ne1
TRANSCRIPT
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Heater 1 Komponen F5 (kg/h)n-Butanol 2184.4150955PTSA 106.3752177total 2290.7903132Steam 1160582.4091
Kapasitas Panas
Rumus Molekul Nama A B C D SuhuT5 (in)
C4H10O n-Butanol 1,131.592 7.64E+04 -2.32E+02 3.07E-01 T5 (out)C10H22O 1-Dekanol 97,978 2.17E+04 -5.16E-02 5.00E-02 TsteamH2O Air 92,053 -4.00E+02 -2.11E+00 5.35E-03 TreffH2O2 Hidrogen Peroksida -15,248 6.77E+03 -1.49E+01 1.20E-02NaOH Sodium Hidroksida 87,639 -4.84E+00 -4.54E-02 1.19E-05 Hv 224 C
Heater 1Q5 (in) Q5 (out)
Qsteam (in)
Qsteam (out)
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Heater 2 Komponen F6 (kg/h)Air 4346.0260036Glukosa 5318.760885total 9664.7868886Steam 1293.5540605
Kapasitas Panas
Rumus Molekul Nama A B C D SuhuT6 (in)C4H10O n-Butanol 6.217 4.20E+02 -1.28E+00 1.69E-03 T6 (out)C10H22O 1-Dekanol 97,978 2.17E+04 -5.16E-02 5.00E-02 TsteamH2O Air 7,671.083 -2.22E+04 -1.17E+02 2.97E-01 TreffH2O2 Hidrogen Peroksida -15,248 6.77E+03 -1.49E+01 1.20E-02NaOH Sodium Hidroksida 87,639 -4.84E+00 -4.54E-02 1.19E-05 Hv 224 C
Heater 2Q6 (in) Q6 (out)
Qsteam (in)
Qsteam (out)
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Heater 3 Komponen F12 (kg/h)Air 188.69289571Dekanol 4528.6294971PTSA 53.18760885total 4717.3223928Steam #DIV/0!
Kapasitas Panas Rumus Molekul Nama A B C D Suhu
T12 (in)C4H10O n-Butanol 6.217 4.20E+02 -1.28E+00 1.69E-03 T12 (out)C10H22O 1-Dekanol 618.993 3.43E+03 -8.16E-03 7.92E-03 TsteamH2O Air 1.105 -7.19E+00 -3.80E-02 9.62E-05 TreffH2O2 Hidrogen Peroksida -15,248 6.77E+03 -1.49E+01 1.20E-02NaOH Sodium Hidroksida 87,639 -4.84E+00 -4.54E-02 1.19E-05 Hv 224 C
Heater 3Q12 (in) Q12 (out)
Qsteam (in)
Qsteam (out)
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Qin (kJ/h) Qout (kJ/h)2905969104 3250675254
0 15.9675240912905969104 32506752703250675270 3250675270
C K30 303.15
150 423.15224 497.15
25 298.15
2800.9 kJ/kg
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Qin (kJ/h) Qout (kJ/h)0 3622095.24610 1020.32196460 3623115.568
3623115.568 3623115.568
C K25 298.15
150 423.15150 423.15
25 298.15
2800.9 kJ/kg
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Qin (kJ/h) Qout (kJ/h)0 278.595274620 695689403.690 00 695689682.28
695689682.28 695689682.28
C K25 298.15
125 398.15125 398.15
25 298.15
2800.9 kJ/kg
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Reaktor 1 Komponen F7 (kg/h)Air 4861.945809451Glukosa 159.5628265487Butanol 65.5324528636PTSA 106.3752176992BG 6764.281898803ReaksiPendinginTotal
Kapasitas Panas
Rumus Molekul Nama A B C DAliran
PendinginC4H10O n-Butanol 1,131.592 7.64E+04 -2.32E+02 3.07E-01C10H22O 1-Dekanol 97,978 2.17E+04 -5.16E-02 5.00E-02H2O Air 1.657 -7.19E+00 -3.80E-02 9.62E-05H2O2 Hidrogen Peroksida -15,248 6.77E+03 -1.49E+01 1.20E-02NaOH Sodium Hidroksida 87,639 -4.84E+00 -4.54E-02 1.19E-05
Entalpi Reaksi
Jenis Ikatan Jumlah Ikatan Total Entalpi (kJ/h)Glukosa Butanol BG air GlukosaC-H 7 9 16 0 413 2891C-C 5 3 8 0 348 1740C-O 7 1 7 0 351 2457H-O 5 1 4 2 463 2315
Total (kJ/kg) 0Entalpi Reaksi (kJ/h)
Entalpi Ikatan
ReaktorQ5 + Q6 Q7
Qpendingin
Qpendingin
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Reaktor 2 Komponen F8 + F12 (kg/h)Air 4346.02600361Glukosa 159.5628265487Butanol 1124.131932505PTSA 159.5628265487BG 3179.212492438Dekanol 2128.455863621APG 4861.111059479ReaksiSteam 542446216.6621Total
Kapasitas Panas
Rumus Molekul Nama A B C D refC4H10O n-Butanol 6.217 4.20E+02 -1.28E+00 1.69E-03 ReaktanC10H22O 1-Dekanol 15.508 3.43E+03 -8.16E-03 7.92E-03 steamH2O Air 1.657 -7.19E+00 -3.80E-02 9.62E-05 Entalpi Vapor (H2O)H2O2 Hidrogen Peroksida -15,248 6.77E+03 -1.49E+01 1.20E-02 ANaOH Sodium Hidroksida 87,639 -4.84E+00 -4.54E-02 1.19E-05 52.053
ReaktorQ8 + Q12 Q13
Qsteam
Qsteam / Qpendingin
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Hv 150 C =Entalpi Reaksi
Jenis Ikatan Jumlah Ikatan Total Entalpi (kJ/h)Dekanol Butanol BG APG DekanolC-H 21 9 16 27 413 8673C-C 9 3 8 14 348 3132C-O 1 1 7 8 351 351H-O 1 1 4 5 463 463
Total (kJ/kg) 0Entalpi Reaksi (kJ/h)
Parameter Konstanta Pers. Harrson and SeatonAtom C H O SSuhu a1 a2 a3 a4 a6300 4.86 9.04 5.69 11.4 15.3400 0.864 12.6 7.37 13.9 17500 -1.85 15.5 8.89 15.7 19.4600 -4.61 17.5 10.5 17.5 20.3
Nilai Interpolasi298.15 4.933926 8.97414 5.65892 11.35375 15.26855 Entalpi (298,15)398.15 0.937926 12.53414 7.33892 13.85375 16.96855 Entalpi (398,15)
Jumlah Molekul (BG) 10 22 6 0 Mr BG298.15 4.933926 8.97414 5.65892 11.35375 15.26855 Entalpi (298,15)398.15 0.937926 12.53414 7.33892 13.85375 16.96855 Entalpi (398,15)
Jumlah Molekul (APG) 16 32 7 0 Mr APG
Entalpi Ikatan
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Qin (kJ/h) Qout (kJ/h)3622095.2460582 72403.448139151020.3219645914 30.60965893773250675253.6785 18609.90405686
15.9675240909 15.96752409090 10390.379236180 2840.5305523
-3254194094.375 0104290.8391676 104290.8391675
T in T out298.15 323.15
Total Entalpi (kJ/h)Butanol BG air
3717 6608 01044 2784 0
351 2457 0463 1852 926
413.235725 3237.0982773 16.668Entalpi Reaksi (kJ/h) 2840.5305523
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Qin (kJ/h) Qout (kJ/h)278.5952746204 278.5952746204
0 00 7104264.98947
0 00 46968.60232841
695689403.68889 326840945.45610 147789.57835950 3204.49055230 361546230.5721
695689682.28417 695689682.2842
Suhu298.15398.15423.15
Entalpi Vapor (H2O)Tc n
647.13 0.321
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37.028374577 kJ/mol0.6665107424 kJ/kg
Total Entalpi (kJ/h)Butanol BG air
3717 6608 111511044 2784 4872
351 2457 2808463 1852 2315
413.235725 3237.0982773 380.628Entalpi Reaksi (kJ/h) 3204.4905523
64889514.152713 J/kg111858116.48112 J/kg
238.28324199468494.1987 J/kg347258072.5582 J/kg
336.42924
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Cooler 2
Kapasitas Panas
Rumus Molekul Nama A B C
C4H10O n-Butanol 6.217 4.20E+02 -1.28E+00C10H22O 1-Dekanol 97,978 2.17E+04 -5.16E-02H2O Air 1.105 -7.19E+00 -3.80E-02H2O2 Hidrogen Peroksida -15,248 6.77E+03 -1.49E+01NaOH Sodium Hidroksida 87,639 -4.84E+00 -4.54E-02
Cooler 2Q8 (in) Q8
(out)
Qair (in)
Qair (out)
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Komponen F8 (kg/h) Qin (kJ/h) Qout (kJ/h)PTSA 106.3752176992 0 0Glukosa 159.5628265487 0 0BG 6764.2818988034 0 0Cooler 0 0 0Total 7030.2199430513 0 0
D Suhu C KT8 (in) 150 423.15
1.69E-03 T8 (out) 125 398.155.00E-02 Tcooler (in) 25 298.159.62E-05 Tcooler (out) 30 303.151.20E-02 Treff 25 298.151.19E-05
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Kapasitas Panas
Rumus Molekul
C4H10OC10H22OH2OH2O2NaOH
Komponen hfk gfk hvk hmk
CH 29.89 58.36 404 179OH -208.04 -189.2 4021 575O -132.22 -105 576 284CH2 -20.64 8.42 532 619CH3 -76.45 -43.96 567 217S 41.87 33.12 1629 987O rangkap 2 -247.61 -250.83 1412 866C rangkap 2 83.99 92.36 511 732CH rangkap 2 37.97 48.53 527 643Konstanta GlukosaPTSABGAPG
Nama A B C
n-Butanol 6.217 4.20E+02 -1.28E+001-Dekanol 15.508 3.43E+03 -8.16E-03Air 1.657 -7.19E+00 -3.80E-02Hidrogen Peroksida -518.661 2.30E+02 -5.08E-01Sodium Hidroksida 3.5053 -1.93E-01 -1.82E-03
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Suhu Referensi T5 IN T5 OUT T6 INC 25 25 30 45K 298.15 298.15 303.15 318.15
cpak cpbk cpck cpdk NkGlukosa PTSA BG APG-23 0.204 -0.000265 0.00000012 5 0 5 525.7 -0.0691 0.000177 -9.88E-008 5 1 4 425.5 -0.0632 0.000111 -5.48E-008 1 0 2 2
-0.909 0.095 -5.4E-005 1.19E-008 1 0 4 1019.5 -0.00808 0.000153 -9.67E-008 0 1 1 119.6 -0.00561 0.0000402 -2.76E-008 0 1 0 06.82 0.0196 0.0000127 -1.78E-008 0 2 0 0-28.1 0.208 -0.000306 1.460E-007 0 2 0 0
-8 1.05E-01 -9.63E-05 3.56E-08 0 4 0 0-37.93 0.21 -3.91E-04 2.06E-07
38.091 7.06E-01 -3.83E-04 6.31E-08-9.76 7.92E-01 -6.02E-04 1.76E-07
54.664 9.89E-01 -0.00046 4.61E-0849.21 1.55912 -0.000786 1.175E-007
D Cp dTT 1501.69E-03 2839807.92E-03 62344749.62E-05 14891.8674.09E-04 169288.774.74E-07 1029.9295
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T6 OUT T8 IN T8 OUT T12 IN T12 OUT60 25 90 25 140
333.15 298.15 363.15 298.15 413.15
t140 t115 t30
1064.801 14821.31 1064.801 1378.233 1064.801871.6736 12273.21 871.6736 1268.423 871.67361536.065 21393.41 1536.065 1886.247 1536.065
2227.83 31131.87 2227.83 2715.83 2227.83
Entalpi (J/mol)
Entalpi (J/mol)
Entalpi (J/mol)
Entalpi (J/mol)
Entalpi (J/mol)
Entalpi (J/mol)
HeaterReaktorCoolerSheet1