Tgas SOAL Trk 1 Ex 4-6

download Tgas SOAL Trk 1 Ex 4-6

of 16

Transcript of Tgas SOAL Trk 1 Ex 4-6

  • 8/11/2019 Tgas SOAL Trk 1 Ex 4-6

    1/16

    Tugas Teknik Reaksi

    Kimia INama : Wahyu

    Faiz

    Jenial S

    Afrielyanda H

    Rafli

    Juni Irwanda1

  • 8/11/2019 Tgas SOAL Trk 1 Ex 4-6

    2/16

    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

    2

  • 8/11/2019 Tgas SOAL Trk 1 Ex 4-6

    3/16

    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

    3

  • 8/11/2019 Tgas SOAL Trk 1 Ex 4-6

    4/16

  • 8/11/2019 Tgas SOAL Trk 1 Ex 4-6

    5/16

    3. Stoichiometry

    Gas-phase, isotermal v = vo

    (1+X)(Po

    /P)

    =

    =

    ( )

    +

    =

    +

    Dimana =

    =

    =

    ( /)

    +

    Untuk stoikiometri umpan = =

    =

    ( )

    +

    5

  • 8/11/2019 Tgas SOAL Trk 1 Ex 4-6

    6/16

    Untuk kerja secara isotermal

    4. Kombinasikan persamaan laju reaksi dan konsentrasi

    Karena (1/2)2/3=0.63

    Dan

    6

  • 8/11/2019 Tgas SOAL Trk 1 Ex 4-6

    7/16

    MakarAmenjadi :

    Dimana

    5. Parameter evaluation per tube

    Etilen :

    Oksigen :

    Inert (I)=N2 :

    7

  • 8/11/2019 Tgas SOAL Trk 1 Ex 4-6

    8/16

    Menghasilkan :

    8

  • 8/11/2019 Tgas SOAL Trk 1 Ex 4-6

    9/16

    y = (1 )/

    =1 (1 1.303/)

    /

    Maka,

    Dimana,

    -rA = FA0

    9

  • 8/11/2019 Tgas SOAL Trk 1 Ex 4-6

    10/16

    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

    10

  • 8/11/2019 Tgas SOAL Trk 1 Ex 4-6

    11/16

    Dibutuhkan nilai G

    mTOadalah laju alir masa total

    11

  • 8/11/2019 Tgas SOAL Trk 1 Ex 4-6

    12/16

    Jadi G =

    Untuk udara pada 260oC dan 10 atm

    12

  • 8/11/2019 Tgas SOAL Trk 1 Ex 4-6

    13/16

    Nilai odikonversi menjadi :

    13

  • 8/11/2019 Tgas SOAL Trk 1 Ex 4-6

    14/16

    Setelah o di dapat, di tentukan nilai

    14

  • 8/11/2019 Tgas SOAL Trk 1 Ex 4-6

    15/16

    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

    15

  • 8/11/2019 Tgas SOAL Trk 1 Ex 4-6

    16/16

    Berat katalis per tabung tanpa

    pressure drop

    = 35,3 lb katalis per tabung

    16