heat ingeration of reactors

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    HEAT INTEGRATION OFREACTORSBy Siti Shawalliah Idris, AMIChemE

    CPE 633 PROCESS ENGINEERING II

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    Heat Integration Characteristics of Reactors

    Adiabatic operation➢ Heat carriers➢ Cold shot

    ➢ Indirect heat transfer with the reactor➢ Quench

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    Heat Integration Characteristics of Reactors (Cont’d)

    Indirect heat transfer with the reactor

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    Heat Integration Characteristics of Reactors (Cont’d)

    Exothermic Reaction

    A maximum can occur in the temperature at an intermediate pointbetween the reactor inlet and exit

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    Heat Integration Characteristics of Reactors (Cont’d)

    Endothermic Reaction

    A minimum can occur in the temperature at an intermediate pointbetween the reactor inlet and exit

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    Heat Integration Characteristics of Reactors (Cont’d)

    For indirect heat transfer, the heat integration characteristicsof the reactor can broken down into the following three case:

    If the reactor can be matched directly with other process stream,then the reactor profile should be included in the heat integrationproblem

    If a heat transfer intermediate is to be used and cooling/heatingmedium is fixed, then the cooling/heating medium should beincluded and not the reactor profile itself

    If a heat transfer intermediate is to be used but the temperatureof the cooling/heating medium should be included

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    Heat Integration Characteristics of Reactors (Cont’d)

    Batch reactor for a fixed rate ofheat transfer (exothermic reaction)A family of curves illustrates theeffect of increasing the rate ofheat removal and/or decreasingheat of reaction

    Each individual curve assumes the

    rate of heat transfer to the coolingmedium to be constant for thatcurve throughout the batch cycle

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    Heat Integration Characteristics of Reactors (Cont’d)

    Batch reactor for a fixedrate of heat transfer(endotherm)

    Fixing the rate of heattransfer in a batch reactor isoften not the best way tocontrolic reaction)

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    Heat Integration Characteristics of Reactors (Cont’d)

    The heat duty on the heating/cooling medium is given by

    Q react = −(Δ H streams+ Δ H react )

    Q react = reactor heating or cooling requiredΔ H streams = enthalpy change between feed and product streamsΔ H react = reaction enthalpy

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    Appropriate Placement of Reactors

    Exothermic reactor

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    Appropriate Placement of Reactors (Cont’d)

    Exothermic reactor integrated below the pinch

    Same hot utility: Cold utility increase!

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    Appropriate Placement of Reactors (Cont’d)

    Exothermic reactor integrated above the pinch

    Required hot utility is reduced by heat integration

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    Appropriate Placement of Reactors (Cont’d)

    Endothermic Reactor

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    Appropriate Placement of Reactors (Cont’d)

    Endothermic reactor integrated above the pinch

    The process needs more hot utility!

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    Appropriate Placement of Reactors (Cont’d)

    Endothermic reactor integrated below the pinch

    Required cold utility is reduced

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    Appropriate Placement of Reactors (Cont’d)

    The various streams associated with the reactor can becombined to form a grand composite curve for reactor

    This can then be matched against the grand composite curvefor the rest of the process

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    Case Study – Pthalic Anhydride

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    Case Study – Phthalic Anhydride (Cont’d)

    Stream Data

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    Case Study – Phthalic Anhydride (Cont’d)

    GCC for the process

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    Case Study – Phthalic Anhydride (Cont’d)

    Divides the GCC into twosections:

    ReactorsRest of the process

    Note:

    Grand composite curve forreactor includes the reactorfeed and effluent streams.

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    Case Study – Phthalic Anhydride (Cont’d)

    Match reactor against the process

    Appropriately placed in this case

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    Case Study – Phthalic Anhydride (Cont’d)

    What if the reactor is not appropriately placed?

    Usually change rest of the process, not reactor, to get appropriateplacement .

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    Heat Integration of Reactors (Cont’d)

    Heat integration will always benefit by making hotstreams hotter and cold streams colder

    This applies whether the heat integration is carried out directlybetween process streams or through an intermediate such as steam

    Care should be taken when preheating reactor feeds within thereactor using the heat of reactionIf the exothermic reactor is appropriately placed above the pinchand feed start below the pinch, then the preheating within the reactoris cross-pinch heat transfer

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    Heat Integration of Reactors – Summary

    The appropriate placement for exothermic reactors is above the pinch

    The appropriate placement for endothermic reactors is below the pinch

    If the reactor is not appropriately placed ,then it is more likely that the

    rest of the process would be changed to bring about appropriateplacement rather than changing the reactor

    If changes to the reactor design are possible, then the simple criterion ofmaking hot streams hotter and cold streams colder can be used to bringabout beneficial changes

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    Heat Integration of Reactors

    Working Session

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    Heat Integration of Reactors

    How can we improve performance ?

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