Blower K-201 Reformer R-203 Cooler H-201
5.14 Blower K-201
Fungsi : Memompa udara menuju pembakar Char Combustor R-202 Bahan konstruksi : Carbon steel Bentuk : Fan Sentrifugal Jumlah : 2 unit Kondisi Operasi Tekanan udara masuk : P 1 = 1 atm = 1,013 bar Suhu masuk : T 1 = 32,222 o C = 305,372 K Tekanan udara keluar : P 2 = 1,497 atm = 1,517 bar Jumlah kmol udara : N = 5587,550 kmol = 5587550,343 mol laju alir volume masuk : Q 1 = 114804,322 m 3 jam Spesifikasi Efisiensi blower : ηp = 0,780 Polytropic head : Hp = 34,622 kN mkg Jumlah stage : n = 1 stages kecepatan putaran blower : v = 1690,063 revmin shaft power : SP = 2005,424 kW Suhu keluar blower aktual : T 2 = 94,331 o C Laju alir volumetrik keluar blower : Q 2 = 111419,283 m 3 jam5.15 Reformer R-203
Fungsi : Membakar char arang CKS hasil dari gasifikasi pada gasifier R-201 Bahan konstruksi : Carbon steel Bentuk : Bubbling Fliudized Bed Reactor Jumlah : 1 unit Kondisi operasi Universitas Sumatera Utara Tekanan : P = 1,497 atm Temperatur : T = 870 o C Densitas gas : ρ g = 0,243 kgm 3 Densitas olivine : ρ olivine = 45,360 kgm 3 Percepatan gravitasi : g = 9,8 ms 2 Diameter partikel olivine : dp olivine = 0,2 mm = 0,0002 m Viskositas gas : μ g = 9,979 × 10 -7 Nsm 2 Pa-s Massa gas : m g = 77556,384 kgjam Massa olivine : m olivine = 197,208 kgjam Spesifikasi Operating gas velocity : Uf = 0,259 ms tinggi bed pada Umf : Lmf = 0,113 m tinggi bed pada Umf : Lmf = 16,952 m Tinggi reformer : Ht = 12 m Tinggi bed yang terekspansi gas : He = 0,183 m Kecepatan gas melalui orifice : Uor = 4,978 ms Jumlah tuyere per area distributor : Nor = 100 tuyerem 2 Diameter orifice pada inlet gas tuyere : dor = 25,771 mm Jumlah lubang per tuyere : Nh = 6 Diameter lubang tuyere : dh = 10,521 mm Jumlah tuyere total : n tuyere = 707 tuyeres Jumlah lubang total : n hole = 4243 holes waktu reaksi : t rx = 54,110 s waktu tinggal reaktan gas : t r = 0,957 s5.16 Cooler H-201
Fungsi : Mendinginkan aliran keluar dari Reformer R-203 sampai dengan 301 o C Bahan konstruksi : Carbon steel Bentuk : 1 – 2 BEM fixed-tubesheet exchanger with conical rear head Jumlah : 1 unit Universitas Sumatera Utara Shell : Diameter dalam ID : 15,25 in = 0,387 m Baffle space B : 9,15 in = 0,232 m 0,6 × ID Passes n : 1 Tube : Diameter dalam ID : 1,152 in = 29,261 mm Diameter luar OD : 1 ¼ in = 31,750 mm BWG : 18 Pitch triangular : 1 916 in Passes : 2 Panjang : 2,1 ft = 0,640 m Fluida panas : Gas sintesis Temperatur masuk T 1 : 750,556 o C = 1383 o F Temperatur keluar T 2 : 276,667 o C = 530 o F Fluida dingin : Steam Temperatur masuk t 1 : 151,581 C = 305 o F Temperatur keluar t 2 : 301,911 C = 575 o F Panas yang diserap Q : 26.082.143 kJjam = 1.372.243 Btujam R D yang diijinkan : 0,002 LMTD : 455,990 o F Luas permukaan A : 26,968 ft 2 Jumlah tube standard N ts : 38 buah Design overall coefficient U D : 150 btujam.ft. °F5.17 Cooler H-202
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