Compressor K-301A Air-cooler H-302A Knock Out Drum S-302A Compressor K-301B
4.11 Compressor K-301A
Tabel 4.13 Neraca Energi pada Compressor K-301A Komponen Masuk kJ Keluar kJ H 23 H discharge H 2 59282660,879 59658779,307 CO 2 12952,665 14060,377 CO 16978960,485 17113606,843 H 2 O 23938024,781 24441435,330 CH 4 12197533,221 13765150,072 C 2 H 4 339331,026 401493,286 C 2 H 6 76658,161 91496,799 C 3 H 8 56713,341 68689,745 C 3 H 6 76431,175 91130,116 C 4 H 10 2130,943 2550,080 C 4 H 8 1936,062 2327,668 Jumlah 112963332,740 115650719,623 Sub total 112963332,740 115650719,623 Q 2687386,882 Total 115650719,623 115650719,623 Universitas Sumatera Utara4.12 Air-cooler H-302A
Tabel 4.14 Neraca Energi pada Air-Cooler H-302A Komponen Masuk kJ Keluar kJ H input H output H 2 59658779,307 59282660,879 CO 2 14060,377 12952,665 CO 17113606,843 16978960,485 H 2 O 24441435,330 23938024,781 CH 4 13765150,072 12197533,221 C 2 H 4 401493,286 339331,026 C 2 H 6 91496,799 76658,161 C 3 H 8 68689,745 56713,341 C 3 H 6 91130,116 76431,175 C 4 H 10 2550,080 2130,943 C 4 H 8 2327,668 1936,062 Jumlah 115650719,623 112963332,740 Sub total 115650719,623 112963332,740 Q -2687386,882 Total 112963332,740 112963332,740 Universitas Sumatera Utara4.13 Knock Out Drum S-302A
Tabel 4.15 Neraca Energi pada Knock Out Drum S-302A Komponen Masuk kJ Keluar kJ H input H recycle H 24 H top H 2 59282660,879 59261867,490 59272997,039 59271531,329 CO 2 12952,665 12948,665 12950,806 12950,525 CO 16978960,485 16969790,625 16974698,900 16974052,210 H 2 O 23938024,781 5210492,999 18291139,394 10857378,386 CH 4 12197533,221 12189144,032 12193634,556 12193042,697 C 2 H 4 339331,026 338546,760 338966,673 338911,113 C 2 H 6 76658,161 76398,651 76537,624 76519,188 C 3 H 8 56713,341 56045,642 56403,725 56355,258 C 3 H 6 76431,175 75672,898 76079,427 76024,647 C 4 H 10 2130,943 2046,504 2092,016 2085,430 C 4 H 8 1936,062 1872,652 1906,786 1901,928 Jumlah 112963332,740 94194826,919 107297406,948 99860752,711 Sub total 207158159,659 207158159,659 Q 0,000 Total 207158159,659 207158159,659 Universitas Sumatera Utara4.14 Compressor K-301B
Tabel 4.16 Neraca Energi pada Compressor K-301B Komponen Masuk kJ Keluar kJ H suction H discharge H 2 59271531,329 59654121,683 CO 2 12950,525 14080,109 CO 16974052,210 17112803,239 H 2 O 10857378,386 11090985,484 CH 4 12193042,697 13793983,822 C 2 H 4 338911,113 402269,171 C 2 H 6 76519,188 91639,190 C 3 H 8 56355,258 68500,419 C 3 H 6 76024,647 90946,391 C 4 H 10 2085,430 2504,147 C 4 H 8 1901,928 2294,487 Jumlah 99860752,711 102324128,142 Sub total 99860752,711 102324128,142 Q 2463375,430 Total 99860752,711 102324128,142 Universitas Sumatera Utara4.15 Air-cooler H-302B
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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