PSA PrecoolerDeaerator Water Preheater 1 H-407 Pre-PSA Knock-Out 1 S-401 Air-Cooler H-408
5.49 PSA PrecoolerDeaerator Water Preheater 1 H-407
Fungsi : Mendinginkan aliran keluar dari R-403 sampai dengan 167,778 o C Jenis : 1 - 2 Shell and Tube Heat Exchanger Jumlah : 1 unit Shell : Diameter dalam ID : 17,250 in = 0,438 m Baffle space B : 12,075 in = 0,307 m 0,7 × 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 : 7,80 ft = 2,377 m Fluida panas : Gas sintesis Laju alir fluida masuk W : 75.515,266 kgjam = 166.482,466 lb m jam Temperatur masuk T 1 : 383,799 o C = 723 o F Temperatur keluar T 2 : 167,778 o C = 334 o F Fluida dingin : Air Laju alir fluida masuk w : 168.888,289 kgjam = 372.334,500 lb m jam Temperatur masuk t 1 : 38,333 C = 101 o F Temperatur keluar t 2 : 125,117 C = 257 o F Panas yang diserap Q : 8.727.167 kJmol.jam = 8.271.758,14 Btujam R D yang diijinkan : 0,002 LMTD : 335,999 o F Luas permukaan A : 273,531 ft 2 Jumlah tube standard N ts : 178 buah Design overall coefficient U D : 100 btujam.ft. °F Universitas Sumatera Utara5.50 Pre-PSA Knock-Out 1 S-401
Fungsi : Memisahkan fase liquid di dalam fase gas Desain : Bejana tangki vertikal dengan tutup dan alas berbentuk segmen elips torispherical head Bahan konstruksi : Carbon Steel Jumlah : 1 unit Kondisi operasi: Tekanan : P = 2344,209 kPa Temperatur : T = 440,928 K Laju alir massa : F = 75515,26599 kgjam Laju alir volume : Q = 191650,3722 m 3 jam = 1880,019 ft 3 s Densitas gas umpan : ρ G = 0,394 kgm 3 Densitas liquid umpan : ρ L = 980,427 kgm 3 Dimensi Knock-out Drum Cross sectional area : A = 107,705138 ft 2 Tinggi : L = 23,42088 ft = 7,1386 m Diameter : D = 11,71044 ft = 3,569342 m Tebal : ts = 0,3774 inch = 9,5849 mm Desain tutup kepala atas dan bawah Tebal : t H = 1,6673 inch = 42,348 mm Tinggi : H = 36,63132 inch = 930,4356 mm5.51 Air-Cooler H-408
Fungsi : Sebagai pendingin gas dari Knockout Drum S-401 Desain : Forced draft, 2 fan Bahan konstruksi : Carbon Steel Jumlah : 1 unit Spesifikasi Type : Forced draft, 2 fan Fin tube : 1 in. OD dengan 58 in. High Fin Universitas Sumatera Utara Tube pitch : 2 14 in. Triangular ∆ Bundle Layout : 3 tube passes, 3 rows of tubes Panjang pipa : 30 ft luas permukaan : A x = 12157,938 ft 2 Lebar : l = 2,071 ft Jumlah pipa : N t = 73 Pressure Drop sisi-pipa : ∆P t = 3,882 psi Koefisien perpindahan keseluruhan : U x = 5,41 Diameter fan : D = 6,205 ft = 1,891 m Pressure drop statis udara : ∆P a = 0,120 inch air Effisiensi fan : η fan = 70 Brake Horse Power per fan : bhp = 1,013 hp = 0,755 kW Effisiensi motor : η motor = 925.52 Aftercooler H-409
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