Conveyor Tabel Neraca Massa pada Conveyer C-101 Reaktor Gasifier R-201 Reaktor Char combustor R-202 Cyclone S-202
BAB III NERACA MASSA
3.1 Conveyor Tabel 3.1 Neraca Massa pada Conveyer C-101 Komponen Masuk kgjam Keluar kgjam Aliran 1 Aliran 2 H 2 O 9960 9960 Cangkang Kelapa Sawit CKS 73040 73040 Subtotal 83000 83000 Total 83000 830003.2 Reaktor Gasifier R-201
Tabel 3.2 Neraca Massa pada Gasifier R-201 Komponen Masuk kg Keluar kg Aliran 2 Aliran 3 Aliran 9 Aliran 4 H 2 3415,854 CO 2 14738,067 CO 12696,231 H 2 O 9960 29216 39176,000 CH 4 6524,665 C 2 H 4 402,994 C 2 H 6 402,994 C 3 H 8 76,761 C 3 H 6 115,141 C 4 H 10 3,838 C 4 H 8 3,838 Olivine 0,000 Char 1972080 1972080,000 CKS 34338,626 Subtotal 83000 29216 1972080 2084296 Total Aliran 2084296 2084296 Universitas Sumatera Utara3.3 Reaktor Char combustor R-202
Tabel 3.3 Neraca Massa pada Char Combustor R-202 Komponen Masuk kg Keluar kg Aliran 7 Aliran 12 Aliran 14a Aliran 8 H 2 O 289,762 N 2 204389,692 204389,692 O 2 62058,714 6649,148 CO 2 87099,191 SO 2 744,162 Olivine 2169,288 1972080,000 1974249,288 MgO 6,844 Abu 1618,486 Char 34338,626 3,434 Subtotal aliran 266448,406 2176,132 2006418,626 2275043,163 Total 2275043,16 2275043,16 3.4 Cyclone S-201 Tabel 3.4 Neraca Massa pada Cyclone S-201 Komponen Masuk kg Keluar kg Aliran 4 Aliran 5 Aliran 13 H 2 3415,854 3415,854 CO 2 14738,067 14738,067 CO 12696,231 12696,231 H 2 O 39176,000 39176,000 CH 4 6524,665 6524,665 C 2 H 4 402,994 402,994 C 2 H 6 402,994 402,994 C 3 H 8 76,761 76,761 C 3 H 6 115,141 115,141 C 4 H 10 3,838 3,838 C 4 H 8 3,838 3,838 Olivine 1972080,000 1970107,920 1972,080 Char 34338,626 34304,287 34,339 Subtotal aliran 2083975,009 2004412,207 79562,802 Total aliran 2083975,009 2083975,009 Universitas Sumatera Utara3.5 Cyclone S-202
Tabel 3.5 Neraca Massa pada Cyclone S-202 Komponen Masuk kg Keluar kg Aliran 13 Aliran 14 Aliran 15 H 2 3415,854 3415,854 CO 2 14738,067 14738,067 CO 12696,231 12696,231 H 2 O 39176,000 39176,000 CH 4 6524,665 6524,665 C 2 H 4 402,994 402,994 C 2 H 6 402,994 402,994 C 3 H 8 76,761 76,761 C 3 H 6 115,141 115,141 C 4 H 10 3,838 3,838 C 4 H 8 3,838 3,838 Olivine 1972,080 1774,872 197,208 Char 34,339 30,905 3,434 Subtotal aliran 79562,802 1805,777 77757,026 Total aliran 79562,802 79562,802 3.6 Cyclone S-203 Tabel 3.6 Neraca Massa pada Cyclone S-202 Komponen Masuk kg Keluar kg Aliran 8 Aliran 9 Aliran 10 H 2 O 289,762 289,762 N 2 204389,692 204389,692 O 2 6649,148 6649,148 CO 2 87099,191 87099,191 SO 2 744,162 744,162 Olivine 1974249,288 1972275,039 1974,249 MgO 0,000 0,000 Abu 1618,486 1618,486 Char 3,434 3,434 Subtotal aliran 2275043,163 1972275,039 302768,124 Total aliran 2275043,163 2275043,163 Universitas Sumatera Utara3.7 Reformer R-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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