Steam Reformer R-401 Flue Gas Reformer Feed Preheater H-401 Flue Gas CoolerSteam Superheater H-404
5.39 Pompa P-302
Fungsi : Memompa air bercampur sludge dari Quench chamber M-301 untuk dikirim menuju pengolahan limbah Jenis : Centrifugal pump Jumlah : 1 unit Bahan konstruksi : Commercial steel Daya motor : 2 hp Head : 16,8020 m Debit : 17,225 m 3 Motor : 220 V AC, 3 fase, 32 Hz5.40 Steam Reformer R-401
Fungsi : Temapat bereaksi antara gas alam dan steam Jenis : Plug flow reactor Bentuk : Tungku pipa Bahan konstruksi : Refractory dengan tube terbuat dari bahan chrome-nickel 25 Cr, 20 Ni, 0,35 – 0,45 C grade HK-40 Jumlah : 1 unit Kondisi operasi : Temperatur masuk : 520 °C Temperatur keluar : 850 °C Universitas Sumatera Utara Tekanan : 30 bar Spesifikasi : Diameter dalam tube : 0,335 ft Panjang tube : 98,42 ft Luas permukaan : 103,735 ft 2 Jumlah tube yang direncanakan : 49 Luas permukaan ekivalen cold plane : 2,222 ft 2 Mean bean length : 3,06 ft Jumlah katalis yang diperlukan : 4.699,516 kg Universitas Sumatera Utara5.41 Flue Gas Reformer Feed Preheater H-401
Fungsi : Memanaskan gas sintesis sebelum masuk kedalam steam reformer sampai suhu 520 o C Jenis : 1 - 2 Shell and Tube Heat Exchanger Jumlah : 1 unit Shell : Diameter dalam ID : 19,250 in = 0,489 m Baffle space B : 11,550 in = 0,293 m 0,6 × ID Passes n : 1 Tube : Diameter dalam ID : 0,652 in = 16,561 mm Diameter luar OD : ¾ in = 19,050 mm BWG : 18 Pitch triangular : 1516 in Passes : 2 Panjang : 4,90 ft = 1,494 m Fluida panas : Flue gas Laju alir fluida masuk W : 72.168,980 kgjam = 159.105,177 lb m jam Temperatur masuk T 1 : 850 o C = 1562 o F Temperatur keluar T 2 : 704,444 o C = 1300 o F Fluida dingin : Gas sintesis Laju alir fluida masuk w : 75.515,303 kgjam = 166.482,546 lb m jam Temperatur masuk t 1 : 227,224 C = 441 o F Temperatur keluar t 2 : 520 C = 968 o F Panas yang diserap Q : 16.049.373,73 kJjam = 15.211.870,869 Btujam R D yang diijinkan : 0,002 LMTD : 718,370 o F Luas permukaan A : 246,795 ft 2 Jumlah tube standard N ts : 234 buah Universitas Sumatera Utara Design overall coefficient U D : 90 btujam.ft. °F5.42 Flue Gas CoolerSteam Superheater H-404
Fungsi : Menghasilkan steam superheated Jenis : 2 - 4 Shell and Tube Heat Exchanger Jumlah : 1 unit Shell : Diameter dalam ID : 23,250 in = 0,591 m Baffle space B : 16,275 in = 0,413 m 0,5 × ID Passes n : 2 Tube : Diameter dalam ID : 0,652 in = 16,561 mm Diameter luar OD : ¾ in = 19,050 mm BWG : 18 Pitch triangular : 1516 in Passes : 4 Panjang : 8,80 ft = 2,682 m Fluida panas : Flue gas Laju alir fluida masuk W : 72.168,980 kgjam = 159.105,177 lb m jam Temperatur masuk T 1 : 704,444 o C = 1300 o F Temperatur keluar T 2 : 336,111 o C = 637 o F Fluida dingin : Saturated Steam Laju alir fluida masuk w : 31.756,146 kgjam = 70.010,235 lb m jam Temperatur masuk t 1 : 301,911 C = 575 o F Temperatur keluar t 2 : 537,778 C = 1000 o F Panas yang diserap Q : 15.575.762,2 kJjam = 14.762.973,772 Btujam R D yang diijinkan : 0,002 LMTD : 150,553 o F Universitas Sumatera Utara Luas permukaan A : 655,691 ft 2 Jumlah tube standard N ts : 364 buah Design overall coefficient U D : 150 btujam.ft. °F Universitas Sumatera Utara5.43 Reformer Syngas CoolerSteam Generator 2 H-402
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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