Bin Katalis Olivine T-105 Screw Conveyor C-102 Olivine Screw Conveyor C-103 Gasifier R-201
5.6 Bin Katalis Olivine T-105
Fungsi : Tempat penyimpanan Katalis Olivine Bahan konstruksi : Carbon steel Bentuk : Ellipsoidal Head Bin Jumlah : 1 unit Kondisi penyimpanan Temperatur : T = 30°C 303,15 K Tekanan operasi : P = 1 atm 101,325 kPa Kebutuhan perancangan : t = 6 bulan Laju alir massa : F = 7618,875271 lb Stok 6 bulan Densitas Olivine : ρ w = 100 lbft 3 Spesifikasi Universitas Sumatera Utara Jari-jari dalam bin : R = 2,1778 ft = 0,66379 m Hc = 1,58226 ft = 0,482273445 m Hh = 1,0889 ft = 0,3319 m Tinggi total bin : H = 6,53339 ft = 1,99138 m Volume Bin V bin : V bin = 76,1888 ft 35.7 Screw Conveyor C-102
Fungsi : Mengalirkan umpan CKS ke Gasifier R-201 Bahan konstruksi : Carbon steel Bentuk : Horizontal scew conveyor Jumlah : 2 unit Kondisi operasi Temperatur : T = 30°C 303,15 K Tekanan operasi : P = 1 atm 101,325 kPa Jarak angkut : L = 10 m Laju alir bahan : F = 36520 kgjam per unit conveyor Densitas bahan : ρ = 1,3 kgL = 1300 kgm 3 = 1,3grcm 3 Spesifikasi Daya conveyor : P = 6,2754 hp Kapasitas conveyor : Q = 1,823 m 3 jam = 64,3786 ft 3 jam Daya motor : P m = 7 hp5.8 Olivine Screw Conveyor C-103
Fungsi : Mengalirkan umpan MgO dan Olivine menuju Char Combustor R-202 Bahan konstruksi : Carbon steel Bentuk : Horizontal scew conveyor Jumlah : 2 unit Universitas Sumatera Utara Kondisi operasi Temperatur : T = 30°C 303,15 K Tekanan operasi : P = 1,7 atm 101,325 kPa Jarak angkut : L = 10 m Laju alir bahan : F = 2172,710 kgjam per unit conveyor Universitas Sumatera Utara Densitas bahan : ρ = 1,6 kgL = 1601,85 kgm 3 = 1,6 grcm 3 Spesifikasi Daya conveyor : P = 0,6205 hp Kapasitas conveyor : Q = 1,356 m 3 jam = 0,00038 m 3 s Daya motor : P m = 1 hp5.9 Gasifier R-201
Fungsi : Mengubah umpan cangkang kelapa sawit CKS menjadi gas sintesa gasifikasi Bahan konstruksi : Carbon steel Bentuk : Fliudized Bed Reactor Jumlah : 2 unit Kondisi operasi Tekanan : P = 1,701 atm Temperatur : T = 870 o C Densitas gas : ρ g = 0,68905 kgm 3 Densitas char : ρ char = 970 kgm 3 Densitas partikel : ρ p = 2566 kgm 3 Percepatan gravitasi : g = 9,8 ms 2 Diameter partikel char : dp char = 0,5 mm = 0,0005 m Diameter partikel olivine : dp olivine = 0,2 mm = 0,0002 m Viskositas gas : μ g = 0,0000099793 Nsm 2 Pa-s Massa gas : m g = 38778,19183 kgjam Massa char : m char = 17169,313 kgjam Massa olivine : m olivine = 986040 kgjam Massa partikel total : m p = 103209,313 kgjam Densitas olivine : ρ olivine = 2600 kgm 3 Spesifikasi Diameter partikel rata-rata : dp” = 0,0002 m Kecepatan sirkulasi solid : Gs = 5,544 kgm 2 s Tinggi freeboard : Hf = 2,229 m Universitas Sumatera Utara tinggi bed pada Umf : Lmf = 16,952 m Tinggi gasifier : Ht = 19,752 m Tinggi dense phase : Hd = 17,523 m Kecepatan gas melalui orifice : Uor = 247,560 ms Jumlah tuyere per area distributor : Nor = 100 tuyerem 2 Diameter orifice pada inlet gas tuyere : dor = 10,71007 mm Jumlah lubang per tuyere : Nh = 6 Diameter lubang tersebut : dh = 4,372 mm Jumlah tuyere total : n tuyere = 5026 tuyeres Jumlah lubang total : n hole = 30160 holes Waktu tinggal : τ = 8,173 s5.10 Cyclone S-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
Show more