پروسه طراحی یک مبدل گرمایی بوسیله aspenplus نرم افزار

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heat exchenger in aspen hysys

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  • 62

    : sulP nepsA . . . . .

    :

    1 - : 21 noerF rh/ gk 06501

    K 042 K 003 . K 053 . . hcaorppA K 01 . 02 GWB 1 gisP 01 ( 76/0)

    .

    : rotalumiSnepsA

    sulPnepsA

    ( )

    regnahcxE taeH a rof erudecorP ngiseD erawftoS sulPnepsA eht no (enO tarP)

  • 72

    . nepsA - {2 43 5 86 9} . pleH

    {1} . 2 puteS 1 . 3 . nepsA

    1- - .

    nepsA DTML . . porD erusserP . . . 2 .

    .

  • 82

    sdohtem U . 3

    . U - .

    :

    eulav U tnatsnoC ( U ): .

    .

    seulav cfiiceps esahP ( ): . ( ....

    )

    noisserpxe wal rewoP ( ) : nepsA . . U 4 .

    1.

    -

  • 92

    .

    yrtemoeg regnahcxE ( ) :

    .

    tneicffieoc mliF ( ) : U (oh ih) . (

    .)

    enituorbus resU : U .

    tneicffieoc mliF . 4 .

    4 . ( .) sdohtem U . " yrtemoeG morF etaluclaC " . ( ) . .

    . . nepsA . 5 . . .

    2.

    3.

  • 03

    : (1) =ML AQUT (/ )

    (Q) . )U) . {6 5 4 3} U . 2 /. WKm 051 {3} . 02 . . . 1 5/1 . 21 noerF

    1 . . 8 02 - 2 8 . . 6 . { 3 }

    : k/tN) * .D.O = (eldnuB ebuT) D)^(1/n)

    : tN :

    D.O. : . n , k : .

    4.

  • 13

    k = 942,0n = 702,2 . . 7 . . 01 09 . {5 3}

    . yrtemoeG . 5

    . .

    epyt llehs AMET : .

    {6} . ssessap ebut fo.oN :

    . 2 .

    5.

  • 23

    noitatneiro regnahcxE : . (

    .)sriap pirts gnilaes fo rebmuN :

    . retemaid llehs edisnI : . (

    .)ecnaraelc eldnub ot llehS :

    . 6 .

    . :

    epyt ebut tceleS : 8 9 . .

    rebmun latoT : . nrettaP : 01

    6.

  • 33

    11 . .

    hctiP : - . 52/1

    . lairetaM : . nepsA .

    .ytivitcudnoC : .

    . eziS ebuT : .

    . . 7

    7.

  • 43

    . . nepsA .

    7 . epyt efflaB : . . . . ( 7

    .) {6} . sessap lla , sefflab fo .oN : . . 5 01 . .

    . tuC efflaB : . 7 52/0 57 % 52 %

    . 0 5/0 . gnicaps efflab ts1 ot teehsebuT :

    . gnicaps efflab ot efflaB :

    . gnicaps teehsebut ot efflab tsaL :

    . : 2 3 . / .

    . ecnaraelc efflab llehS : .

    . ecnaraelc efflab ebuT : .

    .

    8.

  • 53

    9.

    01.

    11.

    () efflaB . 8 . .

    . retemaid elzzon telni llehS : . -

    .

    retemaid elzzon teltuo llehS : .

    .

  • 63

    retemaid elzzon telni ebuT : . - -

    .

    retemaid elzzon teltuo ebuT : .

    . . . txeN . (

    .)

    21.

  • 73

    (yrammuS)

    9 . . .

    . sliateD regnahcxE . 01 . .

    . . nepsA 2 /. WKm 6/86 2 /. WKm 051 .

    .

    . seiticoleV / porD erusserP 11 . . . .

    . .

    nepsA . ( . 01%

  • 83

    .) .

    . 21 sliateD regnahcxE

    . 31 % . ( 21- 01 % nepsA .)

    . stluseR deliateD

    . 31 elffab . nepsA . (SB = 22,0 )

    . . puteS . noitacfiicepS regnahcxE yrtemoeG .

    21 .

    . . . 01 . . 41 . noerF .

    . puteS noitacfiicepS regnahcxE teltuo maerts dloC

    41.

    31.

  • 39

    . .temperature .

    . :

    Aspen Plus Simulator 10.01- User Interface (1998)Branan. Carl. Rules of Thumb for Chemical Engineers , 2nd ed. , Gulf Publishing Company , 1998Coulson and Richardson, Chemical Engineering Fluid Flow , Heat Transfer and Mass Transfer , Volume 1 , 5th ed. , Butterworth and Heinemann , 1996. Geankoplis , Christi J. , Transport Processes and Unit Operation , 3rd ed. Prentice Hall , 1993. 5. Incropera and Dewitt. Fundamentals of Heat and Mass Transfer. 4th ed., John Wiley and Sons, 1996. 6. Perry, P.H. and Green, D. Perrys Chemical Engineering Handbook. 7th ed., McGraw-Hill Co., 1987. 7. Reid, Prausnitz, and Poling. The Properties of Gases and Liquids. 4th ed., McGraw- Hill Book Co., 1987.

    -8 -

    .2-11 . 1386 - 9 -

    .2-11 . 1386

    )Endnotes(Carbon - steel 1

    Detailed 2 Short Cut 3

    Film Coefficient 4Pass 5

    Shell Diameter 6Clearance 7

    Bare 8Fin - tube 9

    Triangular pitch 10Square pitch 11

    Layout 12