Gasifier Cyclone S-201 Cyclone S-202 Char Combustor R-202
BAB IV NERACA ENERGI
Kapasitas : 46000 tontahun Basis perhitungan : 1 jam operasi Temperatur basis : 25 o C4.1 Gasifier
Tabel 4.1 Neraca Energi pada Gasifier R-201 Komponen Masuk kJ Keluar kJ H 2 H 3 H 9 H 4 H 2 52730136,976 CO 2 18808011,492 CO 15243410,871 H 2 O -133751326,734 434973065,879 93209134,630 CH 4 31552002,057 C 2 H 4 1435484,640 C 2 H 6 1760585,872 C 3 H 8 324814,132 C 3 H 6 419066,672 C 4 H 10 15793,139 C 4 H 8 14182,624 Olivine 2262288885,180 2241473616,011 Char 24598081,880 CKS -81926303,331 Jumlah -215677630,065 434973065,879 2262288885,180 2481584320,995 Sub total 2481584320,995 2481584320,995 Q 0,000 Total 2481584320,995 2481584320,995 Universitas Sumatera Utara4.2 Cyclone S-201
Tabel 4.2 Neraca Panas pada Cyclone S-201 Komponen Masuk kJ Keluar kJ H 4 H 5 H 13 H 2 52730136,976 52730136,976 CO 2 18808011,492 18808011,492 CO 15243410,871 15243410,871 H 2 O 93209134,630 93209134,630 CH 4 31552002,057 31552002,057 C 2 H 4 1435484,640 1435484,640 C 2 H 6 1760585,872 1760585,872 C 3 H 8 324814,132 324814,132 C 3 H 6 419066,672 419066,672 C 4 H 10 15793,139 15793,139 C 4 H 8 14182,624 14182,624 Olivine 2241473616,011 2223800387,823 17673228,188 Char 24598081,880 24573483,798 24598,082 Jumlah 2481584320,995 2248373871,621 233210449,374 Sub total 2481584320,995 2481584320,995 Panas reaksi Q 0,000 Total 2481584320,995 2481584320,995 Universitas Sumatera Utara4.3 Cyclone S-202
Tabel 4.3 Neraca Panas pada Cyclone S-202 Komponen Masuk kJ Keluar kJ H 13 H 14 H 15 H 2 52730136,976 52730136,976 CO 2 18808011,492 18808011,492 CO 15243410,871 15243410,871 H 2 O 93209134,630 93209134,630 CH 4 31552002,057 31552002,057 C 2 H 4 1435484,640 1435484,640 C 2 H 6 1760585,872 1760585,872 C 3 H 8 324814,132 324814,132 C 3 H 6 419066,672 419066,672 C 4 H 10 15793,139 15793,139 C 4 H 8 14182,624 14182,624 Olivine 17673228,188 35126,471 17638101,717 Char 24598,082 24156,776 441,306 Jumlah 233210449,374 59283,247 233151166,127 Sub total 233210449,374 233210449,374 Panas reaksi Q 0,000 Total 233210449,374 233210449,374 Universitas Sumatera Utara4.4 Char Combustor R-202
Tabel 4.4 Neraca Energi pada Char Combustor R-202 Komponen Masuk kJ Keluar kJ H 514 H 1112 H 7 H 8 N 2 2708308819,628 3082522581,835 O 2 2193052848,591 2470955892,354 SO 2 650904,888 CO 2 114069676,216 H 2 O 710552,738 Abu 1861095,586 Olivine 2223835514,294 2551091,115 2264777402,954 Char 24597640,574 MgO 6301,421 8925,995 Jumlah 2248433154,868 2557392,537 4901361668,219 7935557032,564 Sub total 7152352215,623 7935557032,564 ∆H R -783204816,941 Q Total 7152352215,623 7152352215,623 Universitas Sumatera Utara4.5 Cyclone S-203
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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