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时间:2020-06-10
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1、ProblemsandSolutionsDistillation1、Acontinuousfractionatingcolumnisusedtoseparate4000kg/hofamixtureof30percentCSand70percentCCl.Bottomproductcontain5percentCSatleast,andtherateofrecoveryofCSintheoverheadproductis88%byweight,required.Calculate(a)themolesflowofoverheadproductperhour.(b)themole
2、fractionsofCSandCClintheoverheadproduct,respectivelySolution:FormoverallmaterialbalanceKnownbythejusticeoftheproblemTaketheplaceof3typesandenter2typesTheunitconverts:(molefraction)2、Aliquidcontaining40molepercentmethanoland60molepercentwateristobeseparatedinacontinuousfractionalcolumnat1atm
3、pressure.Calculatethevalueofqunderthethreefollowingconditions(a)thefeedingisliquidat40C(b)thefeedingissaturatedliquid.Theequilibriumdataformethanol-waterliquidat1atmpressurearegivenintheattachedtable.Ifthecolumnisfedwith100koml/h.Themolarfractionsofmethanolinoverheadproductandbottomproducta
4、re0.95and0.04,respectively.Arefluxratioatthetopofcolumnis2.5.Calculate(a)themoleflowofoverheadproductperhour(b)themoleflowofliquidinrectifyingcolumn(c)themoleflowofvaporinstrippingcolumn.Assumethattheconstantmolarflowappliestothissystem.Solution:FormoverallmaterialbalanceSolvetheequtionweca
5、nhave:AndTheseuppervaluesarefixedunderthethreefeedconditions。Thefeedat40℃,q=1.07Feedsaturatedliquid,q=13、Thefeedingatdewpointisfedtoacontinuousfractionatingcolumn,andtheequilibriumrelationsaregivenbyequations:y=0.723x+0.263(inrectifyingcolumn);y=1.25x–0.0187(instrippingcolumn).Calculate(a)t
6、hecompositionsoffeeding,overheadproductandbottomproduct,respectively(b)therefluxratioSolution:TheslopeoftheoperatinglineinrectifyingcolumnisWecanget:R=2.61TheinterceptoftherectifyinglineonyaxisisTheintersectionofthestrippinglineandthediagonalisY=X=XwsoXw=0.0748Formtheintersectionofthesetwoo
7、peratinglines,gives:Becausethefeedatdewpoint,sothefeedlineishorizon,andthecompositionoffeedis6.12Itisdesiredtoproduceanoverheadproductcontaining95.7molepercentAformaidealmixtureof44moleAand50molepercentBfeedingintoacontinuousfractionatingcolumn.Theaverag
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