Compressor K-301E Air-cooler H-302E After-cooler H-303 Post-Compressor Knock-Out S-303
4.23 Compressor K-301E
Tabel 4.25 Neraca Energi pada Compressor K-301E Komponen Masuk kJ Keluar kJ H suction H discharge H 2 59250289,635 59638511,116 CO 2 12949,718 14098,782 CO 16965537,519 17107942,716 H 2 O 1265100,980 1292869,326 CH 4 12185978,272 13816125,497 C 2 H 4 338360,211 402742,994 C 2 H 6 76347,581 91706,811 C 3 H 8 55976,705 68255,727 C 3 H 6 75589,867 90691,919 C 4 H 10 2035,883 2452,047 C 4 H 8 1866,088 2258,092 Jumlah 90230032,459 92527655,027 Sub total 90230032,459 92527655,027 Q 2297622,568 Total 92527655,027 92527655,027 Universitas Sumatera Utara4.24 Air-cooler H-302E
Tabel 4.26 Neraca Energi pada Air-Cooler H-302E Komponen Masuk kJ Keluar kJ H in H 25 H 2 59638511,116 59250289,635 CO 2 14098,782 12949,718 CO 17107942,716 16965537,519 H 2 O 1292869,326 1265100,980 CH 4 13816125,497 12185978,272 C 2 H 4 402742,994 338360,211 C 2 H 6 91706,811 76347,581 C 3 H 8 68255,727 55976,705 C 3 H 6 90691,919 75589,867 C 4 H 10 2452,047 2035,883 C 4 H 8 2258,092 1866,088 Jumlah 92527655,027 90230032,459 Sub total 92527655,027 90230032,459 Q -2297622,568 Total 90230032,459 90230032,459 Universitas Sumatera Utara4.25 After-cooler H-303
Tabel 4.27 Neraca Energi pada Cooler H-303 Komponen Masuk kJ Keluar kJ H 25 H 26 H 2 59250289,635 59157479,503 CO 2 12949,718 12712,697 CO 16965537,519 16953526,510 H 2 O 1265100,980 1260350,857 CH 4 12185978,272 11881160,145 C 2 H 4 338360,211 325509,945 C 2 H 6 76347,581 73335,513 C 3 H 8 55976,705 53530,715 C 3 H 6 75589,867 72590,306 C 4 H 10 2035,883 1954,283 C 4 H 8 1866,088 1787,528 Jumlah 90230032,459 89793938,003 Sub total 90230032,459 89793938,003 Q -436094,456 Total 89793938,003 89793938,003 Universitas Sumatera Utara4.26 Post-Compressor Knock-Out S-303
Tabel 4.28 Neraca Energi pada Knock Out Drum S-303 Komponen Masuk kJ Keluar kJ H 26 H 28 H 27 H 2 59157479,503 28768,966 59128710,537 CO 2 12712,697 8,669 12704,028 CO 16953526,510 13545,691 16939980,820 H 2 O 1260350,857 990817,555 269533,302 CH 4 11881160,145 12796,349 11868363,796 C 2 H 4 325509,945 1282,688 324227,257 C 2 H 6 73335,513 433,466 72902,048 C 3 H 8 53530,715 1160,575 52370,140 C 3 H 6 72590,306 1321,307 71268,999 C 4 H 10 1954,283 141,633 1812,651 C 4 H 8 1787,528 108,309 1679,219 Jumlah 89793938,003 1050385,208 88743552,795 Sub total 89793938,003 89793938,003 Q 0,000 Total 89793938,003 89793938,003 Universitas Sumatera Utara4.27 Steam Reformer R-401
Parts
» Perumusan Masalah Tujuan Perancangan Ruang Lingkup Perancangan Manfaat Perancangan
» Gambaran Umum Hidrogen TINJAUAN PUSTAKA
» Kelapa Sawit Komposisi Cangkang Kelapa Sawit
» Oksidasi parsial Integrated gasification combined cycle IGCC
» Pirolisis Elektrolisis air Produksi hidrogen secara biologi
» Steam Reformer R-401 Reaktor High Temperature Shift Converter R-402
» Gasifier Cyclone S-201 Cyclone S-202 Char Combustor R-202
» Cyclone S-203 Reformer R-203 Cooler H-201 H-202
» Scrubber Gas Sintesis M-301 M-302 Quench Water Recirculation Cooler Knock Out Drum S-301
» Compressor K-301A Air-cooler H-302A Knock Out Drum S-302A Compressor K-301B
» Air-cooler H-302B Knock Out Drum S-302B Compressor K-301C Air-cooler H-302C
» Knock Out Drum S-302C Compressor K-301D Air-cooler H-302D Knock Out Drum S-302D
» Compressor K-301E Air-cooler H-302E After-cooler H-303 Post-Compressor Knock-Out S-303
» Steam Reformer R-401 NERACA ENERGI
» Air-Cooler H-408 After-cooler H-409 Pre-PSA Knock-Out 2 S-402 Pressure Swing Adsorption Unit S-403
» Bin Katalis Olivine T-105 Screw Conveyor C-102 Olivine Screw Conveyor C-103 Gasifier R-201
» Cyclone S-203 Char Combustor R-202
» Blower K-201 Reformer R-203 Cooler H-201
» Cooler H-202 Quench Chamber M-301
» Venturi Scrubber M-302 Pompa P-301 Quench Water Recirculation Cooler H-301
» Knock Out Drum S-301 Compressor K-301A Air-cooler H-302A
» Knock Out Drum S-302A Compressor K-301B Air-cooler H-302B
» Knock Out Drum S-302B Compressor K-301C Air-cooler H-302C
» Knock Out Drum S-302C Compressor K-301D Air-cooler H-302D
» Knock Out Drum S-302D Compressor K-301E Air-cooler H-302E
» After-cooler H-303 Post-Compressor Knock-Out S-303 Pompa P-302
» Steam Reformer R-401 Flue Gas Reformer Feed Preheater H-401 Flue Gas CoolerSteam Superheater H-404
» Reformer Syngas CoolerSteam Generator 2 H-402 Reformer Syngas CoolerSteam Superheater 1 H-403
» PSA PrecoolerDeaerator Water Preheater 1 H-407 Pre-PSA Knock-Out 1 S-401 Air-Cooler H-408
» Aftercooler H-409 Pre-PSA Knock-Out 2 S-402 Pressure Swing Adsorption Unit S-403
» Tujuan Pengendalian Jenis-Jenis Pengendalian dan Alat Pengendali
» Syarat Perancangan Pengendalian Elemen Pengendali Akhir
» Kebutuhan air proses Kebutuhan air lainnya
» Screening Sedimentasi Klarifikasi Kebutuhan Air
» Filtrasi Demineralisasi Kebutuhan Air
» Kebutuhan Uap air Steam Kebutuhan Bahan Kimia Kebutuhan Listrik Kebutuhan Bahan Bakar
» Bak Penampungan BP Bak Pengendapan Awal BPA Bak Netralisasi BN
» Unit Pengolahan Limbah dengan Sistem Activated Sludge Lumpur Aktif
» Lokasi Pabrik LOKASI DAN TATA LETAK PABRIK
» Tata Letak Pabrik Perincian Luas Tanah
» Bentuk Organisasi Garis Bentuk Organisasi Fungsionil Bentuk Organisasi Garis dan Staf
» Manajemen Perusahaan ORGANISASI DAN MANAJEMEN PERUSAHAAN
» Dewan Komisaris Direktur Sekretaris Manajer Produksi Manajer Teknik
» Sistem Kerja Jumlah Karyawan dan Tingkat Pendidikan
» Sistem Penggajian ORGANISASI DAN MANAJEMEN PERUSAHAAN
» Tata Tertib JAMSOSTEK dan Fasilitas Tenaga Kerja
» Modal Investasi Tetap MIT Fixed Capital Investment FCI Modal Kerja Working Capital WC
» Profit Margin PM Break Even Point BEP Return on Investment ROI Pay Out Time POT
» Perhitungan berat molekul dari olivine dan katalis olivine Komponen
» Char Combustor R-202 KESIMPULAN
» Cyclone S-203 Reformer R-203
» Cooler H-201 H-202 KESIMPULAN
» Scrubber Gas Sintesis M-301 M-302
» Quench Water Recirculation Cooler Knock Out Drum S-301
» Compressor K-301A Air-cooler H-302A
» Knock Out Drum S-302A Compressor K-301B
» Air-cooler H-302B Knock Out Drum S-302B
» Compressor K-301C Air-cooler H-302C
» Knock Out Drum S-302C Compressor K-301D
» Air-cooler H-302D Knock Out Drum S-302D
» Compressor K-301E Air-cooler H-302E
» After-cooler H-303 Post-Compressor Knock-Out S-303
» Steam Reformer R-401 Entalpi aliran umpan dari S-303, H
» Reformer Syngas CoolerSteam Generator 2 H-402
» Reformer Syngas CoolerSteam Superheater 1 H-403 High Temperature Shift Reactor R-402
» Low Temperatura Shift Precooler Deaerator Water Preheater 2 Low Temperature Shift Reactor R-403
» PSA PrecoolerDeaerator Water Preheater 1 H-407
» Air-Cooler H-408 Aftercooler H-409
» Pre-PSA Knock-Out 2 S-402 Pressure Swing Adsorption Unit S-403
» Pre Hydrogen Compressor Knock Out S-501 Compressor Hydrogen 1st Interstage K-501A
» Elevator Cangkang Kelapa Sawit C-101 Landfill Umpan Cangkang Kelapa Sawit T-101
» Bin Umpan Cangkang Kelapa Sawit T-102 Bin Olivine T-103
» Bin MgO T-104 Bin Katalis Olivine
» CKS Feed Screw Conveyor C-102 Olivine Screw Conveyor C-103 Gasifier R-201
» Quench Chamber M-301 KESIMPULAN
» Venturi Scrubber M-302 KESIMPULAN
» Quench Water Recirculation Cooler H-301
» Compressor K-301A KESIMPULAN
» Air-cooler H-302A KESIMPULAN
» Compressor K-301B KESIMPULAN
» Air-cooler H-302B KESIMPULAN
» Compressor K-301C KESIMPULAN
» Air-cooler H-302C KESIMPULAN
» Compressor K-301D KESIMPULAN
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