Low Temperature Shift Precooler Deaerator Water Preheater 2 H-406 Low Temperature Shift Reactor R-403 PSA Precooler Deaerator Water Preheater 1 H-407 Pre-PSA Knock-Out 1 S-401
4.32 Low Temperature Shift Precooler Deaerator Water Preheater 2 H-406
Tabel 4.39 Neraca Energi pada Cooler H-406 Komponen Masuk kJ Keluar kJ H 36-out H 37 H 2 94609046,266 94478485,909 CO 2 25004046,685 24447746,373 CO 7134873,850 7094020,674 H 2 O 70173881,636 69557124,145 CH 4 6123067,190 5890141,495 C 2 H 4 45,465 43,459 C 2 H 6 604,849 576,049 C 3 H 8 7683,065 7305,541 C 3 H 6 10151,260 9682,295 C 4 H 10 521,040 496,031 C 4 H 8 485,271 462,433 Jumlah 203064406,578 201486084,405 Q -1578322,173 Total 201486084,405 201486084,405 Universitas Sumatera Utara4.33 Low Temperature Shift Reactor R-403
Tabel 4.40 Neraca energi pada Reaktor LTS R-403 Komponen Masuk kJ Keluar kJ H 37 H 38 H 2 94478485,909 95105806,094 CO 2 24447746,373 27186247,054 CO 7094020,674 7374302,291 H 2 O 69557124,145 73332922,954 CH 4 5890141,495 7195158,066 C 2 H 4 43,459 53,819 C 2 H 6 576,049 728,542 C 3 H 8 7305,541 9260,159 C 3 H 6 9682,295 12120,440 C 4 H 10 496,031 627,381 C 4 H 8 462,433 579,636 Sub total 201486084,405 210217806,436 ∆H r -8731722,032 Q 0,000 Total 201486084,405 201486084,405 Universitas Sumatera Utara4.34 PSA Precooler Deaerator Water Preheater 1 H-407
Tabel 4.41 Neraca Energi pada Cooler H-407 Komponen Masuk kJ Keluar kJ H 38 H 39 H 2 95105806,094 100536430,331 CO 2 27186247,054 32944093,286 CO 7374302,291 779208,985 H 2 O 73332922,954 61557189,420 CH 4 7195158,066 5656114,107 C 2 H 4 53,819 41,366 C 2 H 6 728,542 546,341 C 3 H 8 9260,159 6912,228 C 3 H 6 12120,440 9194,620 C 4 H 10 627,381 470,185 C 4 H 8 579,636 438,547 Jumlah 210217806,436 201490639,415 Q -8727167,021 Total 201490639,415 201490639,415 Universitas Sumatera Utara4.35 Pre-PSA Knock-Out 1 S-401
Tabel 4.42 Neraca Energi pada Knock Out Drum S-401 Komponen Masuk kJ Keluar kJ H 39 H 40 H 41 H 2 100536430,331 307,616 100536122,715 CO 2 32944093,286 10,817 32944082,469 CO 779208,985 2,724 779206,261 H 2 O 61557189,420 19198,826 61537990,594 CH 4 5656114,107 19,425 5656094,681 C 2 H 4 41,366 0,000 41,365 C 2 H 6 546,341 0,005 546,336 C 3 H 8 6912,228 0,163 6912,066 C 3 H 6 9194,620 0,192 9194,429 C 4 H 10 470,185 0,026 470,159 C 4 H 8 438,547 0,021 438,526 Jumlah 201490639,415 19539,814 201471099,601 Sub total 201490639,415 201490639,415 Q 0,000 Total 201490639,415 201490639,415 Universitas Sumatera Utara4.36 Air-Cooler H-408
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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