Tgas SOAL Trk 1 Ex 4-6
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Transcript of Tgas SOAL Trk 1 Ex 4-6
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Tugas Teknik Reaksi
Kimia INama : Wahyu
Faiz
Jenial S
Afrielyanda H
Rafli
Juni Irwanda1
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Example 4-6
Approximately 7 billion pounds of ethylene oxide were produced
in he United States in 1997. The 1997 selling price was $0.58 a
pound, amounting to a commercial value of $4.0 billion. Over 60%of the ethylene oxide produced is used to make ethylene glycol.
The major end uses of ethylene oxide are antifreeze (30%).
Polyester (30%), surfactants (10%), and solvents (5%). We want to
calculate the catalyst weight necessary to achieve 60% conversion
when ethylene oxide is to be made by the vapor-phase catalytic
oxidation of ethylene with air
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Ethylene and oxygen are fed in stoichiometric proportions to a
packed-bed reactor operated isothermally at 260oC. Ethylene is fed
at a rate of 0.30 Ib mol /s at a pressure of 10 atm. It is proposed to
use 10 banks of 1 -in.-diameter schedule 40 tubes packed with
catalyst with 100 tubes per bank. Consequently, the molar flow
rate to each tube is to be 3 X 10-4mol/s. The properties of the
reacting fluid are to be considered identical to hose of air at this
temperature and pressure. The density of the -in.-catalyst
particles is 120 Ib/ft3
and the bed void fraction is 0.45. The ratelaw is
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3. Stoichiometry
Gas-phase, isotermal v = vo
(1+X)(Po
/P)
=
=
( )
+
=
+
Dimana =
=
=
( /)
+
Untuk stoikiometri umpan = =
=
( )
+
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Untuk kerja secara isotermal
4. Kombinasikan persamaan laju reaksi dan konsentrasi
Karena (1/2)2/3=0.63
Dan
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MakarAmenjadi :
Dimana
5. Parameter evaluation per tube
Etilen :
Oksigen :
Inert (I)=N2 :
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Menghasilkan :
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y = (1 )/
=1 (1 1.303/)
/
Maka,
Dimana,
-rA = FA0
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Orde reaksi
Dibutuhkan nilai o, Ac, c, dan Po
Acuntuk 1 in pipa schedule 40 = 0,01414 lb/h.ft2
Dp = 0,0208 ft = 0,45
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Dibutuhkan nilai G
mTOadalah laju alir masa total
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Jadi G =
Untuk udara pada 260oC dan 10 atm
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Nilai odikonversi menjadi :
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Setelah o di dapat, di tentukan nilai
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Jadi katalis yang dibutuhkan per tabung :
=
1 (1 1.303/)/
=
1 (1 1.303
0,0166.
1,08 .
0,0266
.
)/
0,0166
= 45,4 lb katalis /tabung
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Berat katalis per tabung tanpa
pressure drop
= 35,3 lb katalis per tabung
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