Scrubber Gas Sintesis M-301 M-302 Quench Water Recirculation Cooler Knock Out Drum S-301
4.8 Scrubber Gas Sintesis M-301 M-302
Tabel 4.9 Neraca Energi Pada Venturi Scrubber M-302 Komponen Masuk kJ Keluar kJ H 19 H scrub-02 H 19out H 2 59668504,696 59281021,484 CO 2 14098440,864 12952334,665 CO 17129886,387 16987905,116 H 2 O 70935181,172 151422,219 74198111,343 CH 4 13838268,434 -0,082 12209865,159 C 2 H 4 404667,731 -0,007 340133,781 C 2 H 6 92305,982 0,001 76884,153 C 3 H 8 69066,029 56670,432 C 3 H 6 91596,492 76380,327 C 4 H 10 2562,517 2128,652 C 4 H 8 2338,881 1933,808 Olivine 26966,648 25015,091 Char 66,733 46,423 Jumlah 176359852,564 151422,130 176208430,434 Sub total 176359852,564 176359852,564 Q 0,000 Total 176359852,564 176359852,564 Universitas Sumatera Utara Tabel 4.10 Neraca Energi pada Quench Chamber M-301 Komponen Masuk kJ Keluar kJ H 19out H scrub01 H 20 H 21 H 29 H 2 59281021,48 59280942,88 78,603 CO 2 12952334,66 12952,335 12939382,33 CO 16987905,12 16978205,794 9699,322 H 2 O 74198111,34 151422,22 341998,35 37324190,19 36683345,02 CH 4 12209865,16 -0,082 -0,201 12196844,87 13020,401 C 2 H 4 340133,781 -0,007 -0,017 339268,809 864,981 C 2 H 6 76884,153 0,001 0,002 76638,034 246,117 C 3 H 8 56670,432 56670,357 0,075 C 3 H 6 76380,327 76380,226 0,101 C 4 H 10 2128,652 2128,649 0,003 C 4 H 8 1933,808 1933,806 0,003 Olivine 25015,091 25015,091 Char 46,423 46,423 Jumlah 176208430,43 151422,13 341998,14 126346155,96 49671698,46 Sub total 176359852,564 176359852,564 Q 0,000 Total 176359852,564 176359852,564 Universitas Sumatera Utara4.9 Quench Water Recirculation Cooler
Tabel 4.11 Neraca Energi pada Cooler H-301 Komponen Masuk kJ Keluar kJ H 20 H scrub H 2 O 341998,353 302844,437 CH 4 -0,201 -0,164 C 2 H 4 -0,017 -0,014 C 2 H 6 0,002 0,002 Sub total 341998,137 302844,260 Q -39153,877 Total 302844,260 302844,260 Universitas Sumatera Utara4.10 Knock Out Drum S-301
Tabel 4.12 Neraca Energi pada Knock Out Drum S-301 Komponen Masuk kJ Keluar kJ H 21 H 24 H 22 H 23 H 2 59280942,882 59271531,329 59269813,332 59282660,879 CO 2 12952,335 12950,525 12950,194 12952,665 CO 16978205,794 16974052,210 16973297,519 16978960,485 H 2 O 37324190,192 10857378,386 24243543,797 23938024,781 CH 4 12196844,877 12193042,697 12192354,353 12197533,221 C 2 H 4 339268,809 338911,113 338848,896 339331,026 C 2 H 6 76638,034 76519,188 76499,061 76658,161 C 3 H 8 56670,357 56355,258 56312,274 56713,341 C 3 H 6 76380,226 76024,647 75973,697 76431,175 C 4 H 10 2128,649 2085,430 2083,136 2130,943 C 4 H 8 1933,806 1901,928 1899,671 1936,062 Jumlah 126346155,961 99860752,711 113243575,932 112963332,740 Sub total 226206908,672 226206908,672 Q 0,000 Total 226206908,672 226206908,672 Universitas Sumatera Utara4.11 Compressor K-301A
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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