Tugas Perancangan Proses Kimia
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TUGAS PERANCANGAN PROSES KIMIA
KONVERSI PROPILEN OKSIDA DAN AIR MENJADI PROPILEN GLIKOL
PADA REAKTOR TANGKI IDEAL KONTINU (RTIK/CSTR)
Contoh Kasus 3
ANGGOTA:
Muliasari Kurniati L2C009004
Yudha Duta Utama L2C009023
Giovanni Anward L2C009025
Gita Khaerunnisa L2C009027
Thamrin Manurung L2C008107
JURUSAN TEKNIK KIMIA FAKULTAS TEKNIK
UNIVERSITAS DIPONEGORO
SEMARANG
2012
CHEMCAD 6.0.1 Page 1
Job Name: sk3 Date: 05/24/2012 Time: 17:23:08
Stream No. 1 2 3 4Stream Name Temp F 75.0000* 75.0000* 75.0000 130.0000 Pres psia 16.1650* 16.1700* 16.1650 16.1650 Enth MMBtu/h -7.8119 -75.020 -82.832 -85.459 Vapor mole fraction 0.00000 0.00000 0.00000 0.00000 Total lbmol/h 150.0000 610.6023 760.6023 617.1254 Total lb/h 8712.0000 11000.0000 19712.0000 19712.1230 Total std L ft3/hr 167.0994 176.2033 343.3027 307.1383 Total std V scfh 56921.79 231710.52 288632.31 234185.89 Flowrates in lb/h1,2-Propylene Ox 8712.0000 0.0000 8712.0000 378.7751 Water 0.0000 11000.0000 11000.0000 8415.2334 1,3-Propylene Gl 0.0000 0.0000 0.0000 10918.1152
Stream No. 5 6Stream Name Temp F 143.7886 410.6977 Pres psia 15.0000 15.0000 Enth MMBtu/h -57.053 -26.094 Vapor mole fraction 0.00000 0.00000 Total lbmol/h 472.9251 144.2006 Total lb/h 8781.0615 10931.0693 Total std L ft3/hr 141.8569 165.2815 Total std V scfh 179464.97 54721.05 Flowrates in lb/h1,2-Propylene Ox 378.7751 0.0000 Water 8402.2510 12.9893 1,3-Propylene Gl 0.0360 10918.0801
FLOWSHEET KONVERSI PROPILEN OKSIDA DAN AIR MENJADI PROPILEN GLIKOL PADA REAKTOR TANGKI IDEAL KONTINU
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T 75.00
P 16.17
W 8712.00
M 150.00
T 75.00
P 16.17
W 11000.00
M 610.60
T 75.00
P 16.17
W 19712.00
M 760.60
T 130.00
P 16.17
W 19712.12
M 617.13
T 143.79
P 15.00
W 8781.06
M 472.93
T 410.70
P 15.00
W 10931.07
M 144.20