

70

75

80

Cord

on w

idth

(mm

)

NIVEL I

NIVEL II

NIVEL III

Pipes having similar materials and wall thicknesses can be joined by butt welding or electro-fusion. Pipes having similar materials but different wall thicknesses of can only be joined by means of the electro-fusion.

INCORRECT CORRECT


////////////////////////////////////////////7.5.

Weld-in saddles

Matrix

Saddle

Pipe

Heating Finished connetion

Drilling

Weld in saddles are used for:• branch connections in existing installations• the substitution of a reduction-tee• branch connections in risers• sensor wells, etc.

Step 1 .

Step 2. Remove burrs, debris and other dirts with a chamfering tool. Do not touch the peeled surface any more and protect it from new pollution.

Step 3. The welding device / saddle welding tool must have reached the required operating temperature of 260°C.

Step 4 . Insert the heating tool on the concave side of the weld in saddle tool into the hole drilled in the pipe wall until the tool is completely in contact with the outer wall of the pipe. Next the weld-in saddle tool is inserted into the heating sleeve until the saddle surface is up against the convex side of the welding tool. The heating time of the elements is generally 30 seconds.

Step 5. After the welding tool has been removed, the weld-in saddle tool is immediately inserted into the heated, drilled hole. Then the weld-in saddle should be pressed on the pipe for about 15 seconds. After being allowed to cool for 10 minutes the connection can be exposed to its full loading.

The first step is to drill through the pipe wall at the intended outlet point.


////////////////////////////////////////////7.6.

Damaged pipes may be repaired by using repair plugs:

Step 1 Drain pipes.

Step 2Uncover damaged pipe.

Step 3Drill damaged area of pipe out to a diameter of 8 mm square to the pipe.

Step 4Heat up drill hole and repair plug with the hole welding tool for 15 seconds.

Step 5Insert repair plug inmediately.

Step 6Cut off protruding end of repair plug.

Step 7The repaired area of pipe has reached full strength after aprox. 5 minutes.

Use of repair plugs


////////////////////////////////////////////

// 08

////////////////////////////////////////////

Pressure tests

8.1. Preparation and cleanliness8.2. Tests and putting into service


////////////////////////////////////////////

////////////////////////////////////////////8.1.

All fluid circulation networks must be hydrostatically, proven to ensure water tightness, before being hidden by works of masonry, filling or material by the insulating material.

The procedure to follow for testing hydraulic tightness, depending on the type of transported fluid and to detect failures of continuity in the circulation of fluid-carrying pipes will comprise the phases listed below:

Preparation and cleanliness of the pipelines

1. Before testing watertightness and doing the final filling, networks of water pipes should be cleaned internally to eliminate waste from the assembling.

2. Tightness tests will require the closure of open terminals. It is important to assure that machinery and fittings included in the section of the network which is intended to be tested can withstand pressure to which they will be subjected. Otherwise, such devices and fittings should be excluded, closing valves or replacing them with stoppers.

3. To do this, once completed the installation, cleaning consists in filling and emptying it many times as it is necessary, with water or an aqueous solution of a detergent product, with dispersing agents compatible with the materials used in the circuit, whose concentration is to be established by the manufacturer.

4. The use of detergents is not permitted for pipe networks destined to the distribution of water for sanitary purposes.

5. After filling, the pumps will be put to service and let the water circulate during the time indicated by the manufacturer of the dispersant compound. Subsequently, the network is completely emptied and will be rinsed with water from the feeding device.

6. In case of closed networks, the circulation of fluids with temperature of functioning less than 100 °C, the pH of the water will measure himself of the circuit. If the pH will turn out to be less that 7,5 will repeat the operation of cleanliness and rinsing so many times as it is necessary. Next the installation will put itself in functioning with its treatment devices.

Preparation and cleanliness of the networks

The installation of ABN//INSTAL CT FASER RD system additives, such as adhesives, fluxes, etc. are not used. The junction is carried out exclusively by thermo-fusion. The system maintains the purity of its material also in junction, therefore the simple washing with water is completely sufficient.


The sewage system should be filled slowly with drinking water to ensure the complete elimination of air bags, to avoid pressure blows.

Different tests of hydrostatic pressure for systems of ducting to be installed and put into service of such systems are described in the following test procedures.

Tests and putting into service

////////////////////////////////////////////8.2.

Test procedure AThe procedure “A” of the application of the test hydrostatic pressure comprises the following stages:

a) opening of the bleed-off system;

b) bleeding the system with water to expel all the air that can be drained by this means. Stop the flow and closure of the bleed-off System;

c) application of the test hydrostatic pressure selected, equal to 1.5 times the design pressure, by pumping in accordance with Figure 12, during the first 30 min, during this time inspection should be carried out is to detect any leaks on the system determined to be tested;

d) in the case of an important water leak, reduce the pressure to 0.5 times the design pressure according to Figure 12;

e) closing of the bleed tap. If stabilized at a constant pressure, greater than 0.5 times the pressure design, it is indicative that the pipeline system is good. Monitoring of evolution for 90 minutes. Perform a visual control to locate the leaks. If during this period the pressure has a tendency to get off, this in indicative that there is a leak in the system;

f) the results of the test should be recorded.

0 10 20 30 40 50 60 70 80 90 100 110 1200

x0,5

x1,0

bar

1,5

x de

sign

pre

ssur

e

Water tightness test A Test procedureTime

min

Pres

sure

test


Test procedure B

Procedure “B” for the application of the test hydrostatic pressure comprises the following stages:

(a) opening of the bleed-off System;

(b) bleeding system with water to remove all the air that can be drained by this means.Stop the flow and closure of the bleed-off System;

(c) application of the test hydrostatic pressure selected, equal to 1.5 times the design pressure, by pumping according to Figure 13, during the first 30 min;

(d) the pressure reading at the end of the 30 min;

(e) after other 30 min pressure reading, and p e r fo r m i n g o f a v i s u a l c h e c k o f t h e watertightness. If the pressure is below 0.6 bar, it is deduced that the system does not leak and the test will continue without pumping again;

(f) implementation of the visual control of the water-tightness and If, during the following 2 h, the pressure drop is greater than 0.2 bar, this is indicative that there is a leak within the system;

(g) the results of the test should be recorded.The test procedure B can be reduced (only to the stages) a) to e) and g) in the small sections of an installation.

0 10 20 30 40 50 60 120 min 180Time

Pres

sure

test 1,

5 x

pdes

ign

pres

sure

barPumping

Δρ

1<0,

6 ba

r

Δρ

2<

0,2

bar

Watertightness test. Test procedure B

////////////////////////////////////////////


////////////////////////////////////////////

Transport, handling and collecting9.1. Transport9.2. Handling9.3. Collecting

// 09

////////////////////////////////////////////


////////////////////////////////////////////

Operations of the tubes should be, where appropriate, in accordance with the regulations of traffic, being sometimes a condition for manufacturing lengths, because it is possible to manufacture tubes of more than 12 m.

As a general rule, the loading, transport and subsequent discharge process must be carried out assuring that pipe and fittings do not suffer any deterioration in transit, for it is imperative to take the following precautions:

The tubes must rest completely on the support surface, for which the transport vehicles will have the ground flat and free from any loose items, lump or hard edge that could damage them.

In those cases that the platform of the vehicle is not completely flat, it should contain some element that compensates the outgoing, for example strips of wood separated 0.40 m, or a layer of sand or chip.

Bands or tapes will be used to ensure the load, but it is important not to tighten excessively because they can be deformed. The use of chains or wire in contact with the tubes should always be avoided. It is advisable to grip with wide ribbon slings.

Those rolls of big diameter which, because of their size, the vehicle platform does not support horizontally, are placed vertically, taking care to remain the shortest possible time in this position, and avoiding the placement of any additional burden on them.

If transport includes different diameter pipes, it is necessary to place them in decreasing sense regarding their diameters beginning from the bottom.

Small diameter tubes will be shipped on pallets.

Prevent that tubes protrude from the box of the truck leaving sections cantilever

Transport

////////////////////////////////////////////9.1.


The loading and unloading operations must be performed in such a way that the different elements is not hit each other or the ground. The download should be, to be possible, close to the place where it should be placed, avoiding the tube from resting on isolated points.

Discharging of pipes and fittings must be done orderly, and may be easily done by hand or with equipments. Avoid throwing them from the truck to the ground, or hit them violently; also avoid dragging them along the ground or getting in contacts with cutting edge objects.

Manipulation should be performed with hand, Hose Clamp Pliers or with 50mm-wide nylon slings. Using slings, two points of support are recommended.

If due to faulty handling or storage, a tube is damaged or folds, the affected portion should be completely deleted. Scratches that do not exceed 10% thickness will be accepted.

Special precautions shall be determined by temperatures below 4°C when manipulating pipes.

Handling

////////////////////////////////////////////9.2.


1,5 m

The arrival of the tubes to work and prior to the reception it must be checked that the charge has not gone through any kind of deterioration by loosen moorings, loss of protections, etc., withdrawing any material that raises doubts about its possible use, controlling its location to avoid further confusion.

Discharge of pipes must be done in an orderly manner.

The collection of tubes will preferably be done in covered premises and on flat and clean surfaces, protecting them from the direct sunlight and low temperatures.

The same as in transport, in the collection process, must be taken as a general rule the careful handling that prevents the material falls.

Care to bear in mind during the collection.

In any case, avoid contact with fuels, solvents, adhesives, aggressive paintings with lines of steam or hot water, making sure that the external temperature is not very high, ensuring a correct ventilation to avoid deformation caused by heat.

Stock piling

////////////////////////////////////////////9.3.


////////////////////////////////////////////

// 10

////////////////////////////////////////////

Product range

10.1. Pipe10.2. Socket-welding fittings10.3. Metal-casing fittings10.4. Socket-welding valves10.5. Electrofusion fittings10.6. Butt-welding fittings


////////////////////////////////////////////10.1.

Pipe

MATERIAL:

COLOR:

SERIES:

STANDARDS:

APPLICATIONFIELDS:

DIFFERENTIATINGFEATURES:

• PP RCT RP + FV (fibre reinforcement)

• Metalized grey with white strips

• SERIES 3,2 / SDR 7,4 • SERIES 5 / SDR 11 • SERIES 8 / SDR 17

• UNE-EN ISO 21003 • ASTM F2389*10 • R.P. 01.78 • DIN 8077 • DIN 8078

• Drinking water pipeline networks, for cold and warm installations.• High and low temperature intallations.• Civil and industrial pipeline networks.• Pipelines for pneumatic systems.• Pipelines for agricultural and horticultural use.• Cooling water networks.

• Resistance to disinfection procedures• Antimicrobial protection• Microfiber anti-expansion• UV protection• Anti-incrustation protection

ABN//INSTAL CT Faser RD 10-02// Page

*Product range: available at the price list.

////////////////////////////////////////////10.2.

PIPE

MATERIAL:

COLOUR:

TYPE OF UNION:

STANDARDS:


• ABN//INSTAL CT FASER RD SERIES 3,2 / SDR 7,4• ABN//INSTAL CT FASER RD SERIES 5 / SDR 11• ABN//INSTAL CT FASER RD SERIES 8 / SDR 17

• PP R

• Grey

• Socket-fusion

• UNE-EN ISO 15874. Part 3. Fittings

• Resistance to disinfection procedures• Antimicrobial protection• UV protection

Socket-welding fittings



////////////////////////////////////////////10.3.

Metal-casing

PIPE:

MATERIAL:

COLOUR:

TYPE OF UNION:

STANDARDS:DIFFERENTIATING

FEATURES:


• PP R+brass

• Gris

• Socket-welding + metal threaded


• Resistance to disinfection procedures• Antimicrobial protection• UV protection



////////////////////////////////////////////10.5.

Electrofusion fittings

PIPE:

MATERIAL:

COLOUR:

TYPE OF UNION:

STANDARDS


• PP R+Cu

• Grey

• electrofusion




////////////////////////////////////////////10.6.

Butt-welding fittings

PIPE:

MATERIAL:

COLOUR:

TYPE OF UNION:

STANDARDS:



• PP RCT RP

• Grey

• Butt-welding

• R.P.01.78

•Resistance to disinfection procedures•Antimicrobial protection• UV protection



////////////////////////////////////////////

// 11

////////////////////////////////////////////

Quality11.1. Quality control11.2. Internal quality control of the product11.3. Regulations11.4. Certificates11.5. Warranty


////////////////////////////////////////////

//////////////////////////////////////////// Quality control

11.1.

ABN//INSTAL CT Faser RD pipe manufacturing is a highly-tech industrial process and during which there are numerous quality control tests aiming to verify not only the manufacturing quality assurance but, in addition to verify the manufacturing quality assurance and also that technical characteristics both raw material as tubing manufactured once conform to specifications collected in the corresponding legislation.

We should distinguish between: •Management of quality in manufacturing. •Guarantee of the quality of the product.

System of quality management in manufacturing ISO 9001

The quality management system can follow the principles established in the ISO 9001 standard. This system consists of periodic inspections, procedures and tests or control evaluations both at the raw materials, equipment, components, production processes and product.

All the elements, requirements and provisions adopted by the manufacturer are systematically documented in writing policies and procedures of quality. Production control offers, therefore, operational techniques and all measures that allow the maintenance and control of the conformity of the components of their technical specifications. Its implementation involves inspections and tests to the raw material and other components, processes, equipment of manufacture of finished products.

The implementation of a system of quality management in factory requires actions among others on:

•Personnel (training, skills, experience...) •Equipments of weight, measure, test, manufacturing (calibration, verification...) •Design process •Raw material of components (check of specifications) •Control in the process (production under controlled conditions) •Traceability and marking (batch product ID) •Non-conforming products (treatment of non-conformities) •Corrective actions •Handling, storage and packing

There are organizations that certify compliance with the directions of the ISO 9001 standard and, therefore, the implementation of a quality assurance system.

This certification proves that the company's quality management system which is granted, is subject to audits and controls established in the certification system and that it has obtained adequate confidence in their compliance with the standard ISO 9001.


////////////////////////////////////////////11.2.


Reception of raw materials

The raw material, they are submitted to diverse essays and control panel before being received, to guarantee that they fit to the stated characteristics.

Extrusion Injection

Pipes Fittings

Intermediate essays

During the manufacture intermediate essays, a demand are realized ofquality protocol interned of ABN verifying:

information of the machines of that it takes control in the whole processfinished of the pipes

dimensions

These essays are made in all the lots.

Cross-chez of manufacture information

Final testFinal tests

With the completed product essays are realized to verify the quality ofproduct and the quality of the procedure of manufacture.

Dimensions Finished superficial

Homogeneity of the material Resistance to the internal pressure

Fluency index Mechanical behaviour Behaviour to the heat

Storage

Packing

Expedition

All the control panel interns are documented and engravings according to the protocol of quality.

The received information during production is analysed in detail.

The machinery and devices of laboratory are inspected periodically, being realized its calibrated and putting to point.

Internal quality control of product

11.3.

Dimensional and quality standards

•ISO 15874: Plastic piping systems for hot and cold water installations. Polypropylene (PP). Part 1: Generalities.

•DIN 8077: Polypropylene (PP) pipes - pp, pp, pp-h, PP-RCT – Dimensions

•DIN 8078: Polypropylene (PP) pipes - PP-H, PP-B, PP-R, PP-RCT – General quality requirements and testing

•NTC 4897-2: Systems of plastic pipes for hot and cold water. Polypropylene (PP)

•RP 01.00: Particular regulations of the AENOR brand for plastic materials. Common requirements.

•RP 01.78: Particular Regulation of the Conformity Certificate AENOR for piping systems in Polypropylene Random with modified crystal structure(PP-RCT) and glass fibre (PV) for hot and cold water systems in the interior of the structure of the buildings.

Tests carried out

•EN ISO 1043-1: Plastics. Symbols and abbreviations. Part 1: Base polymers and its special features.

•EN ISO 9080: Plastic pipeline and driving systems. Determination a long-term hydrostatic resistance of thermoplastic materials in the form of pipes through extrapolation.

•EN ISO 7686: pipes and fittings made of plastic materials. Determination of the opacity (ISO 7686:2005).

Study of evolution of the microbial load on pipe doped with bactericides. AQM laboratories.

//////////////////////////////////////////// Standars

UNE


13.4.////////////////////////////////////////////

Certificates


Company certificates

Product certificates

13.5.////////////////////////////////////////////

Garantía

1010añosaños

• G AAÍ RT AN NA TÍR AA •G G• AA RÍ T AN NA TÍR AA G •


ABN Pipe Systems guarantees all the products during 10 years at 2.000.000 euros

In an important insurance company an Insurance policy of Legal liability exists for ours products, which it covers the damages to persons and objects, as well as the necessary assembly costs and dismantling, whenever they have been caused by our products, up to an amount of 2. 000. 000 € for catastrophe and up to 10 years from the starting of the installation or end of the contract of the insurance (later responsibility).

////////////////////////////////////////////

// 12

////////////////////////////////////////////

Important considerations / Information about security

12.1. Important considerations in the installations12.2. Chemical and thermal disinfection12.3. Mix installations of polypropylene PP and metals12.4. Non recommendable installations


////////////////////////////////////////////Important considerations in the installations12.1

In installations with ABN//INSTAL CT FASER RD system particular attention should be paid to the following parameters:

PRESSURE

Do not exceed the pressures described in Chapter 2 of the ABN//INSTAL CT FASER RD technical catalogue, which are indicated depending on the series of pipes, temperature and durability.

In table 1 we recall the most relevant values.

TABLE 1

VELOCITY

Rates of water through a pipe must be studied in detail. It is necessary to establish a criterion which sets a maximum value and other minimum value for the water velocity in the pipes, which can be detrimental both: too high velocity and too low velocity.

Exceeding the velocity limit may:

•Originate water hammer, whose value of over pressure may cause breakage.•Produce excessive losses of head.•Favours corrosion.•Produce noises.

A too low speed:

•Propitiate the formation of deposits of solid, causing obstructions.•Imply an over dimensioning of the installation, turning it unnecessarily more expensive.

The Technical Building Code establishes the following criteria:

The choice of velocity calculation falls within the following ranges:(i) metal pipe: between 0.50 and 2.00 m/s(ii) thermoplastic and multilayer pipes: between 0.50 and 3.50 m/s

As you can see, speeds for the plastic pipes are much higher than those of the metal pipes, reason why installations that combine both systems must not exceed the more restrictive velocity, i.e. 2.00 m/s

TEMPERATURE

The A.C.S. installations usually work between 45 and 60 °C and must not exceed 70°C. Temperature over 70°C in A.C.S. installations will reduce significantly the service life of the polypropylene pipes.

Pressures with 50 years of operation according to DIN 8077

(SF: 1.25)

Serie

Serie

3.2

5

8

60ºC

20ºC

17.7

11.3

12.7

70ºC

50ºC

14.9

9.5

8.3

80ºC*

70ºC

12.7

8.1

6.0*For this temperature are 25 years

20ºC

10ºC

31.7

20.3

14.6

ABN INSTA CT Faser RD - Page 12-02//

////////////////////////////////////////////

Inappropriate treatmentThe execution of the treatment of disinfection without properly following parameters (chlorine concentration, temperature, time) established by the Royal Decree RD 8652003 or selecting an improper treatment can result in oxidative degradation of the different elements of the system.

Chemical and thermal disinfection

Disinfection will not be effective if it is not complemented by a thorough cleaning. Treatment systems and products suitable for drinking water should be used.

Cleaning and disinfection methods stated in RDm865/2003 are:

a) Thermal disinfection

Thermal disinfection is compatible with the ABN//INSTAL CT FASER RD piping systems as referred to in the Royal Decree 8652003, by raising the water temperature up to 70° C.

The admissible maximum limits of usage regarding temperature and pressure of service should be respected and they are explained in chapter 2 of ABN//INSTALL CT FASER RD the technical catalogue.

b) Chemical disinfection

In case of non-continuous disinfection, it is permitted to apply twice a year to ABN//INSTAL CT FASER RD system, a chlorine content 50 mgl-free for a maximum of 12 hours, provided that the water temperature does not exceed 30°C and the PH is between 7 and 8.

Disinfection processes, particularly with chlorinated water can have a direct influenceon the service life of the pipes.

In installations where it is not possible to control the levels of chlorine is recommended not to exceed the 70 ° c of temperature.

The disinfection of installations will require one or the other disinfection process, strictly following the procedure for each of them, and in any case will be a combination both methods.

12.2 Chemical and thermal disinfection

Using chlorine dioxide as disinfectant (ClO) is not permitted

Continuous disinfection

This treatment leads to a long-term contact between the material and the disinfected water. Chemical reactions that can be developed involve all piping materials, namely metals, rubbers and plastics. Therefore, all materials must be carefully selected. Under certain conditions, the presence of chlorine in high concentration combined with water having a low pH, ie <6.5, and under a continuous temperature of 60°C or more, can long-term affect the PP conditions. These recommendations are applied especially in buildings with recirculation circuits to provide instant water.


////////////////////////////////////////////12.3

Mix installations of PP and metals

These recommendations are applicable in systems of Sanitary Hot water with recirculation, where there coexist metallic systems (mainly copper or copper alloys) with systems of polypropylene.

In this type of installations, if the operating parameters are not controlled, the tubes of PP, likewise other polyolefins, can produce cracking due to stress oxidative.

•In combined installations, where there exist tubes of PP and metallurgies, with A. C. S recirculation, it is necessary to be especially careful because:

- The temperature cannot overcome 70ºC - The service pressures cannot overcome those indicated in Chapter 2 of ABN//INSTAL CT FASER RD technical catalogue- The circulation velocities of the metallic tubes will not overcome 2,0 m/s

•Under these circumstances it is very important that the pipe installation allows to compensate its expansion, as well as to do a correct support.

SYSTEMS OF COPPER -PP

The copper is a catalyst that contributes to the process of oxidation of the polypropylene. Specifically:

free copper ions. After starting the process of oxidation, and due to a high level of chlorine, which is

used for the treatment of secondary water, the copper ions have a catalyst effect on the oxidation

process. With the increase of free copper in ions, the effect catalyst increases. The quantity of ions of

copper depends on the specific pipe system used, the exposed surface of copper and the water quality

(pH). This process hastens over 70°C.

Water temperature

Service pressure

Fluid velocity

≤ 70 ºC

It depends on the SDR of the pipes and they are indicated in the chapter 2 of this catalogue

<2,0 m/s

To avoid the corrosion in systems with hot water circulation in combined metal systems / PP, respect the following limitations:

Limitation in combined metal systems / PP with hot water circulation

ABN INSTA CT Faser RD - Page 12-04//

////////////////////////////////////////////12.4Non-recommendable installations

Interchanger

Acumulativedeposit

Boiler

Polypropilene installation it not recommended

ABN//INSTAL CT FASER RD

installations is recommended

Any facility that has metal parts in contact with water is subjected on a permanent basis to electrochemical corrosion and scale production risks. A.C.S. Installations use hot water to different temperatures what increases these risks.

The circuits of ACS (it is always new, chloride water and with 02) contribute continuously salt, gases, solid residues, etc., therefore the effects that they provoke are accumulative, giving origin to the progressive deterioration of the different components of the installation.

The installations with metallic parts in continuous contact with hot water can produce a deterioration in the polypropylene, therefore it is recommended not to install it in the closed circuits of A. C. S recirculation, since an increase of temperature and a big exchange of metallic ions take place and they turn to the polypropylene in the element of sacrifice of the installation.


////////////////////////////////////////////

// 13

////////////////////////////////////////////

Bibliography


////////////////////////////////////////////

Bibliography

////////////////////////////////////////////15

Technical Code of Buildings

Regulation of thermal facilities in the buildings.

Quality management systems -- Requirements

Plastics piping systems for hot and cold water installations - Polypropylene (PP) - Part 1: General (ISO 15874-1:2013)

Plastics piping systems for hot and cold water installations - Polypropylene (PP) - Part 2: Pipes (ISO 15874-2:2013)

Systèmes de canalisations en plastique pour les installations d'eau chaude et froide - Polypropylène (PP) - Partie 3: Raccords (ISO 15874-3:2013)

Plastics piping systems for hot and cold water installations - Polypropylene (PP) - Part 5: Fitness for purpose of the system (ISO 15874-5:2013)

Particular regulation of the brand AENOR for plastic materials. Common requisites.

Particular regulation of the Conformity Certificate AENOR for piping Systems in Polypropylene Random with crystalline structure modified (PP-RCT) and fibreglass (FV) for hot and cold water installations inside the structure of the buildings. Polypropylene (PP) pipes - PP-H, PP-B, PP-R, PP-RCT - Dimensions

Polypropylene (PP) pipes - PP-H, PP-B, PP-R, PP-RCT - General quality requirements and testing

Plastics piping systems - Guidance for the installation inside buildings of pressure piping systems for hot and cold water intended for human consumption

Specifications for installations inside buildings conveying water for human consumption - Part 4: Installation

Plastics piping systems for hot and cold water installations -- Guidance for classification and design

Codes of practice for drinking water installations.

Welding of thermoplastics. Tools of thermo fusion welding of pipes, fittings and PP plates.

Thermoplastic welding. Tools of thermo-fusion for welding pipes, fittings and plates.

Plastic pipes and fittings. Determining opacity (ISO 7686:2005)

Plastics. Symbols and abbreviations. Part 1: Base polymers and their special characteristics (ISO 1043-1:2011)

CTE

RITE

ISO 9001

UNE-EN ISO 15874-1

UNE-EN ISO 15874-2

UNE-EN ISO 15874-3

UNE-EN ISO 15874-5

RP 01.00

RP 01.78

DIN 8077

DIN 8078

UNE ENV 12108

UNE-EN 806-4:2010

ISO 10508: 2006

DIN 1988

DVS 2207-11

DVS 2208-1

EN ISO 7686

EN ISO 1043-1

ABN//INSTAL CT Faser RD - Page 13-03

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PIPE SYSTEMS ABN EVAC ENERGY PLUS

Chemical Resistance Chart

Résistance Chimique

Resistencias Químicas

Resistências Químicas

// ANNEX

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PIPE SYSTEMS

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Chemical resistance of plastics and rubber seals Résistances chimiques des matières plastiques et materiaux en caoutchouc Resistencia química de plásticos y elastómeros Resistência química de plásticos e elastómeros

GENERALINFORMATION

INFORMATIONGÉNÉRALE

INFORMACIÓNGENERAL

INFORMAÇÃO GERAL

• The information provided in this section are general indications of the chemical resistance of the different materials non submitted to pressure.• We take into account the differentapplications from the used materialsas well as the usual conditions ofwork, particulary the temperatures andconcentrations of the chemical fluidthat is in contact with the material.• In the case of mixing different chemical agents or to evaluate the behavior in the presence of internal orexternal mechanical efforts, it will benecessary to carry out additional tests.

• Les informations facilitées dans ceparagraphe sont des indications générales concernant la résistance chimique des différents matériaux non soumis à la pression.• Il est tenu compte des différentesapplications des matériaux utilisésainsi que des conditions de travailhabituelles, en particulier les températures et les concentrations du fluide chimique qui est en contact avec le matériau.• Dans le cas de mélanges de différents produits chimiques ou pour évaluer le comportement en présenced’efforts mécaniques internes ou externes, il sera nécessaire d’effectuer des essais supplémentaires adicionales.

• Las informaciones proporcionadasen este apartado son indicacionesgenerales de la resistencia química delos diferentes materiales no sometidosa presión.• Se tienen en cuenta las diferentesaplicaciones de los materiales usadosasí como las condiciones de trabajousuales, en particular las temperaturasy concentraciones del fluido químicoque está en contacto con el material.• En el caso de mezclar diferentesproductos químicos o para evaluar elcomportamiento en presencia deesfuerzos mecánicos internos o externos, será necesario efectuar ensayos adicionales.

• As informações proporcionadasneste documento, são indicadoresgerais, da resistência química de diferentes materiais não submetidos apressão.• Têm-se em conta as diferentes aplicações dos materiais usados assimcomo as diversas condições de trabalho, em particular nas temperaturas e concentrações de fluído químico que está em contacto com o material.• No caso de mistura de diferentes produtos químicos ou para avaliar o comportamento em presença de esforços mecânicos internos e externos, será necessário efectuar ensaios adicionais.

CLASSIFICATION CLASSIFICATION CLASIFICACIÓN CLASSIFICAÇÃO

• Resistant: within the acceptablelimits of pressure and temperature thematerial is not affected or insignificantly affected.

• Limited resistance: the mediacan attack the material partially orcause swelling. The service life is reduced. It is advisable to reduce the conditions of pressure and temperature of work.

• Not recommended: the material is seriously damaged. It is not recommended the use.

• Résistant: dans les limites de pressions et de températures acceptables, le matériau n’est pas attaqué ou de manière insignifiante.

• Limité: l’environnement peut attaquer partiellement le matériau ou lui causer des boursuflures. La durée de vie se retrouve réduite. Il est conseillé de réduire les conditions de pression et de température de travail afin de ménager le matériau.

• Non reccomandé: le matériau est sérieusement attaqué. Usage déconseillé.

• Resistente: dentro de los límitesaceptables de presión y temperaturael material queda inafectado o insignificantemente afectado.

• Resistencia Limitada: El mediopuede atacar parcialmente al materialo causar hinchamiento. La vida deservicio queda reducida. Es aconsejable reducir las condiciones de presión y temperatura de trabajo.

• No recomendado: el material queda seriamente afetado. No debería usarse.

• Resistente: Dentro dos limites aceitáveis de pressão e temperatura, o material não fica afectado, e a sua durabilidade é maior.

• Limitada: O ambiente pode atacar parcialmente o material e causar o alargamento. A sua vida de serviço poderá reduzir-se. É aconselhável reduzir as condições de P e Tª de trabalho.

• Não recomendado: O material fica seriamente afectado. Não deveráser utilizado.

R Resistant Résistance satisfaisante Resistente Resistente

L Limited resistance Résistance limitée Resistencia limitada Resitência limitada

N Not recomended Résistance non satisfaisante No satisfactoria Não satisfactória

SOLVENT CEMENTED UNIONS

UNIONS PARCOLLAGES

UNIONES ENCOLADAS UNIÕES COLADAS

• PVC solvent cemented unions are generally as resistant as the PVC.The following chemical agents are anexception (the union is classified as“condicionally resistant”):

Sulfuric acid (H 2SO 4) in concentrations higher than 70%.Acid hydrochlorate (HCI) in concentrations higher than 25%.Nitric acid (HNO 3) in concentrationshigher than 20%.Acid hydrofluoric (HF).

• Les unions par collage du PVC sontgénéralement aussi résistant que lePVC lui même. Toutefois, pour les produits chimiques suivants, il convient de nuancer cette résistance:

Acide sulfurique (H 2SO 4) en concentration supérieure à 70%.Acide chloridrique (HCI) en concentration supérieure à 25%.Acide nitrique (HNO 3) en concentration supérieure à 20%.Acide fluoridrique (HF).

• Las uniones encoladas con adhesivos de PVC son generalmente tan resistentes como el PVC. Los siguientes productos químicos son unaexcepción (la unión queda clasificadacomo “condicionalmente resistente”:

Ácido sulfúrico (H 2SO 4) en concentraciones superiores al 70%.Ácido clorhídrico (HCI) en concentraciones superiores al 25%.Ácido nítrico (HNO 3) en concentraciones superiores al 20%.Ácido fluorhídrico (HF).

• As uniões coladas com colas de PVC são na generalidade tão resistentes como o PVC. Os seguintes produtos químicos são uma excepção (a união fica classificada como “condicionalmente resistente”:

Ácido sulfúrico (H 2SO 4) em concentrações superiores a 70%.Ácido clorídrico (HCI) em concentrações superiores a 25%.Ácido nítrico (HNO 3) em concentrações superiores a 20%.Ácido fluorídrico (HF).

ABN EVAC ENERGY PLUS - Page 03//

MIN.

TEMP.

OF USE

(ºC)Acrylonitrile-butadiene-styrene Resistant: salt solutions, diluted acids and alkalis, saturated hydrocarbons, alcohol, mineral ils and fats.

Not resistant to concentrated inorganic acids, aromatic or chlorinated hydrocarbons, esters and ketones.

Acrylonitrile-butadiène-styrène Résistant: sol. salines aqueuse, acides et alcalis dilués, hydrocarbures saturés, alcools, huiles minérales et graisses.

Non résistant : acide inorganiques concentrés, hydrocarbures aromatiques et chlorés, esters et cétones.

Acrilonitrilo-butadieno-estireno Resistente: sol.salinas acuosas, ácidos y álcalis diluidos, hidrocarburos saturados, alcoholes, aceites minerales y grasas.

No resiste: ácidos inorgánicos concentrados, hidrocarburos aromáticos y clorados, ésteres y cetonas.

Acrilonitrilo-butadieno-estireno Resistente: sol. Sal aquoso, ácidos e álcalis fluidos, hidrocarbonetos saturados, óleos mi n e r a i s e gases.

Não resistente: ácidos inorgânicos concentrados, hidrocarbonetos aromáticos e clorados, éteres e acetonas.

Ethylene-propylene-diene terpolymers Good resistance to ozone and weather. Resistant to ketones and alcohols.

Not resistant to oils, fats and strong acids or alkalis.

Caoutchoucs éthylène-propylène-diène Bonne résistance à l’ozone et au vieillissement. Résistant aux cétones et alcools.

Non résistant aux huiles, graisses, acides ou alcalis forts.

Caucho etileno-propileno-dieno Buena resistencia al ozono y al envejecimiento. Resiste a cetonas y alcoholes.

No resiste a aceites, grasas, ácidos o álcalis fuertes.

Caucho etileno-propileno-dieno Boa resistência ao ozono e ao envelhecimento. Resistente a acetona de potássio e álcoois.

Não resistente a óleos, lubrificantes, ácidos ou álcalis fortes.

Vinil Ethilen Acetate Good resistance to most non-oxidizing acids, alkalis and salt solutions.

Not resistant oxidicing acids, halogens, hydrocarbons, alcohols, esters and ketones.

Acétate de Vinil Ethylen Résistant aux acides non oxydants dilués, alccols et alcalis dilués.

Pas résistant aux acides oxydants, halogènes, hydrocarbures, alcools, ésthers, cétones,huiles et graisses.

Etilén vinil acetato Resistente a ácidos no oxidantes, alcoholes y álcalis.

No resistente a ácidos oxidantes, halógenos, hidrocarburos, alcoholes, ésteres, cetonas, aceites y grasas.

Etilén vinil acetato Resistente a ácidos não oxidantes, álcoois e álcalis.

Não resiste a ácidos oxidantes, alógenos, hidrocarbonetos, acetonas, óleos e acetona.

Fluorinated rubbers Resistant to most chemical products.

Caoutchoucs fluorocarbonés Compatible avec la majorité des produits chimiques.

Caucho fluorado Compatible con la mayoría de productos químicos.

Caucho fluorado Compatível com a maioria dos produtos químicos.

Nitrile rubber Good resistance to oils and petroleum.

Caoutchoucs de butadiène-nitrile acrylique Bonne résistance aux huiles et au pétrole.

Caucho nitrilo (acrilonitrilo-butadieno) Buena resistencia a los aceites y al petróleo.

Caucho nitrilo (acrilonitrilo-butadieno) Boa resistência aos óleos e petróleo.

High-density polyethylene Resistant: diluted acids, alkalis, salt solutions, water, alcohols, esters, fats and gasoline.

Not resistant to strong oxidizing. It swells with aromatic and aliphatic hydrocarbons.

Polyéthylène haute densité Résiste aux: acides dilués, alcalis, solucions salines, eau, alcool, esters, huiles et gaz-oil.

Ne résiste pas à: oxydants forts, se boursoufle avec des hydrocarbures alifatiques et aromatiques.

Polietileno de alta densidad Resiste a: ácidos diluidos, álcalis, soluciones salinas, agua, alcohol, ésteres, aceites y ga.solina

No resiste a: oxidantes fuertes. Se hincha con hidrocarburos alifáticos y aromáticos.

Polietileno de alta densidade Resiste a: ácidos diluídos, álcalis, soluções salinas, água, álcool, éter, óleos e gasolina.

Não resistente a: oxidantes fortes. Dilata com hidrocarboneto alifáticos e aromáticos.

Polypropylene Resistant: hidrous solutions of inorganic acid, weak organic acids, bleach, alcohols and some oils.

Not resistant: strong oxidizings, halogenated hydrocarbons, it swells with aliphatic and aromatic hydrocarbons.

Polypropylène Résiste aux : solutions aqueuses d’acides inorganiques, acides organiques debiles, lessives, alccol et huiles.

Ne résiste pas aux:oxydants forts,hydrocarbures halogènes,se boursoufle avec les hydrocarbures alifatiques y aromatiques.

Polipropileno Resiste a : soluciones acuosas de ácidos inorgánicos, ácidos orgánicos débiles, lejías, alcohol y algunos aceites.

No resiste a: oxidantes fuertes, hidrocarburos halogenados, se hincha con hidrocarburos alifáticos y aromáticos.

Polipropileno Resiste a: soluções aquosas de ácidos inorgânicos, ácidos orgânicos débeis, ácidos, álcool e óleos.

Não resiste a: oxidantes fortes, hidrocarbonetos halogenados, danifica-se com hidrocarbonetos alifáticos e aromáticos.

Polytetrafluoroehylene Resistant to all chemicals in this list.

Polytetrafluoroéthylene Résistant à tous les produits de la liste.

Politetrafluoroetileno Resistente a todos los productos de la lista.

Politetrafluoroetileno Resistente a todos os produtos da lista.

Chlorinated polyvinyl chloride Resistant: solutions of salts, acids and alkalis and organic compounds dissolved in water.

Not resistant to aromatic or chlorinated hydrocarbons.

Polychlorure de vinyle chloré Résiste aux: solutions d’acides, alcalis, sels et composés organiques dissous dans de l’eau.

Non résistant aux hydrocarbures aromatiques non chlorés.

Policloruro de vinilo clorinado Resiste a: soluciones de ácidos, álcalis, sales y compuestos orgánicos disueltos en agua.

No resistente a hidrocarburos aromáticos ni clorados.

Policloruro de vinil clorinado Resiste a: soluções de ácidos, álcalis, sais e componentes orgânicos dissolvidos em água.

Não resiste a hidrocarbonetos aromáticos nem a cloretos.

Unplasticised polyvinyl chloride Resistant: solutions of salts, acids and alkalis and organic compounds dissolved in water.

Not resistant to aromatic or chlorinated hydrocarbons.

Polychlorure de vinyle non plastifié Résiste aux: solutions d’acides, alcalis, sels et composés organiques dissous dans d.e l’eau

Non résistant aux hydrocarbures aromatiques non chlorés.

Policloruro de vinilo no plastificado Resiste a: soluciones de ácidos, álcalis, sales y compuestos orgánicos disueltos en agua.

No resiste a hidrocarburos aromáticos ni clorados.

Policloruro de vinil não plastificado Resiste a: soluções de ácidos, álcalis, sais e componentes orgânicos dissolvidos em água.

Não resiste a hidrocarbonetos aromáticos nem a cloretos.

Polyvinilidene fluoride Resistant to inorganic acids and bases, aliphatic and aromatic hydrocarbons, organic acids, alcohols, halogenated solvents and halogens except fluorine.

Not resistant to metallic hydroxides, strong basic primary amines, Polar or aprotic solvents and hot fuming concentrated acids.

Fluorure de polyvinilidene Résistant aux acides et bases non organiques, hydrocarbures aliphatiques et aromatiques, acides organiques, alcool, dissolvants et halogènes excepté le fluor.

Non résistant aux hydroxydes métalliques, bases fortes d’amine primaire, dissolvants polaires et aprotiques et acides concentrés émetteurs de vapeur chaude.

Polifluoruro de vinilideno Resistente a ácidos y bases inorgánicos, hidrocarburos alifáticos y aromáticos, ácidos orgánicos, alcoholes, disolventes halogenados y halógenos, excepto el fluor.

No resistente a hidróxidos metálicos, aminas primarias fuertemente básicas, disolventes polares o apróticos y ácidos concentrados calientes y humeantes.

Polifluoreto de vinilideno Resistente a ácidos e bases inorgânicos, hidrocarbonetos alifáticos e aromáticos, ácidos orgânáicos, lcoois, dissolventes halogenados e alógenos, excepto o flúor.

Não resistente a hidróxidos metálicos, aminas primárias fortemente básicas, dissolventes polares ou apróticos e ácidos concentrados quentes e fumegantes.

SYMBOL MATERIAL CHEMICAL RESISTANCE

MAX. TEMP. OF USE

(ºC)

Constant Short term

PVC-C 90 105

PVC-U 45 60

-10

-10

PP 80 100

PTFE®(Teflon )

250 300

-10

-260

NBR 90 120

PE-HD 60 80

-30

-40

EVA 45 -

FPM®(Viton )

150 200

-20

-20

ABS 70 -

EPDM 90 120

-40

-40

PVDF -40 140 -

STANDARDS NORME NORMATIVA NORMAS

This list has been made on the basis ofdifferent sources of information, among them the following standards:

UNE 53389 IN “Tubos y accesoriosde materiales plásticos. Tabla de clasificación de la resistencia química”.

ISO/TR 10358 “Plastics pipes andfittings; Combined Chemical resistance classification table”

ISO/TR 7620 “Chemical resistanceof rubber material”

Cette liste a été réalisée grâce à différentes sources d’information, nottament en se référant aux normes suivantes:




Esta lista ha sido realizada en base adiferentes fuentes de información,entre ellas las siguientes normas:




Esta lista foi realizada com base emdiferentes fontes de informação, entreelas as seguintes normas:

UNE 53389 IN “Tubos e acessóriosde materiais plásticos. Tabela declassificação da resistência química”.




CONCENTRATION CONCENTRATION CONCENTRACIÓN CONCENTRAÇÃO

Dil. Sol. Dilute aqueous solution at a concentration equal to or less than 10%.

Sol. Aqueous solution at a concentration higher than 10%, but no saturated.

Sat. Sol. Saturated aqueous solution,prepared at 20°C.

Sol. trab. Working solution of the concentration usually used in the industry concerned.

Susp. Solid suspension in a solutionsaturated at 20ºC.

Tg. At least of technical quality.

Tg-s. Technical quality, solid.

Tg-l. Technical quality, liquid.

Tg-g. Technical quality, gas.

The concentrations, unless it is said the opposite, are expressed like percentage in mass to 20ºC.

Dil. Sol. Solution aqueuse diluée de concentration égale ou inférieure à 10%.

Sol. Solution aqueuse de concentration superieure à 10% mais non saturée.

Sat. Sol. Solution aqueuse saturée, préparée à 20°C.

Sol. trab. Solution de travail ayant la concentration habituelle aux utilisations industrielle.

Susp. Suspenssion de solides dansune solucion saturée a 20°C.

Tg. Au moins de la qualité technique.

Tg-s. Qualité technique, solide

Tg-l. Qualité technique, liquide.

Tg-g. Qualité technique, gaz.

Les concentrations, sauf qu’il soit précisé le contraire, sont exprimées enpourcentage de la masse a 20°C.

Dil. Sol. Solución acuosa diluida a una concentración igual o menor de 10%.

Sol. Solución acuosa de una concentración superior a 10%, pero no saturada.

Sat. Sol. Solución acuosa saturada, preparada a 20°C.

Sol. trab. Solución de trabajo de concentración habitual empleada en la industria.

Susp. Suspensión de sólidos en una solución saturada a 20ºC.

Tg. Mínimo de calidad técnica.

Tg-s. Calidad técnica, sólido.

Tg-l. Calidad técnica, líquido.

Tg-g. Calidad técnica, gas.

Las concentraciones, excepto que se diga lo contrario, están expresadas como porcentaje en masa a 20ºC.

Dil. Sol. Solução aquosa diluída a uma concentraçaão igual ou menor de 10%.

Sol. Solução aquosa de uma concentração superior a 10%, mas não saturada.

Sat. Sol. Solução aquosa saturada, preparada a 20°C.

Sol. trab. Solução de trabalho de concentração habitual empregue na indústria.

Susp. Suspensão de sólidos e uma solução saturada a 20ºC.

Tg. Mínimo de qualidade técnica.

Tg-s. Qualidade técnica, sólido.

Tg-l. Qualidade técnicas, líquido.

Tg-g. Qualidade técnicas, gás.

As concentrações, excepto as que sejam descriminadas em contrário, estão expressas como percentagem em massa a 20ºC.

COMPRESIBLE MEDIAMILIEUXCOMPRESSIBLES

MEDIOSCOMPRIMIBLES

AMBIENTESCOMPRIMIDOS

When we work with a low boiling pointfluid, as are the case of liquefied gases or gases dissolved in liquids, it must be considered the vapor pressure of the media.

In addition, the gas loosening (due to changes in media) or the vaporization (caused by excess of pressure) have to be prevented by limiting the working temperature and the overpressures. It must be considered that in these cases that cause gas flights, we will be in dangerous conditions of work.

Quand nous nous rencontrons avec des fluides avec un faible point d’ébullition, comme c’est le cas des gaz liquéfiés ou des gaz dissous dans des liquides, il faut tenir compte de la pression de vapeur du milieu.

De plus, le dégagement de gaz (dû a des changements dans le milieu) ou la vaporisation (provoquée par excès de pression) doivent être prévenus en limitant la température de travail et les surpressions. Il faut surtout tenir en compte que dans ces cas qui provoquent des fuites de gaz, nous seront dans des conditions de travail dangereuses.

Cuando nos encontramos con fluidos con un bajo punto de ebullición, como es el caso de los gases licuados o gases disueltos en líquidos, se tiene que tener en cuenta la presión de vapor del medio.

Además, el desprendimiento de gas (Debido a cambios en el medio) o la vaporización (provocada por exceso de presión) se deben prevenir limitando la temperatura de trabajo y las sobrepresiones. Se debe tener muy en cuenta que en estos casos que provocan fugas de gases, estaremos en condiciones de trabajo peligrosas.

Quando nos encontramos com flúidoscom um baixo ponto de ebulição, como é o caso dos gases líquidos e gases dissolvidos em líquidos, tem que se ter em conta a pressão de vapor do ambiente.

Além disso o, desprendimento de gases (devido ao desgaste do meio ambiente), ou a vaporização (provocada por excesso de pressão) devem ser evitadas, limitando a temperatura de trabalho e as sobrepressões. Devese ter muito em conta que são estes casos que provocam fugas de gases, e como tal estaremos em condições de trabalho potencialmente perigosas.

EXCLUSION OFRESPONSABILITY

EXCLUSION DERESPONSABILITÉ

EXCLUSIÓN DERESPONSABILIDAD

EXCLUSÃO DERESPONSABILIDADES

The information in this section has been supplied by sources that, we think, are trustworthy. However, it is provided without no guarantee, express or implicit, of its exactitude.

The conditions or methods of manipulation, storage or use of the material are out of our control and/or knowledge. By this and other reasons, we did not assume responsibility and we resigned specifically to the obligations of damages caused or related to the information expressed here.

L’information contenue dans ce paragraphe à été obtenue de sources supposées fiables. Cependant, l’information est fournie sans aucune garantie expresse ou implicite, en ce qui concerne son exactitude.

Les conditions ou méthodes de manipulation, de stockage ou d’utilisation du matériel sont en dehors de notre contrôle et/ou de notre connaissance. Pour cette raison et pour d’autres motifs, nous n’assumons aucune responsabilité en ce qui concerne les dégats causées en relation avec l’information mentionnée ci-contre.

La información de este apartado la hemos obtenido de fuentes que, pensamos, son fiables. No obstante, la información se proporciona sin ninguna garantía, expresa o implícita, en lo que se refiere a su exactitud.

Las condiciones o métodos de manipulación, almacenaje o uso del material están fuera de nuestro controly/o conocimiento. Por este y otros motivos, no asumimos responsabilidad y renunciamos expresamente a las obligaciones de daños causados o relacionados con la información aquí expresada.

Esta informação e estes documentos foram obtidos de fontes, que pensamos serem fiáveis. No entanto a informação é apresentada sem nenhuma garantia expressa ou implicita, no que se refere à sua exactidão.

As condições e os métodos de manipulação, manuseamento e uso deste material estão fora do nosso controlo ou conhecimento. Por este e outros motivos, não assumimos responsabilidade e renunciamos expressamente as obrigações de danos causados e relacionados com a informação aqui expressada.


Aceite de Ricino Castor Oil Huile de Ricin 100 20 N68 N

Aceite de Alcanfor Camphor Oil Huile de Camphre Tg-L 20 N R R N N N N68Aceite de Almendras Oil of Almonds Huile des Amandes Tg-L 20 R N68Aceite de Cacahuete Peanut Oil Huile d'Arachide Sol. trab. 20 N R R R R R N68Aceite de Coco Coconut Oil Huile de Noix de Coco Sol. trab. 20 R N68Aceite de Hígado de Bacalao Oil of Codfish Liver Huile de Foie de Morues Sol. trab. 50 N R122

20 68 N R R N

40 104 R R

60 140 R L

20 68 R R R N R

60 140 R R R N

20 68 R R R N R60 140 R R L N

Aceite de Menta Mint Oil Huile de Menthe Sol. trab. 20 68 R N

20 68 N R R R R N R

60 140 R R R R

80 176 R

20 68 N R R R R

40 104 R L R

60 140 R L L

80 176 L

20 68 N N R R R R N R50 122 N R R N R

60 140 R R N

20 68 R R R R R R

60 140 R R R R

100 212 R

20 68 R R N

60 140 L

20 68 N R L R N

60 140 R

20 68 N R R R40 104 R R

60 140 R L80 176 L20 68 L N R R R R R40 104 N R R L R60 140 R R L R80 176 R R20 68 N R R R R N60 140 R R L R20 68 N R R N R N N N40 104 R R60 140 R L L80 176 R N20 68 N R L N R N N N40 104 L N60 140 N L20 68 R50 122 R20 68 N L N N R L N N N60 140 L N N20 68 R R R R R40 104 R R L R R60 140 R R R R80 176 L R20 68 R L N L N N N40 104 N N60 140 N20 68 N R N N R L N N N60 140 N N N N20 68 N N R N N N

60 140 R N20 68 R40 104 R

20 68 R R R R R

60 140 R R R20 68 R R R R R50 122 R R R R R

60 140 R R R R

93 200 R20 68 R R R R R R R R R

50 122 R R R R R R R R R60 140 R R R R R R R

93 200 R

20 68 R N R

60 140 R R

93 200 R20 68 R N R R R R R

40 104 R R R R

60 140 R R R R93 200 R R

Acetato de Vinilo Vinyl Acetate Acétate de Vyny CH COOCH=CHle T3 2 g-L 20 68 R N N N N N

20 68 R N N N

60 140 L N

20 68 R L N40 104 R L

60 140 R N

20 68 N R N N L R N N N60 140 R L

Aceite de La Palma Palm Oil Huile de Palme

Aceite de Linaza Linseed Oil Huile de Lin

Aceite de Maiz Corn Oil Huile de Maïs

Aceite de Oliva Olive Oil Huile d'Olive

R N

Sol. trab.

Sol. trab.

Sol. trab.

Aceite de Parafina

Cottonseed Oil Huile de Coton

Tg-LParafin Oil Huile de Parafine

Aceite de Semillas de Algodón Sol. trab.

Aceite de Silicona Huile de Silicone

Aceite de Trementina

Tg-LSilicone Oil

Aceite de Soja Soybean Oil Huile de Soja Sol. trab.

Turpentine Oil

Tg-L

Huile de Térébenthine

Lubricating OilAceites Lubricantes Huile de Graissage

Mineral OilAceites Minerales Huiles Minérales

Oil and FatsAceites y Grasas Huile et Graisses

Sol. trab.

Tg-L

40

CH CHOAcetaldehido Acetaldehyde Acétaldéhyde 3

Tg-L

CH CONHAcetamida Acetamide Acétamide 53 2

Tg-L

Ammonium AcetateAcetato de Amonio Acetate d'Ammonium NH (C H O )4 2 3 2

CH COOC HAcetato de Amilo Amyl Acetate Acétate d'Amyle 3 5 11

Sol. sat.

CH COOCH(CH )C HAcetato de Butilo Butyl Acetate 3 3 2 5

CH COOC HAcetato de Etilo Tg-L3 2 5

Acétate de Butyle

Methyl Acetate Acetate de Methyl

Ethyl Acetate Acétate d'Éthyl

Tg-L

Tg-L

CH CO CHAcetato de Metilo 3 2 3

Acetato de Níquel Nickel Acetate Acetate de Nickel Ni(OOC H ) ·4H O2 3 2 2 Sol. sat.

Sol. sat.

Sol. dil.

Sol. sat.

Pb(C H O ) ·3H O2 3 2 2 2

AgC H OSilver Acetate 2 3 2

Potassium Acetate Acétate de Potassium

Acetato de Plata Acetate d'Argent

Lead Acetate

Acetato de Potassio

Acetato de Sodio Sodium Acetate Sodium Acetate

Acetato de Plomo Acétate de Plomb

CH COONa3

Sol. sat.

Sol. sat.

CH COOK3

Tg-S

10%

C H COCHAcetofenona Acetophenone Acétophénone 6 5 3

CH COCHAcetona Acetone Acétone 3 3

Tg-L

PRODUCTO PRODUCT PRODUIT FORM. CONC.

TEMP.

ºC ºF

EV

A

EP

DM

FP

M

N

BR

H

DP

E

P

P

P

VC

-U

P

VC

-C

A

BS


20 68 R L R R R R R R

40 104 R N L50 122 L R R

60 140 R R R R

100 212 R

20 68 R R R R N

50 122 R N

60 140 R L R

20 68 R L N R R R R N

60 140 R L R

80 176 R

100 212 L20 68 R R R N

60 140 L

80 20 68 R N20 68 L

40 104 N

20 68 R L N R R N N

50 122 R N

60 140 L L N100 212 N

Acido Acetico Trifloruro Trifluoro Acetic Acid Trifluorure Acide Acetiq F C-COOHue 3 Hasta 50 20 68 L N NAcido Acrilico Metil Ester Acrylic Acid Methyl Ester Acide Acrylique Méthy CH =CHCOOCHlester T2 3 g-L 20 68 L N

20 68 R R R R R R R

60 140 R R R R R L R

80 176 R

93 200 LÁcido Antraquinona Sulfónico Anthraquinone Sulfonic Acid Acide Antraquinone Sulfoniq C H O ·SO ·3H Oue 14 7 2 3 2 Susp. 60 140 R

20 68 R R R R

50 122 R R

60 140 R L

20 68 R R R60 140 R R R

80 176 R R L100 212 R20 68 R40 104 R20 68 L R R N R R L R R40 104 L R R R R N R60 140 R R R N80 176 L20 68 R R R R R R R R40 104 R R R R R R50 122 R R R R R R60 140 R R R R L80 176 R R100 212 R20 68 R R R R R50 122 R R R R60 140 R R93 200 R20 68 R R R40 104 R R60 140 R L20 68 N R R L R R R R40 104 R R N R L R60 140 L R R L L80 176 N L100 212 N N20 68 R R60 140 R

Ácido Brómico Bromic Acid Acide Bromique HBrO 103 20 68 R

< 1 80 176 R20 68 R L N60 140 N

20 68 L L N R N N N

60 140 L20 68 R R60 140 R R

20 68 R R L R

40 104 L L N R93 200 R

20 68 R R R R R R R R40 104 R R R R R R R R R60 140 R R L R R R R93 200 R R20 68 R R L R R R R R

40 104 R R N R R R R R

60 140 R R R R R R

80 176 R R R

100 212 R R N20 68 R R R R R R R

50 122 R R R R R R

60 140 R R R L R80 176 R R R

100 212 R R N

20 68 R R N R R R R R

40 104 R R R R R

60 140 L R R L R80 176 R L R

20 68 L R N R R R R L

40 104 L L R R R N60 140 N R R R

80 176 R R

20 68 R R L R N50 122 R R N R N

60 140 R R R20 68 R R L R N

50 122 R R N R N

60 140 R R R20 68 R N N R N R

60 140 R20 68 R N N L N

40

Ácido Acético Acetic Acid Acide Acétique

Acetic Acid Glacial

104 R

CH COOHÁcido Acético Glacial Acide Acétique Glacial 3

COOH(CH ) COOH2 4

60

95

CH COOH3

>96

Hasta 10

10 a 40

50

Ácido Adípico Adipic Acid Acide Adipique

Ácido Arsénico

Ácido Benzenosulfonico

C H COOHÁcido Benzoico 6 5

C6H5SO3H

Sol. sat. (1,4%)

H ASO ·½H OArsenic Acid Acide Arsénique 3 4 2

Sol. sat.

80

Tg-LBenzenesulfonic Acid

Sol. sat.

Acide Benzenesulfonique

Benzoic Acid

Boric Acid Acide Borique

Acide Benzoïque

Sol. dil.

H BOÁcido Bórico 3 3

Sol. sat.

Hydrobromic AcidÁcido Bromhídrico Acide Bromhydrique HBr

Hasta 20

50

Tg-G

20

H CO2 3

CH CH CH COOHÁcido Butírico Butyric Acid Acide Butyrique 3 2 2

Tg-L

Carbonic Acid

C H OÁcido Cítrico Sol. sat.6 8 7

Acido Carbonico Acide Carbonique

10

Tg-L

Citric Acid Acide Citrique

10

20

30

36 (Conc.)

Hydrochloric Acid, Gas Dry

Ácido Clorhídrico* HCl

Hydrochloric Acid, Gas Wet

Tg-G

Hydrochloric Acid*

Ácido Clorhídrico, Gas Húmedo Acide Chlorhydrique HCl

Acide Chlorhydrique*

Chloric Acid Acide Chlorique

Tg-G

Ácido Clorico

Ácido Clorhídrico, Gas Seco Acide Chlorhydrique HCl

HClO3

10

20


TEMP.

ºC ºF

EV

A

EP

DM

FP

M

N

BR

H

DP

E

P

P

P

VC

-U

P

VC

-C

A

BS


20 68 R R R R

60 140 R L R80 176 R

100 212 L

20 68 L N N R100 212

Ácido Clorosulfónico Chlorosulfonic Acid Acide Chlorosulfonique ClSO OH2 Tg-S 20 68 N N N N N L N N

20 68 R R L R

60 140 R R R

20 68 R R L N

60 140 R R N

20 68 R N R R N

40 104 R

60 140 L

20 68 R R L

50 122 R N

80 176 R

20 68 N L R N R R R R

40 104 N L R R N

60 140 L R L L L R

100 212 N N20 68 R L N

40 104 R L

60 140 R N

20 68 R L N L N N

40 104 R N

60 140 R N

20 68 R N N N

40 104 R60 140 L

Sol. dil. 60 140 RSol. sat. 20 68 R

20 68 R60 140 L

30 20 68 R L RAcido Dioctil Ester Ftalico Phtalic Acid Dioctyl Ester Acide Phtalique Diocty C H Ol Ester 2024 38 4 68 R N N

20 68 R R R40 104 R R R60 140 L L L

Ácido Fluobórico (Dec a 130ºC) Fluoroboric Acid Acide Fluoboriq HBFue T4 g-S 20 68 R<3 20 68 R

20 68 R R R R50 122 N60 140 R R20 68 N R N R L40 104 R60 140 L N20 68 L60 140 L20 68 R L N60 140 L N20 68 L60 140 N20 68 R R50 122 R60 140 R20 68 R R R50 122 R N60 140 R R80 176 R

20 68 R R L L R R R50 122 R N R R60 140 R R

80 176 R

20 68 R R R60 140 R R20 68 R R R R R

60 140 R R R R

80 176 R100 212 L N20 68 R R

60 140 R R

80 176 R

20 68 R R R L R50 122 R L R

20 68 R R N R R R L N

40 104 R R L60 140 L L R L N

80 176 N N

20 68 R R N R R L N

50 122 N N

60 140 R R N N80 176 L N

20 68 R R L R

40 104 R R L R60 140 L R N R

80 176 R R

100 212 R

20 68 R R N R R R R R

50 122 L R R R60 140 R R R R

80 176 R R100 212 L R

20 68 R R R N R R R R

50 122 R R R R R60 140 L R R R

80 176 R R

100 212 L R20 68 R N N R R

40 104 L

50 122 R20 68 R

50 122 R

Sol. sat.

Ácido Cloroacético

50

CH ClCOOHChloroacetic Acid Acide Chloroacétique 2

C H OAcide Crésylique 7 8 Sol. sat.

Ácido Crómico Chromic Acid Acide Cromique

50

Tg-L

Sol. sat.

H CrO2 4

Tg-L

10

40

Dichloracetic Acid C H Cl OÁcido Dicloroácetico Acide Dichloracetic 2 2 2 2

Dichloroacetic Acid Methyl Ester

O(CH COOH)2 2

Cl CHCOOCHAcido Dicloroacetico Metil Ester Acide Dichloracetique Ou Methyl 2 3

Diglycol Acid

Tg-L

Acide Diglycolique

Stearic Acid Acide Stéarique

Ácido Diglicólico18

C H COOHAcido Esteárico 17 35

Hydrofluoric Acid*Ácido Fluorhídrico* Acide Fluorhydrique* HF

Hasta 10

40

48

60

Hydrfluoric Acid, Gas

40

Ácido Fluorhídrico, Gas Acide Fluorhydrique, Gas HF

Ácido Fórmico HCOOH

Tg-G

Fluorosilicic Acid

Sol. sat.

H SiFÁcido Fluosilícico Acide Fluosilicique 2 6

25

32

10

25

40

50

85 a Tg-L

Phosphoric Acid

Hasta 30

H POÁcido Fosfórico Acide Phosphorique 3 4 Hasta 50

Formic Acid Acide Formique

hasta 85

C H (COOH)Ácido Ftálico Phtalic Acid Acide Phtalique 6 5 2

(HO) C H CO HAcido Gálico Gallic Acid Acide Galique 3 6 2 2

Susp.

Sol. sat.

50%Ácido Cresílico Cresylic Acid


TEMP.

ºC ºF

EV

A

EP

DM

FP

M

N

BR

H

DP

E

P

P

P

VC

-U

P

VC

-C

A

BS


20 68 R R

60 140 R R

20 68 R R R

50 122 R

60 140 R

37 20 68 R R

20 68 R

60 140 R

20 68 R N R R R R

40 104 L R

60 140 L L R R L R

80 176 N L R93 200 R

20 68 R R R

60 140 R R R

93 200 R

20 68 R R R L R

60 140 R R R N L

20 68 R L

60 140 R N

20 68 R R N R R R

50 122 R60 140 R R R L

80 176 N

50 80 176 R

20 68 R R R

60 140 R R R R

20 68 R R R

60 140 R R R

20 68 R

80 176 R

20 68 R60 140 R

20 68 L N R60 140 R20 68 R R R R50 122 R60 140 R R20 68 R R N R R R R R40 104 R R R N60 140 L L R R80 176 N20 68 R R R R R50 122 R N60 140 R N R80 176 R20 68 R R R R L50 122 R N60 140 R N R80 158 L20 68 R R R R N50 122 R N60 140 R N R20 68 L R R R N50 122 L R N60 140 N L20 68 L R R N50 122 L R N20 68 L R R N R R N50 122 L R R R N60 140 L L L80 176 N20 68 L R R N

50 122 L L R N

20 68 N R N L L N R N45 113 L R N

60 140 N N N N L20 68 N N R N

40 104 R N

60 140 N N LÁcido Nítrico, Fumante Nitric Acid, Fuming Acide Nitrique HNO ·NO3 X 20 68 N N N NAcido Nitrilo-Triacetico Nitrilotriacetic Acid Acide Nitriloacetique N(CH -COOH) 202 3 68 RAcido Nitroso Nitrous Acid Acide Nitreux HNO 202 68 R R

20 68 N N R L R R R R R

40 104 L N

50 122 N R L60 140 N R L R R

80 176 L

100 212 N

20 68 R R R

60 140 L R20 68 R R R L R R R

40 104 R N R

50 122 R R60 140 L R L R R

80 176 N L

100 212 N

20 68 L R L

40 104 L N60 140 N

20 68 R R N R R

40 104 L R60 140 R L

80 176 L

20 20 68 R20 68 N R N L

40 104 R60 140 R N

80 176 L20 68 L R R L R R R N

40 104 L R R N R N

60 140 R R

Sol.

30Glycolic Acid

Hypochlorous Acid Sol. sat.

OHCH COOHÁcido Glicólico Acide Glycolique 2

Ácido Hipocloroso Acide Hypocloreux HOCl

Ácido Maleico (Dec. a 160ºC) HOOCCH=CHCOOH

10

25

10 a 85

CH CHOHCOOHÁcido Láctico Lactic Acid Acide Lactique 3

Tg-L

Sol. sat.

CH O S4 3

C H OÁcido Málico (Subl.) 4 6 5

Ácido Metilsulfónico (Dec.) Acide Methylsulfonique Tg-L

Maleic Acid Acide Maléique

Malic Acid Acide Malique

Acid Methylsulfonic

25

Nicotinic Acid

30

Acide Nicotinique

Nitric Acid* Acide Nitrique*

Sol. sat.

Sol.

Ácido Nicotínico CsH NCOOH4

85

> 85

Monochloroacetic Acid

Susp.

CH ClCOOHÁcido Monocloroacético Acide Monochloroacetique 2

Ácido Nítrico*

Sol. sat.

5

HNO3

10

20

35

40

Hasta 45

50

Ácido Oxálico (Subl.) HOOCCOOH

Tg-L

> 50

CH (CH ) CH(CH ) COOHÁcido Oleico Oleic Acid Acide Oléique 3 2 7 2 7 Tg-L

Sol. dil.

Oxalic Acid Acide Oxalique

C H COOHAcido Palmitico Palmitic Acid 15 31Acide Palmitique

Ácido Perclórico Acide PerchloriquePerchloric Acid

Picric Acid Acide Picrique 10

10

70

HClO4

C H (NO ) OHÁcido Pícrico 6 2 2 3


TEMP.

ºC ºF

EV

A

EP

DM

FP

M

N

BR

H

DP

E

P

P

P

VC

-U

P

VC

-C

A

BS


<2 80 176 R

20 68 R R N R L N

40 104 R R L

60 140 L R L

> 50 20 68 R L N

20 68 R R N R N N

40 104 L R

60 140 R L

80 176 L

20 68 R R R R R R R R

40 104 R R

60 140 R R

20 68 R R R

40 104 R

50 122 R R20 68 R R R

40 104 R R R

60 140 R R R

80 176 R

20 68 R R R R R

50 122 R R

60 140 R R R R

80 176 R

100 212 R N

20 68 R R R R R

50 122 R R

60 140 R R R

80 176 R

20 68 R R R R R

60 140 R R R R

80 176 R

20 68 R L R40 104 R R N R

60 140 R R R80 176 L L R20 68 R R R R R60 140 R R R80 176 R20 68 R R N R R R R R40 104 R R R L60 140 L R R L R R80 176 N L R20 68 N R R R60 140 N R L R80 176 R20 68 L R N R R N40 104 L R R N60 140 N L L R80 176 N R20 68 N R N R40 104 R R60 140 R75 167 R20 68 L R N50 122 R N60 140 N L65 149 N20 68 N N R N R L R N40 104 R50 122 N R N60 140 L N R65 149 N

20 68 N L N R L N R N40 104 R50 122 N N N R

60 140 N

20 68 N L N N

50 122 N60 140 N N N

Ácido Sulfúrico Fumante (Oleum) H SOOléum Oléum 202 4 68 N N N N N N L N

20 68 R R N40 104 N R

60 140 L80 176 N

20 68 R R R R R

50 122 R R

60 140 R R

20 68 R R R R R R R50 122 R60 140 R R R

20 68 R R R R R R R R

40 104 R R R

50 122 R

60 140 R R L R R R20 68 R R R R R

50 122 R R R R

20 68 L N N R R40 104 R

60 140 RTg-L 20 68 L N N

Ácido Úrico (Dec. a >400ºC) Uric Acid Acide Uriq C H N Oue 205 4 4 3 68 R RAcidos Grasos > C6 Fatty Acids > C6 Acides Gras R-COOH 20 68 R R LAcrilato de Etilo Ethyl Acrylate Acrylate d'Ethy CH =CHCOOC Hl T2 2 5 g-L 20 68 N N

20 68 R L N R N40 104 R L

50 122 N

60 140 L N20 68 R R R R R

50 122 R R60 140 R R R R

80 176 R93 200 R R

20 68 N R N R

93

CH CH COOHÁcido Propiónico Propionic Acid 3 2

C H (OH)(COOH)Ácido Salicílico Salicylic Acid Acide Salicilique 6 4

200 R

Acide Propionique

50

Tg-L

Sol. sat.

Susp.Silicic Acid Acide Silicique

Succinic Acid Sol.Acide Succinique

SiO ·nH O2 2

Acido Succinico

Ácido Silícico

HOOC-CH -CH -COOH2 2

Sulfuric Acid*

Hasta 10

H SOÁcido Sulfúrico* Acide Sulfurique* 2 4

15

10 a 30

Hasta 40

98

10 a 50

50

50 a 75

Hasta 80

86

95

96

Fumante

H SOÁcido Sulfuroso Sulfurous Acid Acide Sulfureaux 2 3

Sol. sat.

Hasta 30

C H OÁcido Tánico Acide Tanique Sol.76 52 46

Sol.HOOC(CHOH) COOHÁcido Tartárico 2

Tannic Acid

Sol. sat.

Trichloroacetic Acid Acide Trichloroacetique

Tartaric Acid Acide Tartaric

Hasta 50CCl COOHÁcido Tricloroacético 3

H C=CHCNAcrilonitrilo Acrylonitrile Acrylonitrile 2

H OAgua 2

Tg-L

Agua de Bromo Bromine Water Eau de Brome

Water Eau

Sol. sat.


TEMP.

ºC ºF

EV

A

EP

DM

FP

M

N

BR

H

DP

E

P

P

P

VC

-U

P

VC

-C

A

BS


20 68 L L N L R R R

50 122 R R

60 140 N L R

93 200 R

20 68 N L N N N N R N50 122 N

20 68 R R R R R

50 122 R R

60 140 R R R R

93 200 R

100 212 R N

20 68 R R R R R R R50 122 R R R R R

60 140 L R R R R R R

80 176 N R R R R90 194 R R R R

100 212 R

20 68 R R R R R

50 122 R R

60 140 R R R R

80 176 R

100 212 R20 68 R R R R R R R

40 104 R R

50 122 R R

60 140 R R R R R R R

80 176 R R R R

100 212 R R R L

20 68 R R R R R R R

40 104 R R R

50 122 R R

60 140 L R R R R R R80 176 R L R

100 212 R R20 68 R R R R R50 122 R R60 140 R R R R100 212 R20 68 L L R R R L N40 104 L N R60 140 L R R R N80 176 N R20 68 R L R R R R L N60 140 R R L R L100 212 R20 68 N R N R N N50 122 L N N20 68 R R R40 104 R R R60 140 R R R20 68 L N N R N N60 140 L N20 68 R L L50 122 N60 140 R20 68 R R R R R60 140 R R R100 212 R20 68 R R R N50 122 R R N60 140 L R R80 176 L R

>10 L

20 68 L R R R R N N

50 122 L R N N60 140 R L R R L N

20 68 R R R R R50 122 R R

60 140 R R R R

80 176 R100 212 L20 68 R R R

40 104 R R R

60 140 R R R

80 176 R R

100 212 R20 68 R R R R R

50 122 R R60 140 R R R R

20 68 R R R R R R N N

40 104 L

50 122 N N60 140 R R N

20 68 R R L N

60 140 R N20 68 L N N R R N N N

60 140 L N

20 68 L N L N R R N N N

50 122 N L N N

60 140 L L R N N20 68 R R R R R

50 122 R R60 140 R R R R

20 68 R R R R R R

50 122 R R R60 140 R R R R R

20 68 R R

60 140 R R20 68 N N R L L L N N N60 140 L N N20 68 R R N N N

60 140 R L N N

Sol. sat.

Agua Regia Aqua Regia Aqua Regia

Agua de Cloro Chlorinated Water Eau de Chlore

HCl/HNO3=3/1

H OAgua, de Mar Water, Sea Eau de Mer 2

H OAgua, Destilada Water, Distilled Eau Distillée 2

H OAgua, Dulce Water, Candy Eau, Sucrerie 2

H OAgua, Mineral Mineral Water Eau Minérale 2

H OAgua, Potable 2

Sol. trab.

Sol. trab.

Aire Air Air

Water, Potable Eau Potable

Tg-G

Tg-L

C H OHAlcohol Amílico Amyl Alcohol Alcool Amylique 5 11

CH =CHCH OHAlcohol Alílico Allyl Alcohol Alcool Allylique 2 2

Tg-L

C H CH OHAlcohol Bencílico Benzyl Alcohol 6 5 2

C H OHAlcohol de Cera 31 63

Alcool Benzylique

Furfuryl Alcohol Alcool Furfurylique

Wax Alcohol Alcool de Cire

Tg-L

Tg-L

C H OAlcohol Furfurílico 5 6 2

Isobutyl Alcohol

(CH ) CHOHAlcohol Isopropílico 3 2

(CH ) CHCH OHAlcohol Isobutílico Alcool Isobutylique 3 2 2 Tg-L

Sol.

Methyl Alcohol

Sol. sat.

Méthylique Alcool

Tg-L

KCr(SO )4 2

< 10

Isopropyl Alcohol

CH OHAlcohol Metílico 3

Tg-L

Alcool Isopropylique

Chrome Alum

Amoníaco, Acuoso Ammonia, Aqueous Ammoniac Sol. sat.

Alumbre de Cromo Alun de Chrome

NH3

Tg-G

Ammonia LiquidAmoníaco, Líquido Ammoniac, Liquide

Amoníaco, Gas Seco Ammonia Gas Ammoniac, Gaz

NH Tg-G3

NH3

(CH CO) OAnhídrido Acético 3 2

C H NHAnilina 6 5 2

Acetic Anhydride

Tg-l

Anhydrique Acétique

Sodium Antimoniate

Aniline Aniline

Antimoniate de Sodium

Tg-L

Sol. sat.Antimoniato de Sodio

Sodium Arsenite Sol. sat.Arsenito de Sodio Arsenite Sodique Na AsO3 3

C H CHO6 5

C H OAzúcar, Sol. Acuosa Sugar Sucre Sol.6 12 6

C HBenceno Benzene Benzène Tg-L6 6

Benzaldheído Benzaldehyde Benzaldéhyde Tg-L


TEMP.

ºC ºF

EV

A

EP

DM

FP

M

N

BR

H

DP

E

P

P

P

VC

-U

P

VC

-C

A

BS


20 68 R R R R R

40 104 L R R R

60 140 R R R

80 176 L R

20 68 R R R

60 140 L R

20 68 R R R R R R R R

50 122 R R R R

60 140 R R R R R

93 200 R

100 212 R

20 68 R R R R R R R R40 104 R R

50 122 R R R

60 140 R R R R R R R80 176 R R R

100 212 R

20 68 R

60 140 R

20 68 R R R R R R

50 122 R R R

60 140 R R R R R80 176 R R

93 200 R

20 68 R R R R R R R

40 104 R R R

50 122 R R

60 140 R R R R R R

93 200 R

20 68 R R R

40 104 L R L

60 140 R N93 200 R

20 68 R R N R R50 122 R R93 200 R R20 68 R L L R40 104 L N N R60 140 N R20 68 R R50 122 R R20 68 R R R R40 104 R R R60 140 R R R20 68 R R R R R50 122 R R60 140 R R R R20 68 R R R R40 104 R R R50 122 R R60 140 R R R20 68 R R R R R R R40 104 R R R50 122 R R60 140 R R R R R R R80 176 R R R20 68 R R R R R R50 122 R R R60 140 R R L R80 176 R93 200 R20 68 R R R R R R50 122 R R R R R

60 140 R R R R R

80 176 R R R100 212 R

20 68 R R R R R R50 122 R R R

60 140 R R R R

93 200 R20 68 R R R R40 104 R L R

60 140 R N R

20 68 N R N N N N N N

60 140 N N N NBromo, Líqu. Bromine Liquid Brome, Liq Bruide T2 g-L 20 68 N R N N N N N N

C H BrBromobenzeno Bromobenzene Bromobenzène 6 5 20 68 R N

20 68 N N

60 140 N20 68 R R R R

50 122 R

60 140 R R R100 212 R

20 68 R R R R

40 104 R R

50 122 R R

60 140 R R20 68 N

60 140 NBromuro de Litio Lithium Bromide Bromure de Lithium LiBr 20 68 R R RBromuro de Metil Methyl Bromide Methy CH Brl Bromure T3 g-G 20 68 L N N

20 68 R R R R R R R R R

50 122 R R R R R R60 140 R R R R R R R

80 176 R L R

100 212 R L20 68 R R R R R R R R

40 104 R L R50 122 R R60 140 R R R R R80 176 R

Sodium Benzoate

KHCOBicarbonato de Potasio 3

R

C H COONaBenzoato de Sodio Benzoate de Sodium 6 5

Sol. sat.

35

Sol. sat.

Sodium BicarbonateBicarbonato de Sodio Bicarbonate de Sodium

Potassium Bicarbonate

NaHCO Sol. sat.3

Bicarbonate de Potassium

Ammonium Bifluoride

KHSOBisulfato de Potasio 4

Bifluoruro de Amonio Bifluorure d'Ammonium NH HF Sol. sat.4 2

Sol. sat.Potassium Bisulfate

Sol. sat.

Sodium Bisulfate

Bisulfate de Potassium

Calcium BisulfideBisulfuro de Calcio Bisulfite de Calcium

Bisulfato de Sodio Bisulfate de Sodium

Sol. sat.Ca(HS) ·6H O2 2

NaHSO4

10

Sodium BisulphiteBisulfito de Sodio Bisulfite de Sodium

Borato de Potasio Potassium Borate

Borato de Sodio

Borate de Potassium

Sol.

Sol. sat.

Tg-L

Na BO3 3 Sol. sat.

NaHSO3

1

K BO3 310

Sol. sat.

Borax

Sodium Borate Borate de Sodium

NaB O ·10H OBorax Borax 4 7 2

Potassium Bromate

Sodium Bromate Tg-LBromate de Sodium

Sol. sat.

Hasta 10

KBrO3

Bromato de Sodio

Bromato de Potasio Bromate de Potassium

NaBrO3

Tg-G

C H BrBromoetano Bromoethane Bromoethane 2 5

BrBromo, Gas Bromine Gas Brome, Gaz 2

Tg-L

Bromuro de Calcio

Bromuro de Bario

CaBr2

BaBrBarium Bromure 2

Sol. sat.

Bromure de Barium

Ethylene Bromide Bromure d'Ethylene

Calcium Bromide

Tg-L

Bromure de Calcium

Sol. sat.

Bromuro de Etileno BrCH CH Br2 2

Bromuro de Sodio

Potassium Bromide

NaBr

Bromuro de Potasio Bromure de Potassium KBr Sol. sat.

Sodium Bromide Sol. sat.Bromure de Sodium


TEMP.

ºC ºF

EV

A

EP

DM

FP

M

N

BR

H

DP

E

P

P

P

VC

-U

P

VC

-C

A

BS


20 68 N L N R R

60 140 R20 68 N R R R R R R R

50 122 R

60 140 R R20 68 R R R R N

40 104 R R R

50 122 R R R RButilfenoles Butyl Phenol Butylp C H C H OHhénol 4 9 6 4 Sol. sat. 20 68 N L N R N N

20 68 R R

50 122 N

20 68 R R R

40 104 R R R

60 140 R R R

80 176 R R

20 68 R R R R R

50 122 R R

60 140 R R R

20 68 R R R R R R R R R

40 104 R R R R

50 122 R R R

60 140 R R R R R93 200 R R

20 68 R R R R R

50 122 R R

60 140 R R R

20 68 R R R R R R R

50 122 R R R R R R R

60 140 R R R R R R

80 176 R R R

93 200 R R

20 68 R R R R R R50 122 R R R

60 140 R R R R93 200 R R20 68 R R R R R R R R40 104 R R R50 122 R R R60 140 R R R R80 176 R93 200 R20 68 R R R R R R R R R40 104 R R R R50 122 R R R60 140 R R R R R R R80 176 R R93 200 R20 68 R R R R R50 122 R R60 140 R R R R80 176 R93 200 R20 68 R R R R R50 122 R R60 140 R R R R80 176 R93 200 R20 68 R R R R R50 122 R R60 140 R R R R93 200 R20 68 R R R R R R R

50 122 R R60 140 R R R R93 200 R

20 68 R R R R

60 140 R R R R93 200 R20 68 R R R R R R R R

40 104 R R R

60 140 R R R R R93 200 R

20 68 R R R R R50 122 R R

60 140 R R R

20 68 R R R R R R R

40 104 L R R

50 122 N R R

60 140 R R R R80 176 R R R93 200 R

20 68 R R R R R R R

40 104 R R R

60 140 R R R R

80 176 R20 68 R

80 176 R

20 68 R R R R R R R R50 122 R R R R R60 140 R R R R R R R

93 200 R20 68 N N R R R N R

50 122 N N L20 68 R N N N

50 122 N N N

20 68 N R L R R N N R50 122 N L

60 140 R L N N

20 68 L N N R L N N N50 122 N N

60 140 L

H C=CHHC=CHButadieno, Gas Butadiene Butadiène Tg-G2 2

C HButano, Gas Butane Butane 4 10

Butanodiol Butanediol Butanediol

N N N

HO-(CH ) -OH2 4

Tg-G

10

Tg-L

50

Carbonato de Amonio

C H OButilglicol Butylglycol Butylglycol 6 14 2

CH O ·2H NAmmonium Carbonate 2 3 3

Sol. sat.

Carbonate d'Ammonium

Carbonato de Calcio

Barium Carbonate

Carbonato de Bismuto

CaCO3

Carbonato de Bario Carbonate de Barium Susp.

Sol. sat.Bismuth Carbonate

Susp.

Carbonate de Bismuth

BaCO3

(BiO) CO2 3

Calcium Carbonate

Susp.

Carbonate de Calcium

Magnesium CarbonateCarbonato de Magnesio Carnonate de Magnesium MgCO2

Potassium Carbonate K COCarbonato de Potasio Carbonate de Potassium Sol. sat.2 3

Sodium CarbonateCarbonato de Sodio Carbonate de Sodium

Sol. sat.

Na CO2 325

Hasta 50

Susp.

Cerveza Beer Bière

Zinc Carbonate

Sol. trab.

Carbonato de Zinc Carbonate de Zinc ZnCO3

Cianuro de Plata

Cianuro de Cobre (II)

AgCN

Cu(CN)Copper Cyanide 2

Sol. sat.

Cyanure de Cuivre

Potassium Cyanide

Silver Cyanide

Cyanure de Potassium

Cianide d'Argent

Sol. sat.

Sol.

Sol. sat.

Cianuro de Potasio KCN

Sodium Cyanide Sol. sat.Cianuro de Sodio Cianide de Sodium NaCN

Cianuro Mercúrico

Zinc Cyanide

Hg(CN) Sol. sat.2

Sol. sat.

Mercuric Cyanide

Cianuro de Zinc Cianide de Zinc

Cianure de Mercure

Zn(CN)2

Tg-L

C H OHCiclohexanol Cyclohexanol Cyclohexanol 6 11

Sol. sat.

C HCiclohexano Cyclohexane Cyclohexane 6 12

Tg-S

C H OCiclohexanona Cyclohexanone 6 10Cyclohexanone Tg-L


TEMP.

ºC ºF

EV

A

EP

DM

FP

M

N

BR

H

DP

E

P

P

P

VC

-U

P

VC

-C

A

BS


Ciclohexilamina Cyclohexilamine Cy C H Nclohexilamine T6 13 g-L 20 68 N N

20 68 R R R R R R50 122 R R R

60 140 R R R R

93 200 R

20 68 R R R R R R R R

40 104 R R L R

50 122 R R

60 140 R R R R R

80 176 R R

93 200 R R

20 68 R R R R R R R

40 104 R L

50 122 R R

60 140 R R N R R R R

80 176 L R R

93 200 N R

20 68 R L L N N

40 104 R N N

20 68 R L N

40 104 R N

60 140 L L

80 176 NClorito de Potasio Potassium Chlorite Chlorite de Potassium KClO Sol. sat.2 93 200 R

20 68 R N R R R R R

60 140 R R L R

93 200 N R

20 68 R R R

40 104 R

60 140 L RCloro, Acuoso Chlorine Chlore Cl,aq Tg-L 20 68 N L N N

ClCloro, Gas Húmedo Chlorine Chlore T2 g-G 20 68 N R N N N20 68 N R N L N L N

60 140 N N NC H ClClorobenceno Chlorobenzene Chlorobenzene T6 5 g-L 20 98 N N N N N N

20 68 L N R R N N60 140 N20 68 N L N N N60 140 N N N N

CH ClClorometano, Gas Chloromethane Chloromethane T3 g-G 20 68 L N NCloropropanos Chloropropane Chloroprop C H Clane T3 7 g-L a 47 20 68 N NCloruro de Acetilo Acetyl Chloride Chlorure d'Acéty CH COClle T3 g-L 20 68 R N N NCloruro de Alilo Allyl Chloride Chlorure d'Ally CH CHCH Cll 2 2 Sol. Sat 20 68 N N

40 104 R R R R60 140 R R L80 176 R R100 212 R R20 68 R R R R R R R R40 104 R R R50 122 R R60 140 R R R R R R R80 176 R L R100 212 R N L

Cloruro de Amilo Amyl Chloride Chlorure d'Amy C H Clle T5 11 g-L 20 68 N N N N20 68 R R R R R R R R R40 104 R R R R50 122 R R R60 140 R R R R R R R80 176 R R R93 200 R R R20 68 R R R N R R R R R50 122 R R R

60 140 R R R R93 200 R20 68 R R R R R R R R

40 104 R R R R

50 122 R R60 140 R R R R R R80 176 R R

93 200 R RCloruro de Bencilo Benzyl Chloride Chlorure Benzyliq C H Clue T7 7 g-L 20 68 N N

Sol. sat. 20 68Tg-L 20 68 N N

Cloruro de Butirilo Butyric Chloride Chlorure Butyriliq C H ClOue T4 7 g-L 20 68 N20 68 R R R R R R R R R

40 104 R R R

50 122 R R R60 140 R R R R R R R

80 176 R R L R

93 200 L R R R

20 67 R R R R R R

50 122 R R R R R60 140 R R R R

93 200 R

20 68 R R R R R50 122 R R

60 140 R R R R

20 68 R R R R R

50 122 R R

60 140 R R R R20 68 N L N N N N N

60 140 N N20 67 R N N

60 140 L N

20 68 R50 122 R

20 68 R R R R R R

50 122 R R R60 140 R R R R93 200 R

Cloruro de Metil Methyl Chloride Chlorure de Methy CH Cll T3 g-G 20 68 N N

Clorato de Potasio Clorate de Potassium

Calcium Chlorate

KClO3

Clorato de Calcio Chlorate de Calcium Ca(ClO )·2H O3 2 Sol. sat.

C H ClNClorhidrato de Anilina 6 8

Sol. sat.

Sodium ChlorateClorato de Sodio Chlorate de Sodium NaClO Sol. sat.3

Potassium Chlorate

Sol. sat.

Phénylhydrazine Hydrochloride C H -NH-NH HClClorhidrato de Fenilhidrazina Phénylhydrazine Chlorhydrate 6 5 2

Aniline Hydrochloride

Sol. dil.

Chlorydrate d'Aniline

2

Chlorine Chlore

C H ClO Tg-L2 3

20

Sodium Chlorite

ClCloro, Gas Seco Tg-G2

Clorito de Sodio Chlorite de Sodium NaClO2

Cloroetanol Chlorethanol Chlorethanol

CHClCloroformo Chloroform Chloroforme Tg-L3

Ammonium Chloryde

Sol. sat.

Cloruro de Amonio Chlorure d'Ammonium

Aluminium Chloride

NH Cl4

Cloruro de Aluminio Chlorure d'Aluminium

10

SbCl3

Sol. sat.

Sol. sat.

AlCl3

Antimony Trichloride

Sol. sat.

Chlorure d'Antimoine (III)

Barium ChlorideCloruro de Bario Chlorure de Barium

Cloruro de Antimonio (III)

BaCl ·2H O2 2

Cloruro de Calcio

Benzoyl Chloride

CaCl2

C H ClOCloruro de Benzoílo Chlorure de Benzoyl 7 5

Sol. sat.

Copper ChlorideCloruro de Cobre (II) Chlorure de Cuivre (II)

Calcium Chloride

CuCl Sol. sat.2

Chlorure de Calcium

Sol. sat.

Stannic ChlorideCloruro de Estaño (IV) Etain Chlorure (IV)

Stannous Chloride

SnCl Sol.4

Cloruro de Estaño (II) Etain Chlorure (II) SnCl2

C H ClCloruro de Etilo, Gas 2 5

PClCloruro de Fósforo (III) 3

Ethyl Chloride Chlorure d'Ethyl

Tg-L

Lauryl Chloride Chlorure Laurylique

Phosphorous Trichloride

Sol. sat.

Trichlorure de Phosphore

Tg-G

C H ClCloruro de Laurilo 12 25

Magnesium ChlorideCloruro de Magnesio Chlorure de Magnésium MgCl Sol. sat.2


TEMP.

ºC ºF

EV

A

EP

DM

FP

M

N

BR

H

DP

E

P

P

P

VC

-U

P

VC

-C

A

BS


20 68 N L N L N N N

60 140 N N N N20 68 R R R R R R

50 122 R R R

60 140 R R R R93 200 R

20 68 R R R R R R R R R

50 122 R R R R R R

60 140 R R R R R R R

80 176 R R

100 212 R N

20 68 R R R R R R R R40 104 R R R

50 122 R R R

60 140 R R R R R R80 176 R R R

100 212 R N

20 68 R R R R R

50 122 R R

60 140 R R R R

80 176 R

100 212 R NCloruro de Tionilo Thyonil Chloride Chlorure de Thy SOClonile T2 g-L 20 68 L R N N N NCloruro de Vinilo Vinyl Chloride Chlorure de Viny CH =CHClle T2 g-G 20 68 N R N

20 68 R R R R R R R

40 104 R R

50 122 R R

60 140 R R R R R R

80 176 R

20 68 R R R R R

50 122 R R

60 140 R R R R

20 68 L R R R R R R R

40 104 R R50 122 L R R60 140 R R R R R R80 176 R R90 194 R R R20 68 L R R R R R R R40 104 R R50 122 L R R60 140 R R R R R R80 176 R R R90 194 R R R100 212 R R20 68 R R R R R R R R R50 122 R R R R R R60 140 R R R R R R R90 194 R20 68 R R R40 104 R R R80 176 R R R90 194 R R

Cloruro Sulfuril Sulfuryl Chloride SO ClChlorure de Soufre T2 2 g-L 20 68 R N20 68 N R R40 104 R R20 68 N R L R N N N40 104 R L N50 122 N N60 140 N N20 68 R R R R R R R40 104 R L50 122 R R

60 140 R N R R R

93 200 R20 68 R R R R R60 140 R R R R

20 68 R R R R R R

40 104 R L R50 122 R R60 140 R R N R R R

80 176 R

Sol. sat. 20 68 N NTg-L 20 68 R R R N N

20 68 R R R90 194 R

20 68 R N

60 140 L N

20 68 R R R R R R R R R

40 104 R R R R50 122 R R R

60 140 R R R R R L R

93 200 R20 68 R R R R R R R R

40 104 R R

50 122 R R R

60 140 R R R R R R

80 176 R R R93 200 R R R

C H BrDibromobenzeno Dibromobenzene Dibromobenzène T6 5 2 g-L 20 68 N R N NDibutil Cetona Di Isobutyl Ketone Di Isobutyl Ketone [(CH3)2CHCH2]2CO Tg-L 20 68 L N N N

20 68 N R R N40 104 R L

60 140 L NDicloro-Bencenos Dichlorobenzene C H ClDichlorobenzene T6 4 2 g-L 20 68 N N NDicloro-Etilenos Dichloroethylene Dichloroethy C H Cllene T2 4 2 g-L 20 68 N L N L

CH ClCloruro de Metileno Tg-L2 2

Nickel Chloride

N N N

Cloruro de Níquel Chlorure de Nickel

Methylene Chloride

NiCl Sol. sat.2

Chlorure de Methylene

Cloruro de Sodio

Potassium Chloride

NaCl

Cloruro de Potasio Chlorure de Potassium KCl

Ferric Chloride

Sol. sat.

FeClChlorure de Fer (III) 3

Sol. sat.

10

Sodium Chloride

Sol. sat.

Chlorite de Sodium

Cloruro de Zinc Zinc Chloride Chlorure de Zinc

58

ZnCl2

Cloruro Mercúrico

Sol. sat.

HgCl2

Sol. sat.

Cloruro Férrico

FeClCloruro Ferroso Ferrous Chloride Chlorure de Fer 2

Sol. sat.Mercuric Chloride

Sol. sat.

Chlorure de Mercure

Ferric ChloridsulfateCloruro Sulfato Ferrico Chloridsulfate Ferrique FeClSO4

Diesel FuelCombustible Diesel Carburant Diesel

CH C H OHCresoles Cresol Crésols 3 6 4

Sol. trab.

Tg-L

Sol. sat.

40

Potassium Chromate

Sodium Chromate Sol. dil.

K CrO2 4

Cromato de Sodio Chromate de Sodium Na CrO ·10H O2 4 2

Cromato de Potasio Chromate de Potassium

Croton Aldehyde CH CH=CHCHOCrotonaldehído Aldéhyde Crotonique 3

Sol. sat.

Decalina Decaline Decaline

Potassium Cuprocyanide

Tg-L

Cuprocianuro de Potasio Cuprocyanure de Potassium

(C H O ) · xHDextrina Dextrine Dextrine 6 10 5 n 2O

C H ODextrosa (Dec a 200ºC) Dextrose Dextrose Sol.6 12 6

Dibutyl Ether Dibutyl Ether

Sol.

C H OC HDibutileter Tg-L4 9 4 9


TEMP.

ºC ºF

EV

A

EP

DM

FP

M

N

BR

H

DP

E

P

P

P

VC

-U

P

VC

-C

A

BS


20 68 N R L L N N

40 104 R N N60 140 R L N

1,2 - Dicloruro de Etileno 1,2 - Ethylene Dichloride 1,2 - Dichlorure d'Ethy C H Cllene T2 4 2 g-L 20 68 N L N L N N N

20 68 R R R R R R R R40 104 R L

50 122 R R R

60 140 R R R

80 176 R

100 212 R

20 68 R R R R R

50 122 R R60 140 R R R

90 176 R

20 68 R R R R R R R40 104 R R R

60 140 R R R R

80 176 R R

20 68 N R

50 122 RDietilamina Diethylamine Diéthy C H NHlamine T4 10 g-L 20 68 L N N N N

20 68 R R N R50 122 R R

60 140 R

20 68 N R

50 122 RDimetilamina Dimethylamine Dimhety (CH ) NHlamine 3 2 30 20 68 R N

20 68 L N N R N N

50 122 NDimetilanilina Dimethylaniline Dimethy C H N(CH )laniline T6 5 3 2 g-L 20 68 R

20 68 L N L R N N

60 140 R NDinonil Ftalato Dinony C H ((CH ) CH )l Phthalate T6 4 2 8 3 2 g-L 20 68 L R N

20 68 N L R L N N60 140 R L N20 68 N L N R R N40 104 R60 14020 68 R R N R R R R40 104 L L60 140 N R R R20 68 R R R R R R R R40 104 R R R R50 122 R R60 140 R R R R R R80 176 R R20 68 R R R R R50 122 R R60 140 R R R R20 68 R R R50 122 R R60 140 R R20 68 R L R40 104 R N R60 140 R R R80 176 R20 68 R N L R N N N60 140 N N N20 68 R R90 194 R20 68 N R R40 104 R R60 140 R L

80 176 R

20 68 R R L40 104 R R20 68 R L R

40 104 R

50 122 R REster Acrilico Acrylic Ester Ester Acryliq CH =CH-COOCH CHue T2 2 3 g-L 20 68 L N N NEstireno Styrene Sty H C -CH=CHrène 205 6 2 68 R N

< 5 80 176 R R

20 68 L N

50 122 L L20 68 R R L L R R L N

50 122 R R L L

60 140 R L R L LC H NOEtanolamina Ethanolamine Ethanolamine T2 7 g-L 20 68 R N

20 68 L R

60 140 L REtil Benzeno Ethyl Benzene Benzène Éthyliq C H -CH CHue T6 5 2 3 g-L 20 68 N R N N

20 68 N N N N L R N N N60 140 L N N

20 68 N N

50 122 N

20 68 R L R N

40 104 L L60 140 N N

80 176 R20 68 R R R R R R L R

40 104 R R R L

50 122 L R60 140 R R L R R R L

80 176 R L REtilglicol Ethyl Glicol Ethyl Gly HOCH CHcol T2 2 g-L 50 122 N

20 68 N R N N N

40 104 R60 140 L

1,1 - Ethylene Dichloride

N

C H Cl21,1 - Dicloruro de Etileno 1,1 - Dichlorure d'Ethylene 2 4 Tg-L

Sol. sat.

40

Dicromato de Sodio Sol. sat.Na Cr O ·2H O2 2 7 2

Dicromato de Potasio Potassium Dichromate Dichromate de Potassium

Sodium Dichromate

K Cr O2 2 7

Dichromate de Sodium

Tg-S

Diethylen Glycol

C H NODietanolamina Diethanolamine Diethanolamine 4 11 2

C H ODietilenglicol Diethylen Glycol Tg-L4 10 3

(C H ) NHDifenilamina 6 5 2

(CH ) NHDimetilamina, Gas 3 2

Diphenyl Amine Diphenyl Amine

Tg-G

Dimethyl Formamide Dimethyl Formamide

Dimethylamine Dimethylamine

Tg-L

Sol. trab.

Dimetil-Formamida HCON(CH )3 2

Dioxano Dioxane Dioxane

SODióxido de Azufre, Gas Húmedo 2

O=(CH ) =O2 4 Tg-L

Sulfur Dioxide, Gas Dry

Sulfur Dioxide, Gas Wet

SODióxido de Azufre, Gas Seco Dioxyde de Soufre 2

Dioxyde de Soufre

Tg-G

Carbon Dioxide

Carbon Dioxide

CODióxido de Carbono, Gas Seco Dioxide de Carbone, Gaz Sec Tg-G2

CODióxido de Carbono, Gas Húmedo Dioxide de Carbone, Gaz Humide 2

Disulfito de Sodio

CODióxido de Carbono, Sol. Acuosa Carbon Dioxide 2

Na S O Sol. sat.2 2 5

Dioxide de Carbone

Carbon Disulfide

Sodium Disulphite Disulfit de Sodium

Disulfure de Carbone

Sol. sat.

Tg-LCSDisulfuro de Carbono 2

C H N OEdta Edta Edta 10 16 2 8

Paraffin Emulsions Sol. trab.Émulsions de Paraffine

Photographic Emulsions

Emulsiones de Parafina

Emulsiones Fotograficas Émulsions Photograpuiques

Estearato de Zinc Zinc Stearate Stearat de Zinc Zn(C H -COO) Susp.17 35 2

C H OHEtanol Ethanol Ethanol 2 5

40

Tg-L

Éter de Petróleo (Ligroína)

(C H ) OÉter Etílico 2 5 2

Ligroine Ligroine

Tg-L

Ethylene Chlorohydrin

Ethyl Ether Ethyl Ether

Ethylene Chlorohydrine

Sol. trab.

Etilenclorohidrina Tg-LClCH CH OH2 2

H N-CH -CH -NHEtilendiamina Ethylene Diamine Ethylène Diamine Tg-L2 2 2 2

< 50

Tg-L

Etilenglicol Ethylèneglycol

C H NHNHFenilhidrazina Tg-L6 5 2

CH OHCH OHEthylene Glycol 2 2

Phenylhydrazine Phénylhydrazine


TEMP.

ºC ºF

EV

A

EP

DM

FP

M

N

BR

H

DP

E

P

P

P

VC

-U

P

VC

-C

A

BS


20 68 R R

60 140 R R

80 176 L

20 68 R R N R N

40 104 L R60 140 R R

20 68 R N

40 104 R

60 140 R R

80 176 L L

20 68 N R N R N R

40 104 L R

60 140 N N N

20 68 R R R R R

60 140 R R R R

20 68 R R R R R

60 140 R R R R

20 68 R R R

40 104 R R R

60 140 R R R

80 176 R

100 212 R20 68 R R R

40 104 R R RFlúor Gas, Húmedo FFluorine Gas Wet Fluor T2 g-G 20 68 N N N N N N N

20 68 N N N N N N

60 140 N N

20 68 R R R R R

50 122 R R

60 140 R R R R

93 200 R

20 68 R R R R R60 140 R R L

Sol. sat. 93 200 R20 68 R93 200 R20 68 R R R R R50 122 R R60 140 R R R R20 68 R R R R R R50 122 R60 140 R R R20 68 R R R R R R R40 104 R R R50 122 R R60 140 R R L R R R R93 200 R20 68 R R R60 140 L R80 176 R20 68 R R R R R R R R R40 104 R R R50 122 L R R60 140 R R L R R R

37 100 21220 68 R60 140 R

Formamida Formamide Foramyde HCONH T2 g-L 20 68 R L R20 68 R R R R R R R40 104 R R R L50 122 R60 140 R L R100 212 R20 68 R R R R

40 104 R R R R

60 140 R R R R90 194 R20 68 R R R R R

50 122 R R R

60 140 R R R80 176 R20 68 R R R R

50 122 R R

60 140 R R R

80 176 R RFosfato de Tributilo Tribut yl Phosphate Tributyl Phosp (C H ) POhate T4 9 3 4 g-L 20 68 R N N N

20 68 R N L40 104 N

Fosfato de Trioctil Trioctyl Phosphate Trioctyl Phosp (C H ) POhate 208 17 3 4 68 R N L

20 68 R R

40 104 R R

60 140 R R

80 176 R20 68 R R R

60 140 R R RTg-L 20 68 N R L

20 68 R R R

40 104 R R

60 140 L R

20 68 L R

50 122 L R20 68 R R R R

50 122 R R R R93 200 R R

20 68 R N N N

60 140 L N20 68 R N N

60 140 L N20 68 L L R N R L N N N50 122 N N60 140

C H OHFenol Phenol Phénol 6 5

L L N

Sol.

5

Hasta 10

90

Sodium Ferrycianide

Sol. sat.

Sodium Ferricianide

Sodium Ferrocyanide Sodium Ferrocianide

Na Fe(CN) ·H O3 6 2Ferricianuro de Sodio Sol. sat.

Ferrocianuro de Sodio

Fertilizantes Fertilizers Engrais

Fijadores Fotograficos

Na Fe(CN) ·10H O4 6 2

Sol.

Sol. trab.Photographic Fixer

Tg-G

Fixateur Photographique

Fluorine Gas Dry Fluor

Aluminium Fluoride Susp.

F2

Fluoruro de Aluminio Fluorure d'Aluminium

Flúor Gas, Seco

AlF3

Ammonium FluorideFluoruro de Amonio Fluorure d'Ammonium NH F4Hasta 20

Copper FluorideFluoruro de Cobre Fluorure de Cuivre (II)

Sol. sat.

2

Fluoruro de Sodio

Fluoruro de Potasio KF

NaF

Potassium Fluoride

Sol. sat.

Fluorure de Potassium

Sodium Fluoride

Formaldheyde Formaldheyde

Fluoride de Sodium

Sol. sat.

Formaldehído HCHO

NH H PO3 3 4

Sol. dil.

30 a 40

50

Fosfato de Sodio, Ácido

Sol. sat.

Sodium Phosphate

NaH PO2 4

Fosfato de Sodio Fosfate de Sodium

Ammonium Phosphate

Na PO3 4

Fosfato de Amonio Fosfate d'Ammonium

Sol. sat.

Sodium Phosphate, Acid Sol. sat.Fosfate de Sodium, Acide

Sol. sat.

Tricresyl Phosphate

Sodium Phosphate, Neutral

(H C-C H O) POFosfato de Tricresil Tricresyl Phosphate 3 6 4 3

Fosfato de Sodio, Neutro Fosfate de Sodium, Neutre Na HPO2 4

Zn (PO )Fosfato de Zinc Zinc Phosphate 3 4 2

Fosfina Tg-G

Phosphate de Zinc

Phosgene Phosgène

Phosphines Phosphines

Tg-G

Sol. sat.

COClFosgeno 2

CCl FFréon - F12 Freon 12 Freon 12 Sol. trab.2 2

C H OFructosa 6 12 6 Sol.

Butyl PhtalateFtalato de Butilo Phtalate de Butyl

Fructose Fructose

Tg-L

Tg-L

Dioctyl Phtalate

Diisoctyl Phtalate

C H (COOC H )Ftalato de Dioctilo Phtalate de Dioctyl Tg-L6 4 8 14 2

Ftalato de Diisooctilo Phtalate de Diisoctyl


TEMP.

ºC ºF

EV

A

EP

DM

FP

M

N

BR

H

DP

E

P

P

P

VC

-U

P

VC

-C

A

BS


20 68 N R R

40 104 R R

60 140 R R

20 68 R R R

50 122 R

20 68 R R R R R R

50 122 R RGas, Sintético Gas, Synthetic Gaz, Syntethique Tg-G 20 68 R R

20 68 R L

40 104 R N

60 140 L R

20 68 N R R R N R N N60 140 R R L N R N

20 68 R R R R R R R R

40 104 R R R

50 122 R R

60 140 R R R R

20 68 R R R R R R

50 122 R R R R

60 140 R R R R

93 200 R R

20 68 R R R

40 104 L R R

60 140 L L R

80 176 N N

20 68 R R

40 104 R L

20 68 R R R R R R R R

50 122 R R

60 140 R R R R R R R

80 176 R R R R

93 200 R R R20 68 N N R R R L R L R

40 104 R R50 122 N60 140 R R N N20 68 R R R R R R R50 122 R R60 140 R R R R20 68 R60 140 R20 68 N R R R R N40 104 R R50 122 R N60 140 R R L R20 68 R R60 140 R R

Hidrato de Hidrazina Hydrazine Hydrate Hydrazine Hy H N-NH ·H Odrate 2 2 2 Sol. 20 68 R L N NHidrofluoruro de Amonio Ammonium Hydrogen Fluoride Ammonium Hydrogen Fluoride NH HF 504 2 20 68 R R

20 68 R R R R R R40 104 R R R60 140 R R R R R R80 176 R R R100 212 R20 68 R R R R60 140 R R R R20 68 R R R R R40 104 R R60 140 R R R90 194 R20 68 R R R R R60 140 R R R

93 200 R20 68 R R R R R40 104 R R R R

60 140 R R R R R

93 200 R30 20 68 R

20 68 R R R R R

50 122 R R

60 140 R R R20 68 R R R R R R R

40 104 R R50 122 R R R

60 140 R R R R R

93 200 R

20 68 R N R N

40 104 R L N60 140 L L N

20 68 R R R R R R R R

50 122 R R R R60 140 R R R R R R

80 176 R R

93 200 R R

20 68 R R R R R R R R R

40 104 R R R R50 122 R R R

60 140 R R L R R R R

80 176 R R R93 200 R R

20 68 R R R R R R

50 122 R R R

60 140 R R R R93

Fuel Oil

Gas, Natural, Húmedo

200 R

Fuel Oil Fioul

Tg-G

Gas, Natural, Dry Gaz, Naturelle, Sec

Gas, Natural, Wet

Tg-G

Gaz, Naturelle, Humide

Gas, Natural, Seco

Gases Nitrosos Nitrous Gases Gaz d'Azote

Gasolina

NO Sol. dil.X

Sol. trab.

Gelatina Gelatin Gelatine

Gasoline Gasoline

Sol.

Tg-L

HOCH -CHOH-CH OHGlicerol Glycerol Glycérol 2 2

C H (OH)Glicerina Glycerine Glycérine 2 5 3

Tg-L

Glicocol

C H O ·H OGlucosa (Dec a >200ºC) 6 12 6 2

NH -CH -COOH2 2Glycocoll Glycocoll

Sol.

Heptane Heptane

Glucose Glucose

Tg-L

10

C HHeptano 7 16

Potassium Ferrocyannanide

C H OHHexadecanol 16 33

K Fe(CN) ·3H OHexacianoferrato (II) de Potasio Potassium Ferrycianure 4 6 2 Sol. sat.

Hexadecanol Hexadecanol Sol. trab.

C HHexano Hexane Hexane Tg-L6 14

CH (CH ) CH OH Hexanol Hexanol Hexanol Tg-L3 2 4 2

HHidrógeno Hydrogen Hydrogène Tg-G2

HCO NHHidrogeno Carbonato de Amonio Ammonium Hydrogen Carbonate 3 4

KHSOHidrogenosulfito de Potasio Sol.3

Hydrogen Carbonate d'Ammonium

Sodium Bisulfate Sodium Bisulfate

Potassium Hydrogensulfite

Sol. sat.

Hydrogensulfite de Potassium

Sol. sat.

Hidrogenosulfito de Sodio NaHSO3

Calcium Hydrogensulfide

C H (OH)Hidroquinona 6 4 2

Hidrogenosulfuro de Calcio Hydrogensulfure de Calcium Ca(HS) Sol.2

Sol. sat.

Aluminium HydroxideHidróxido de Aluminio Hydroxide d'Aluminium AlO ·3H O3 2

Hydroquinone Hydroquinone

Susp.

Sol. sat.

Barium HydroxideHidróxido de Bario Hydroxide de Barium

Ammonium Hidroxyde

Ba(OH) Sol. sat.2

Hidroxido de Amonio Hydroxide d'Ammonium NH OH4

Hidróxido de Magnesio

Hidróxido de Calcio

Mg(OH)2

Ca(OH)Calcium Hydroxide 2Hydroxide de Calcium

Magnesium Hydroxide Magnesium Hydroxide

Sol. sat.

Sol. sat.


TEMP.

ºC ºF

EV

A

EP

DM

FP

M

N

BR

H

DP

E

P

P

P

VC

-U

P

VC

-C

A

BS


20 68 R R R R

50 122 R R R R60 140 R R R

80 176 R

20 68 R R R R50 122 R R R R

60 140 R R

20 68 N L R R

40 104 N R R

60 140 R R R

80 176 L R

100 212 R20 68 R R N L R R R

40 104 R N R R R

50 122 R R R R60 140 R R R

80 176 R

20 68 R R R R R

50 122 R R R

60 140 R R

Sol. sat. 93 200 R

20 68 R L R R60 140 L R

90 194 R

20 68 R R R

50 122 R R

60 140 R R

20 68 R R R N

50 122 R N

60 140 R R

20 20 68 R N

20 68 R R N R R R N

50 122 R N60 140 R L R93 200 R20 68 R N R N L50 122 N20 68 R R R R R R40 104 R L R50 122 R R R60 140 R N R80 176 R R20 68 R R R R40 104 R R R60 140 R L R

Isobutironitrilo Isobutyronitrile Isobuty C H Nronitrile T4 7 g-L 20 68 N20 68 R R L R60 140 N

Isopropil Éter Isopropyl Ether Isopropy (CH ) CHOCH(CH )l Ether T3 2 3 2 g-L 20 68 L N N L N N20 68 R R R R R40 104 R R R60 140 R R R R93 200 R20 68 R R L R40 104 R R R L60 140 R R R L20 68 R R R40 104 R R R R60 140 R R R R80 176 R R R R20 68 R R R

40 104 R R R R60 140 R R R R80 176 R R R

20 68 R R R R

40 104 R R50 122 R R R60 140 L

20 68 R R R R R R R

50 122 R R60 140 R R R R100 212 R

20 68 R R R R R R

40 104 R R R R

60 140 R LMahonesa Mayonnaise Mayonnaise Sol. trab. 20 68 R R R

20 68 R50 122 R

20 68 R R R R R R R

40 104 R R R

50 122 R R

60 140 R R R L80 176 R R

20 68 R R R R R R R R

60 140 R R R R R R R80 176 R R

Metacrilato de Metilo Methyl Methacrylate Méthyle Méthacry C H Olate T5 8 2 g-L 20 68 N N

20 68 R R R60 140 R R R

100 212 R

20 68 R R N50 122 R N

20 68 N N N

60 140 N N N20 68 N N R N N N

50 122 N N60 140 N N

Metilamina Methyl Amine Methy CH NHl Amine Hasta 323 2 20 68 R N R20 68 N R50 122 N R20 68 L

50

Hidróxido de Potasio

122 N

Potassium Hydroxide Potassium Hydroxyde KOH

Sodium Hydroxyde

20

Hasta 50

50

10

Hipoclorito de Potasio KClO

Hipoclorito de Sodio

NaOH

Hipoclorito de Calcio

Hidróxido de Sodio

Ca(ClO)Calcium Hypochlorite 2

Sodium Hydroxide

Hypochlorite de CalciumSol.

Sol.

Sodium Hypochlorite Sodium Hypochlorite

5

NaClO·5H O2

10 a 15

Potassium Hypochlorite

13% Cl

Hipochlorite de Potassium

Yoduro de Potasio KI

Yodo (En Yoduro de Potasio) Iodine Iode

Sol. sat.

Sol. sat.

Potassium Iodide

I2

Iodure de Potassium

Sodium Iodide

Tg-L

Ioduro de Sodio Iodure de Sodium NaI

(CH ) CCH CH(CH )Isooctano Isooctane Isooctane 3 3 2 3 2

Tg-L

Sol.

Jabón Detergente, Solución Acuosa Detergents Détergents

Jabón Soaps Savon

Tg-L

(C H O )Jarabe de Almidon Starch Syrup Sirop d'Amidon 6 10 5 n

Jarabe de Azucar Sol. trab.

Lanolin Lanoline

Sugar Syrup Sirop de Sucre

Sol. trab.

Sol. trab.

Lanolina

Leche Milk Lait

Levadura

Sol. trab.

Susp.

Margarina Margarine Margarine

Yeast Levure

Sol. trab.

Sol. trab.

Mercurio Mercury Mercure Hg

Melaza Molasses Mélasse

Tg-L

Metafosfato de Sodio

Metafosfato de Amonio

(NaPO )3 n

NH POAmmonium Metafosfate 4 3

Sol.

Metafosfate d'Ammonium

Methyl Butyl Ketone Methyl Butyl Cetone

Sodium Metaphosphate

Tg-L

Sodium Metafosfate

Sol. sat.

CH CO(CH ) CHMetil Butil Cetona 3 2 3 3

Methyl Ethyl Ketone

C H OMetilciclohexanonas 7 12

CH COC HMetil Etil Cetona Methyl Ethyl Cetone Tg-L3 2 5

Tg-L

CH -OCH CH OHMetilglicol Methyl Glycol Methyl Glycol 3 2 2

Methyl Cyclohexanone

Tg-L

Methyl Cyclohexanone


TEMP.

ºC ºF

EV

A

EP

DM

FP

M

N

BR

H

DP

E

P

P

P

VC

-U

P

VC

-C

A

BS


20 68 R R R R

50 122 R60 140 R R R

20 68 R R

50 122 R

20 68 R R R R R

50 122 R R

60 68 R R R R

93 200 RMorfolina Morpholin Morp C H NOholine T4 9 g-L 20 68 R NMostaza, Acuosa Mustard Moutarde Sol. trab. 20 68 R R R RMowilith D Mowilith D Mowilith D Sol. trab. 20 68 R R

20 68 R R R R R R L N

40 104 R L R

60 140 R N R R L L L100 212 L N

20 68 R N N

60 140 N N

20 68 N R R N

40 104 R R

60 140 R R

20 68 R R R R R R50 122 R R R

60 140 R R R R R

93 200 R

20 68 R R R R R R R R R

50 122 R R R R R R R R

60 140 R R L R R R R

80 176 R R R

100 212 R L

20 68 R R R R R R R R R

50 122 R R R R R R

60 140 R R R R R R

93 200 R R20 68 R R R R R R R R40 104 R R R R R R R R60 140 R R R R R80 176 R20 68 R R R R R R50 122 R R R60 140 R R R R93 200 R R20 68 R R R R R R50 122 R R R60 140 R R R R93 200 R20 68 R R R R R R50 122 R R R60 140 R R R R93 200 R20 68 R R R R R R R40 104 R R R R60 140 R R R R R L R93 200 L R20 68 R R R R R R50 122 R R R60 140 R R R R20 68 R R R R40 104 R R R60 140 R R R90 194 R20 68 R R R R R R R

40 104 R R R50 122 R R60 140 R R R R R R R

93 200 R

20 68 R R R R R R R40 104 R R50 122 R R

60 140 R R R R R R

80 176 R R93 200 R

20 68 L R R R R R50 122 L R R

60 140 R R R R

93 200 R R

20 68 R R R40 104 R R R

60 140 R R R80 176 R R

93 200 R R20 68 R R R R R R R R

50 122 R R R R R R R R

60 140 R R R R R R R80 176 R

20 68 R R R R

60 140 R R R R

20 68 R R R R R R R R

40 104 R L R R R R R50 122 R R R R R60 140 R N R R R R

93 200 R

20 68 N L N R N N N60 140 L N

20 68 N L L

40 104 N N20 68 R R R R R R R

50 122 R R

60 140 R R R R R L R80 176 R

20 68 R R R50 122 R R R

60 140 R R

90 197 R

Sol. trab.

Ammonium MolibdateMolibdato de Amonio Molibdate Amonique

Miel Honey Miel

NH Mo O .7H O4 7 24 2

Monóxido de Carbono, Gas CO

C H ON - Butanol 4 10

Carbon Monoxide

Tg-L

Monoxide de Carbon

Naphta Naphte

Butanol Butanol

Sol. trab.

Tg-G

Nafta

Nitrato de Aluminio

C HNaftalina Naphtalene Naphtalène Tg-L10 8

Al(NO ) ·9H O3 3 2 Sol. Sat

Ammonium NitrateNitrato de Amonio Nitrate d'Ammonium

Aluminium Nitrate

NH NO Sol. sat.4 3

Nitrate d'Aluminium

Calcium NitrateNitrato de Calcio Nitrate de Calcium Ca(NO )3 2

Copper NitrateNitrato de Cobre (II) Nitrate de Cuivre Cu(NO ) ·3H O3 2 2

Sol. sat.

50

Sol. sat.

Sol. sat.Magnesium Nitrate

Sol. sat.

Magnesium Nitrate

Nickel Nitrate Nickel Nitrate

Mg(NO )3 2

Nitrato de Níquel

Nitrato de Magnesio

Ni(NO ) ·6H O3 2 2

Nitrato de Plata Silver Nitrate Argent Nitrate AgNO Sol. sat.3

Potassium NitrateNitrato de Potasio Potassium Nitrate

Sol. sat.

KNO3

50

Nitrato de Zinc

Nitrato de Sodio

Zn(NO ) ·6H O3 2 2

NaNOSodium Nitrate 3

Sol. sat.

Nitrate de Sodium

Zinc Nitrate Nitrate de Zinc

Ferric Nitrate Nitrate de Fer

Sol. sat.

Nitrato Férrico Sol. sat.Fe(NO ) ·9H 03 3 2

Nitrato Ferroso Ferrous Nitrate Nitrate Ferreux Fe(NO ) Sol. sat.3 2

Sol.

Sol. sat.

Nitrito de Sodio Sol. sat.

Nitrato Mercurioso Mercrous Nitrate Nitrate de Mercure

NaNOSodium Nitrite Nitrite de Sodium 2

HgNO ·2H O3 2

C H NONitrobenceno Nitrobenzene Nitrobenzene Tg-L6 5 2

C H NONitrotolueno Nitrotoluene Nitrotoluène Tg-L7 7 2

Orina

K POOrtofosfato de Potasio 3 4

Urine Urine

Potassium Ortophosphate Sol. sat.Ortophosphate de Potassium


TEMP.

ºC ºF

EV

A

EP

DM

FP

M

N

BR

H

DP

E

P

P

P

VC

-U

P

VC

-C

A

BS


Oxalato de Amonio Ammonium Oxalate H NOOC-COONHOxalate d'Ammonium 204 4 68 ROxalato de Sodio Sodium Oxalate Oxalate de Sodium Na C O Sol. sat.2 2 4 20 68 R R

20 68 R R R R

50 122 R R R R

60 140 R R R20 68 L N R

40 104 RÓxido de Mesitilo Mesityl Oxide Oxide de Mesity C H Ole 6 10 20 68 N NOxido de Propileno Propylene Oxide Oxyde de Propy C H Olène T3 6 g-L 20 68 L N N N

20 68 R R R R R

50 122 R R R R R

60 140 R R R R

20 68 R R R R R R R R

40 104 R R R R

50 122 R R R R

60 140 R R L R R

2 en aire 20 68 L R N L L R R N

20 68 N R N L L R R N

40 104 L N R R

93 200 N R

C HParafina Parafin Parafine Tg-L36 74 20 68 R R

Pentano CH (CH ) CHPentane Pentane 203 2 3 3 68 N

20 68 R R R R R

50 122 R R

20 68 R R R R R R

40 104 R R L R R

50 122 R R R R

60 140 R R R

80 176 R R20 68 R R

60 140 R RPerclorato de Sodio Sodium Perchlorate Perchlorate de Sodium NaClO Sol. sat.4 20 68 R R

20 68 R L N N40 104 R N60 140 R20 68 N R R L R40 104 R N R60 140 R R80 176 R R20 68 R R60 140 R R80 176 R20 68 R R R60 140 R R R20 68 R L R R R R L40 104 L L N50 122 N N L60 140 R R20 68 R L R N R R R R50 122 L60 140 R L R

50 20 68 L R R20 68 L N R60 140 N20 68 R R R R R R50 122 R R R R L R60 140 R R R20 68 R R N R R R R R40 104 R R R R R50 122 R R R R60 140 R R R L20 68 N R R N N

40 104 R R N N

60 140 L R N N20 68 N R R R R R40 104 N R R R R

20 68 L N N R L N N

60 140 L N

Pirogallol Pyrogallol Pyrogallol C H (OH) 1006 3 3 20 68 R

Propano, Gas Propane Prop C Hane T3 8 g-G 20 68 N R R RPropano, Liquido Propane Prop C Hane T3 8 g-L 20 68 N R R

20 68 R R R L

40 104 R R L L

60 140 R N L

<25 80 176 R20 68 R R R R L

40 104 R R R L L

50 122 R L N LQueroseno Kerosene Querosene Sol. trab. 20 68 R

20 68 R R R R

50 122 R R R R

60 140 R R RRefresco de Jengibre (Ginger Ale) Ginger Ale Ginger Ale Sol. trab. 20 68 R R R R

20 68 R R L R R R40 104 R R L R R R

60 140 R R R

20 68 R R R R R R R R

40 104 R R R R R R R R

60 140 R R R R R R R80 176 R R R R

20 68 R R R R R R R R40 104 R R R R R R R R

60 140 R L R R R R

80 176 R R R20 68 R R R R R R R R

40 104 R R R R R R R R60 140 R R R R R R R

80 176 R R

Aluminium Oxychloride

R R

Oxychlorure d'Aluminium Susp.

ZnO

Oxicloruro de Aluminio

Phosphore Oxichloride Tg-LPOClOxicloruro de Fósforo Oxichlorure de Phosphore 3

Óxido de Zinc Zinc Oxide Oxyde de Zinc Susp.

Oxygen, Gas Oxygène Tg-G

OOzone Ozone 3

KClOPotassium Perchlorate 4

OOxígeno, Gas 2

Sol. sat.Perchlorate de Potassium

Ozono, Gas

10

Sol. sat.

Perborato de Sodio Sol. sat.NaBO ·H O ·3H OSodium Perborate 2 2 2 2Perborate de Sodium

Perclorato de Potasio

Perchloro-Ethylene Cl C=CClPercloroetileno Perchloro-Ethylene 2 2

30

Permanganato de Potasio

90

KMnO4

Hydrogen Peroxide

Potassium Permanganate

H OPeróxido de Hidrógeno Peroxide d'Hydrogèn 2 2

Potassium Permanganate

Sol. sat.

10

20

Hasta 10

Ammonium Persulphate

K S OPersulfato de Potasio Sol. sat.2 2 8

Persulfato de Amonio Persulfate d'Ammonium Sol. sat.

Potassium Persulfate Persulfate de Potassium

(NH ) S O4 2 2 8

Petróleo Petroleum Pétrole

Petroléo Bruto Crude Oil Pétrole Brut Tg-L

80/20

Tg-L

C H OHPropanol Propanol Propanol 3 7

Piridina Pyridine Pyridine

Tg-L

N(CH) CH4

C H OPropileno Glicol Propylene Glycol Propylène Glycol 3 8 2

Rábano Sol. trab.

Photographic Developer Revealers (Photographique)

Radish Radis

Sol. trab.

Tg-L

Reveladores (Fotográficos)

Sales de Bario Barium Salts Sels de Barium

Sales de Cobre

Tg-L

Tg-L

Sales de Hierro Iron Salts Sels de Fer

Cooper Salts Sels de Cuivre

Sol.


TEMP.

ºC ºF

EV

A

EP

DM

FP

M

N

BR

H

DP

E

P

P

P

VC

-U

P

VC

-C

A

BS


20 68 R R R R R R R

50 122 R R R R R R R

60 140 R R R R R R R

20 68 R R

50 122 R R

80 176 R

20 68 R R R R

40 104 R R R R R

60 140 R R R R

20 68 R R R R R R R R R

40 104 R R R R R R R R R

60 140 R R R R R R R

80 176 R R

20 68 R R R R R R R R

50 122 R R R R R R R R

60 140 R R R R R R R

80 176 R R R

20 68 R R R R R R R R R

40 104 R R R R R R R R R

60 140 R R L R R R R

80 176 R R R

20 68 R R R R R R R R50 122 R R R R R R R R

60 140 R R R R R R R

93 200 R R

20 68 R

40 104 R

60 140 R

20 68 R R R R R R R R R

40 104 R R R R R R R R R

50 122 R R R R R R R R R

60 140 R R R R R R R93 200 R

20 68 R R R R R R R R R50 122 R R R R R R R R R60 140 R R R R R R R93 200 R20 68 R R R R R R N40 104 R L20 68 R R R93 200 R20 68 R R R R R R R R R50 122 R R R R R R R R R60 140 R R R R R R R93 200 R R R R20 68 R R R R R R R R R50 122 R R R R R R R R R60 140 R R R R R R R93 200 R R R R20 68 R R R R R R R R R40 104 R R R R R R R R R50 122 R R R R R R R R R60 140 R R R R R R80 176 R R93 200 R20 68 R R R R R R R R R40 104 R R R R R R R R R50 122 R L R R R R R R R60 140 R R R R R R80 176 R R20 68 R R R R R50 122 R R R R R

60 140 R R R R20 68 R R R R R R R R R50 122 R R R R R R R R R

60 140 R R R R R R R

80 176 R R R

20 68 L R R R R R R R R40 104 L R R R R R R R R50 122 L R R R R R R R R

60 140 R R R R R R

80 176 R R93 200 R R R

20 68 R R R R R R R R

50 122 R R R R R60 140 R R R R R R R

93 200 R

20 68 R R R

40 104 R R R

60 140 R R R80 176 R

20 68 R R R R R R R R

50 122 R R R R R R R R60 140 R R R R R R

90 197 R

20 68 R R R R R R R R

40 104 R R L R R R

60 140 R R N R R L R90 194 R

20 68 R R R R R

60 140 R R R90 194 R R

20 68 R R R

40 104 R R R60 140 R R R

20 68 R R N R40 104 R

60 140 R

80 176 R20 68 R R R R R R L R

40 104 R L R R R R L R50 122 R R R L R

60 140 R N

Silicato de Sodio Sodium Silicate Sodium Silicate

R R R R L

Starch Solution

Al (SO )2 4 3

(C H O )Solución de Almidon Solution d'Amidon 6 10 5 n

Sulfate d'Aluminium

Sol.

Sol. sat.

Sol.

Na SiO2 3

Sol. sat.

Sol. sat.Sulfato de Aluminio-Potasio

Sol. sat.

Sulfato de Aluminio

AlK(SO )·12H O4 2

Ammonium SulphateSulfato de Amonio Sulfate d'Ammonium

Aluminium Sulfate

Aluminium Potassium Sulfate

(NH ) SO4 2 4

Sulfate d'Aluminium-Potassium

Sulfato de Bario BaSO Susp.4

Sulfato de Calcio Sulfate de Calcium

Barium Sulfate Sulfate de Barium

BeSOSulfato de Berilio 4

CaSO4

Sulfato de Hidroxilamina

Berylium Sulfate

Susp.

(NH 0H) SO3 2 4

Sulfate de Berylium

Hydroxilamine Sulphate Sulfate de Hydroxilamine

Sol. sat.

Calcium Sulfate

Sol

Lithium Sulfate

Sol. sat.

Sulfate de Lithium

Magnesium Sulfate Sulfate de Magnésium

Li SO2 4

Sulfato de Magnesio

Sulfato de Litio

MgSO ·7H O4 2

Sulfato de Níquel Nickel Sulfate Nickel Sulfate NiSO4

Potassium Sulfate

Sol. sat.

K SOSulfato de Potasio Sulfate de Potassium 2 4 Sol. sat.

Sol. sat.

0,1

Sulfato de Sodio Sulfate de SodiumSodium Sulfate

Zinc Sulfate Sulfate de Zinc Sol. sat.

Na SO2 4

Sulfato de Zinc

Fe (SO )Sulfato Férrico Sulfate de Fer (III) 2 4 3

ZnSO ·7H O4 2

Sulfato Mercuroso

Ferric Sulfate Sol. sat.

FeSOSulfato Ferroso Ferrous Sulfate Sulfate de Fer Sol. sat.4

HgSO4

Potassium Sulfite K SO ·2H OSulfito de Potasio Sulfite de Potassium 2 3 2

Mercrous Sulfate

Sol. sat.

Sulfate Mercureux

Fatty Alcohol Sulphonates Sulfonates d'Alcool Gras

S

Sol. sat.

40

Sulfito de Sodio Sodium Sulfite Sodium Sulfite

Sulfonatos de Alcoholes Grasos Tg-L

Na SO2 3

Sulfur Sulfure

Ammonium Sulphide Sol. sat.Sulfuro de Amonio Sulfure d'Ammonium

Sulfato de Cobre (II) Copper Sulfate Sulfate de Cuivre

Sulfuro

(NH ) S4 2

CuSO ·5H O4 2


TEMP.

ºC ºF

EV

A

EP

DM

FP

M

N

BR

H

DP

E

P

P

P

VC

-U

P

VC

-C

A

BS


20 68 R R R R R R R R

50 122 R R R R R R R R

60 140 R R R R R R R

93 200 R R

20 68 R R R L R R R

60 140 R R R L

Sol. dil. 80 176 R

20 68 R R N

40 104 N R N

60 140 R

80 176 L

20 68 R R R R R R R R

40 104 N R L R R R R R

50 122 R R R R R

60 140 L N R R R R

20 68 R R R R R R

50 122 R R R R R R

60 140 R R R R R

93 200 R

20 68 R R R R R R

40 104 R R R R

60 140 R R R RTetracloroetano Tetrachloroethane Cl CH-CHClTetrachloroethane T2 2 g-L 20 68 N N L N

20 68 N R N L N N N N

60 140 N N NTetraetileno de Plomo Tetraeth ylene Lead Plomb Tetraethy (C H ) Pblène 2 5 4 20 68 L R RTetraetilplomo (Dec a 200ºC) Tetraethile Lead Plomb Tétraethy C H Pble T8 20 g-L 20 68 R R

20 68 N L N N L N N N

50 122 N N

20 68 L N N

60 140 N

20 68 R R R R R R50 122 R R R R R R

60 140 R R R R93 200 R20 68 R60 140 L20 68 R R R R50 122 R60 140 R R R20 68 R R R R R R40 104 L R R50 122 N R R90 194 R20 68 N N R N L L N N N60 140 N N

Trementina Tur pentine Turpentine Tg-L 20 68 N R NTriclo-Robenceno Trichlorobenzene C H ClTrichloro-Benzene Sol. Trab.6 3 3 20 68 N N NTricloroetileno Trichloro-Ethylene Tricholo-Éthylène CHCl=CCl T2 g-L 20 68 N N R N N N N N N

20 68 R R N R50 122 R60 140 L

Tg-L 20 68 L N L NTrietilamina Trieth ylamine N(CH -CH ) T2 3 3 g-L 20 68 N N N NTrietilenglicol Triethylene Glycol Triethylene Gly C H Ocol 506 14 4 20 68 R R RTrifluoruro de Boro BFTrifluorure de Bore Sol. sat.3 20 68 R R R R

20 68 R R40 104 R60 140 L20 68 N N N60 140 N20 68 R R R R R R R R

50 122 R R R R R R60 140 R R R R L R80 176 R

100 212 N

20 68 N R R40 104 R R60 140 R R

80 176 R R

20 68 R L N R R R R R60 140 N R R R R

80 176 R20 68 R R R R R R R R

50 122 R R R R R

60 140 R R R R

20 68 R R R R R R R R

50 122 R R R R R60 140 R R R R

20 68 R R R R R R R R

50 122 R R R R R60 140 R R R R

20 68 N N R N L N N N N

40 104 L

20 68 R R R R R R R R

40 104 R R R R R R60 140 R R R R R

100 212 R R R R

20 68 R R R R R50 122 R R R

60 140 R R

20 68 R R R

50

Barium Sulfide

122 R

Sulfuro de Bario Sulfure de Barium BaS Sol. sat.

Calcium SulfideSulfuro de Calcio Sulfure de Calcium CaS Sol. dil.

H SSulfuro de Hidrógeno, Acuoso 2

H SSulfuro de Hidrógeno, Gas Seco 2

Hydrogen Sulfide

Tg-G

Sulfure d'Hydrogène

Potassium Sulfide Sulfure de Potassium

Hydrogen Sulfide, Gas Dry

Sol. sat.

Sulfure d'Hydrogène

Sol. sat.

K SSulfuro de Potasio 2

Sodium Sulfide

CClTetracloruro de Carbono 4

Sulfuro de Sodio Sulfure de Sodium Na S2 Sol. sat.

Tg-L

C H OTetrahidrofurano Tetrahydrofurane Tetrahydrofuran 4 8

Carbon Tetrachloride

Tg-L

Tétrachlorure de Carbone

Tg-L

Ammonium ThiocyanateTiocianato de Amonio Thyocianate d'Ammonium NH SCN4

C HTetralina Tetralin Tetralin 10 12

Sol. sat.

C H STiofeno 4 4

K S OTiosulfato de Potasio 2 2 3

Tiophene Tiophene

Sol. sat.

Sodium Thiosulfate Sodium Thiosulfate

Potassium Tiosulphate

Sol. sat.

Tiosulfate de Potassium

Tg-L

Tiosulfato de Sodio (Hiposulfito) NaS O ·5H O2 3 2

CH C HTolueno Toluene Toluène Tg-L3 6 5

(HOCH CH ) NTrietanolamina 2 2 3Sol.

Trimethylpropane

Triethanolamine Triethanolamine

(CH OH) C HTrimetil-Propano Trimethyl-Propane Hasta 102 3 3 5

Tg-L

Urea Urea Urée

Sulfur Trioxide

CO(NH ) 102 2

SOTrióxido de Azufre Trioxyde de Soufre 3

Vaselina Vaseline Vaseline

Vinagre Vinegar Vinaigre Sol. trab.

Vinos y Licores

Wine

Sol. trab.

Sol. trab.

Wine and Liquors

Vino Vin

Vin et Boissons Alcoolisées

Whiskey

C H (CH )Xilenos Tg-L6 4 3 2

Sol. trab.

Xylene Xylènes

Zumo de Manzana

Sol. trab.

Sol. trab.

Pomelo Juice

Whisky Whisky

Zumo de Fruta

Apple Juice Jus de Pomme

Zumo de Pomelo Jus de Pamplemousse

Fruit Juice Jus de Fruit Sol. trab.


TEMP.

ºC ºF

EV

A

EP

DM

FP

M

N

BR

H

DP

E

P

P

P

VC

-U

P

VC

-C

A

BS


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