condensate recovery system -technical guide

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  • 7/30/2019 Condensate Recovery System -Technical Guide

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    What is it?

    Condensate Recovery Systems are specically designedequipment to recover condensate rom steam

    installations in order to maximise their overall energyeciency.

    Condensate Recovery Systems equipment are

    considered to include the ollowing:

    Condensate Recovery Vessels

    These are designed to handle hot condensate, which is

    commonly returned or use as boiler eedwater.

    Steam TrapsAre devices which allow the

    discharge o condensatewithout the release o steam

    rom steam lines in a steam andcondensate system.

    Deaeration Tanks

    Remove oxygen and otherdissolved gasses rom steam

    boiler eedwater to reduce

    corrosion and improveeciency in the steam system.

    How does it work?

    A Condensate Recovery Unit is avessel which receives condensate

    rom all practical points in aprocess plant or heating system

    where condensate is produced.The vessel stores the condensate

    and mixes it with resh make upwater prior to it being used as

    boiler eedwater.

    Steam Traps are essentially valves which diferentiatebetween steam and condensate. They open to discharge

    condensate, but do not allow steam to escape. A steamtrap has three important unctions:

    To remove the condensate ormed either within the

    steam pipework or within the process equipment. To prevent large amounts o steam escaping.

    To enable any air and other gases in the system toescape.

    In a Deaeration Tankboiler eedwater is trickled downover perorated plates, low pressure steam is passed

    upwards to strip of oxygen and other dissolved gasses.The steam and gas rise to the top o the tank and are

    then vented to atmosphere.

    In another type o deaeration tank low pressure steam isinjected into the stored eedwater again the steam and

    gas rise to the top o the tank and are then vented to

    atmosphere. Depending on the size o the installationthe deaeration tank also acts as the eedwater storagetank.

    Technical GuideCondensate Recovery

    System

    Figure 1. Condensate

    Recovery Unit

    Figure 2. Ball Float Steam Trap

    (Image courtesy o Spirax Sarco)

    Figure 3. Dearation Tank

    (Image courtesy o Spirax Sarco)

    Dearation Tank(Image courtesy o Amarinth)

    Steam Trap

    (Image courtesy o Spirax Sarco)

    (mage courtesy o Spirax Sarco)

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    What are the energy saving benefts?

    Installing energy ecient technologies on an existing

    standard steam and condensate installation is a meanso improving boiler perormance without having to

    replace the entire steam boiler or system.

    Typical Energy savings or each o the technologies arelisted below:

    Condensate Recovery Vessels

    68%reductioninfuelcosts Typicalpaybackperiods1-4years

    Reducedcarbonemissions

    Steam Traps

    2-3%reductioninfuelcosts Typicalpaybackperiods2-4years

    Shorterstart-uptimes Reducedcarbonemissions

    Deaeration Tanks

    1-2%reductioninfuelcosts

    Typicalpaybackperiods4-6years Reducedriskofcorrosionfailures

    Reducedwatertreatmentcosts Reducedcarbonemissions

    Issues to consider when choosing a Condensate

    Recovery System:

    Condensate Recovery Vessels

    a) Where very long pipe runs would be requiredto return condensate to the boiler house,

    condensate recovery may not be viable inenergy terms.

    b) Even where long pipe runs make energy recoveryuneconomic condensate recovery may still be

    viable when the water treatment costs andwater replacement costs are taken into account.

    c) I the condensate can be contaminated bycontact with process materials it can cause

    ouling o the heat transer surace in the boiler.

    In such circumstances the condensate should

    be passed through a heat exchanger to recover

    heat energy.

    Steam Traps

    a) It is essential to select the correct size and typeo trap or both starting and normal operating

    loads. It is particularly important to size the trapto accommodate the increased condensate

    capacity at start-up, an incorrectly sized trapmaynotoperatecorrectlyandstart-uptimesare

    likely to increase.

    b) Trap sizing is based upon - normaloperationalload

    - (kg/hofcondensate) - start-upload

    - (kg/hofcondensate) - Condensatetemperature(max/min)

    - SteamPressure(max/min) - Backpressurethetrapmustoperateagainst

    c) Consult a reputable manuacturer or specicdesign and installation inormation.

    d) All types o steam trap ail i they are not properlymaintained or protected. The best method or

    ensuring correct trap operation and eciency is aplanned preventative maintenance programme.

    e) Failure monitoring o steam traps noties userwhen a steam trap has ailed.

    Deaeration Tanks

    a) Sucient space has to be available within or

    near to the boiler house to accommodate thedeaeration tank.

    b) Deaeration must be used in conjunction with

    other water treatment measures.c) Monitoring o the water condition must be

    carried out regularly, automatically or by

    sampling.

    Energy ecient Localised Steam Generator Systemsare eligible or the ACA (Accelerated Capital Allowance)

    and included on the Triple E product register. Moreinormation can be ound at www.seai.ie/Your_Business/

    Triple_E_Product_Register/

    Wilton Park House, Wilton Place, Dublin 2

    Teach Phirc Wilton, Pls Wilton, Baile tha Claith 2T. +353 1 808 2100

    F. +353 1 808 2002

    [email protected]

    www.seai.ie

    TheSutainableEnergy Authority of Ireland ispartlynanced by IrelandsEU StructuralFunds Programmeco-funded by theIris h Governmentand theEuropeanUnion.