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Chemical Plant Cooling Systems

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    Filename and location14/03/2006 1

    Cooling Systems

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    Purpose of Cooling Systems

    Prevention of over-heating of process equipment

    Prevention of product damage

    Ensure desired performance of process equipment

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    Cooling Systems

    Generally, the types of cooling available offshore are- Closed Circuit Cooling Water (CCCW)

    Direct seawater

    Air cooling

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    Typical Cooling Loads

    Process cooling - Crude oil ~ 0.6-0.7 kW/(m3/h.oC)

    Condensate ~ 0.3-0.4 kW/(m3/h.oC)

    Gas (no condensation) ~ 500-800 kW/(m3/h.oC)

    Produced water cooling ~ 1.2 kW/(m3/h.oC)

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    Utility Cooling - Instrument/plant air after cooling ~ 350 kW/(106Sm3/h.oC)

    Turbine lube oil / seal oil cooling ~ 10% of driver rating(kW)

    Compressor lube oil / seal oil cooling ~ 10% of driver rating

    Pump motor cooling ~ 10% of motor rating

    Diving facilities ~ 200kW

    Air conditioning - small ~ 150kW

    medium ~ 300kW

    large ~ 500kW

    Typical Cooling Loads

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    Schematic of a Typical CCCW System

    SEA WATERSUPPLY

    OPEN

    DRAINS

    GLYCOLMAKE-UP

    WATERMAKE-UP

    LP FLARE

    SEAWATER

    RETURNTC

    TCV

    CCCW CIRCULATINGPUMPS

    FC

    TURBINE

    GENERATOR

    COOLERS

    FCV

    CRUDE OILLOADING

    COOLERS

    COMPRESSIONCOOLERS

    PLATE HEATEXCHANGERS

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    Closed Circuit Cooling Water

    (CCCW) Systems

    Utilises a closed circuit of glycol and water mixture which

    is cooled by exchange with sea water

    Type of glycol used is dependent on glycol that is used on

    the platform, i.e. TEG or MEG. Typical glycol concentration is 30 - 40% w/w

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    Corrosion inhibitors are injected into the cooling medium

    Permits use of carbon steel piping

    Use of CCCW is limited to situations where contamination

    by seawater of the cooled stream is to be avoided I.e. compressor seal / lube oil cooler, crude shipping pump coolers

    Closed Circuit Cooling Water

    (CCCW) Systems

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    CCCW System Design

    To determine total cooling loads, Q, summate allcoincident loads and add an allowance for run-up of

    largest spare machine.

    To determine flowrate, m, use inlet and outlet

    temperatures, T and specific heats, CP of glycol solution

    i.e.

    TmCQ P=

    Pump design capacity is approximately 1.25*calculated

    total load flowrate as a safety margin

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    CCCW System Design

    Header sizing is based on pressure drop and velocity offluid

    Non-boiling liquid should be approximately 15oC below bubble

    point

    The sea water circulating pumps should have a flat head

    characteristic in order to avoid excessive design pressureon the plate heat exchangers

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    CCCW System Design

    Heat Exchangers - For initial sizing of heat exchangers use -

    CCCW 32oC in and 18oC out

    Seawater 15oC in and 27oC out

    Header Tanks -

    Size based on thermal expansion and the design pressure of the

    system to cater for tube rupture on the heat exchangers

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    Direct Seawater Cooling System

    TO SEAWATER

    DUMP HEADER

    FROM SEAWATER

    FILTER PACKAGE

    INLET GAS

    COOLER

    TEST

    SEPARATOR

    COOLER

    FLASH GAS

    AFTER

    COOLERDEW

    POINT

    COOLER

    CRUDE OIL

    COOLER

    PIPELINE COMPRESSOR

    AFTER COOLER

    FLASH GAS

    COOLERS

    BOOSTER

    COMPRESSOR

    COOLER

    PLATFORM

    TOILETS

    SEWAGE

    TREATMENT

    UNIT

    HVACSYSTEM

    DESALINATION

    PACKAGE

    SEAWATER

    CCCW

    EXCHANGER

    EQUIPMENT

    OVERFLOWS

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    Direct Seawater Cooling Systems

    - Advantages

    Results in a lower overall system weight and space

    compared to CCCW

    Due to lower operating temperature and hence larger temperature

    difference and elimination of the seawater/CCCW heat exchangers

    Process outlet temperatures down to 18oC are possible

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    Corrosion resistant (more expensive) materials needed for

    construction

    E.g. cupro-nickel

    Colder skin temperatures may cause hydrate or waxing

    problems in exchangers

    Higher maintenance / downtime

    Seawater to be used must be treated with hypochlorite and

    filtered to 80 - 120m

    Flow rates may be high due to lower return temperaturelimitations

    Direct Seawater Cooling Systems

    - Disadvantages

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    Air Cooling Systems - Advantages

    Can still be used in the event of CCCW failure Ideal for emergency and life support equipment

    Low power requirement

    Only occasionally are air coolers considered for offshore

    cooling duties

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    Large in size and weight occupying a lot of space

    Expensive to operate

    Required temperatures lower than ~ 65oC are not possible

    Low efficiency

    Variable cooling rates difficult to achieve

    Air Cooling Systems - Disadvantages


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