plnat design

CHEMCAD 6.3.1 Page 1

Simulation: plant 1 Date: 06/15/2015 Time: 17:07:55FLOW SUMMARIES:

Stream No. 1 2 3 4Stream Name Feed 1 Temp F 0.0000 0.0000 0.0000 0.0000 Pres psia 0.0000 0.0000 0.0000 0.0000 Enth MMBtu/h 0.00000 0.00000 0.00000 0.00000 Vapor mole frac. 0.00000 0.00000 0.00000 0.00000 Total lbmol/h 17216.9512 260.9067 1474.8538 260.9067 Total lb/h 961669.0000 12019.7129 37957.0000 12019.7129 Total std L ft3/hr 12465.8562 286.1174 556.6500 286.1174 Total std V scfh 6533465.00 99008.53 559675.50 99008.53 Flowrates in lb/hsulfuric acid, m 760063.0625 0.0000 13284.9463 0.0000 Water 201606.0000 0.0000 24672.0410 0.0000 Dimethyl Ether 0.0000 12019.7129 0.0000 12019.7129 2-Methyl-1-Propa 0.0000 0.0000 0.0000 0.0000

Stream No. 5 6 7 8Stream Name Temp F 0.0000 0.0000 0.0000 0.0000 Pres psia 0.0000 0.0000 0.0000 1.0000*Enth MMBtu/h 0.00000 0.00000 0.00000 0.00000 Vapor mole frac. 0.00000 0.00000 0.00000 0.00000 Total lbmol/h 933.0436 300.9315 0.0000 1229.0664 Total lb/h 37957.0000 37957.0000 0.0000 50609.3125 Total std L ft3/hr 512.6242 461.2608 0.0000 808.8752 Total std V scfh 354070.09 114197.09 0.00 466404.44 Flowrates in lb/hsulfuric acid, m 24672.0410 37957.0000 0.0000 24672.0410 Water 13284.9463 0.0000 0.0000 13917.5625 Dimethyl Ether 0.0000 0.0000 0.0000 12019.7129 2-Methyl-1-Propa 0.0000 0.0000 0.0000 0.0000

Stream No. 9 10 11 12Stream Name Temp F 0.0000 0.0000 0.0000 0.0000 Pres psia 0.0000 0.0000 0.0000 0.0000 Enth MMBtu/h 0.00000 0.00000 0.00000 0.00000 Vapor mole frac. 0.00000 0.00000 0.00000 0.00000 Total lbmol/h 0.0000 22956.0000 0.0000 0.0000 Total lb/h 0.0000 1864889.0000 0.0000 0.0000 Total std L ft3/hr 0.0000 25701.9062 0.0000 0.0000 Total std V scfh 0.00 8711311.00 0.00 0.00 Flowrates in lb/hsulfuric acid, m 0.0000 1411545.5000 0.0000 0.0000 Water 0.0000 131982.7500 0.0000 0.0000 Dimethyl Ether 0.0000 12558.5703 0.0000 0.0000 2-Methyl-1-Propa 0.0000 308802.0938 0.0000 0.0000


Simulation: plant 1 Date: 06/15/2015 Time: 17:07:55FLOW SUMMARIES:

Stream No. 13 14 15 16Stream Name Bottom Top Temp F 0.0000 0.0000 0.0000 0.0000 Pres psia 0.0000 0.0000 0.0000 0.0000 Enth MMBtu/h 0.00000 0.00000 0.00000 0.00000 Vapor mole frac. 0.00000 0.00000 0.00000 0.00000 Total lbmol/h 1925.7537 195.6055 215.9590 909.5845 Total lb/h 72178.7578 24672.0410 16006.1465 16751.3477 Total std L ft3/hr 998.1174 299.8195 318.0263 273.0001 Total std V scfh 730782.38 74228.11 81951.81 345167.88 Flowrates in lb/hsulfuric acid, m 42990.1406 24672.0410 0.0000 0.0000 Water 28143.6836 0.0000 0.0000 16151.6611 Dimethyl Ether 1044.9327 0.0000 2.2668 599.6869 2-Methyl-1-Propa 0.0000 0.0000 16003.8789 0.0000

Stream No. 17 18 19Stream Name Temp F 0.0000 0.0000 0.0000 Pres psia 0.0000 0.0000 0.0000 Enth MMBtu/h 0.00000 0.00000 0.00000 Vapor mole frac. 0.00000 0.00000 0.00000 Total lbmol/h 0.0000 0.0000 340.8355 Total lb/h 0.0000 0.0000 42990.1406 Total std L ft3/hr 0.0000 0.0000 522.4246 Total std V scfh 0.00 0.00 129339.79 Flowrates in lb/hsulfuric acid, m 0.0000 0.0000 42990.1406 Water 0.0000 0.0000 0.0000 Dimethyl Ether 0.0000 0.0000 0.0000 2-Methyl-1-Propa 0.0000 0.0000 0.0000


Simulation: plant 1 Date: 06/15/2015 Time: 17:08:36STREAM PROPERTIES

Stream No. 1 2 3 4 Name Feed 1 - - Overall - -Molar flow lbmol/h 17216.9512 260.9067 1474.8538 260.9067 Mass flow lb/h 961669.0000 12019.7129 37957.0000 12019.7129 Temp F 0.0000 0.0000 0.0000 0.0000 Pres psia 0.0000 0.0000 0.0000 0.0000 Vapor mole fraction 0.0000 0.0000 0.0000 0.0000 Enth MMBtu/h 0.00000 0.00000 0.00000 0.00000 Tc F 974.6399 260.5100 804.4067 260.5100 Pc psia 4627.4873 778.8813 4475.2168 778.8813 Std. sp gr. wtr = 1 1.236 0.673 1.092 0.673 Std. sp gr. air = 1 1.929 1.591 0.889 1.591 Degree API -16.9931 78.7738 -1.9536 78.7738 Average mol wt 55.8559 46.0690 25.7361 46.0690 Actual dens lb/ft3 0.0000 0.0000 0.0000 0.0000 Actual vol ft3/hr -1.#IND -1.#IND -1.#IND -1.#IND Std liq ft3/hr 12465.8564 286.1174 556.6500 286.1174 Std vap 60F scfh 6533465.0000 99008.5313 559675.5000 99008.5313 - - Liquid only - -Molar flow lbmol/h 17216.9512 260.9067 1474.8538 260.9067 Mass flow lb/h 961669.0000 12019.7129 37957.0000 12019.7129 Average mol wt 55.8559 46.0690 25.7361 46.0690 Actual dens lb/ft3 Actual vol ft3/hr Std liq ft3/hr 12465.8564 286.1174 556.6500 286.1174 Std vap 60F scfh 6533465.0000 99008.5313 559675.5000 99008.5313 Cp Btu/lbmol-F Z factor 0.0000 0.0000 0.0000 0.0000 Visc cP 1.000 1.000 1.000 1.000 Th cond Btu/hr-ft-F Surf. tens. dyne/cm CHEMCAD 6.3.1 Page 2


Stream No. 5 6 7 8 Name - - Overall - -Molar flow lbmol/h 933.0436 300.9315 0.0000 1229.0664 Mass flow lb/h 37957.0000 37957.0000 0.0000 50609.3125 Temp F 0.0000 0.0000 0.0000 0.0000 Pres psia 0.0000 0.0000 0.0000 1.0000 Vapor mole fraction 0.0000 0.0000 0.0000 0.0000 Enth MMBtu/h 0.00000 0.00000 0.00000 0.00000 Tc F 913.2514 1082.9300 0.0000 718.0881 Pc psia 5035.6353 1302.4435 0.0000 3131.2742 Std. sp gr. wtr = 1 1.186 1.318 0.000 1.002 Std. sp gr. air = 1 1.405 4.355 0.000 1.422 Degree API -12.1995 -24.1530 0.0000 9.6842 Average mol wt 40.6808 126.1316 0.0000 41.1770 Actual dens lb/ft3 0.0000 0.0000 0.0000 0.0000 Actual vol ft3/hr -1.#IND -1.#IND 0.0000 -1.#IND Std liq ft3/hr 512.6242 461.2608 0.0000 808.8752 Std vap 60F scfh 354070.0938 114197.0938 0.0000 466404.4375 - - Liquid only - -Molar flow lbmol/h 933.0436 300.9315 1229.0664 Mass flow lb/h 37957.0000 37957.0000 50609.3125 Average mol wt 40.6808 126.1316 41.1770 Actual dens lb/ft3 Actual vol ft3/hr Std liq ft3/hr 512.6242 461.2608 808.8752 Std vap 60F scfh 354070.0938 114197.0938 466404.4375 Cp Btu/lbmol-F Z factor 0.0000 0.0000 0.0531 Visc cP 1.000 1.000 1.000 Th cond Btu/hr-ft-F Surf. tens. dyne/cm CHEMCAD 6.3.1 Page 3


Stream No. 9 10 11 12 Name - - Overall - -Molar flow lbmol/h 0.0000 22956.0000 0.0000 0.0000 Mass flow lb/h 0.0000 1864889.0000 0.0000 0.0000 Temp F 0.0000 0.0000 0.0000 0.0000 Pres psia 0.0000 0.0000 0.0000 0.0000 Vapor mole fraction 0.0000 0.0000 0.0000 0.0000 Enth MMBtu/h 0.00000 0.00000 0.00000 0.00000 Tc F 0.0000 911.0906 0.0000 0.0000 Pc psia 0.0000 2432.7656 0.0000 0.0000 Std. sp gr. wtr = 1 0.000 1.162 0.000 0.000 Std. sp gr. air = 1 0.000 2.805 0.000 0.000 Degree API 0.0000 -9.7561 0.0000 0.0000 Average mol wt 0.0000 81.2375 0.0000 0.0000 Actual dens lb/ft3 0.0000 0.0000 0.0000 0.0000 Actual vol ft3/hr 0.0000 -1.#IND 0.0000 0.0000 Std liq ft3/hr 0.0000 25701.9063 0.0000 0.0000 Std vap 60F scfh 0.0000 8711311.0000 0.0000 0.0000 - - Liquid only - -Molar flow lbmol/h 22956.0000 Mass flow lb/h 1864889.0000 Average mol wt 81.2375 Actual dens lb/ft3 Actual vol ft3/hr Std liq ft3/hr 25701.9063 Std vap 60F scfh 8711311.0000 Cp Btu/lbmol-F Z factor 0.0000 Visc cP 1.000 Th cond Btu/hr-ft-F Surf. tens. dyne/cm CHEMCAD 6.3.1 Page 4


Stream No. 13 14 15 16 Name Bottom Top - - Overall - -Molar flow lbmol/h 1925.7537 195.6055 215.9590 909.5845 Mass flow lb/h 72178.7578 24672.0410 16006.1465 16751.3477 Temp F 0.0000 0.0000 0.0000 0.0000 Pres psia 0.0000 0.0000 0.0000 0.0000 Vapor mole fraction 0.0000 0.0000 0.0000 0.0000 Enth MMBtu/h 0.00000 0.00000 0.00000 0.00000 Tc F 882.8276 1082.9300 526.2063 688.9069 Pc psia 4890.9482 1302.4435 623.8232 2961.6443 Std. sp gr. wtr = 1 1.158 1.318 0.806 0.983 Std. sp gr. air = 1 1.294 4.355 2.559 0.636 Degree API -9.3461 -24.1530 44.0138 12.4621 Average mol wt 37.4808 126.1316 74.1166 18.4165 Actual dens lb/ft3 0.0000 0.0000 0.0000 0.0000 Actual vol ft3/hr -1.#IND -1.#IND -1.#IND -1.#IND Std liq ft3/hr 998.1174 299.8195 318.0263 273.0001 Std vap 60F scfh 730782.3750 74228.1094 81951.8125 345167.8750 - - Liquid only - -Molar flow lbmol/h 1925.7537 195.6055 215.9590 909.5845 Mass flow lb/h 72178.7578 24672.0410 16006.1465 16751.3477 Average mol wt 37.4808 126.1316 74.1166 18.4165 Actual dens lb/ft3 Actual vol ft3/hr Std liq ft3/hr 998.1174 299.8195 318.0263 273.0001 Std vap 60F scfh 730782.3750 74228.1094 81951.8125 345167.8750 Cp Btu/lbmol-F Z factor 0.0000 0.0000 0.0000 0.0000 Visc cP 1.000 1.000 1.000 1.000 Th cond Btu/hr-ft-F Surf. tens. dyne/cm CHEMCAD 6.3.1 Page 5


Stream No. 17 18 19 Name - - Overall - -Molar flow lbmol/h 0.0000 0.0000 340.8355 Mass flow lb/h 0.0000 0.0000 42990.1406 Temp F 0.0000 0.0000 0.0000 Pres psia 0.0000 0.0000 0.0000 Vapor mole fraction 0.0000 0.0000 0.0000 Enth MMBtu/h 0.00000 0.00000 0.00000 Tc F 0.0000 0.0000 1082.9300 Pc psia 0.0000 0.0000 1302.4435 Std. sp gr. wtr = 1 0.000 0.000 1.318 Std. sp gr. air = 1 0.000 0.000 4.355 Degree API 0.0000 0.0000 -24.1530 Average mol wt 0.0000 0.0000 126.1316 Actual dens lb/ft3 0.0000 0.0000 0.0000 Actual vol ft3/hr 0.0000 0.0000 -1.#IND Std liq ft3/hr 0.0000 0.0000 522.4246 Std vap 60F scfh 0.0000 0.0000 129339.7891 - - Liquid only - -Molar flow lbmol/h 340.8355 Mass flow lb/h 42990.1406 Average mol wt 126.1316 Actual dens lb/ft3 Actual vol ft3/hr Std liq ft3/hr 522.4246 Std vap 60F scfh 129339.7891 Cp Btu/lbmol-F Z factor 0.0000 Visc cP 1.000 Th cond Btu/hr-ft-F Surf. tens. dyne/cm

Kesimpulan:Simulasi ini masih terjadi error, sehingga masih dibutuhkan pendalaman untuk mengkaji dan memperbaiki equipment ataupun streams yang masih error.

PLANT DESIGNTUGAS PERHITUNGAN DENGAN KOMPUTER

Dosen Pembimbing : Dr. Eko Ariyanto, M.ChemEng

KELOMPOK 1

Ahmad Irawan122013001Mutiara Rakhma P122013008Ali Amar Maruf122013013Rexsi Mainaki122013019Batariyah Triyuliana122013021

plnat design

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