Hydrogen Compressor 1st Interstage Knock Out S-502 Compressor Hydrogen 2st Interstage K-501B Hydrogen Compressor Air-cooler Aftercooler H-501B
5.58 Hydrogen Compressor 1st Interstage Knock Out S-502
Fungsi : Memisahkan fase liquid di dalam fase gas sebelum gas dikompres. Desain : Bejana tangki vertikal dengan tutup dan alas berbentuk segmen elips torispherical head Bahan konstruksi : Carbon Steel Type SA 515 Gr. 60 Jumlah : 1 unit Kondisi operasi: Tekanan : P = 4177,389 kPa Temperatur : T = 333,15 K Laju alir massa : F = 5804,498 kgjam Laju alir volume : Q = 1949,381 m 3 jam = 19,123 ft 3 s Densitas gas umpan : ρ G = 2,978 kgm 3 Densitas liquid umpan : ρ L = 31,25 kgm 3 Dimensi Knock-out Drum Cross sectional area : A = 17,731 ft 2 Tinggi : L = 9,503 ft = 2,896 m Diameter : D = 4,751 ft = 1,448 m Tebal : ts = 2,119 inch = 53,814 mm Desain tutup kepala atas dan bawah Tebal : t H = 2,259 inch = 57,366 mm Tinggi : H = 15,754 inch = 400,157 mm5.59 Compressor Hydrogen 2st Interstage K-501B
Fungsi : Menaikkan tekanan gas sintesis Desain : Reciprocating compressor Bahan konstruksi : Carbon Steel SA 285 C Jumlah : 1 unit Spesifikasi Diameter silinder : D = 6 in Stroke : S t = 12 in Universitas Sumatera Utara Speed : N = 300 rpm Diameter tangkai piston : d = 2,5 in Clearance : c = 12 Komponen Gas : H 2 H 2 O Tekanan suction : P 1 = 4177,389 kPa = 605,879 psia Tekanan discharge : P 2 = 7030,560 kPa = 1019,696 psia Temperatur suction : T 1 = 60 o C = 333,15 o K Piston displacement : Pd = 113,719 cfm Temperatur discharge : T 2 = 618,413 o R = 158,413 o F Theoritical volumetric efficiency : E vt = 87,65 Kapasitas pada suction dalam silinder : Q 1 = 99,697 cfm Speed dari piston : PS = 600 fpm feet per minute Effisiensi kompressor : η = 75 Power yang dibutuhkan : W = 113,227 hp = 84,433 kW5.60 Hydrogen Compressor Air-cooler Aftercooler H-501B
Fungsi : Sebagai pendingin gas dari discharge Compressor K-501B Desain : Forced draft, 2 fan Bahan konstruksi : Carbon Steel A-214 Jumlah : 1 unit Spesifikasi Type : Forced draft, 2 fan Fin tube : 1 in. OD dengan 58 in. High Fin Tube pitch : 2 14 in. Triangular ∆ Bundle Layout : 3 tube passes, 6 rows of tubes Panjang pipa : 15 ft luas permukaan : A x = 219,590 ft 2 Lebar : l = 0,091 ft Jumlah pipa : N t = 3 Pressure Drop sisi-pipa : ∆P t = 4,467 psi Koefisien perpindahan keseluruhan : U x = 7, 46 Universitas Sumatera Utara Diameter fan : D = 0,590 ft = 0,180 m Pressure drop statis udara : ∆P a = 0,167 inch air Effisiensi fan : η fan = 70 Brake Horse Power per fan : bhp = 0,063 hp = 0,047 kW Effisiensi motor : η motor = 925.61 Hydrogen Compressor Water-Cooler Aftercooler H-502
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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