Knock Out Drum S-302C Compressor K-301D Air-cooler H-302D Knock Out Drum S-302D
4.19 Knock Out Drum S-302C
Tabel 4.21 Neraca Energi pada Knock Out Drum S-302C Komponen Masuk kJ Keluar kJ H umpan H recycle H bottom H top H 2 59261867,490 59250289,635 59259250,438 59252906,687 CO 2 12948,665 12949,718 12951,442 12946,942 CO 16969790,625 16965537,519 16969488,853 16965839,292 H 2 O 5210492,999 1265100,980 3915307,611 2560286,367 CH 4 12189144,032 12185978,272 12189592,947 12185529,358 C 2 H 4 338546,760 338360,211 338697,857 338209,114 C 2 H 6 76398,651 76347,581 76459,247 76286,986 C 3 H 8 56045,642 55976,705 56262,777 55759,570 C 3 H 6 75672,898 75589,867 75915,062 75347,704 C 4 H 10 2046,504 2035,883 2071,507 2010,879 C 4 H 8 1872,652 1866,088 1892,946 1845,793 Jumlah 94194826,919 90230032,459 92897890,687 91526968,691 Sub total 184424859,378 184424859,378 Q 0,000 Total 184424859,378 184424859,378 Universitas Sumatera Utara4.20 Compressor K-301D
Tabel 4.22 Neraca Energi pada Compressor K-301D Komponen Masuk kJ Keluar kJ H suction H discharge H 2 59252906,687 59640312,096 CO 2 12946,942 14092,930 CO 16965839,292 17107704,976 H 2 O 2560286,367 2616322,367 CH 4 12185529,358 13811249,415 C 2 H 4 338209,114 402399,918 C 2 H 6 76286,986 91594,495 C 3 H 8 55759,570 67959,883 C 3 H 6 75347,704 90363,028 C 4 H 10 2010,879 2420,874 C 4 H 8 1845,793 2232,555 Jumlah 91526968,691 93846652,538 Sub total 91526968,691 93846652,538 Q 2319683,846 Total 93846652,538 93846652,538 Universitas Sumatera Utara4.21 Air-cooler H-302D
Tabel 4.23 Neraca Energi pada Air-Cooler H-302D Komponen Masuk kJ Keluar kJ H input H output H 2 59640312,096 59252906,687 CO 2 14092,930 12946,942 CO 17107704,976 16965839,292 H 2 O 2616322,367 2560286,367 CH 4 13811249,415 12185529,358 C 2 H 4 402399,918 338209,114 C 2 H 6 91594,495 76286,986 C 3 H 8 67959,883 55759,570 C 3 H 6 90363,028 75347,704 C 4 H 10 2420,874 2010,879 C 4 H 8 2232,555 1845,793 Jumlah 93846652,538 91526968,691 Sub total 93846652,538 91526968,691 Q -2319683,846 Total 91526968,691 91526968,691 Universitas Sumatera Utara4.22 Knock Out Drum S-302D
Tabel 4.24 Neraca Energi pada Knock Out Drum S-302D Komponen Masuk kJ Keluar kJ H umpan H 28 H bottom H top H 2 59252906,687 28768,966 31386,018 59250289,635 CO 2 12946,942 8,669 5,893 12949,718 CO 16965839,292 13545,691 13847,463 16965537,519 H 2 O 2560286,367 990817,555 2286002,942 1265100,980 CH 4 12185529,358 12796,349 12347,435 12185978,272 C 2 H 4 338209,114 1282,688 1131,591 338360,211 C 2 H 6 76286,986 433,466 372,870 76347,581 C 3 H 8 55759,570 1160,575 943,440 55976,705 C 3 H 6 75347,704 1321,307 1079,144 75589,867 C 4 H 10 2010,879 141,633 116,629 2035,883 C 4 H 8 1845,793 108,309 88,015 1866,088 Jumlah 91526968,691 1050385,208 2347321,440 90230032,459 Sub total 92577353,899 92577353,899 Q 0,000 Total 92577353,899 92577353,899 Universitas Sumatera Utara4.23 Compressor K-301E
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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