Cyclone S-203 Char Combustor R-202
5.12 Cyclone S-203
Fungsi : Memisahkan 99,9 olivine dari gas pembakaran lalu olivine dikirim kembali ke gasifier R-201 Bahan konstruksi : Carbon steel Bentuk : Lapple Conventional Cyclone with 4 inch insulation Vesuvius Cercast 3300 castable refractory Jumlah : 2 unit Kondisi operasi Massa gas : m g = 102194,846 kgjam Universitas Sumatera Utara Massa char : m char = 1,717 kgjam Massa olivine : m olivine = 987124,644 kgjam Massa total : m total = 1089321,207 kgjam Densitas char : ρ char = 520,6 kgm 3 Densitas olivine : ρ olivine = 1601,846251 kgm 3 Densitas campuran partikel : ρ p = 1524,416381 kgm 3 Densitas campuran gas : ρ g = 0,254087297 kgm 3 Diameter partikel char : dp char = 200 μm Diameter partikel olivine : dp olivine = 200 μm Viskositas gas : μ g = 0,035925488 kgm.jam laju alir volumetric : Q = 289294,874 m 3 jam = 80,360 m 3 s Efisiensi pemisahan : η = 99,9 Spesifikasi : Lebar inlet cyclone : W = 0,896 m Kecepatan aliran masuk cyclone : V = 40,053 ms = 144189,967 mjam Tinggi inlet cyclone : H = 2,239 m Panjang badan cyclone : L b = 6,718 m Panjang kerucut cyclone : L c = 11,198 m Jumlah putaran di dalam vorteks terluar : Ne = 5,5 Diameter badan cyclone : D = 1,991 m Diameter outlet gas : De = 0,995 m Diameter pemecah vorteks : S = 0,995 m Diameter outlet partikel : Dd = 0,747 m5.13 Char Combustor R-202
Fungsi : Membakar char arang CKS hasil dari gasifikasi pada gasifier R-201 Bahan konstruksi : Carbon steel Bentuk : Fliudized Bed Reactor Jumlah : 2 unit Universitas Sumatera Utara Kondisi operasi Tekanan : P = 1,5 atm = 151987,5 Pa Temperatur : T = 1021 o C Densitas gas : ρ g = 1,5 kgm 3 Densitas char : ρ char = 970 kgm 3 Densitas olivine : ρ olivine = 160,846 kgm 3 Densitas partikel : ρ p = 2566 kgm 3 Percepatan gravitasi : g = 9,8 ms 2 Diameter partikel char : dp char = 0,2 mm = 0,0002 m Diameter partikel olivine : dp olivine = 0,2 mm = 0,0002 m Viskositas gas : μ g = 2,124 x 10 -5 Nsm 2 Pa-s Massa gas : m g = 149585,977 kgjam Massa char : m char = 17169,313 kgjam Massa olivine : m olivine = 987124,644 kgjam Massa partikel total : m p = 1004293,957 kgjam Spesifikasi Diameter partikel rata-rata : dp” = 0,0002 m Kecepatan sirkulasi solid : Gs = 5,544 kgm 2 s Tinggi freeboard : Hf = 2,229 m tinggi bed pada Umf : Lmf = 16,952 m Tinggi gasifier : Ht = 19,752 m Tinggi dense phase : Hd = 17,715 m Kecepatan gas melalui orifice : Uor = 167,847 ms Jumlah tuyere per area distributor : Nor = 100 tuyerem 2 Diameter orifice pada inlet gas tuyere : dor = 9,876 mm Jumlah lubang per tuyere : Nh = 6 Diameter lubang tuyere : dh = 4,032 mm Jumlah tuyere total : n tuyere = 5027 tuyeres Jumlah lubang total : n hole = 30159 holes Waktu terbakar penuh : Tbc = 1,597 jam Universitas Sumatera Utara5.14 Blower K-201
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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