Neraca Panas

NERACA PANAS SEKITAR VAPORIZER

Nama alat : OX tank

Kode alat : T-01

P operasi : 760

T operasi : 303.15

T reff : 298.15

a. Menghitung panas masuk vaporizer

T reff (K) : 298.15

T out (K) : 303.15

Komponen BM Xi A B C D E

O-xylene 106.167 3547.76 33.42 0.9800 8.1200E-01 5.1344E-01 -2.0212E-04 -2.1615E-08 2.3212E-11

M-xylene 106.167 72.40 0.68 0.0200 -1.6725E+01 5.6424E-01 -2.6465E-04 1.3381E-08 1.5869E-11

TOTAL 3620.16 34.10 1.0000

b. Menentukan panas keluar vaporizer

Nama alat : Vaporizer

Kode alat : V-01

P operasi : 1026

A. Menentukan T bubble

T bubble (K) : 429.28 k 1.5613E+02 C

O-xylene 106.167 3547.76 33.4168 0.9800 3.7241E+01 -3.4573E+03 -1.0126E+01 9.0676E-11 2.6123E-06

M-xylene 106.167 72.40 0.6820 0.0200 3.4680E+01 -3.2981E+03 -9.2570E+00 -4.3563E-10 2.4103E-06

TOTAL 3620.16 34.0988 1.0000

F1 (kg/jam) ni (kmol/jam)

B. Menentukan T dew

429.30 K 1.5615E+02 C

Komponen BM Yi A B C D E

O-xylene 106.167 3547.76 33.4168 0.9800 3.7241E+01 -3.4573E+03 -1.0126E+01 9.0676E-11 2.6123E-06

M-xylene 106.167 72.40 0.6820 0.0200 3.4680E+01 -3.2981E+03 -9.2570E+00 -4.3563E-10 2.4103E-06

TOTAL 3620.16 34.0988 1.0000

Jadi OX keluar vaporizer pada 429,3 K dan 1026 mmHg

T input : 303.15

T output : 429.30

Menghitung panas penguapan

T dew (K) : 429.30

Komponen BM A Tc (K) n Hv (kJ/jam)

O-xylene 106.167 3547.76 33.42 5.5606E+01 6.3037E+02 3.7500E-01 36.23

M-xylene 106.167 72.40 0.68 6.0216E+01 6.1705E+02 4.5800E-01 34.92

TOTAL 3620.16 34.10 71.14

Menghitung panas sensibel

T reff (K) : 298.15

T out (K) : 429.30

O-xylene 106.167 3547.76 33.42 0.9800 8.1200E-01 5.1344E-01 -2.0212E-04 -2.1615E-08 2.3212E-11

M-xylene 106.167 72.40 0.68 0.0200 -1.6725E+01 5.6424E-01 -2.6465E-04 1.3381E-08 1.5869E-11

TOTAL 3620.16 34.10 1.0000

T dew (K) :

NERACA PANAS

Cp mean medium pemanas (kJ/kg K) : 4.39

Kebutuhan medium pemanas (kJ/jam) : 691320.85

Kebutuhan medium pemanas (kg/jam) : 5520.64

Panas yang dilepas pemanas (kJ/jam) : 2369296.94 1677976.09

H input (kJ/jam) : 23250.13 T in med (K) = 473.15

H output (kJ/jam) : 714570.98 T out med (K) = 375.37

NERACA PANAS SEKITAR HE-01 9.2053E+01

Nama alat : Air Blower

Kode alat : B-01

T in (K) : 303.15 P in (mmHg) : 760.00

T trial (K) : 303.18 P out (mmHg) : 1064.00

Oxygen 32.000 17558.50 548.70 0.1888 2.9526E+01 -8.8889E-03 3.8083E-05 -3.2629E-08 8.8607E-12

Nitrogen 28.014 66053.50 2357.87 0.8112 2.9342E+01 -3.5395E-03 1.0076E-05 -4.3116E-09 2.5935E-13

TOTAL 83612.00 2906.58 1.0000

a. Menentukan panas masuk HE-01

T reff (K) : 298.15

T in (K) : 303.18

Oxygen 32.000 17558.50 548.70 0.1888 2.9526E+01 -8.8889E-03 3.8083E-05 -3.2629E-08 8.8607E-12

Nitrogen 28.014 66053.50 2357.87 0.8112 2.9342E+01 -3.5395E-03 1.0076E-05 -4.3116E-09 2.5935E-13

TOTAL 83612.00 2906.58 1.0000

b. Menentukan panas keluar HE-01

T reff (K) : 298.15

T out (K) : 429.30 K 1.5615E+02

Oxygen 32.000 17558.50 548.70 0.1888 2.9526E+01 -8.8889E-03 3.8083E-05 -3.2629E-08 8.8607E-12

Nitrogen 28.014 66053.50 2357.87 0.8112 2.9342E+01 -3.5395E-03 1.0076E-05 -4.3116E-09 2.5935E-13

TOTAL 83612.00 2906.58 1.0000

c. Menentukan kebutuhan pamanas

Cp mean medium pemanas (kJ/kg K) : 4.88

Panas laten (kJ/jam) : 1614.00

Panas sensibel (kJ/jam) : 334.08

TOTAL (kJ/jam) : 1948.08

9.2053E+01

NERACA PANAS SEKITAR GAS MIXER

T bubble (K) : 81.36

O-xylene 106.167 3547.76 33.42 0.0114 3.7241E+01 -3.4573E+03 -1.0126E+01 9.0676E-11 2.6123E-06

M-xylene 106.167 72.40 0.68 0.0002 3.4680E+01 -3.2981E+03 -9.2570E+00 -4.3563E-10 2.4103E-06

Oxygen 32.000 17558.50 548.70 0.1866 2.0670E+01 -5.2697E+02 -6.7062E+00 1.2926E-02 -9.8832E-13

Nitrogen 28.014 66053.50 2357.87 0.8018 2.3857E+01 -4.7668E+02 -8.6689E+00 2.0128E-02 -2.4139E-11

TOTAL 87232.16 2940.68 1.0000

B. Menentukan T dew

307.96

O-xylene 106.167 3547.76 33.42 0.0114 3.7241E+01 -3.4573E+03 -1.0126E+01 9.0676E-11 2.6123E-06

M-xylene 106.167 72.40 0.68 0.0002 3.4680E+01 -3.2981E+03 -9.2570E+00 -4.3563E-10 2.4103E-06

Oxygen 32.000 17558.50 548.70 0.1866 2.0670E+01 -5.2697E+02 -6.7062E+00 1.2926E-02 -9.8832E-13

Nitrogen 28.014 66053.50 2357.87 0.8018 2.3857E+01 -4.7668E+02 -8.6689E+00 2.0128E-02 -2.4139E-11

TOTAL 87232.16 2940.68 1.0000

NERACA PANAS SEKITAR HE-02

a. Menentukan panas masuk HE-02

T reff (K) : 298.15

T in (K) : 429.30

Menentukan T bubble

T dew (K) :

O-xylene 106.167 3547.76 33.42 0.0114 1.8200E-01 5.1344E-01 -2.0212E-04 -2.1615E-08 2.3212E-11

M-xylene 106.167 72.40 0.68 0.0002 -1.6725E+01 5.6424E-01 -2.6465E-04 1.3381E-08 1.5869E-11

Oxygen 32.000 17558.50 548.70 0.1866 2.9526E+01 -8.8889E-03 3.8083E-05 -3.2629E-08 8.8607E-12

Nitrogen 28.014 66053.50 2357.87 0.8018 2.9342E+01 -3.5395E-03 1.0076E-05 -4.3116E-09 2.5935E-13

TOTAL 87232.16 2940.68 1.0000

b. Menentukan panas keluar HE-02

T reff (K) : 298.15

T out (K) : 613.15

O-xylene 106.167 3547.76 33.42 0.0114 1.8200E-01 5.1344E-01 -2.0212E-04 -2.1615E-08 2.3212E-11

M-xylene 106.167 72.40 0.68 0.0002 -1.6725E+01 5.6424E-01 -2.6465E-04 1.3381E-08 1.5869E-11

Oxygen 32.000 17558.50 548.70 0.1866 2.9526E+01 -8.8889E-03 3.8083E-05 -3.2629E-08 8.8607E-12

Nitrogen 28.014 66053.50 2357.87 0.8018 2.9342E+01 -3.5395E-03 1.0076E-05 -4.3116E-09 2.5935E-13

TOTAL 87232.16 2940.68 1.0000

c. Menentukan kebutuhan pamanas

NERACA PANAS SEKITAR REAKTOR

a. Mencari harga panas pembentukan standar

T (K) : 623.15

Cp mean oiltherm (kJ/kg K) :

Komponen BM Produk F4 (kg/jam) A B C H standar (kJ/mol)

O-xylene 106.167 3547.76 33.42 70.96 0.67 46.756 -1.0824E-01 4.9928E-05 -1.31

M-xylene 106.167 72.40 0.68 0.00 0.00 46.618 -1.1480E-01 5.3371E-05 -4.19

Phthalic anhydride 148.118 0.00 0.00 3521.98 23.78 -371.308 -8.4063E-02 3.5447E-05 -409.93

Maleic anhydride 98.058 0.00 0.00 137.58 1.40 -401.302 6.6610E-03 1.0283E-05 -393.16

Ortho tolualdehide 136.150 0.00 0.00 7.87 0.06 -4.44E+01 6.3161E-01 -3.8644E-04 199.14

Phthalide 134.136 0.00 0.00 8.79 0.07 46.756 -1.0824E-01 -1.0824E-01 -42052.01

Carbon monoxide 28.011 0.00 0.00 355.90 12.71 0 0.0000E+00 0.0000E+00 -110.50

Carbon dioxide 44.011 0.00 0.00 1800.40 40.91 0 0.0000E+00 0.0000E+00 -393.50

Oxygen 32.000 17558.50 548.70 13170.50 411.58 0 0.0000E+00 0.0000E+00 0.00

Nitrogen 28.014 66053.50 2357.87 66053.50 2357.87 0 0.0000E+00 0.0000E+00 0.00

Water 18.016 0.00 0.00 4839.14 268.60 -238.41 -1.2256E-02 2.7656E-06 -244.97

TOTAL 87232.16 89966.61

b. Mencari panas keluar reaktor

T reff (K) : 298.15

T out (K) : 623.15

O-xylene 106.167 70.96 0.67 0.0002 1.8200E-01 5.1344E-01 -2.0212E-04 -2.1615E-08 2.3212E-11

M-xylene 106.167 0.00 0.00 0.0000 -1.6725E+01 5.6424E-01 -2.6465E-04 1.3381E-08 1.5869E-11

Phthalic anhydride 148.118 3521.98 23.78 0.0080 4.0083E+01 3.6084E-02 9.5956E-04 -1.2341E-06 4.6597E-10

Maleic anhydride 98.058 137.58 1.40 0.0005 -7.2015E+01 1.0423E+00 -1.8716E-03 1.6527E-06 -5.5647E-10

Ortho tolualdehide 136.150 7.87 0.06 0.0000 5.8201E+01 1.1353E+00 -2.6405E-03 2.4764E-06 -1.6767E-11

Phthalide 134.136 8.79 0.07 0.0000 1.9986E+01 7.7860E-01 2.9980E-04 1.7486E-08 5.6823E-11

Carbon monoxide 28.011 355.90 12.71 0.0043 2.9556E+01 -6.5807E-03 2.0130E-05 -1.2227E-08 2.2617E-12

Carbon dioxide 44.011 1800.40 40.91 0.0138 2.7437E+01 4.2315E-02 -1.9555E-05 3.9968E-09 -2.9872E-13

Oxygen 32.000 13170.50 411.58 0.1393 2.9526E+01 -8.8889E-03 3.8083E-05 -3.2629E-08 8.8607E-12

Nitrogen 28.014 66053.50 2357.87 0.7979 2.9342E+01 -3.5395E-03 1.0076E-05 -4.3116E-09 2.5935E-13

Water 18.016 1909.54 105.99 0.0359 3.3933E+01 -8.8146E-03 2.9906E-05 -1.7825E-08 3.6934E-12

TOTAL 87037.01 2955.03 1.0000

c. Menentukan kebutuhan pendingin

Reaktan F3 (kg/jam) ni (kmol/jam) ni (kmol/jam)

Cp mean molten salt (kJ/kg K) : 1.56

Kebutuhan medium pendingin (kJ/jam) : 95574993.41

Kebutuhan medium pendingin (kg/jam) : 1225320.43

H output (kJ/jam) : -66349776.52 T out med (K) = 648.15

NERACA PANAS SEKITAR SG-01

Panas yang dibawa molten salt : 95574993.41

Massa BFW keluar dari HE-04 : 37419.83

Dari steam table diperoleh temperatur jenuh uap (K) : 541.55

Panas laten (kJ/kg) : 1614.00

T in (K) : 494.11

T out (K) : 541.55

Cp mean (kJ/kg K) : 4.96

Panas sensibel : 8805544.34

Panas laten : 60395497.74

TOTAL : 69201042.08 -26373951.34

Asumsi : pressure drop 1 atm, shg tekanan menjadi 53 atm

a. Mencari panas keluar HE-03

T reff (K) : 298.15

T out (K) : 583.15

O-xylene 106.167 70.96 0.67 0.0002 1.8200E-01 5.1344E-01 -2.0212E-04 -2.1615E-08 2.3212E-11

M-xylene 106.167 0.00 0.00 0.0000 -1.6725E+01 5.6424E-01 -2.6465E-04 1.3381E-08 1.5869E-11

Ortho tolualdehide 136.150 7.87 0.06 0.0000 5.8201E+01 1.1353E+00 -2.6405E-03 2.4764E-06 3.7290E-10

Phthalide 134.136 8.79 0.07 0.0000 1.9986E+01 7.7860E-01 2.9980E-04 1.7486E-08 5.6823E-11

Oxygen 32.000 13170.50 411.58 0.1393 2.9526E+01 -8.8889E-03 3.8083E-05 -3.2629E-08 8.8607E-12

Nitrogen 28.014 66053.50 2357.87 0.7979 2.9342E+01 -3.5395E-03 1.0076E-05 -4.3116E-09 2.5935E-13

Water 18.016 1909.54 105.99 0.0359 3.3933E+01 -8.8146E-03 2.9906E-05 -1.7825E-08 3.6934E-12

TOTAL 87037.01 2955.03 13.7013

b. Menentukan kebutuhan pendingin

Cp mean steam (kJ/kg K) : 1.98

Kebutuhan medium pendingin (kg/jam) : 31899.19 168161.80

Panas sensibel medium pendingin (kJ) : 3975638.75

Digunakan steam jenuh sebagai pendingin A

3.3933E+01

PROFIL SUHU F4

T bubble (K) : 80.43

O-xylene 106.167 70.96 0.67 0.0002 3.7241E+01 -3.4573E+03 -1.0126E+01 9.0676E-11 2.6123E-06

M-xylene 106.167 0.00 0.00 0.0000 3.4680E+01 -3.2981E+03 -9.2570E+00 -4.3563E-10 2.4103E-06

Phthalic anhydride 148.118 3521.98 23.78 0.0082 3.0633E+01 -3.8783E+03 -7.8671E+00 1.1146E-09 2.5885E-06

Maleic anhydride 98.058 137.58 1.40 0.0005 -4.2978E+01 -1.6928E+03 2.2430E+01 -2.7916E-02 1.1707E-05

Ortho Tolualdehide 136.150 7.87 0.06 0.0000 -4.4384E+01 6.3161E-01 -3.8644E-04 9.1760E-08 -2.9424E-12

Phthalide 134.136 8.79 0.07 0.0000 2.9657E+01 -3.5463E+03 -7.8974E+00 1.0046E-07 1.1320E-06

Water 18.016 1909.54 105.99 0.0365 2.9861E+01 -3.1522E+03 -7.3030E+00 2.4247E-09 1.8090E-06

Oxygen 32.000 13170.50 411.58 0.1419 2.0670E+01 -5.2697E+02 -6.7062E+00 1.2926E-02 -9.8832E-13

Nitrogen 28.014 66053.50 2357.87 0.8127 2.3857E+01 -4.7668E+02 -8.6689E+00 2.0128E-02 -2.4139E-11

TOTAL 84880.72 2901.42 1.0000

Menentukan T dew

407.32

O-xylene 106.167 70.96 0.67 0.0002 3.7241E+01 -3.4573E+03 -1.0126E+01 9.0676E-11 2.6123E-06

M-xylene 106.167 0.00 0.00 0.0000 3.4680E+01 -3.2981E+03 -9.2570E+00 -4.3563E-10 2.4103E-06

Ortho Tolualdehide 136.150 7.87 0.06 0.0000 -4.4384E+01 6.3161E-01 -3.8644E-04 9.1760E-08 -2.9424E-12

Phthalide 134.136 8.79 0.07 0.0000 2.9657E+01 -3.5463E+03 -7.8974E+00 1.0046E-07 1.1320E-06

Water 18.016 1909.54 105.99 0.0365 2.9861E+01 -3.1522E+03 -7.3030E+00 2.4247E-09 1.8090E-06

Oxygen 32.000 13170.50 411.58 0.1419 2.0670E+01 -5.2697E+02 -6.7062E+00 1.2926E-02 -9.8832E-13

Nitrogen 28.014 66053.50 2357.87 0.8127 2.3857E+01 -4.7668E+02 -8.6689E+00 2.0128E-02 -2.4139E-11

TOTAL 84880.72 2901.42 1.0000

Menentukan T bubble

T dew (K) :

Didinginkan hingga T dew arus F4

a. Mencari panas keluar HE-04

T reff (K) : 298.15

T out (K) : 407.32

O-xylene 106.167 70.96 0.67 0.0002 1.8200E-01 5.1344E-01 -2.0212E-04 -2.1615E-08 2.3212E-11

M-xylene 106.167 0.00 0.00 0.0000 -1.6725E+01 5.6424E-01 -2.6465E-04 1.3381E-08 1.5869E-11

Ortho Tolualdehide 136.150 7.87 0.06 0.0000 -4.4384E+01 6.3161E-01 -3.8644E-04 9.1760E-08 3.7290E-10

Phthalide 134.136 8.79 0.07 0.0000 1.9986E+01 7.7860E-01 2.9980E-04 1.7486E-08 5.6823E-11

Oxygen 32.000 13170.50 411.58 0.1472 2.9526E+01 -8.8889E-03 3.8083E-05 -3.2629E-08 8.8607E-12

Nitrogen 28.014 66053.50 2357.87 0.8435 2.9342E+01 -3.5395E-03 1.0076E-05 -4.3116E-09 2.5935E-13

TOTAL 82971.18 2795.43 1.0000

b. Menentukan kebutuhan pendingin

9.2053E+01

Digunakan BFW bertekanan 54 atm (high pressure)

NERACA PANAS SEKITAR SWITCH CONDENSER (SC-01)

a. Tahap receiving

Terjadi proses desublimasi dan separasi antara condensable dan non-condensable gas

Menghitung panas keluar

Komponen terdesublimasi

T reff (K) : 298.15

T out (K) : 333.15

Phthalic anhydride 148.118 3521.98 23.78 0.9948 2.6320E+01 3.9060E-01 2.1260E-04 0.0000E+00 0.0000E+00

ortho tolualdehide 136.150 7.87 0.06 0.0024 -4.2265E+01 7.2871E-01 0.0000E+00 0.0000E+00 0.0000E+00

Phthalide 134.136 8.79 0.07 0.0027 3.4220E+01 6.1431E-01 0.0000E+00 0.0000E+00 0.0000E+00

TOTAL 3538.64 23.90 1.0000

Komponen non-condensable gas

T reff (K) : 298.15

T out (K) : 333.15

Oxygen 32.000 13170.50 411.58 0.1462 2.9526E+01 -8.8889E-03 3.8083E-05 -3.2629E-08 8.8607E-12

Nitrogen 28.014 66053.50 2357.87 0.8375 2.9342E+01 -3.5395E-03 1.0076E-05 -4.3116E-09 2.5935E-13

TOTAL 81161.98 2815.27 1.0000

Komponen yang tercairkan

T reff (K) : 298.15

T out (K) : 333.15

O-xylene 106.167 70.96 0.67 0.0062 5.6460E+01 9.4926E-01 -2.4902E-03 2.6838E-06 0.0000E+00

M-xylene 106.167 0.00 0.00 0.0000 7.0916E+01 8.0450E-01 -2.1885E-03 2.5061E-06 0.0000E+00

Maleic anhydride 98.058 137.58 1.40 0.0130 -1.2662E+01 1.0564E+00 -2.3244E-03 2.0518E-06 0.0000E+00

Water 18.016 1909.54 105.99 0.9808 9.2053E+01 -3.9953E-02 -2.1103E-04 5.3469E-07 0.0000E+00

TOTAL 2118.07 108.06 1.0000

Komponen BM Xi Hd (J/mol) Hd (kJ/jam)

Phthalic anhydride 148.118 3521.9800 23.7782 0.9948 21437.50 509745.25

ortho tolualdehide 136.150 7.8699 0.0578 0.0024 24044.70 1389.86

Phthalide 134.136 8.7921 0.0655 0.0027 11926.00 781.70

TOTAL 3538.6420 23.9016 1.0000 511916.80

Komponen BM A Tc (K) n Hk (kJ/jam)

O-xylene 106.167 70.96 0.67 5.5606E+01 6.3037E+02 3.7500E-01 28033.17

M-xylene 106.167 0.00 0.00 6.0216E+01 6.1705E+02 4.5800E-01 0.00

Maleic anhydride 98.058 137.58 1.40 5.9574E+01 7.2100E+02 2.1600E-01 73107.19

Water 18.016 1909.54 105.99 5.2053E+01 6.4713E+02 3.2100E-01 4374147.33

TOTAL 2118.07 108.06 4475287.69

Menentukan kebutuhan pendingin

Cp mean oiltherm (kJ/kg K) : 2.34

H output (kJ/jam) : -1664835.15 T out med (K) = 348.15

Menghitung panas desublimasi pada 134,2 oC

Menghitung panas pencairan pada 134,2 oC

b. Tahap melting

379.72

Komponen BM Xi Hm (J/mol) Hm (kJ/jam)

ortho tolualdehide 136.150 7.87 0.06 0.0024 3536.00 204.39

Phthalide 134.136 8.79 0.07 0.0027 9775.00 640.71

TOTAL 3538.65 23.90 1.0000 93508.89

Menghitung panas sensibel

Fase padat

T reff (K) : 298.15

T out (K) : 379.72

ortho tolualdehide 136.150 7.87 0.06 0.0024 -4.2265E+01 7.2871E-01 0.0000E+00 0.0000E+00 0.0000E+00

Phthalide 134.136 8.79 0.07 0.0027 3.4220E+01 6.1431E-01 0.0000E+00 0.0000E+00 0.0000E+00

TOTAL 3538.65 23.90 1.0000

Fase cair

T reff (K) : 298.15

T out (K) : 379.72

O-xylene 106.167 70.96 0.67 0.0257 5.6460E+01 9.4926E-01 -2.4902E-03 2.6838E-06 0.0000E+00

Phthalic anhydride 148.118 3521.98 23.78 -1.0563E+02 1.9840E+00 -3.8847E-03 2.8513E-06 0.0000E+00

ortho tolualdehide 136.150 7.87 0.06 5.8201E+01 1.1353E+00 -2.6405E-03 2.4764E-06 0.0000E+00

Menghitung panas pelelehan pada T = 106,57 oC

Phthalide 134.136 8.79 0.07 -8.0350E+00 2.4304E+00 -3.9847E-03 1.6541E-07 0.0000E+00

TOTAL 208.53 25.97 0.0798

Menentukan kebutuhan pemanas

Cp mean oiltherm (kJ/kg K) : 2.34

H input (kJ/jam) : -4552894.79 T in med (K) = 398.15

c. Tahap cooling

Pada tahap ini condenser tidak mempunyai beban, namun karena waktu operasi cooling 1/8 waktu operasi receiving maka :

Kebutuhan oil pendingin = 29040.14

NERACA PANAS SEKITAR PRE DISTILLATION COLUMN

Panas yang dibawa oleh uap masuk kondensor (Vo)

a. Panas sensibel

T reff (K) : 298.15

T out (K) : 396.22

O-xylene 106.167 70.96 0.67 0.0257 5.6460E+01 9.4926E-01 -2.4902E-03 2.6838E-06 0.0000E+00

Phthalic anhydride 148.118 3521.98 23.78 0.9155 -1.0563E+02 1.9840E+00 -3.8847E-03 2.8513E-06 0.0000E+00

ortho tolualdehide 136.150 7.87 0.06 0.0022 5.8201E+01 1.1353E+00 -2.6405E-03 2.4764E-06 0.0000E+00

Phthalide 134.136 8.79 0.07 0.0025 -8.0350E+00 2.4304E+00 -3.9847E-03 1.6541E-07 0.0000E+00

Vo (kg/jam) ni (kmol/jam)

TOTAL 3747.18 25.97 1.0000

b. Panas laten penguapan

T dew (K) : 396.22

O-xylene 106.167 70.96 0.67 5.5606E+01 6.3037E+02 3.7500E-01 25634.71

M-xylene 106.167 0.00 6.0216E+01 6.1705E+02 4.5800E-01 0.00

Phthalic anhydride 148.118 3521.98 23.78 5.5495E+01 7.9100E+02 3.8000E-02 1285180.93

TOTAL 3730.52 25.85 1381173.40

Panas yang keluar dari kondensor

a. Panas uap

T reff (K) : 298.15

T out (K) : 377.46

O-xylene 106.167 2.16 0.02 0.0001 1.8200E-01 5.1344E-01 -2.0212E-04 -2.1615E-08 2.3212E-11

M-xylene 106.167 90.09 0.85 0.0033 -1.6725E+01 5.6424E-01 -2.6465E-04 1.3381E-08 1.5869E-11

Water 18.016 4613.99 256.11 0.9934 3.3933E+01 -8.8146E-03 2.9906E-05 -1.7825E-08 3.6934E-12

TOTAL 4789.82 257.81 1.0000

b. Panas cairan destilat

T reff (K) : 298.15

T out (K) : 377.50

O-xylene 106.167 0.36 0.00 0.0023 5.6460E+01 9.4926E-01 -2.4902E-03 2.6838E-06 0.0000E+00

M-xylene 106.167 12.92 0.12 0.0810 7.0916E+01 8.0450E-01 -2.1885E-03 2.5061E-06 0.0000E+00

Water 18.016 200.57 11.13 7.4123 9.2053E+01 -3.9953E-02 -2.1103E-04 5.3469E-07 0.0000E+00

TOTAL 365.32 1.50 1.0000

Panas laten kondensasi destilat

T dew (K) : 377.50

O-xylene 106.167 0.36 0.00 5.5606E+01 6.3037E+02 3.7500E-01 135.46

M-xylene 106.167 12.92 0.12 6.0216E+01 6.1705E+02 4.5800E-01 4750.24

Water 18.016 200.57 11.13 5.2053E+01 6.4713E+02 3.2100E-01 437530.86

TOTAL 365.32 12.64 513416.42

c. Panas cairan refluks

T reff (K) : 298.15

T out (K) : 377.50

O-xylene 106.167 0.00 0.00 0.0000 5.6460E+01 9.4926E-01 -2.4902E-03 2.6838E-06 0.0000E+00

M-xylene 106.167 0.31 0.00 0.0096 7.0916E+01 8.0450E-01 -2.1885E-03 2.5061E-06 0.0000E+00

Water 18.016 4.77 0.26 0.8814 9.2053E+01 -3.9953E-02 -2.1103E-04 5.3469E-07 0.0000E+00

TOTAL 8.67 0.30 1.0000

Panas laten kondensasi refluks

Lo (kg/jam) ni (kmol/jam)

T dew (K) : 377.50

O-xylene 106.167 0.00 0.00 5.5606E+01 6.3037E+02 3.7500E-01 0.00

M-xylene 106.167 0.31 0.00 6.0216E+01 6.1705E+02 4.5800E-01 112.87

Water 18.016 4.77 0.26 5.2053E+01 6.4713E+02 3.2100E-01 10395.34

TOTAL 8.67 0.30 12195.15

Menghitung muatan kondensor

Qc = 1697019.94

Cp mean cooling water (kJ/kg K) : 4.18

T in med (K) = 303.15

T out med (K) = 323.15

Panas yang dibawa oleh residu

T reff (K) : 298.15 A

T out (K) : 571.67 9.2053E+01

ortho tolualdehide 136.150 0.39 0.00 0.0001 -1.0686E+02 2.1576E+00 -4.4616E-03 3.5101E-06 0.0000E+00

Phthalide 134.136 12.75 0.10 0.0027 -8.0350E+00 2.4304E+00 -3.9847E-03 1.6541E-07 0.0000E+00

TOTAL 5203.31 35.15 1.0000

Menghitung muatan reboiler

Qr = 4435650.49

T in med (K) = 583.15

T out med (K) = 566.89

NERACA PANAS SEKITAR MAIN DISTILLATION COLUMN

Panas yang dibawa oleh uap masuk kondensor (Vo)

a. Panas sensibel -31575.90

T reff (K) : 298.15

T out (K) : 480.26

Ortho Tolualdehide 136.150 0.51 0.00 0.0001 -1.0686E+02 2.1576E+00 -4.4616E-03 3.5101E-06 0.0000E+00

Phthalide 134.136 4.20 0.03 0.0007 -8.0350E+00 2.4304E+00 -3.9847E-03 1.6541E-07 0.0000E+00

Phthalic acid 166.133 2.98 0.02 0.0004 -1.1530E+02 1.4157E+00 -1.2256E-03 1.1640E-07 0.0000E+00

TOTAL 6667.21 45.03 1.0000

b. Panas laten penguapan

T dew (K) : 480.26

Maleic anhydride 98.058 4.50 0.05 5.9574E+01 7.2100E+02 2.1600E-01 2155.31 input

Ortho Tolualdehide 136.150 0.51 0.00 9.1444E+01 7.5100E+02 3.8800E-01 231.17 4408394.79

Phthalide 134.136 4.20 0.03 4.5551E+01 7.1000E+02 3.8000E-02 1365.82 3554.43

TOTAL 6664.23 45.01 2410197.83 411.05

3266.99

4415627.25

Panas yang keluar dari kondensor

a. Panas uap

T reff (K) : 298.15

T out (K) : 477.45

TOTAL 343.96 2.33 1.0000

b. Panas cairan destilat

T reff (K) : 298.15

T out (K) : 477.47

Ortho Tolualdhide 136.150 0.39 0.00 0.0001 -1.0686E+02 2.1576E+00 -4.4616E-03 3.5101E-06 0.0000E+00

Phthalide 134.136 3.19 0.02 0.0007 -8.0350E+00 2.4304E+00 -3.9847E-03 1.6541E-07 0.0000E+00

TOTAL 4797.93 32.40 1.0000

T dew (K) : 477.47

Ortho Tolualdehide 136.150 0.39 0.00 9.1444E+01 7.5100E+02 3.8800E-01 176.19

Phthalide 134.136 3.19 0.02 4.5551E+01 7.1000E+02 3.8000E-02 1037.32

TOTAL 4797.93 32.40 1735720.77

c. Panas cairan refluks

T reff (K) : 298.15

T out (K) : 477.47

Phthalide 134.136 1.01 0.01 0.0007 -8.0350E+00 2.4304E+00 -3.9847E-03 1.6541E-07 0.0000E+00

TOTAL 1522.34 10.28 1.0000

Panas laten kondensasi refluks

T dew (K) : 477.47

Ortho Tolualdehide 136.150 0.12 0.00 9.1444E+01 7.5100E+02 3.8800E-01 55.90

Phthalide 134.136 1.01 0.01 4.5551E+01 7.1000E+02 3.8000E-02 329.13

TOTAL 1522.34 10.28 550728.70

Qc = 4775654.34

126126.74

T in med (K) = 323.15 A

T out med (K) = 330.97 9.2053E+01

Panas yang dibawa oleh residu

T reff (K) : 298.15

T out (K) : 556.52

Phthalide 134.136 9.56 0.07 0.0403 -8.0350E+00 2.4304E+00 -3.9847E-03 1.6541E-07 0.0000E+00

Phthalic acid 166.133 224.14 1.35 0.7620 -1.1530E+02 1.4157E+00 -1.2256E-03 1.1640E-07 0.0000E+00

TOTAL 285.56 1.77 1.0000

Menghitung muatan reboiler

Qr = 2177721.03

Kebutuhan medium pemanas (kg/jam) : 180981.70 64415.46

T in med (K) = 566.89

T out med (K) = 561.75

Menghitung neraca panas sekitar kondensor (CN-03)

a. Panas uap keluar

T reff (K) : 298.15

T out (K) : 477.15

TOTAL 94.99 0.64 1.0000

b. Panas destilat

T reff (K) : 298.15

T out (K) : 477.15

TOTAL 248.97 1.68 1.0000

T dew (K) : 477.15

TOTAL 248.97 1.68 90137.19

Qc = 57944.58

56745.47

T in med (K) = 330.97 317.85

T out med (K) = 331.07 57063.33

NERACA PANAS SEKITAR MIXING VALVE

Panas total pencampuran = 1493229.22

T keluar mixing valve (trial) = 477.46 0.04 136.94

T reff (K) : 298.15

T out (K) : 477.46

Phthalide 134.136 3.19 0.02 0.0007 -8.0350E+00 2.4304E+00 -3.9847E-03 1.6541E-07 0.0000E+00

TOTAL 5046.58 34.08 1.0000

NERACA PANAS SEKITAR FLAKER

Asumsi : kebutuhan air dihitung pada saat aliran dari pure PA tank hanya menuju flaker (maksimum)

Menentukan T bubble

557.83

Ortho Tolualdehide 136.150 0.39 0.00 0.0001 -3.5882E+01 -3.2354E+03 2.1133E+01 -3.0165E-02 1.1587E-05

Phthalide 134.136 3.19 0.02 0.0007 2.9657E+01 -3.5463E+03 -7.8974E+00 1.0046E-07 1.1320E-06

TOTAL 5046.58 34.08 1.0000

Menentukan T dew

558.26

PROFIL SUHU ARUS F19 PADA 1 ATM

T bubble (K) :

T dew (K) :

Ortho Tolualdehide 136.150 0.39 0.00 0.0001 -3.5882E+01 -3.2354E+03 2.1133E+01 -3.0165E-02 1.1587E-05

Phthalide 134.136 3.19 0.02 0.0007 2.9657E+01 -3.5463E+03 -7.8974E+00 1.0046E-07 1.1320E-06

TOTAL 5046.58 34.08 1.0000

Menghitung panas keluar

a. Panas sensibel

T reff (K) : 298.15

T out (K) : 404.15

Orto Tolualdehide 136.150 0.39 0.00 0.0001 -1.0686E+02 2.1576E+00 -4.4616E-03 3.5101E-06 0.0000E+00

Phthalide 134.136 3.19 0.02 0.0007 -8.0350E+00 2.4304E+00 -3.9847E-03 1.6541E-07 0.0000E+00

TOTAL 5046.58 34.08 1.0000

Komponen BM Xi Hb (J/mol) Hb (kJ/jam)

Maleic anhydride 98.058 2.76 0.03 0.0008 2911.00 81.87

Ortho Tolualdehide 136.150 0.39 0.00 0.0001 2425.00 6.91

Phthalide 134.136 3.19 0.02 0.0007 8664.00 205.85

TOTAL 5046.58 34.08 1.0000 95098.28

T reff (K) : 298.15

Menghitung panas pembekuan pada T = 131 oC

Didinginkan hingga 35 oC

T out (K) : 308.15

Maleic anhydride 98.058 2.7578 0.0281 0.0008 3.2500E+01 2.0960E-01 2.7330E-04 0.0000E+00 0.0000E+00

Ortho Tolualdehide 136.150 0.3882 0.0029 0.0001 -4.2265E+01 7.2871E-01 0.0000E+00 0.0000E+00 0.0000E+00

Phthalide 134.136 3.1870 0.0238 0.0007 3.4220E+01 6.1431E-01 0.0000E+00 0.0000E+00 0.0000E+00

TOTAL 5046.58 34.08 1.0000

Menghitung kebutuhan pendingin

Berat F19 (kg/jam) ni (kmol/jam)

Cpl dT (J/mol) H sensibel (kJ/jam)

682.55 22808.60

647.42 441.53

23250.13

T bubble (K) Pi (mmHg) P (mmHg)total Ki Yi Parsial

429.28 1.0229E+03 1026.00 9.9702E-01 0.9771 1002.48400221

429.28 1.1758E+03 1026.00 1.1460E+00 0.0229 23.5158918704

1.0000

T dew (K) Pi (mmHg) P (mmHg) Ki Xi

429.30 1.0233E+03 1026.00 9.9740E-01 0.9826

429.30 1.1762E+03 1026.00 1.1464E+00 0.0174

1.0000

Cpg dT (J/mol) H sensibel (kJ/jam)

20969.10 700719.96

20205.82 13779.87

714499.83

T input (K) : 473.15

T output (K) : 375.37

B C D E

-3.9953E-02 -2.1103E-04 5.3469E-07 0.0000E+00

T out (K) : 303.18

Cpg dT (J/mol) H sensibel(Kj/jam) Cpg.Yi (J/mol K)

0.88 485.55 5.57

0.87 2056.80 23.59

2542.36 29.16

148.29 81368.76

146.24 344816.13

426184.90

3925.16 2153746.10

3828.49 9027102.54

11180848.64

T input (K) : 541.55

T output (K) : 473.15

B C D E

-3.9953E-02 -2.1103E-04 5.3469E-07 0.0000E+00

T bubble (K) Pi (mmHg) P (mmHg) Ki Yi

81.36 2.6368E-25 1003.20 2.6284E-28 0.0000

81.36 2.9893E-24 1003.20 2.9798E-27 0.0000

81.36 2.7082E+02 1003.20 2.6996E-01 0.0504

81.36 1.1881E+03 1003.20 1.1843E+00 0.9496

1.0000

307.96 1.1587E+01 1003.20 1.1550E-02 0.9838

307.96 1.4564E+01 1003.20 1.4518E-02 0.0160

307.96 1.7809E+06 1003.20 1.7752E+03 0.0001

307.96 8.6176E+06 1003.20 8.5901E+03 0.0001

1.0000

20886.48 697959.01

20205.82 13779.87

3925.16 2153746.10

3828.49 9027102.54

11892587.52

59676.60 1994200.12

58433.55 39850.24

9675.58 5309018.98

9280.45 21882147.56

29225216.90

-43639.60 -872.79 42766.81

-2860.76 0.00 2860.76

0.00 -9747333.10 -9747333.10

0.00 -551611.41 -551611.41

0.00 11511.08 11511.08

0.00 -2756335.27 -2756335.27

0.00 -1403966.58 -1403966.58

0.00 -16097280.23 -16097280.23

0.00 0.00 0.00

0.00 -65800371.42 -65800371.42

-46500.36 -96346259.72 -96299759.36

62062.75 41478.75

60797.66 0.00

51802.78 1231777.05

47053.15 66016.83

87382.44 5050.97

146259.54 9586.71

9671.00 122875.71

13984.82 572090.19

9997.28 4114659.89

9580.69 22590068.24

11287.51 1196378.50

29949982.84

Hr (kJ/mol) Hp (kJ/mol) Hf (kJ/mol)

T input (K) : 494.11

T output (K) : 541.55

A B C D E

9.2053E+01 -3.9953E-02 -2.1103E-04 5.3469E-07 0.0000E+00

52677.23 35206.08

51504.54 0.00

43731.86 1039865.08

40462.89 56770.52

79503.94 4595.57

121856.32 7987.18

8716.00 3587315.42

8382.24 19764264.06

8449.93 107361.27

12117.57 495705.07

9844.54 1043435.65

0.00 26142505.90

T input (K) : 541.55

T output (K) : 604.35

B C D E

-8.8146E-03 2.9906E-05 -1.7825E-08 3.6934E-12

80.43 9.5162E-26 836.00 1.1383E-28 0.0000

80.43 1.1255E-24 836.00 1.3463E-27 0.0000

80.43 2.7533E-33 836.00 3.2934E-36 0.0000

80.43 3.5003E-24 836.00 4.1870E-27 0.0000

80.43 4.1988E-45 836.00 5.0225E-48 0.0000

80.43 3.3477E-30 836.00 4.0044E-33 0.0000

80.43 5.8189E-24 836.00 6.9604E-27 0.0000

80.43 2.3938E+02 836.00 2.8634E-01 0.0406

80.43 1.0753E+03 836.00 1.2863E+00 1.0453

1.0859

407.32 5.7351E+02 836.00 6.8601E-01 0.0003

407.32 6.6513E+02 836.00 7.9561E-01 0.0000

407.32 1.0195E+01 836.00 1.2195E-02 0.6720

407.32 9.5197E+01 836.00 1.1387E-01 0.0042

407.32 4.1360E-45 836.00 4.9474E-48 0.0000

407.32 3.3650E+00 836.00 4.0251E-03 0.0056

407.32 2.2980E+03 836.00 2.7488E+00 0.0133

407.32 1.3740E+07 836.00 1.6436E+04 0.0000

407.32 1.8203E+08 836.00 2.1774E+05 0.0000

0.6955

16958.66 11334.08

16371.70 0.00

13673.68 325135.52

13772.05 19322.55

15295.87 884.15

36454.26 2389.43

3258.00 1340921.83

3184.14 7507807.45

9207795.01

T input (K) : 393.15

T output (K) : 494.11

B C D E

-3.9953E-02 -2.1103E-04 5.3469E-07 0.0000E+00

Cps dT (J/mol) H sensibel (kJ/jam)

5978.59 142160.23

6571.33 379.84

7984.44 523.35

143063.42

1019.32 5006.45

1363.83 55791.36

1035.22 426073.37

1018.37 2401188.46

2888059.64

6733.76 4500.41

6497.42 0.00

5379.11 7547.04

2634.17 279198.83

291246.28

14947.60 355427.53

16699.04 965.26

19775.11 1296.18

357688.96

16049.65 10726.55

12898.29 18096.65

18844.78 448095.64

19251.67 1112.81

29551.73 1936.99

479968.64

Cpl dT (J/mol) H sensibel (kJ/jam) A B C D E T P

19459.53 13005.50

22901.94 544567.75

23307.94 1347.27

35238.96 2309.77

15656.11 21965.95

583196.23

11890.17 241.85

11442.44 9709.80

9539.47 238.76

9728.58 7924.23

2675.65 685246.34

703360.97

15595.53 53.51

15055.70 1831.93

18304.62 6016.09

12530.96 13135.03

5971.90 66485.54

87522.10

15595.53 0.00

15055.70 43.53

18304.62 142.94

12530.96 312.09

5971.90 1579.64

2078.19

T input (K) : 303.15

T output (K) : 323.15

B C D E

-3.9953E-02 -2.1103E-04 5.3469E-07 0.0000E+00

70016.63 2451679.16

48715.99 1850.11

75790.34 216.09

78059.17 7418.54

2461163.90

44556.52 2001949.27

30513.96 1399.11

47892.82 179.87

60744.21 1901.17

46236.36 830.02

2006259.44

output

-359414.78

-239.05

-55.24

512.00

-359197.07 4774824.32

24529.18 56745.47

23901.95 317.85

57063.33

input output

2451679.16 4531616.20

1850.11 3688.64

216.09 424.35

7418.54 8573.01

2461163.90 4544302.20

43812.33 1417422.99

29996.39 740.29 2083138.29

47087.38 134.25

60018.19 1425.99

1419723.53

1.29921477

Cpl dT (J/mol) H sensibel (kJ/jam) ai xf

43812.33 449735.42 2.62E+01 0 0.00E+00 2.49E+01 0.00E+00

29996.39 235.07 2.97E+01 0.0096 2.85E-01 2.84E+01 1.00E-02

47087.38 42.60 1.00E+00 0.026 2.60E-02 -2.99E-01 -8.69E-02

60018.19 452.46 7.45E+00 0.083 6.19E-01 6.16E+00 1.01E-01

450465.54 1.15E+02 0.8814 1.01E+02 1.13E+02 8.91E-01

9.15E-01

T input (K) : 323.15

T output (K) : 330.97

B C D E

-3.9953E-02 -2.1103E-04 5.3469E-07 0.0000E+00

65634.78 22982.46

76171.23 5429.34

69490.91 93752.72

122164.52

24479.41 15591.62

23856.97 158.63

15750.25

Cp dT (J/mol) H sensibel (kJ/jam)

43727.09 73306.64

29937.15 199.06

73505.69

output

-925.51

-881.25 57944.58

T input (K) : 330.97

T output (K) : 331.07

A B C D E

9.2053E+01 -3.9953E-02 -2.1103E-04 5.3469E-07 0.0000E+00

43810.97 1490825.46

29995.45 843.59

47085.91 134.25

60016.85 1425.96

1493229.26

557.83 7.5707E+02 760.00 9.9614E-01 0.9945

557.83 4.5940E+03 760.00 6.0447E+00 0.0050

557.83 1.3770E+03 760.00 1.8118E+00 0.0002

557.83 9.1643E+01 760.00 1.2058E-01 0.0001

0.9998

558.26 7.6394E+02 760.00 1.0052E+00 0.9932

558.26 4.6303E+03 760.00 6.0926E+00 0.0001

558.26 1.3900E+03 760.00 1.8289E+00 0.0000

558.26 9.2228E+01 760.00 1.2135E-01 0.0057

0.9992

24876.09 846498.22

16999.01 478.08

26702.50 76.13

37911.48 900.75

847953.18

1642.70 55898.79

1211.59 34.07

1786.43 5.09

2204.48 52.38

55990.33

T input (K) : 303.15

T output (K) : 317.15

A B C D E

9.2053E+01 -3.9953E-02 -2.1103E-04 5.3469E-07 0.0000E+00

KAPASITAS PANAS GAS

T reff (K) : 298.15

T out (K) : 433.15

Komponen BM Berat (kg) ni (kmol) Xi A B C

O-xylene 106.167 104.0437 0.9800 9.8000E-01 1.8200E-01 5.1344E-01 -2.0212E-04

M-xylene 106.167 2.1233 0.0200 2.0000E-02 -1.6725E+01 5.6424E-01 -2.6465E-04

Phthalic anhydride 148.118 0.0000 0.0000 0.0000E+00 4.0083E+01 3.6084E-02 9.5956E-04

Maleic anhydride 98.058 0.0000 0.0000 0.0000E+00 -7.2015E+01 1.0423E+00 -1.8716E-03

Ortho Tolualdehide 136.150 0.0000 0.0000 0.0000E+00 -4.4383E+01 6.3161E-01 -3.8644E-04

Phthalide 134.136 0.0000 0.0000 0.0000E+00 1.9986E+01 7.7860E-01 2.9980E-04

Carbon monoxide 28.011 0.0000 0.0000 0.0000E+00 2.9556E+01 -6.5807E-03 2.0130E-05

Carbon dioxide 44.011 0.0000 0.0000 0.0000E+00 2.7437E+01 4.2315E-02 -1.9555E-05

Oxygen 32.000 0.0000 0.0000 0.0000E+00 2.9526E+01 -8.8889E-03 3.8083E-05

Nitrogen 28.014 0.0000 0.0000 0.0000E+00 2.9342E+01 -3.5395E-03 1.0076E-05

Water 18.016 0.0000 0.0000 0.0000E+00 3.3933E+01 -8.8146E-03 2.9906E-05

TOTAL 106.1670 1.0000 1.0000

KAPASITAS PANAS CAIRAN

T reff (K) : 298.00

T out (K) : 298.00

O-xylene 106.167 104.0437 0.9800 4.9000E-01 5.6460E+01 9.4926E-01 -2.4902E-03

M-xylene 106.167 2.1233 0.0200 1.0000E-02 7.0916E+01 8.0450E-01 -2.1885E-03

Phthalic anhydride 148.118 148.1180 1.0000 5.0000E-01 -1.0563E+02 1.9840E+00 -3.8847E-03

Maleic anhydride 98.058 0.0000 0.0000 0.0000E+00 -1.2662E+01 1.0564E+00 -2.3244E-03

Ortho Tolualdehide 136.150 0.0000 0.0000 0.0000E+00 5.8201E+01 1.1353E+00 -2.6405E-03

Phthalide 134.136 0.0000 0.0000 0.0000E+00 -8.0350E+00 2.4304E+00 -3.9847E-03

Carbon monoxide 28.011 0.0000 0.0000 0.0000E+00 1.2560E+02 -1.7022E+00 1.0707E-02

Carbon dioxide 44.011 0.0000 0.0000 0.0000E+00 -3.9810E+03 5.2511E+01 -2.2708E-01

Oxygen 32.000 0.0000 0.0000 0.0000E+00 4.6432E+01 3.9506E-01 -7.0522E-03

Nitrogen 28.014 0.0000 0.0000 0.0000E+00 7.6452E+01 -3.5226E-01 -2.6690E-03

Water 18.016 0.0000 0.0000 0.0000E+00 9.2053E+01 -3.9953E-02 -2.1103E-04

TOTAL 254.2850 2.0000 1.0000

KAPASITAS PANAS PADATAN

T reff (K) : 298.15

T out (K) : 379.70

O-xylene 106.167 1.0000 0.0094 1.0000 3.0200E-01 7.8782E-01 -8.1442E-04

M-xylene 106.167 0.0000 0.0000 0.0000 3.9130E+00 8.4357E-01 -1.4305E-03

Phthalic anhydride 148.118 0.0000 0.0000 0.0000 2.6320E+01 3.9060E-01 2.1260E-04

Maleic anhydride 98.058 0.0000 0.0000 0.0000 3.2500E+01 2.0960E-01 2.7330E-04

Ortho Tolualdehide 136.150 0.0000 0.0000 0.0000 -3.3836E+01 6.4085E-01 0.0000E+00

Phthalide 134.136 0.0000 0.0000 0.0000 3.4220E+01 6.1431E-01 0.0000E+00

Carbon monoxide 28.011 0.0000 0.0000 0.0000 2.1830E+01 -4.7101E-02 6.4073E-03

Carbon dioxide 44.011 0.0000 0.0000 0.0000 4.1195E+01 3.1470E-02 6.4118E-05

Oxygen 32.000 0.0000 0.0000 0.0000 -1.6683E+01 1.5925E+00 -2.9859E-03

Nitrogen 28.014 0.0000 0.0000 0.0000 2.4334E+01 2.8866E-01 1.1577E-03

Water 18.016 0.0000 0.0000 0.0000 9.6950E+00 7.4955E-02 -1.5584E-05

TOTAL 1.0000 0.0094 1.0000

ENTHALPY PENGUAPAN

T dew (K) :

D E Cpg dT (J/mol) H sensibel (kJ) Komponen

-2.1615E-08 2.3212E-11 2.1592E+04 2.1160E+04 O-xylene

1.3381E-08 1.5869E-11 2.0896E+04 4.1791E+02 M-xylene

-1.2341E-06 4.6597E-10 1.7488E+04 0.0000E+00 Phthalic anhydride

1.6527E-06 -5.5647E-10 1.7408E+04 0.0000E+00 Maleic anhydride

9.1760E-08 -2.9424E-12 1.8751E+04 0.0000E+00 Ortho Tolualdehide

1.7486E-08 5.6823E-11 4.6870E+04 0.0000E+00 Phthalide

-1.2227E-08 2.2617E-12 3.9551E+03 0.0000E+00 Carbon monoxide

3.9968E-09 -2.9872E-13 5.4623E+03 0.0000E+00 Carbon dioxide

-3.2629E-08 8.8607E-12 4.0426E+03 0.0000E+00 Oxygen

-4.3116E-09 2.5935E-13 3.9416E+03 0.0000E+00 Nitrogen

-1.7825E-08 3.6934E-12 4.5796E+03 0.0000E+00 Water

2.1578E+04 TOTAL

D E Cpl dT (J/mol) H sensibel (kJ)

2.6838E-06 0.0000E+00 0.0000E+00 0.0000E+00

2.5061E-06 0.0000E+00 0.0000E+00 0.0000E+00

2.8513E-06 0.0000E+00 0.0000E+00 0.0000E+00

2.0518E-06 0.0000E+00 0.0000E+00 0.0000E+00

2.4764E-06 0.0000E+00 0.0000E+00 0.0000E+00

1.6541E-07 0.0000E+00 0.0000E+00 0.0000E+00

4.1584E-06 0.0000E+00 0.0000E+00 0.0000E+00

3.2866E-04 0.0000E+00 0.0000E+00 0.0000E+00

3.9897E-05 0.0000E+00 0.0000E+00 0.0000E+00

5.0057E-05 0.0000E+00 0.0000E+00 0.0000E+00

5.3469E-07 0.0000E+00 0.0000E+00 0.0000E+00

0.0000E+00

D E Cps dT (J/mol) H sensibel (kJ)

0.0000E+00 0.0000E+00 1.4133E+04 1.3312E+02

0.0000E+00 0.0000E+00 1.0170E+04 0.0000E+00

0.0000E+00 0.0000E+00 1.4943E+04 0.0000E+00

0.0000E+00 0.0000E+00 1.1016E+04 0.0000E+00

0.0000E+00 0.0000E+00 1.4953E+04 0.0000E+00

0.0000E+00 0.0000E+00 1.9770E+04 0.0000E+00

0.0000E+00 0.0000E+00 6.0789E+04 0.0000E+00

0.0000E+00 0.0000E+00 4.8328E+03 0.0000E+00

0.0000E+00 0.0000E+00 1.4549E+04 0.0000E+00

0.0000E+00 0.0000E+00 2.0860E+04 0.0000E+00

0.0000E+00 0.0000E+00 2.7156E+03 0.0000E+00

1.3312E+02

ENTHALPY PENGUAPAN

433.60

BM Berat (kg) ni (kmol) A Tc (K) n H vap (kJ)

106.167 104.0437 0.9800 5.5606E+01 6.3037E+02 3.7500E-01 3.5216E+04

106.167 2.1233 0.0200 6.0216E+01 6.1705E+02 4.5800E-01 6.9098E+02

148.118 0.0000 0.0000 5.5495E+01 7.9100E+02 3.8000E-02 0.0000E+00

98.058 0.0000 0.0000 5.9574E+01 7.2100E+02 2.1600E-01 0.0000E+00

136.150 0.0000 0.0000 9.1444E+01 7.5100E+02 3.8800E-01 0.0000E+00

134.136 0.0000 0.0000 4.5551E+01 7.1000E+02 3.8000E-02 0.0000E+00

28.011 0.0000 0.0000 8.0030E+00 1.3292E+02 3.1800E-01 0.0000E+00

44.011 0.0000 0.0000 1.8260E+01 3.0419E+02 2.4000E-01 0.0000E+00

32.000 0.0000 0.0000 8.0400E+00 1.5458E+02 2.0100E-01 0.0000E+00

28.014 0.0000 0.0000 9.4300E+00 1.2610E+02 5.3300E-01 0.0000E+00

18.016 0.0000 0.0000 5.2053E+01 6.4713E+02 3.2100E-01 0.0000E+00

106.1670 1.0000 3.5907E+04

MENGHITUNG CP MEAN COOLING WATER

T input (K) : 485.15

T output (K) : 541.55

A B C D E

9.2053E+01 -3.9953E-02 -2.1103E-04 5.3469E-07 0.0000E+00

MENGHITUNG CP MEAN COOLING WATER

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