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Thread: Thumb Rules For Process Engineers

  1. Re: Thumb Rules For Process Engineers

    Please send to totoacosta@gmail.com. A lot of thanks!

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  3. #206

    Join Date
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    Re: Thumb Rules For Process Engineers

    Please send me to emkan90@gmail.com. Thank you very much!!!

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  5. #207

    Re: Thumb Rules For Process Engineers

    thanks please send to me rezaasgarie@yahoo.com mostafa jan

  6. Re: Thumb Rules For Process Engineers

    kindly send me on mkshah42@yahoo.com
    THANK YOU

  7. Re: Thumb Rules For Process Engineers

    please send to me rangga.hendri@gmail.com , thanks

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  9. #210

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    Jakarta, Indonesia, Indonesia
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    Re: Thumb Rules For Process Engineers

    send it to rkmnsetiawan@gmail.com

    thanks a lot

  10. #211

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    Re: Thumb Rules For Process Engineers

    HI

    Please somebody send it to mee it is very importan to me.

    apusztaszeri@gmail.com

  11. Re: Thumb Rules For Process Engineers

    please send it to wilman252000@yahoo.com, thanks

  12. Re: Thumb Rules For Process Engineers

    HI

    Please somebody send it to me

    sathish_che@yahoo.co.in
    with regards
    sathish kumar

  13. Re: Thumb Rules For Process Engineers

    Kindly send it to yogacruise@gmail.com

    Thank you

  14. Re: Thumb Rules For Process Engineers

    Please somebody send to me

    cborrsan@gmail.com

    Regards

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  16. Re: Thumb Rules For Process Engineers

    Dear Mr. Jprocess,
    Could you please sem me all documents? My email nguyenlethuanhoang@gmail.com
    Quote Originally Posted by jprocess View Post
    Dear All,

    My new offer for all of you regarding to Knowledge Sharing is a spreadsheet called "Thumb Rules For Process Engineers" and covers the following subjects:

    PIPING PRESSURE DROP : For Raynold's no 2100 to 106
    EQUIVALENT LENGHTS for Pressure drop in the system
    MAXIMUM ALLOWABLE FLOW OF STEAM THROUGH PIPE 41, 12 & 2" only
    ALLOWABLE VELOCITIES FOR PROCESS FLUIDS
    SONIC VELOCITY CALCULATION
    PERMANENT HEAD LOSS THROUGH ORIFICE
    VENTURI Pressure Drop
    FLOW RECTANGULAR WEIR
    CONTROL VALVE SIZING
    RELIEF VALVE SIZING FOR LIQUID EXPANSION
    STORAGE VESSEL VOLUMES
    NPSH
    Pressure Drop in Pipeline
    TUBESIDE PRESSURE DROP IN SHELL & TUBE HEAT EXCHANGER
    MOTORS kVA
    MOTORS AMPS ETIMATE
    CENTRIFUGAL COMPRESSOR HP
    CENTRIFUGAL COMPRESSOR HEAD
    TEMPERATURE RISE IN COMPRESSION
    PUMP EFFICIENCY
    PUMP HORSE POWER
    RELATION OF HP, IMPELLER DIA & SPEED
    RELATION BETWEEN PUMP HEAD, IMPELLER DIA & SPEED
    CHANGE IN PUMP CAPACITY WITH IMPELLER DIAMETER
    TUBESIDE PRESSURE DROP IN AIR COOLED HEAT EXCHANGER
    MOTOR HP OUTPUT
    MOTOR TORQUE
    GAS EXPANDERS : AVAILABLE ENERGY
    POWER FACTOR
    SELECTION OF TYPE OF VACUUM EQUIPMENT
    FAN / BLOWER OR COMPRESSOR
    SPRAY WATER FOR PRDS
    MAXIMUM AVAILABLE ENERGY (EXERGY)
    FUEL TO AIR RATIO
    COOLING TOWERS : WINDAGE LOSSES
    COOLING WATER CONCENTRATION RATIO
    APPROXIMATE EFFICIENCIES OF COMPRESSORS
    Physical Properties

    Anyone who is interested of having a copy of it can send his/her request to my e-mail address (jprocessman@yahoo.com)

    Best of Luck,
    Mojtaba

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