Cyclone S-203 Reformer R-203 Cooler H-201 H-202
4.5 Cyclone S-203
Tabel 4.5 Neraca Panas pada Cyclone S-203 Komponen Masuk kJ Keluar kJ H 8 H 9 H 10 N 2 3082522581,835 3082522581,835 O 2 2470955892,354 2470955892,354 SO 2 650904,888 650904,888 CO 2 114069676,216 114069676,216 H 2 O 710552,738 710552,738 Abu 1861095,586 1861095,586 Olivine 2264777402,954 2262288885,180 2488517,774 Char 0,000 0,000 MgO 8925,995 8925,995 Jumlah 7935557032,564 2262288885,180 5673268147,384 Sub total 7935557032,564 7935557032,564 Q 0,000 Total 7935557032,564 7935557032,564 Universitas Sumatera Utara4.6 Reformer R-203
Tabel 4.6 Neraca Panas pada Reformer R-203 Komponen Masuk kJ Keluar kJ H 15 H 16 H 17 H 18 H 2 52730136,976 62114308,680 CO 2 18808011,492 18307363,874 CO 15243410,871 19365017,021 H 2 O 93209134,630 84749697,745 CH 4 31552002,057 23757836,942 C 2 H 4 1435484,640 685523,793 C 2 H 6 1760585,872 166695,166 C 3 H 8 324814,132 123618,603 C 3 H 6 419066,672 159668,817 C 4 H 10 15793,139 4545,779 C 4 H 8 14182,624 4060,575 Olivine 17638101,717 14845,011 21272,483 34935,040 Char 441,306 378,925 Jumlah 233151166,127 14845,011 21272,483 209473650,961 Sub total 233166011,138 209494923,444 ∆H R 23671087,694 Panas reaksi Q 0,000 Total 233166011,138 233166011,138 Universitas Sumatera Utara4.7 Cooler H-201 H-202
Tabel 4.7 Neraca Energi pada Cooler H-201 Komponen Masuk kJ Keluar kJ H 18 H 18-out H 2 62114308,680 60008563,797 CO 2 18307363,874 15434136,476 CO 19365017,021 17515892,368 H 2 O 84749697,745 73450441,616 CH 4 23757836,942 16153936,471 C 2 H 4 685523,793 485390,424 C 2 H 6 166695,166 112323,200 C 3 H 8 123618,603 84635,338 C 3 H 6 159668,817 110826,156 C 4 H 10 4545,779 3123,400 C 4 H 8 4060,575 2841,181 Olivine 34935,040 29149,109 Char 378,925 247,491 Sub total 209473650,961 183391507,028 Q -26082143,932 Total 183391507,028 183391507,028 Universitas Sumatera Utara Tabel 4.8 Neraca Energi pada Cooler H-202 Komponen Masuk kJ Keluar kJ H 18-out H 19 H 2 60008563,797 59668504,696 CO 2 15434136,476 14098440,864 CO 17515892,368 17129886,387 H 2 O 73450441,616 70935181,172 CH 4 16153936,471 13838268,434 C 2 H 4 485390,424 404667,731 C 2 H 6 112323,200 92305,982 C 3 H 8 84635,338 69066,029 C 3 H 6 110826,156 91596,492 C 4 H 10 3123,400 2562,517 C 4 H 8 2841,181 2338,881 Olivine 29149,109 26966,648 Char 247,491 66,733 Sub total 183391507,028 176359852,564 Q -7031654,464 Total 176359852,564 176359852,564 Universitas Sumatera Utara4.8 Scrubber Gas Sintesis M-301 M-302
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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