Pre-PSA Knock-Out 2 S-402 Pressure Swing Adsorption Unit S-403
4.85 Pre-PSA Knock-Out 2 S-402
Fungsi : Mengurangi kadar air dan sisa hidrokarbon yang tidak bereaksi. Dimana percikan cairan air dan hidrokarbon yang dikondensasi harus di pindahkan karena secara permanen membahayakan adsorben pada PSA yang terdiri atas campuran karbon aktif dan zeolit. Untuk itu digunakan knockout drum guna mengurangi kadar airnya. a. Entalpi aliran 43, H 43 , pada 60 o C = 194110364,968 kJ b. Menghitung entalpi aliran 45, H 45 pada T = 43,333 o C = 316,483 K Komponen m kg n mol Cp, kJmol ∑H i kJ H 2 6828,790 3387296,843 28,937 98019299,173 CO 2 33151,075 753267,451 37,969 28601086,730 CO 719,671 25692,542 29,192 750018,034 H 2 O 255,631 14189,834 33,795 479539,773 CH 4 2008,786 125213,414 36,588 4581362,129 C 2 H 4 0,018 0,628 45,557 28,618 C 2 H 6 0,192 6,396 55,105 352,423 C 3 H 8 1,701 38,568 77,833 3001,827 C 3 H 6 2,757 65,526 67,017 4391,366 C 4 H 10 0,056 0,969 103,149 99,998 C 4 H 8 0,066 1,175 90,266 106,038 H 45 132439286,110 c. Menghitung entalpi aliran 44, H 44 , pada T = 43,333 o C = 316,483 K H 44 = H 43 – H 45 = 194110364,968 – 132439286,110 H 44 = 61671078,858 kJ S-402 43 44 45 Universitas Sumatera Utara Tabel LB-50 Neraca Energi pada Knock Out Drum S-402 Komponen Masuk kJ Keluar kJ H 43 H 44 H 45 H 2 99621738,766 1602439,593 98019299,173 CO 2 29256815,107 655728,377 28601086,730 CO 770169,110 20151,076 750018,034 H 2 O 59700795,161 59221255,388 479539,773 CH 4 4747329,594 165967,465 4581362,129 C 2 H 4 32,422 3,804 28,618 C 2 H 6 422,828 70,405 352,423 C 3 H 8 5236,891 2235,064 3001,827 C 3 H 6 7126,752 2735,386 4391,366 C 4 H 10 362,510 262,512 99,998 C 4 H 8 335,828 229,790 106,038 Jumlah 194110364,968 61671078,858 132439286,110 Sub total 194110364,968 194110364,968 Q 0,000 Total 194110364,968 194110364,968 Universitas Sumatera Utara4.86 Pressure Swing Adsorption Unit S-403
Fungsi : memurnikan produk gas H 2 . a. Entalpi aliran 45, H 45 , pada 43,33 o C = 132439286,110 kJ b. Menghitung entalpi aliran 46, H 46 , dari T = 43,3333 o C sampai 42,77778 o C T 1 = 43,3333 o C = 316,4833 K T 2 = 42,77777778 o C = 315,92778 K Komponen n mol CpdT, kJmol ∑H i kJ H 2 2879202,317 28,936 83311870,2 H 2 O 1,41898337 33,790 47,94804902 H 46 83311918,15 c. Menghitung entalpi aliran 47, H 47 , dari T = 43,3333 o C sampai suhu optimum Setelah di trial sampai harga Q = 0, diperoleh suhu optimum aliran 47 adalah T = 43,444 o C = 316,5936 K PRESSURE SWING ADSORPTION UNIT S-403 45 46 47 H 2 99,99 mol H 2 O 0,01 mol Universitas Sumatera Utara T 1 = 43,3333 o C = 316,4833 K T 2 = 43,4435774835 o C = 316,5936 K Komponen n mol CpdT, kJmol ∑H i kJ H 2 508094,526 28,938 14703053,410 CO 2 753267,451 37,974 28604668,223 CO 25692,542 29,192 750020,817 H 2 O 14188,415 33,795 479503,589 CH 4 125213,414 36,595 4582139,359 C 2 H 4 0,628 45,569 28,626 C 2 H 6 6,396 55,120 352,520 C 3 H 8 38,568 77,856 3002,743 C 3 H 6 65,526 67,036 4392,578 C 4 H 10 0,969 103,178 100,026 C 4 H 8 1,175 90,293 106,070 H 47 49127367,961 Tabel LB-51 Neraca Energi pada unit PSA S-403 Komponen Masuk kJ Keluar kJ H 45 H 46 H 47 H 2 98019299,173 83311870,201 14703053,410 CO 2 28601086,730 28604668,223 CO 750018,034 750020,817 H 2 O 479539,773 47,948 479503,589 CH 4 4581362,129 4582139,359 C 2 H 4 28,618 28,626 C 2 H 6 352,423 352,520 C 3 H 8 3001,827 3002,743 C 3 H 6 4391,366 4392,578 C 4 H 10 99,998 100,026 C 4 H 8 106,038 106,070 Jumlah 132439286,110 83311918,149 49127367,961 Sub total 132439286,110 132439286,110 Q 0,000 Total 132439286,110 132439286,110 Universitas Sumatera Utara Universitas Sumatera Utara S-501 46 53 544.87 Pre Hydrogen Compressor Knock Out S-501
Parts
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» Gambaran Umum Hidrogen TINJAUAN PUSTAKA
» Kelapa Sawit Komposisi Cangkang Kelapa Sawit
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» 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
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» 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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