HW8_Solt - C1 WW 3 ' Eli-i; flenmnafigmgne 1 0.2 0.3 0.4...

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Unformatted text preview: C1 WW 3 ' Eli-i; flenmnafigmgne 1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 .09 0.1 0 w, "9??? " / {NRA/V H “45*: " E?“ “M vhf». wwma- WWWMAIMAMWWWWJ'_. .._ ‘. w , _ _ ‘ ___ “V I I r “a. E“ \v “v4. My. 3?ch .. \ 4“ TE; \_ m {nib "(3fm):_%figwmmm r—" V “4: “fis’ww‘i ‘ w HIM :23 wmmu-qmannm-mmm.‘ J m / W fl :5: w W W a W m IN 400 H M Z w V W W f L, W __ ; a a .1 W ,L M W, a g ‘ m w .u m u p. 1 3 “w m ix M Q; U; 1/. 5 fix. “11+ : < OK] m): a 1 D Pm an %<<m. x <ux row. 2 <m. xv ‘ 5m. 2 <9 i 552 $3; PROBLEM 4: Minimum reflux ratio: Actual reflux ratio: Minimum number of stages: Number of actuai stages: Feed stage: Number of actual stages above feed: Reboiler heating required: Condenser cooling required: Distillate temperature: Bottom temperature: Distillate to feed fraction: HETP: “MNflREFLUX ACT_REFLUX MlN_STAGES AorgsTAeES FEEDWLOCATN RECT_STAGES REB*DUTY COND_DUTY menquMP BOTTOMMTEMP _ [NSTWVSWFEED HETP 104855045 2 4.6146912 743529134 440675711 340675711 339584243 Btu/hr 108880.193 Btu/hr “43.363051 1: 356187101 F 059400096 Btu! hr Btui’hr {3/1 2m wm mo hoom\om\oa H wmmm mmmmo.HH mmmoa.am m¢wmwmfi. mumommmm.m mm0Nm¢.H: mommh.¢h: m+fi0mmm.m- Hmam.mbmx mm.mrwm¢| 0.0 0.0 000000.H mmmmm.wfl 00000.00 NmN.h00N mmm0.mhm thbmm.b mhbrmmr. mmmmHN.N mwmwm#.w MOmdb Hm Qmmm Hmfluwumz memmuum WMMEEEM mmmm¢fihm mummm.¢¢ mmmmm.mm wamamm. wammm.fl‘ mmmhm.bm- m+MWHN¢.NI www.mwwfll mm.NOMmms 0.0 oooooo.H 0.0 scoop.¢a mommm.mw- mmwmwm.m wmmw.$ma wmmwmm.w w-mmflwoa.p mmmm¢wo. ommm+m.w QHDOHA Hm mHQ wufiflmmm mmmmmm.w mmmmM.Hm meNH.wm mwmmmwm. wmmmww.flr mmwO.MMH: m+flmbfio.wn mmm.wm0H: mmlflwmhwu 0.0 000000.d 0.0 00000.0H HPmHm.mm 0w0mHm.¢ wwor.mmfi mmvm00.m Hebhmmr. mwmva.N Nmrhmmo. QHDOHQ Hm mEOEBON H HOMHMHSEflmHfism ga\uuwu um5u\na ymuu\aoana mlgfi\5um m-floena\dum Hn\5um nfi\num Hoenw\num wmm h H:\umsu u:\nfl an\Hognfi Hfl\MOEQH mom Ho> wfla 32 ammumbm muflmfiwm huwmfimn hmouufim wmonufim hmamnufim wmfimnufim %mamnufim omym wflflow Gwyn @fiuvfiq umum Momm> mHummem wHSHMMmewB scam Hmuoa zoam Hmuoa Scam Hmuoh m29¢2flmz WZ¢BDNZ mzmmomm soah maoz meHE "EwwHquSm DISTILLATION CROSSWO RD fl-~- {3,flmmflr unamnnnauflnam_ u . m--.m am-n unaflnnmnau nanmum m . . a n a .m nunnnmnm » flflflfiu u_ n m nan EEEEEHEME E u . -ll mafia mannnma uaaflnma-u Down 1. A conduit that directs iiquio‘ from one tray to another 3. Liquid carried by vapor up to the tray above XX 5. This is determined by the amount of material going through the coiumn 8. Brought about by excessive vapor flow 13. An aiternative to the use of trays or plates 14. Made up of two components Across 2. A liquid mixture which when vaporized, produces the same composition as the liquid 4. Used to cool vapor coming off the top of the column 6. Distillation operations require lots of this (especially the reboiler) 7. Operation performed by the top- section of a column 9. Product stream taken off the top of the column 10. Liquid that is fed back to the top of the column 11. Used to raise vapor 12. The mixture that is to be separated 15. Expansion of liquid due to passage of vapor or gas _ 16. The operation performed by the bottom section of a column 17. Ensures that there is sufficient iiquid on a distillation tray ‘ XX 18. Caused by low vapor flow XX 19. Product stream taken off the bottom of a coiumn ...
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HW8_Solt - C1 WW 3 ' Eli-i; flenmnafigmgne 1 0.2 0.3 0.4...

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