data reaktor

1
KONSTANTA 1. Inisiasi 2. Propagasi Hubungan kd dan suhu (Brandrup, 1975 ) Ep/R 3.9103E+03 (Buback, 1995) T, C 1/T, K kd, s -1 Ap 4.2658E+07 34.8 0.0032473 3.89E-08 kp dalam (L/mol/s) 49.4 0.0031003 5.28E-07 61 0.0029927 2.58E-06 74.8 0.002874 1.83E-05 100 0.0026799 4.58E-04 3. Terminasi Et 14200.00 (Brandrup, 1975) At 2.55E+04 maka, Ad 5.5258E+15 s -1 R 8.31 Ed/R 1.6397E+04 K kt dalam (L/mol/s) y kd x 1/T 0.8 (Flory, 1953) 1350 140589 0.906 0.034799309 mol/L 8.699827156 mol/L t1 477.5 s= 0.13 jam [M] 0.08864 mol/L [I] 3.47E-02 mol/L T 90 o C= 363.15 K Konversi 98.98 % Menghitung konstanta pada suhu 90 C kd 1.36E-04 s -1 kp 898.81299 L/mol/s kt 231.19 L/mol/s Rho 8.0667981 mol/L= 840.076359 g/L RHO=c1/(c2**(1+(1-(T/c3))**c4)) BM 104.14 c1 0.7397 c2 0.2603 r0 0.005 dm c3 636 r1 0.01 dm c4 0.3009 t2 1649.0398 s= 0.46 jam t, s r1, dm V, L Fs0, mol/s Fi0, mol/s Fs0, kg/jam Fi0, kg/jam 0 0.00500 5.23599E-07 5.33E-09 2.47E-12 2.00E-06 2.15E-09 200 0.00544 6.73795E-07 6.85E-09 3.17E-12 2.57E-06 2.77E-09 400 0.00592 8.67076E-07 8.82E-09 4.08E-12 3.31E-06 3.56E-09 600 0.00643 1.1158E-06 1.14E-08 5.26E-12 4.26E-06 4.58E-09 800 0.00700 1.43587E-06 1.46E-08 6.76E-12 5.48E-06 5.90E-09 1000 0.00761 1.84776E-06 1.88E-08 8.70E-12 7.05E-06 7.59E-09 1200 0.00828 2.37779E-06 2.42E-08 1.12E-11 9.07E-06 9.77E-09 1400 0.00901 3.05987E-06 3.11E-08 1.44E-11 1.17E-05 1.26E-08 1600 0.00980 3.93761E-06 4.01E-08 1.86E-11 1.50E-05 1.62E-08 1649.04 0.01000 4.18879E-06 4.26E-08 1.97E-11 1.60E-05 1.72E-08 TAHAP 2 HASIL PROGRAM -CHECK FORTRAN- [Io] TAHAP 1 f Xn Mr Spec gravity stiren [Mo] y = 5.5258E+15e -1.6397E+04x 1.00E-08 1.00E-07 1.00E-06 1.00E-05 1.00E-04 1.00E-03 1.00E-02 1.00E-01 1.00E+00 0.0025 0.0026 0.0027 0.0028 0.0029 0.003 0.0031 0.0032 0.0033

Upload: shinta-lieviana

Post on 18-Dec-2015

219 views

Category:

Documents


3 download

DESCRIPTION

gggg

TRANSCRIPT

  • KONSTANTA1. Inisiasi 2. PropagasiHubungan kd dan suhu (Brandrup, 1975 ) Ep/R 3.9103E+03 (Buback, 1995)

    T, C 1/T, K kd, s-1 Ap 4.2658E+0734.8 0.0032473 3.89E-08 kp dalam (L/mol/s)49.4 0.0031003 5.28E-0761 0.0029927 2.58E-06

    74.8 0.002874 1.83E-05100 0.0026799 4.58E-04

    3. TerminasiEt 14200.00 (Brandrup, 1975)At 2.55E+04

    maka, Ad 5.5258E+15 s-1 R 8.31Ed/R 1.6397E+04 K kt dalam (L/mol/s)y kdx 1/T

    0.8 (Flory, 1953)1350

    1405890.906

    0.034799309 mol/L8.699827156 mol/L

    t1 477.5 s= 0.13 jam[M] 0.08864 mol/L[I] 3.47E-02 mol/LT 90 oC= 363.15 KKonversi 98.98 %

    Menghitung konstanta pada suhu 90 Ckd 1.36E-04 s-1

    kp 898.81299 L/mol/skt 231.19 L/mol/s

    Rho 8.0667981 mol/L= 840.076359 g/L RHO=c1/(c2**(1+(1-(T/c3))**c4))BM 104.14 c1 0.7397

    c2 0.2603r0 0.005 dm c3 636r1 0.01 dm c4 0.3009

    t2 1649.0398 s= 0.46 jam

    t, s r1, dm V, L Fs0, mol/s Fi0, mol/s Fs0, kg/jam Fi0, kg/jam0 0.00500 5.23599E-07 5.33E-09 2.47E-12 2.00E-06 2.15E-09

    200 0.00544 6.73795E-07 6.85E-09 3.17E-12 2.57E-06 2.77E-09400 0.00592 8.67076E-07 8.82E-09 4.08E-12 3.31E-06 3.56E-09600 0.00643 1.1158E-06 1.14E-08 5.26E-12 4.26E-06 4.58E-09800 0.00700 1.43587E-06 1.46E-08 6.76E-12 5.48E-06 5.90E-09

    1000 0.00761 1.84776E-06 1.88E-08 8.70E-12 7.05E-06 7.59E-091200 0.00828 2.37779E-06 2.42E-08 1.12E-11 9.07E-06 9.77E-091400 0.00901 3.05987E-06 3.11E-08 1.44E-11 1.17E-05 1.26E-081600 0.00980 3.93761E-06 4.01E-08 1.86E-11 1.50E-05 1.62E-08

    1649.04 0.01000 4.18879E-06 4.26E-08 1.97E-11 1.60E-05 1.72E-08

    TAHAP 2

    HASIL PROGRAM -CHECK FORTRAN-

    [Io]

    TAHAP 1

    fXnMrSpec gravity stiren

    [Mo]

    y = 5.5258E+15e-1.6397E+04x1.00E-08

    1.00E-07

    1.00E-06

    1.00E-05

    1.00E-04

    1.00E-03

    1.00E-02

    1.00E-01

    1.00E+000.0025 0.0026 0.0027 0.0028 0.0029 0.003 0.0031 0.0032 0.0033