Air-cooler H-302B Knock Out Drum S-302B Compressor K-301C Air-cooler H-302C
4.15 Air-cooler H-302B
Tabel 4.17 Neraca Energi pada Air-Cooler H-302B Komponen Masuk kJ Keluar kJ H input H output H 2 59654121,683 59271531,329 CO 2 14080,109 12950,525 CO 17112803,239 16974052,210 H 2 O 11090985,484 10857378,386 CH 4 13793983,822 12193042,697 C 2 H 4 402269,171 338911,113 C 2 H 6 91639,190 76519,188 C 3 H 8 68500,419 56355,258 C 3 H 6 90946,391 76024,647 C 4 H 10 2504,147 2085,430 C 4 H 8 2294,487 1901,928 Jumlah 102324128,142 99860752,711 Sub total 102324128,142 99860752,711 Q -2463375,430 Total 102324128,142 99860752,711 Universitas Sumatera Utara4.16 Knock Out Drum S-302B
Tabel 4.18 Neraca Energi pada Knock Out Drum S-302B Komponen Masuk kJ Keluar kJ H input H recycle H 24 H top H 2 59271531,329 59252906,687 59262570,526 59261867,490 CO 2 12950,525 12946,942 12948,801 12948,665 CO 16974052,210 16965839,292 16970100,877 16969790,625 H 2 O 10857378,386 2560286,367 8207171,754 5210492,999 CH 4 12193042,697 12185529,358 12189428,023 12189144,032 C 2 H 4 338911,113 338209,114 338573,466 338546,760 C 2 H 6 76519,188 76286,986 76407,523 76398,651 C 3 H 8 56355,258 55759,570 56069,185 56045,642 C 3 H 6 76024,647 75347,704 75699,452 75672,898 C 4 H 10 2085,430 2010,879 2049,806 2046,504 C 4 H 8 1901,928 1845,793 1875,069 1872,652 Jumlah 99860752,711 91526968,691 97192894,483 94194826,919 Sub total 191387721,402 191387721,402 Q 0,000 Total 191387721,402 191387721,402 Universitas Sumatera Utara4.17 Compressor K-301C
Tabel 4.19 Neraca Energi pada Compressor K-301C Komponen Masuk kJ Keluar kJ H suction H discharge H 2 59261867,490 59647676,776 CO 2 12948,665 14089,194 CO 16969790,625 17110616,981 H 2 O 5210492,999 5323883,763 CH 4 12189144,032 13806687,052 C 2 H 4 338546,760 402477,627 C 2 H 6 76398,651 91650,069 C 3 H 8 56045,642 68246,604 C 3 H 6 75672,898 90676,656 C 4 H 10 2046,504 2461,627 C 4 H 8 1872,652 2263,069 Jumlah 94194826,919 96560729,419 Sub total 94194826,919 96560729,419 Q 2365902,499 Total 96560729,419 96560729,419 Universitas Sumatera Utara4.18 Air-cooler H-302C
Tabel 4.20 Neraca Energi pada Air-Cooler H-302C Komponen Masuk kJ Keluar kJ H input H output H 2 59647676,776 59261867,490 CO 2 14089,194 12948,665 CO 17110616,981 16969790,625 H 2 O 5323883,763 5210492,999 CH 4 13806687,052 12189144,032 C 2 H 4 402477,627 338546,760 C 2 H 6 91650,069 76398,651 C 3 H 8 68246,604 56045,642 C 3 H 6 90676,656 75672,898 C 4 H 10 2461,627 2046,504 C 4 H 8 2263,069 1872,652 Jumlah 96560729,419 94194826,919 Sub total 96560729,419 94194826,919 Q -2365902,499 Total 94194826,919 94194826,919 Universitas Sumatera Utara4.19 Knock Out Drum S-302C
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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