butanoisis T 413 K P Pati butanol BG air konsentrasi pati mula2 konsentrasi butanol mula2 mass flow 103468.4604332 kg/jam volumerik 74.98024220139 m3 volumerik 74.98024220139 m3/jam 1 m 0.3048 tho 0.33 jam 1 m3 35.315 V liquid 24.74347992646 m3 1 m 39.3701 faktor keamanan 10% V 0,14 x D^ V liquid 27.2178279191 m3 961.1976 Ft3 V liquid (bbl) 228.2621100009 bbl tinggi tangki 18 ft 5.2864 meter diameter tangki 9.517363205286 ft 2.900892 meter diameter liquid = diamter ta 9.517363205286 ft 2.900892 meter H liquid 14.27604480793 ft 4.351338 meter tekanan design= tekanan operasi +tekanan hidro tekanan hidro 58857.07987837 pa tekanan operasi 470000 pa tekanan design 528857.0798784 pa 5.288571 tekanan design 5.817427878662 bar 0.581743 N/mm2 design T 413 K design stress 117 N/mm2 Carbon steel 16969.446 psia design ketebalan tekanan 84.374810467 psia faktor korosi 0.215 in stress 16969.446 psia efisiensi sambu 80% R 57.104210068 in ketebalan (ts) 0.571242599376 in 0.01451 meter diameter luar tangki (OD) 115.3509053347 in 2.929911 meter head design ketebalan tutup (th) 0.529294343363 in 0.013444069062 meter say OD A 1.4504461525 meter say t AB 1.2758212468 meter r BC 2.568573613 meter icr AC 0.0566245999 meter sf sf OA OD b B a A C r t icr
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butanoisis T 413 K P 4.7Pati butanol BG airkonsentrasi pati mula2konsentrasi butanol mula2mass flow 103468.4604332 kg/jamvolumerik 74.98024220139 m3
volumerik 74.98024220139 m3/jam 1 m 0.3048 fttho 0.33 jam 1 m3 35.315 ft3V liquid 24.74347992646 m3 1 m 39.3701 infaktor keamanan 10% V 0,14 x D^2*HV liquid 27.2178279191 m3 961.1976 Ft3V liquid (bbl) 228.2621100009 bbltinggi tangki 18 ft 5.2864 meter R tangkidiameter tangki 9.517363205286 ft 2.900892 meter karena coursenya ada 3diameter liquid = diamter tangki 9.517363205286 ft 2.900892 meterH liquid 14.27604480793 ft 4.351338 meter gean koplistekanan design= tekanan operasi +tekanan hidrotekanan hidro 58857.07987837 patekanan operasi 470000 pa 1 bartekanan design 528857.0798784 pa 5.288571tekanan design 5.817427878662 bar 0.581743 N/mm2 84.37481design T 413 K Tdesign stress 117 N/mm2 Carbon steel 100
Laju Alir Massa 91174.71volumerik 71.42834 m3/jam 1 ft 0.3048 mtho 0.166667 jam 1 m3 35.315 ft3V liquid 11.90472 m3 1 m 39.3701 infaktor keamanan 10% V 0,14 x D^2*H brownell and young app EV liquid 13.0952 m3 462.4568 Ft3V liquid (bbl) 109.8228 bbltinggi tangki 18 ft 5.4864 meter R tangki 1.006076diameter tangki 6.60155 ft 2.012152 meter karena coursenya ada 3diameter liquid = diamter tangki 6.60155 ft 2.012152 meterH liquid 9.902325 ft 3.018229 meter gean koplistekanan design= tekanan operasi +tekanan hidrotekanan hidro 37763.36 Pa
tekanan operasi 100000 Pa 1 bar 14.5038tekanan design 137763.4 Pa 1.377634tekanan design 1.515397 bar 0.15154 N/mm2 21.97902 psiadesign T 353 K T stressdesign stress 129 N/mm2 Carbon steel 50 135
dari brownell R 39.60932 in 0,254cmketebalan (ts) 0.269787 in 0.006853 meterdiameter luar tangki (OD) 79.75821 in 2.025858 meter say 3 meter
head designketebalan tutup (th)0.263453 in0.006692 meter say OD 84 in
A 1.006076 meter say t 0.375 inAB 0.875901 meter r 84 inBC 2.003424 meter icr 5.125 inAC 0.045766 meter sf 1,5 to 2,5 say B 0.130175 meterOA 0.187667 meter