40-a-00008_e_tech spec gas module1.pdf

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    DOC. ID: 40-A-00008 REV/STATUS: E / Approved

    DATE: 17 Dec 2013 MADE/APPROVED: SIVAKOMA / TUUKAHON

    PAGE: 1(17)

    NAME: Technical Specification

    SUBJECT: Gas Receiving, Metering & ESD module

    CUST. DOC. ID:

    CITEC OY ABP.O. Box 109, FI-65101 VAASA, FINLAND, Tel. +358 6 3240 700 Fax +358 6 3240 850

    www.citec.com

    FUEL GAS RECEIVING,

    METERING & ESD

    MODULE

    (GAS MODULE 1)

    TECHNICAL SPECIFICATION

    Revision history

    Revision Made by Approved by Reason for revision

    ARamaswamyNeelakantan

    Jonas Nylund Original revision

    BRamaswamyNeelakantan

    Tuukka Ahonen Gas Filters added

    C SivakumarKomarasamy

    Tuukka Ahonen Updated gas fuelcomposition. Materialrequirements updated.

    D RamaswamyNeelakantan

    Jonas Nylund Module ArrangmentChanged

    E SivakumarKomarasamy

    Tuukka Ahonen Gas flowrate updation andESD location changed

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    TABLE OF CONTENTS

    1. DESIGN BASIS .......................................................................................................... 32. CODES AND STANDARDS ...................................................................................... 53. DESIGN INPUTS ....................................................................................................... 64. SYSTEM DESCRIPTION .......................................................................................... 75. SCOPE OF WORK ...................................................................................................... 96. TECHNICAL SPECIFICATIONS ............................................................................ 127. TERMINAL POINTS ................................................................................................ 13

    8.

    DATASHEET ............................................................................................................. 15

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    1. DESIGN BASIS

    FUEL GAS ANALYSIS - NATURAL GAS

    Natural gas will be used as preliminary fuel and Jet A1 fuel is used as back up fuel.

    Components Volume % Weight% Mol. Wt g/Mol

    C1(Methane) 97.83 94.98 16.04C2(Ethane) 1.22 2.22 30.07C3(Propane) 0.01 0.03 44.10i-C4(i-Butane) 0.07 0.21 58.12n-C4(n-Butane) 0.07 0.24 58.12

    i-C5(i-Pentane) 0.02 0.09 72.15n-C5(n-Pentane) 0.01 0.04 72.15C6+ (Hexane +) 0.01 0.05 84.0Mcyclo-C5 0.00 0.02 84.16Benzene 0.00 0.00 78.11Cyclo C6 0.00 0.01 84.16C7Heptane 0.072 0.43 96.0McycloC6 0.00 0.01 98.19Toluene 0.00 0.00 92.14C8 0.0078 0.05 107.00C2-Benzene 0.00 0.00 106.17mp-Xylene 0.00 0.00 106.17O-Xylene 0.00 0.00 106.17C9 0.00 0.01 121.0C10 0.00 0.00 134.0C11 0.00 0.00 147.0C12 0.00 0.00 161.0C13 0.00 0.00 175.0C14 0.00 0.00 190.0C15 0.00 0.00 206.0H2O 0.0006 0.00 18

    Nitrogen 0.20 0.34 28.01CO2 0.26 0.68 44.01H2S ( Refer Note) 0.00 0.00 34.08C7+ 0.01 0.09 102.7C12+ 0.00 0.00 210.0Total 100% 100%

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    For design, 5% on composition is considered. Fuel gas temperature will be vary depends on ambient

    conditions from 15C to 38C.

    Design ambient temperature for gas system 26C

    Min. Ambient temperature for gas system 14CMax. Ambient temperature for gas system 38C

    GENERAL FUEL GAS PROPERTIES

    Description Unit Value

    Molecular weight g/Mol 16.53Molar Density Kg mole/m3 4.503Mass Density Kg/m3 74.41Mass heat capacity kJ/kg C 2.947

    Specific heat kJ/kg mole C 48.70Thermal conductivity W/m K 4.305E-002Viscosity cP 1.400E-002HC dew point C -27.07

    Note: The above given general fuel gas property is based on 23.71C and 92 bar pressure.

    For all basic information about project, site details and requirements, please refer to

    the general specifications that are attached (Doc Id: 40-0000520).

    Components Unit Values

    Specific Gravity 0.567C7+ Density g/cc 0.750C12+ Density g/cc 0.834Dry Gross Cal. Value BTU/SCF 1022.0Wet Gross Cal. Value BTU/SCF 1004.0Water dew point C -25@90bar

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    2.

    CODES AND STANDARDS

    The module components shall comply with the latest editions of relevant standardsissued by EN standards unless otherwise specified. Here some of them mentioned,but this is not an exhaustive/full list:

    PED 97/23/EC The European Pressure Equipment Directive

    EN 1776 Requirements for the design, construction, commissioning,operation and maintenance of new gas measuring stations

    EN 12186 Gas supply systems, gas pressure regulating stations fortransmission and distribution. Functional requirements

    EN 1594:2009 Gas supply systems. Pipelines for maximum operating pressureover 16 bar. Functional requirements.

    EN 14382 Safety devices for gas pressure regulating stations andinstallations. Gas safety shut-off devices for operating pressureup to 100 bar

    EN 12732:2000 Gas supply systems. Welding steel pipework. Functional

    requirements

    EN 10204:2004 Metallic materials. Types of inspection documents

    EN 10208-2:2009 Steel pipes for pipelines for combustible fluids. Technicaldelivery conditions. Pipes of requirement class B

    EN 12068:1999 Cathodic protection. External organic coatings for the corrosionprotection of buried or immersed steel pipelines used inconjunction with cathodic protection. Tapes and shrinkablematerials

    EN 12327:2000 Gas supply systems. Pressure testing, commissioning anddecommissioning procedures. Functional requirements

    EN 12954:2001 Cathodic protection of buried or immersed metallic structures.General principles and application for pipelines

    EN 13445:2009 Unfired pressure vessels.

    EN 13480 Metallic industrial piping

    EN 14141:2003 Valves for natural gas transportation in pipelines. Performancerequirements and tests

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    EN 15001-1:2009 Gas infrastructure. Gas installation pipework with an operatingpressure greater than 0,5 bar for industrial installations andgreater than 5 bar for industrial and non-industrial installations.Detailed functional requirements for design, materials,construction, inspection and testing

    3.

    DESIGN INPUTS

    Fuel gas supply pressure & temperature at Gas Receiving & Metering module inlet batterylimit

    PressureNormal Fuel gas supply pressure = 54 Bar (g)Mechanical Design pressure = 86 Bar (g)

    TemperatureMinimum Fuel gas supply temperature = 15 CNormal Fuel gas supply temperature = 25 CMaximum temperature = 38 CMechanical Design temperature = 50 C

    Flow

    Minimum * = [GE to specify later, will be from zero] kg/hr x 1 GT runningNormal ** = 7904 kg/hr x 4 GT = 31616 kg/hr (GT at base load & Chiller ON)

    OR

    Maximum = 10272.73 kg/hr x 4 GT = 41090.92 kg/hr

    * GT at ambient temperature of 35 C, GT at base load & Chiller Off** GT at ambient temperature of 15 C, GT at base load & Chiller ON (463 kBtu/hr)

    For all information about mechanical design values and conditions, please refer to

    the general specifications that are attached (Doc Id: 40-0000520).

    Design shall be according to EN codes & Standards.

    E

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    4. SYSTEM DESCRIPTION

    The Fuel Gas System for the plant conveys natural gas from the terminal point of plantnormally at 54 Bar (g) & operating temperature of 15-38 C at proper conditions, aboveground to the Gas turbine unit. Maximum supply pressure will be 86bar(g).

    The gas fuel supply system consists of following modules common for 4 Gas turbines:

    #1 Gas Receiving & Metering with ESD Modules (2 X 75%)

    2 x 75 % filters (for liquid drops and particles removal),

    2 x 75 % flow meters, 2 x 75 % Emergency shutdown valves Online provision for 2 Gas chromatographs in each stream 1 x 100 % Condensate Drain Tank

    For normal and emergency operation / condition one (2x75%) solenoid operated quick actingtype Emergency Shutdown valve (ESD) is provided for supply and isolation of Fuel gas. ESDvalve shall be single or double solenoid operated pneumatic on-off valve. Flow meter (2x75%)provided for invoicing measuring purpose. Drains from the modules are directly led to thecommon plant fuel gas condensate drain tank (1 x100%).The module is provided with Onlineprovision for connecting Gas chromatographs. Drains from the modules are directly led to

    the common plant fuel gas condensate drain tank (1 x100%).

    #2 Gas conditioning Module (1 X 100%)

    1 x 100 % indirect gas fired water bath heater with gas burner & Chimney

    Fuel gas Scrubber/filter for burners

    The fuel gas from the Gas Receiving & Metering with ESD Modules will be directed to 1 x100% indirect water bath heater with gas burner.

    Indirect bath gas heater (1 x100%) is provided to compensate the temperature drop due tothe heat loss to the ambient from the pipeline and to increase/control the Fuel gastemperature required by the Gas Turbine. Fuel gas heating is done to a temperature of 70Deg.C.

    #3 Pressure Control Module (2 x 100% + 1 x 30%)

    Two (2x100%) main Pressure reduction and control valves and one (1x30%) start up controlvalve are located at the downstream of indirect gas fired water bath heater to meet the flowrange of gas requirement of One (1) Gas Turbine start up to Four (4) Gas Turbines on full

    load operation.

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    The shut off valves shall be provided with open/close limit switches and the PRVs are

    provided with position feedback for monitoring the status of the valves in LCP (local controlpanel) and provisionally DCS.

    Regarding all modules

    A pipeline vent connection will be provided near gas turbine inlet to vent out entrappedgases during cold start-up of the plant to vent stack. Module vendor to provide equipmentand pipeline vent connections at module border. Normally, for all equipment, one vent linewill contain manually operated ball valves for initial purging. All vents on natural gas linesshall be connected to vent stack. The pressure safety system shall be ensured by providingsuitable pressure safety valves and the system vents will be connected to vent stack (ventstack excluded from module scope).

    Natural Gas lines shall be carbon steel piping.

    Vendor is responsible for the module engineering. Customer has the right to review andrequire changes to the vendor engineering documents. Vendor is allowed optionally topropose gas fuel supply system in a different amount of modules. I.e. the total system can bedivided into modules in a different way than presented here and there can be fewer modulesthan presented here. However the functionality & performance must fulfil the requirementsin these specifications.

    The fuel gas modules shall be designed for outdoor installation and shall be suitably sized to

    meet the fuel gas requirement of 4 gas turbines for the site design conditions and the purityof gas as per gas turbine manufacturers requirement / specification.

    This specification covers the scope of work for Fuel gas receiving, metering, ESD Module (GasModule 1)

    TANESCO JEL 100% JEL GE

    100%

    30%

    BATH HEATER PCV

    PCV

    PCV

    ESD

    ESD

    FILTER

    FILTER

    FLOW METER

    FLOW METER

    PROCESS FLOW SKETCH - FUEL GAS

    E

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    5. SCOPE OF WORK

    The scope of supply of the vendor under this specification and associated data sheetis intended to cover design, engineering, manufacture, assembly, testing and supplyof the skid with all accessories, site installation supervision, commissioningsupervision, performance guarantee testing, operator training and training materialand handing over of items related to 2 x 75% Gas Module 1 as defined in Scope ofwork, Technical Specification or elsewhere in this specification.

    All supplied materials/equipment shall be new and unused. The vendor shall acceptfull responsibility for his work including documentation, manufacture, preparationfor shipment, inspection, warranty provisions, compliance with the applicable codesand standards and the requirements of this Specification. The scope of supply and

    services shall include all necessary work and supply of equipment and materialwhether mentioned in these specifications or not, but which are necessary for thesatisfactory, reliable and safe operation and maintenance of the plant and requiredfor achieving guaranteed performance of the plant. Any equipment, device ormaterial even if not included in the original bid but found necessary for the safe andsatisfactory functioning of the units under the bid shall be supplied by the vendor atno extra cost. The module should be delivered in a properly packed condition asspecified here in under but not limited to:

    Gas Module #1 is comprised of 2 x75% Stream. The skid details proposed in thisspecification and P&ID (Doc No 40-0000809) are indicative only. Vendor can also

    suggest better system than specified. Complete gas Module #1 shall be designed tomeet the main fuel requirements of 4 Gas turbines and comprises of:

    Inlet manual isolation station according to double block & bleed arrangement

    2 x 75% Solenoid assisted (with single or double solenoid coils) pneumaticallyoperated emergency shutdown (ESD) valve Class VI leakage class (fire safe).Vendor can also consider also motor operated (not primary option).

    2x75% filters to remove foreign particles & liquids. Filters shall be equippedwith automatic drain arrangement and pressure difference measurement and

    alarm. The natural gas shall pass filter tubes and elements that capture solidparticles and cause liquids to coalesce into larger droplets, which are thencaptured by the wire mesh or vane mist extractor.

    2 x 75% fuel gas meters shall be of EN approved type for invoicing purposes,with flow transmitters connected to DCS and with totaliser(s). The metershall be able to measure the flow rate from (0) zero to design flow at therequired accuracy for invoicing purposes.

    Standard instrumentation and valves for the safe and efficient operation ofthe module mounted equipment

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    Connection for two online Gas chromatograph(s) for each streams and as an

    option two gas chromatographs. The chromatograph kits, complete in allrespects, (including calibration gas etc) shall be able to measure for exampleH2S, specific gravity and gas composition. (Prices for these optional gaschromatographs to be given separately.)

    One (1) above ground horizontal fuel gas condensate drain tank, for collectingdrains from all the modules. Drain tank shall be complete with vent withflame arrestor & instrumentation and other accessories as required. The draintank shall be also provided with a condensate trap arrangement, levelindication & alarm to local panel and DCS. Manual condensate dra in pump tobe provided on drain tank for the final disposal of hydrocarbon condensate.The pump shall be mounted on the top of tank or side mounted suitable forthis application. The discharge of pump will be connected to truck throughhose connection which is to be terminated at module battery limit. Vendorshall note that due to drain tank shall be above ground the other units mayhave to be on elevated level in order to ensure gravity draining to tank.

    Only one external nitrogen connection for each module will be provided to thevendor. Vendor to tap off as per module requirements from externalconnection.

    Nitrogen purging line with check valve and double isolating manual ball valveto be provided inside the skid area to purge the pipeline & skid equipment,

    before charging with fuel gas and also to purge the entrapped gas in pipeline& skid equipment while taking-up maintenance jobs/long shutdown.

    Internal nitrogen purging connections & internal piping inside the module asrequired based on the system design shall be taken care by the vendor (onlyone external connection is allowed). Bidder shall provide requisite number oftapings for nitrogen purging as the standard practices, the number indicatedin the P&ID attached shall be treated as minimum

    Drain lines with double isolation valve

    Two numbers of portable gas detectors (totally 2 numbers for all three gasmodules together) of the flame ionization metering type, capable of detectingfuel gas in concentration of one part per million. All necessary detectoraccessories shall be included.

    Manual depressurisation line with double isolation valves to be providedaccordingly inside the module wherever needed.

    Relief valves to be provided accordingly inside the module.

    All the vents / drains to be connected to a common header & terminated at

    module terminal

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    All piping, valves and accessories as required to complete the system

    All equipment, C&I devices shall be suitable for E Ex _ II A T1 for Naturalgas systems (normally T class, however, T3 or higher T4, is ok). Ex classnormally E Ex d. Instruments normally other type depending on the zone andif barriers are used or not.

    Modules/skids for Natural gas are located at Ex zone 2.

    All interconnecting piping, valves, specialities, supports within Modulemounted equipment as shown in the P&ID as minimum. It is Suppliersresponsibility to provide all piping components as necessary for the safeoperation of the system

    Instrumentation & control system including instruments, interlocking &protection devices complete in all respects required for safe, efficient andreliable operation of the system as per P&ID (Doc No 40-0000809).

    All foundation bolts/anchor bolts, insert plates, pipe sleeves, embedment, etcrequired for any equipment/ foundation/ concrete under the package.(Foundations are excluded from scope.)

    Local control station/Local Push Button Station (Flame proof) shall beprovided for each skid to enable complete operation of skid. Module1# and

    module 3# shall have a common Local control station

    All instrumentation valves shall have double isolation valves.

    It shall be possible to provide all analogue and digital signals to plant DCS.

    All required documentation from vendor is presented in attachedRequirements for Documentation , doc nr 40-A-00175.

    E

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    7.

    TERMINAL POINTS

    S.NO DESCRIPTION SCOPE

    A. MECHANICAL

    1. Fuel Gas

    Inlet of the Module terminal withcounter flanges

    Outlet of the Module terminal withcounter flanges

    2. Drains

    All drains connected to a commonheader & terminated at Outlet ofModule with counter flange/stubconnection.

    3. Vents

    Gas vents / safety valve dischargeto be connected individually to acommon header. The header to be

    terminated at the module terminalpoint.

    4. Nitrogen Connection at module terminal

    5. Instrument air7 barg, dryness +3 deg C(flange connection at moduleterminal)

    B. ELECTRICAL

    1. Earthing Two earthing terminals atdiagonally opposite locations of theskid

    Notes

    1. Flange connections shall be provided with its counter flange, bolts, nuts andgaskets.

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    Exclusions

    1.Foundations of Gas Receiving, Metering & ESD Module2.Civil construction work like building, equipment foundation etc3.Erection of Module and its accessories4.Fire fighting system5.Nitrogen piping up to supply point in module6.Instrument piping up to supply point in module7.Supply of Cables from local JB to Control room

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    8. DATASHEET

    The given below datasheet to be filled in by the Vendor .

    S.NO PARTICULARS UNIT VALUES

    1.0 General

    Design Standard

    Module

    Equipment shall be designed forseismic loads

    Fuel Gas Supply Conditions

    Gas Flow at inlet of Module

    Gas Supply Pressure at inlet ofmoduleGas Supply Temperature at inletof module

    2.0 Design & Performance Requirement

    General

    Maximum Gas Velocity insidepipeline under maximum operatingconditions

    M/SEC

    20 unfiltered35 filtered

    Gas Pressure at outlet of Module

    Gas Temperature at outlet of Module

    Max. Pressure drop across the

    ModuleGas Design Pressure

    Gas Design Temperature

    Filter

    Type

    Quantity Nos. 2 X 75%

    Design gas flow

    Mesh Size

    E

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    Particle Size Removal

    Pressure Drop at design flow bar

    Emergency shut-down Valve

    Type of valve Ball

    Type of operation

    Actuator

    Quantity 2 X 75%

    Leakage class

    Operation time (fully open-close) sec

    Material (Body/trim)

    Size

    PN-class

    Fuel Gas Condensate Drain Tank

    Type Horizontal

    Quantity One (1)x100%

    Capacity*(3 m3) or vary

    accorindgly* The drain tank capacity indicated is for guideline only. It is Biddersresponsibility to size the drain tank based on his engineering andexperience. Drain tank evacuation cycle shall be once in 14 days ormore seldom. Drain tank discharge pump shall be capable of emptyingthe tank into a truck in one hour

    3.0 Safety valves

    Quantity

    Capacity

    Type

    Set point Bar(g)

    Leakage class

    Size DNin/DNout

    PN-class PN

    Materials

    3.0 Isolation valves

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    Quantity

    Capacity

    Type

    Leakage class

    Size DN

    PN-class PN

    Material (Body/Trim)

    4.0 Instruments

    Type

    Make

    Model

    Range

    Accuracy / Accuracy class

    5.0 External signals

    Name

    Type

    6.0 Material of Construction

    Gas Pipes

    Other valves (Body/Trim)

    Flanges

    Bolts

    Nuts

    Note : Vendor to Submit complete details of all items (if additional from this

    data sheet) as suitable required for this Skid