简介：ＥｎｅｒｇｙＣｏｎｓｕｍｐｔｉｏｎｉｎＴｕｎｇｓｔｅｎＥｘｔｒａｃｔｉｖｅＭｅｔａｌｌｕｒｇｙＭｏｒｉＧ．ＡｎｄＰａｓｃｈｅｎＰ．（ＤｅｐａｒｔｒｎｅｎｔｏｆＮｏｎｆｅｒｒｏｕｓＭｅｔａｌｌｕｒｇｙ，ＵｎｉｖｅｒｓｕｙｏｆＬｅｏｂｅｎ，Ｆｒａｎｚ－Ｊ...

简介：Theextractivereactionprocessofoxygen-workingsolution-waterthree-phasesystemfortheproductionofhydrogenperoxidebytheanthraquinonemethodwasinvestigatedinasieveplatecolumnof50mmininternaldiameter.Theoxidationreactionofanthrahydroquinoneintheworkingsolutionwithoxygenandtheextractionofhydrogenperoxidefromtheworkingsolutionintoaqueousphaseoccurredsimultaneouslyinthecountercurrentmode.Theagitatingeffectcausedbygaseousphasemadethedropletsofthedispersedphasebecomesmaller,thus,increasingtheliquid-liquidinterfacialcontactareasandresultingintheimprovementofthemasstransfervelocity.Resultsshowedthatthegas-agitationhadabeneficialeffectontheextractionofhydrogenperoxidefromtheworkingsolutionintotheaqueousphase;theconcentrationofhydrogenperoxideintheraffinatedecreasedwiththeincreaseofthegaseoussuperficialvelocities;andtheconcentrationofH2O2intheraffinateincreasedwiththeincreaseofthedispersedphasesuperficialvelocityatthesamesuperficialvelocityofthegaseousphase.IntheG-L-Lextractivereactionprocess,withtheincreaseofthegaseoussuperficialvelocities,boththeconversionoftheanthrahydroquinoneoxidationandtheextractionefficiencyofhydrogenperoxidefirstincreasedsignificantly,thenincreasedgradually.

简介：为2-propanol/water/ethanediol/KAc系统的咸包含的引得出的蒸馏列和咸包含的代理人恢复列被NRTL模型和修改罗斯松驰方法模仿。模拟结果证明在蒸汽液体平衡和NRTL参数的关联方法(TDCM)的盐效果的预言对说的系统合适。四个不同蒸馏技术过程被调查；结果证明咸包含的引得出的蒸馏过程是最好的。引得出的蒸馏列的模仿的设计在不同全部的阶段数字的条件下面被执行，喂地点，倒流比率，混合代理人的数量和KAc的集中。结果证明象17个阶段，在第9舞台的一个喂的地点，1.2的倒流比率，和喂的一个混合代理人的如此的因素1.141kmol/h评价，最好可能被适合操作条件。模仿的设计也为恢复咸包含的代理人为列被做。咸包含的引得出的蒸馏的模拟方法在这个工作简单、有效。

简介：Inordertoseparatemethylacetateandmethanolazeotrope,theionicliquid(IL)1,3-dimethylimidazoliumdimethylphosphate([DMIM]DMP)wasusedasthesolvent.TheAspenPlussoftwarewasusedtodesignandoptimizetheextractivedistillationprocess.Undertheoptimizedconditions,themassfractionsofmethylacetateandmethanolwerebothabove99.5%.Comparedwiththedimethylsulfoxide(DMSO)process,the[DMIM]DMPprocesshastheadvantagesofsavingenergyandlowerequipmentinvestmentcost.Theresultshowsthatusing[DMIM]DMPasthesolventtoseparateamethylacetateandmethanolazeotropehasbetterprospectinindustrialapplication.

简介：Thispaperhasstudiedthevapor-liquidequilibrium(VLE)forthesalt-containingextractivedistillationofthe1-propanol/watersystem.BinaryVLEdataweremeasuredforthesystemsof1-propanol(1)/KAc(4),ethanediol(3)/KAc(4),and1-propanol(1)/ethanediol(3),withtheVLEdatacorrelatedwiththeNRTLmodelinordertoobtainthemodelparametersofthesebinarysystems.ThebinaryVLEdatacitedintechnicalliteraturewerecorrelatedtoobtainthemodelparametersforotherbinarysystems.VLEdataofternaryandquaternarysystemspredictedbytheNRTLmodelagreedwellwiththeliteraturedata.TheinfluenceofKAc,ethanediol,andtheKAc/ethanediolmixtureonvolatilitybetween1-propanolandwaterwasinvestigatedrespectively.Testresultsshowedthattheabove-mentionedmaterials(KAc,ethanediol)andtheirmixture(KAcandethanediol)havedifferentinfluenceonthevolatility.Whenx3=0.5,andx4=0.05,theazeotropicpointcanbeeliminated.TheNRTLmodelmethodofsalt-containingVLEissimpleandeffectiveforthepredictionofthesystem’sVLEdata.