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CLIMBING FILM PIPE EVAPORATOR MODEL: BP 210 HE Climbing Film Pipe Evaporator (Model: BP 210) has been designed for student demonstration on climbing film evaporation process. This floor standing pilot-plant unit consists mainly of an evaporator tube, a feed tank, a feed pump, a cyclone separator, vessels for distillate and concentrate, and a The dilute feed from the feed tank enters the bottom of the evaporator tube, on the outside of which steam is condensing. The feed is often below its boiling point, and for a short distance, the feed to the tube flows upward as a liquid and receives heat from the condensing steam. Bubbles of vapour are formed when boiling of the liquid commences, and they increase the linear velocity of the flow, thus increasing the rate of heat transfer. Towards the end of the tube, bubble growth is rapid, and bubbles of vapour alternating with slugs of liquid rise quickly through the tube and discharge at a high velocity from the top. The resulting mixture of liquid and vapour then enters the separator, where the linear velocity of the vapour is reduced, allowing the separation of the liquid and vapour streams to take place. The concentrated liquor can then be removed from the system (once through operation) or can be recycled for further concentration (re-circulation). The vapour leaves the top of the separator to a condenser and collected or discarded as distillate. vacuum pump. The unit is suitable for the evaporation and concentration of heat sensitive products such as milk, fruit juices, etc. Using the existing laboratory steam supply students will conduct experiments to study the effects on evaporation rate of feed flow rate and temperature, and evaporator temperature and pressure. Students will also study the effect of process parameters on the evaporator economy. T SOLTEQ-QVF Equipment for Engineering Education & Research

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CLIMBING FILM PIPE

EVAPORATORMODEL: BP 210

HE Climbing Film Pipe Evaporator (Model: BP 210) has been designed for student demonstration

on climbing film evaporation process. This floor standing pilot-plant unit consists mainly of an evaporator

tube, a feed tank, a feed pump, a cyclone separator, vessels for distillate and concentrate, and a

The dilute feed from the feed tank enters the bottom

of the evaporator tube, on the outside of which steam

is condensing. The feed is often below its boiling

point, and for a short distance, the feed to the tube

flows upward as a liquid and receives heat from the

condensing steam. Bubbles of vapour are formed

when boiling of the liquid commences, and they

increase the linear velocity of the flow, thus increasing

the rate of heat transfer. Towards the end of the tube,

bubble growth is rapid, and bubbles of vapour

alternating with slugs of liquid rise quickly through the

tube and discharge at a high velocity from the top.

The resulting mixture of liquid and vapour then enters

the separator, where the linear velocity of the vapour

is reduced, allowing the separation of the liquid and

vapour streams to take place. The concentrated liquor

can then be removed from the system (once through

operation) or can be recycled for further concentration

(re-circulation). The vapour leaves the top of the

separator to a condenser and collected or discarded

as distillate.

vacuum pump. The unit is suitable for the evaporation and concentration of heat sensitive products such as

milk, fruit juices, etc. Using the existing laboratory steam supply students will conduct experiments to study the

effects on evaporation rate of feed flow rate and temperature, and evaporator temperature and pressure. Students

will also study the effect of process parameters on the evaporator economy.

T

SOLTEQ-QVF™Equipment for Engineering Education & Research

SOLTEQ

EXPERIMENTAL CAPABILITIES

♦ Mass and heat balances.

♦ Determination of evaporator capacity and

economy.

♦ The effect of steam pressure, feed flow rate and

evaporator pressure on the evaporation rate.

♦ The effect of sensible and evaporative heat loads

on evaporator capacity.

♦ The effect of process parameter on the evaporator

economy.

SPECIFICATIONS

Evaporator Tube (W1)

Shell and tube made of borosilicate glass

Size: DN25 (shell); DN15 (tube)

Length = 1,700 mm

Inlets for steam and feed liquid.

Outlets for thick liquor, vapour, steam condensate, and

non-condensable gasses from the steam.

Feed Vessel (B1)

5-L graduated vessel made of glass with charge port,

vacuum connection and venting.

Concentrate Vessel (B2)

2.5-L graduated cylindrical vessel made of glass with

charge port.

Cyclone Separator (B3)

High efficiency cyclone made of glass for separation

of concentrate and vapour (distillate).

Distillate Vessels (B4 & B5)

5-L graduated vessel made of glass with vacuum

connection and venting.

Condenser (W2)

High efficiency coil heat exchanger made of

borosilicate glass with cooling water connectioins.

Exchange area: 0.7 m2.

Feed Pump (P1)

Chemical metering pump with bypass valve.

Capacity: 10 L/hr.

Vacuum Pump (P2)

Chemical resistant diaphragm pump delivering down

to 8 mbar vacuum at a flow rate of up to 2.5 m3/h.

Comes complete with a vacuum controller, suction side

separator and pressure side emission condenser.

Instrument and Control

Temperature measurements for concentrate, steam,

and cooling water inlet and outlet.

Flow rate mesurements for feed, steam and cooling

water.

Pressure measurements for evaporator and steam.

Framework

Stainless steel pipe with all necessary holders and

brackets.

Technical Data

Evaporation rate : up to 10 kg/h (water)

Steam consumption : max. 15 kg/h

Max. steam pressure : 1.7 bar

Operating pressure : vacuum, standard pressure.

Over pressure max. 0.5 bar

OPTIONAL ITEMS

-EI

DIGITAL INSTRUMENTATIONS

i) 4 units of temperature sensors

ii) 2 units of flow transducers

iii) 2 units of pressure transducers

iv) 3 units of digital indicators

-DAS

SOLDAS DATA ACQUISITION SYSTEM

i) PC with latest Pentium Processor

SOLTEQ-QVF™Equipment for Engineering Education & Research

SOLTEQ-QVF™Equipment for Engineering Education & Research

ii) Electronic signal conditioning system

iii) Stand alone data acquisition modules

iv) Windows based software

- CAL

SOLCAL COMPUTER AIDED LEARNING

SOFTWARE

i) Interactive multimedia features

ii) Graphical simulation

iii) Experiment results samples

iv) Full experiment manuals

REQUIREMENTS

Steam Supply : 20 kg/hr @ 2 bar (g)

Water Supply : 25 LPM @ 10 m head

SOLTEQ

OVERALL DIMENSIONS

Height : 3.00 m

Width : 1.00 m

Depth : 0.60 m

MANUAL

The unit is supplied with Operating and Experiment

Manuals in English giving full descriptions of the unit,

summary of theory, experimental procedures and

typical experimental results.

Our range of teaching equipment can be complemented with our

SOLDAS and SOLCAL software.

SOFTWARE & E - LEARNING

SOLDAS® - Supervisory Control & Data Acquisition

- Data Logging

- Signal Analysis

- Process Control

- Real-Time Display

- Tabulated Results

- Graph of Experimental Results

SOLCAL® - Computer Aided Learning

- Multimedia Features

- Interactive

- Graphic Simulation

- Experiment Result Samples

- Full Experiment Manuals

Contact us for a catalog CD

SOLUTION ENGINEERING SDN. BHD.(Co. No. 174876-M)

Sales Office :

No.3, Jalan TPK 2/4, Taman Perindustrian Kinrara,47100 Puchong, Selangor Darul Ehsan, Malaysia.Tel. No. : +(603) 80758000Fax. No. : +(603) 80755784

R&D Office :

G-2A, Incubator 3, Technology Park Malaysia,Bukit Jalil, 57000 Kuala Lumpur, Malaysia.Tel. No. : +(603) 8996 0023

Email : [email protected] site : http//www.solution.com.my/

AGENT:

SOLTEQ-QVF™Equipment for Engineering Education & Research

BUATAN MALAYSIA

MSC- StatusCompany