Reformer Syngas CoolerSteam Generator 2 H-402 Reformer Syngas CoolerSteam Superheater 1 H-403 High Temperature Shift Reactor R-402 Low Temperature Shift PrecoolerBoiler Feed Water Preheater1 H-405
4.28 Reformer Syngas CoolerSteam Generator 2 H-402
Tabel 4.35 Neraca Energi pada Cooler H-402 Komponen Masuk kJ Keluar kJ H 34 H 34out H 2 82772431,965 82738670,85 CO 2 18707,357 18699,98 CO 26767705,797 26765308,02 H 2 O 108147321,715 108093543,58 CH 4 9973481,839 9965194,11 C 2 H 4 70,621 70,58 C 2 H 6 999,669 998,92 C 3 H 8 12460,304 12451,81 C 3 H 6 16166,957 16156,19 C 4 H 10 835,741 835,30 C 4 H 8 765,893 765,40 Jumlah 227710947,857 227612694,73 Q -98253,128 Total 227612694,729 227612694,729 Universitas Sumatera Utara4.29 Reformer Syngas CoolerSteam Superheater 1 H-403
Tabel 4.36 Neraca Energi pada Cooler H-403 Komponen Masuk kJ Keluar kJ H 34out H 35 H 2 82738670,850 78597734,849 CO 2 18699,979 16044,969 CO 26765308,024 24386587,558 H 2 O 108093543,582 93043358,749 CH 4 9965194,107 6960349,430 C 2 H 4 70,576 52,104 C 2 H 6 998,921 702,604 C 3 H 8 12451,806 8935,608 C 3 H 6 16156,190 11713,791 C 4 H 10 835,295 605,290 C 4 H 8 765,400 560,362 Jumlah 227612694,729 203026645,314 Q -24586049,415 Total 203026645,314 203026645,314 Universitas Sumatera Utara4.30 High Temperature Shift Reactor R-402
Tabel 4.37 Neraca energi pada Reaktor HTS R-402 Komponen Masuk kJ Keluar kJ H 35 H 36 H 2 78597734,849 97489992,041 CO 2 16044,969 30216139,622 CO 24386587,558 7913165,452 H 2 O 93043358,749 81023180,317 CH 4 6960349,430 9257157,593 C 2 H 4 52,104 66,733 C 2 H 6 702,604 934,462 C 3 H 8 8935,608 11717,691 C 3 H 6 11713,791 15224,275 C 4 H 10 605,290 792,453 C 4 H 8 560,362 723,048 Jumlah 203026645,314 225929093,688 Sub total 203026645,314 225929093,688 ∆H r -22902448,374 Q 0,000 Total 203026645,314 203026645,314 Universitas Sumatera Utara4.31 Low Temperature Shift PrecoolerBoiler Feed Water Preheater1 H-405
Tabel 4.38 Neraca Energi pada Cooler H-405 Komponen Masuk kJ Keluar kJ H 36 H 36-out H 2 97489992,041 94609046,266 CO 2 30216139,622 25004046,685 CO 7913165,452 7134873,850 H 2 O 81023180,317 70173881,636 CH 4 9257157,593 6123067,190 C 2 H 4 66,733 45,465 C 2 H 6 934,462 604,849 C 3 H 8 11717,691 7683,065 C 3 H 6 15224,275 10151,260 C 4 H 10 792,453 521,040 C 4 H 8 723,048 485,271 Jumlah 225929093,688 203064406,578 Q -22864687,110 Total 203064406,578 203064406,578 Universitas Sumatera Utara4.32 Low Temperature Shift Precooler Deaerator Water Preheater 2 H-406
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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