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

16969.446 psia 150design ketebalan tekanan 84.3748104665 psia

faktor korosi 0.215 instress 16969.446 psiaefisiensi sambung 80%R 57.104210068 in

ketebalan (ts) 0.571242599376 in 0.01451 meterdiameter luar tangki (OD) 115.3509053347 in 2.929911 meter say

head designketebalan tutup (th)0.529294343363 in0.013444069062 meter say OD 114

A 1.45044615249 meter say t 0.625AB 1.27582124678 meter r 108BC 2.56857361297 meter icr 6.875AC 0.05662459995 meter sf 1,5 to 2,5

sf

OA

OD

b

B

a

A

C

r

t

icr

B 0.1746249057 meterOA 0.23886894733 meter

conclusionID 2.90089230497 meterOD 2.92991141335 meterts 0.01450955419 meterth 0.01344406906 meterOA 0.23886894733 meterH 5.2864 meterHt 5.31328813812 meter

design pengadukandimensi Dt 2.92991141335 meter

Da/Dt 0,3-0,5 say 0.3Da 0.878973424 meterC/Dt #1/3C/Dt 0.97663713778 meterW/Da #1/5W 0.1757946848 meterDd/Da #2/3Dd 0.58598228267 meterL/Da #1/4L 0.219743356 meterJ/Dt #1/12J 0.24415928445 meter

renold number specific gravity 0.7246676126 less than 1besar dari 0,6oleh karena itu v

miu 0.00079377996Nre 3084576.75121 say 3100000

bar densitas pati 1.657227 g/ml 1657.227 kg/m3 denssitas air (413)densitas butanol 1.395371 g/ml 1395.371 kg/m3 ptsa

delta T delta POH 5 pati (298) 1.566O 1 0.138 0.16 pati(413) 1.65722738255034CH 7 0.09 0.182

untuk OH

brownell and young app E

1.450446 m 57.10421 inbrownell and youngkarena coursenya ada 3 aliran masuk, keluar dan man hole

gean koplis

14.5038 psia

psiastress

125115

3 metertorispherical head

inin 1 meter 39.3701 inininsay 2 in

sf

OA

OD

b

B

a

A

C

r

t

icr

0.7 ft/s2.296588 m/s

998 kg/m3 impuritis 1657.227 kg/m3 viskositas1388.889 kg/m3 rho campu 1379.943 kg/m3 1.379943 g/ml air -0.707573 0.196077

butanol -0.556658 0.277551g/ml pati 3.299125

ptsa 0.575361impuritis 3.299125

miu campu 0.793780.000794

pati aldehide delta Nt 3.38 alkohol pr delta Nt 10.606 - 0.276Ndelta Bt 146.45 - 25.11N* delta Bt -589.44 + 70.519N*N Bintang 39.66To 677.9088Bo 370.2679B 3718.519

cP log miu 0.518399Pa s miu 3.299125

pTSA benzena delta Nt 0.6 acid delta Nt 6.795 + 0.365Ndelta Bt -140.04 + 13.869N* delta Bt -249.12 + 22.449N*N Bintang 16.95To 375.3389Bo 761.6681B 988.0982log miu -3.24006miu 0.000575

alkohol se delta Nt 11.200 - 0.605Ndelta Bt #497,58

ρ (g/cm3) ρ (kg/m3)Pati 1.707676 1707.676Impuritis 1.707676 1707.676PTSA 1.388889 1388.889Dodekanol 1.256062 1256.062APG 1.411 1411NaOH 2.110148 2110.148Air 0.998 0.998

rho campur 1.27645 1276.45

viskositas pati aldehide delta Ntair -0.453143 0.352255 delta Bt

N Bintangpati 0.083127 Toptsa 1.46756 Boimpuritis 0.083127 BDodekanol 0.418172 2.61922 log miuAPG 0.41223 2.583628 miuNaOH -1.091424 0.081017 pTSA benzena delta Ntmiu campur 2.593449 cp delta Bt

0.002593 Pa s N BintangToBoBlog miumiu

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

18709.9 psia 100 125design ketebalan tekanan 21.97902 psia 150 115

faktor koro 0.215 instress 18709.9 psiaefisiensi 85% 2,54cm

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

conclusionID 2.012152 meterOD 2.025858 meterts 0.006853 meterth 0.006692 meterOA 0.187667 meterH 5.4864 meterHt 5.499783 meter

design pengadukandimensi Dt 2.025858 meter

Da/Dt 0,3-0,5 say 0.4Da 0.810343 meterC/Dt #1/3C 0.675286 meterW/Da #1/5

sf

OA

OD

b

B

a

A

C

r

t

icr

W 0.162069 meterDd/Da #2/3Dd 0.540229 meterL/Da #1/4L 0.202586 meterJ/Dt #1/12J 0.168821 meter

renold number specific gra 0.783423 less than 1besar dari 0,6power number oleh karena itu v 0.7

rho 1276.45 kg/m3 0.21336miu 0.002593 Pa s 0.263296Nre 85095.8Np 5P 1.264139 j/s

0.001264 KWe pengadu 80%P 0.001011 KW

jacketjacket insi 2.117021 meter 83.34733 inkorosi 0.215 intebal jaket 0.263978 in 0.006705 meter

pati (298) 1.566 g/mlpati(413) 1.657227PTSA 1388.889

3.38 alkohol pr delta Nt 10.606 - 0.276N alkohol se delta Nt 11.200 - 0.605N146.45 - 25.11N* delta Bt -589.44 + 70.519N* delta Bt #497,58

24.52438.4249817.2314

3477.99-1.0802580.083127

0.6 acid delta Nt 6.795 + 0.365N-140.04 + 13.869N* delta Bt -249.12 + 22.449N* mass flow 103468.5

16.95 volumerik #DIV/0!375.3389761.6681988.0982

-2.8334040.001468

brownell and young app E

m 39.60932 inbrownell and youngkarena coursenya ada 3 aliran masuk, keluar dan man hole

psia

1 in0,1 in

torispherical head

1 meter 39.3701 in

2 in

ft/sm/srad/s

kg/jamm3