book1fafawtyeruytrghytrfgtrfgherrert

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1 calculate the benzene quench rate required for a gas feed rate of 1000 kgmol/h, assuming quencing occurs adiabatically. (With Tref = 00o!" #ns$er % &iasumsikan ' = 0 )arena *rocess ter+adi secara adiabatik ehingga %  = *ers -  = *ers -- *ada *ersamaan - % maka dida*at % f1 a = 00 f1 b = 23.1 f1 c = 4.53 f1 d = 213.44 f1 e = 5.006 maka nilai f1 7 c* dt= 65450000 8 205301  = 2.1319801 ) +/h *ada *ersamaan -- % # *rocess gas stream at 00 o ! is to be ra*idly cooled to 00 * ! !:  and 0; :  W = 0 à )arena tidak ada *erubahan <olume yang ter+adi

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Page 1: Book1fafawtyeruytrghytrfgtrfgherrert

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1

calculate the benzene quench rate required for a gas feed rate of 1000 kgmol/h,

assuming quencing occurs adiabatically. (With Tref = 00o!"

#ns$er %

&iasumsikan

' = 0 )arena *rocess ter+adi secara adiabatik

ehingga %

  = *ers -

 = *ers --

*ada *ersamaan - %

maka dida*at %

f1 a = 00

f1 b = 23.1

f1 c = 4.53

f1 d = 213.44

f1 e = 5.006

maka nilai f1 7 c* dt= 65450000 8 205301

  = 2.1319801 )+/h

*ada *ersamaan -- %

# *rocess gas stream at 00o! is to be ra*idly cooled to 00*! !: and 0; :

 

W = 0 à )arena tidak ada *erubahan <olume yang ter+adi

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&engan data % ormal >oilling *oint of benzene is 3.5 ), dan ada

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&iketahui

?#T #

16,36 20.11 0.131 20.046

1,60 20.15153 0.1 20.643

6,6 20.55 0.04046 20.0563

1,54 0.5005 20.0114 0.010366

 T1 = 5.

 T = .

 8 5610603 23.4149801 1.3198013

> @ 101 ! @ 10 & @ 103

!5:

5

!5:

3!:

!:

:

00Ac =

00Ac =

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enzen yang berubah fasa dari gas2cair

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Blo$

0.103 00

0.113 00

0.0060056 100

20.00416 00

9 @ 106

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