Reformer R-203 NERACA MASSA
3.7 Reformer R-203
Tabel 3.7 Neraca Massa pada Reformer R-203 Komponen Masuk kg Keluar kg aliran 15 aliran 16 aliran 17 aliran 18 H 2 3415,854 4123,510 CO 2 14738,067 14738,067 CO 12696,231 16289,010 H 2 O 39176,000 36865,318 CH 4 6524,665 5219,732 C 2 H 4 402,994 201,497 C 2 H 6 402,994 40,299 C 3 H 8 76,761 30,704 C 3 H 6 115,141 46,056 C 4 H 10 3,838 1,151 C 4 H 8 3,838 1,151 Olivine 197,208 19,199 19,199 197,208 Char 3,434 3,434 Subtotal aliran 77757,026 19,199 19,199 77757,026 Total aliran 77776,225 77776,225 3.8 Scrubber M-301 Tabel 3.8 Neraca Massa pada Scrubber M-301 Komponen Masuk kg Keluar kg Aliran 19 Aliran 20 Aliran 21 Aliran 29 H 2 4123,510 4123,505 0,005 CO 2 14738,067 14,738 14723,329 CO 16289,010 16279,709 9,300 H 2 O 36865,318 16589,137 19821,934 454,248 CH 4 5219,732 0,006 5214,169 5,558 C 2 H 4 201,497 0,001 200,985 0,511 C 2 H 6 40,299 0,000 40,171 0,128 C 3 H 8 30,704 30,704 0,000 C 3 H 6 46,056 46,056 0,000 C 4 H 10 1,151 1,151 0,000 C 4 H 8 1,151 1,151 0,000 Olivine 197,208 197,208 Char 3,434 3,434 Subtotal 77757,140 16589,144 45774,274 15393,722 Universitas Sumatera Utara Total 77757,140 77757,140 3.9 Kompresi gas sintesis Tabel 3.9 Neraca massa untuk Knock Out Drum S-301 Komponen Masuk kg Keluar kg Aliran 21 Aliran 22 Aliran 23 H 2 4124,960 1,335 4123,624 CO 2 14,743 0,004 14,738 CO 16288,549 8,116 16280,433 H 2 O 26770,432 14057,552 12712,880 CH 4 5217,773 3,310 5214,463 C 2 H 4 201,450 0,428 201,022 C 2 H 6 40,306 0,125 40,181 C 3 H 8 31,056 0,328 30,728 C 3 H 6 46,503 0,416 46,087 C 4 H 10 1,193 0,040 1,153 C 4 H 8 1,186 0,033 1,153 Subtotal 52738,150 14071,688 38666,462 Total 52738,150 52738,150 Tabel 3.10 Neraca massa untuk Knock Out Drum S-302A Komponen Masuk kg Keluar kg Top S-301 Aliran 24 Top S-302A H 2 4124,933 2,083 4122,850 CO 2 14,743 0,007 14,736 CO 16288,383 12,656 16275,727 H 2 O 15711,611 9945,532 5766,079 CH 4 5217,704 5,161 5212,543 C 2 H 4 201,440 0,666 200,773 C 2 H 6 40,303 0,195 40,108 C 3 H 8 31,043 0,509 30,534 C 3 H 6 46,488 0,646 45,842 C 4 H 10 1,189 0,061 1,128 C 4 H 8 1,184 0,051 1,132 Subtotal 41679,019 9967,566 31711,453 Total 41679,019 41679,019 Universitas Sumatera Utara Universitas Sumatera Utara Tabel 3.11 Neraca massa untuk Knock Out Drum S-302B Komponen Masuk kg Keluar kg Top S-302A Bottom S-302B Top S-302B H 2 4124,100 1,923 4122,178 CO 2 14,740 0,006 14,734 CO 16283,323 11,682 16271,640 H 2 O 7173,947 4406,786 2767,161 CH 4 5215,640 4,763 5210,877 C 2 H 4 201,172 0,614 200,557 C 2 H 6 40,225 0,179 40,045 C 3 H 8 30,833 0,467 30,366 C 3 H 6 46,223 0,593 45,630 C 4 H 10 1,163 0,056 1,107 C 4 H 8 1,162 0,047 1,115 Subtotal 33132,527 4427,117 28705,410 Total 33132,527 33132,527 Tabel 3.12 Neraca massa untuk Knock Out Drum S-302C Komponen Masuk kg Keluar kg Top S-302B Bottom S-302C Top S-302C H 2 4123,415 1,860 4121,554 CO 2 14,738 0,006 14,732 CO 16279,154 11,302 16267,852 H 2 O 3455,091 2095,387 1359,703 CH 4 5213,939 4,608 5209,331 C 2 H 4 200,951 0,594 200,357 C 2 H 6 40,160 0,173 39,987 C 3 H 8 30,661 0,450 30,211 C 3 H 6 46,005 0,572 45,434 C 4 H 10 1,141 0,053 1,088 C 4 H 8 1,143 0,044 1,099 Subtotal 29406,398 2115,050 27291,348 Total 29406,398 29406,398 Universitas Sumatera Utara Tabel 3.13 Neraca massa untuk Knock Out Drum S-302D Komponen Masuk kg Keluar kg Top S-302C Bottom S-302D Aliran 25 H 2 4123,556 2,184 4121,372 CO 2 14,742 0,007 14,735 CO 16280,831 13,269 16267,562 H 2 O 1887,412 1215,549 671,863 CH 4 5214,933 5,410 5209,523 C 2 H 4 201,145 0,698 200,447 C 2 H 6 40,222 0,204 40,018 C 3 H 8 30,859 0,530 30,328 C 3 H 6 46,253 0,673 45,580 C 4 H 10 1,164 0,063 1,101 C 4 H 8 1,164 0,053 1,111 Subtotal 27842,281 1238,639 26603,642 Total 27842,281 27842,281 Tabel 3.14 Neraca massa untuk Knock Out Drum S-303 Komponen Masuk kg Keluar kg Aliran 26 Aliran 27 Aliran 28 H 2 4121,372 4119,368 2,004 CO 2 14,735 14,725 0,010 CO 16267,562 16254,565 12,998 H 2 O 671,863 143,682 528,181 CH 4 5209,523 5203,912 5,611 C 2 H 4 200,447 199,657 0,790 C 2 H 6 40,018 39,782 0,237 C 3 H 8 30,328 29,671 0,658 C 3 H 6 45,580 44,750 0,830 C 4 H 10 1,101 1,021 0,080 C 4 H 8 1,111 1,044 0,067 Subtotal 26603,642 26052,177 551,465 Total 26603,642 26603,642 Universitas Sumatera Utara3.10 Steam Reformer R-401
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
Show more