1、一直想用aspenplus做一個關(guān)于間歇精餾的模擬，當(dāng)開始做之后才發(fā)覺困難重重。間歇精餾和連續(xù)精餾差別比較大，面板上好多屬性的設(shè)置都變了樣，位置也改變了。還多出了夾套蒸汽加熱，間歇進料時間設(shè)置等。iiipr-inF3wTTi1-a棗MJTFLDloEblIhcchfcpFJun-CillL加.Q|aXAJdirilLjg耳iiipr-inF3wTTi1-a棗MJTFLDloEblIhcchfcpFJun-CillL加.Q|aXAJdirilLjg耳li|ryUi：ir或（ih-S:-a|iJf!Gft-4GD-iiB（：）:j翼睚CaalliiftiiaidlvcJSh-孚雨胚（D|站耳豹r-

2、旦”也匕齊u乂曲爭*舟SUTMK曲Enrluq:WDsn|HilM州hailBLiii曹EuiaUdbCwMrl.il哥5jHrti.iEI-rMFfi:laiiUAit-3“角跑rtAdkiHQEHmws費htriCsrdtEnimtjifiTdQoiii-arr-apfiri.grHil.-ed.irrrinMialdtarC一打開間歇精餾設(shè)置發(fā)現(xiàn)多出了圖中一塊，以前從沒接觸過。只認識一些比較簡單的選項，夾套加熱，效率等。經(jīng)過多方查找才知道setup項里的configuration是設(shè)置理論塔板數(shù)和有效項PotGeometry標(biāo)簽頁中定義塔釜的大小尺寸PotHeatTransfer標(biāo)簽頁中

3、定義加熱方式Condenser標(biāo)簽頁中定義冷凝的類型Reflux標(biāo)簽頁中定義回流比或者回流量等等JacketHeating子項中定義加熱介質(zhì)或者設(shè)定熱負荷然后是pressure/holdup選項定義操作壓力和塔的壓降在pressureprofileandHoldup中有兩個類型Fixed和Calculator這里塔初始化是Empty選用calculatorHoldup是塔板持液量設(shè)置料再塔內(nèi)的滯留量iMain然后是初始狀態(tài)設(shè)置iMainInitialChargeSideDrawReceiversInitial匚onditiorrInitialdrumliquidvolumefraction;I

4、nitialtemperature:Initialpressure:Initial匚onditiorrInitialdrumliquidvolumefraction;Initialtemperature:Initialpressure:InitialCanditioiMain中選擇初始化條件TotalRefluxInitialCharge標(biāo)簽頁中設(shè)置塔釜初始條件塔的設(shè)置完成后再設(shè)置操作步驟OperatingSteps項一_jOperatingSteps匚harigedParameters：EndConditionLocation:JackfitHeatingVDutyV在EndConditio

5、n標(biāo)簽頁中定義結(jié)束精餾的條件當(dāng)六甲基二硅氮烷的含量為0.05時結(jié)束精餾我一直在惦記著還有兩個問題沒解決，一個是進料的事后屬于間歇進料需要設(shè)置間歇進料的時間昨天在實驗室看書剛剛找到了這方面的內(nèi)容-勺SatupSpe:iia-a.13ans母SiirnjlationOpticiLS涉StreamClass0-:衲Subetrs-iTisn|一_jOperatingSteps匚harigedParameters：EndConditionLocation:JackfitHeatingVDutyV在EndCondition標(biāo)簽頁中定義結(jié)束精餾的條件當(dāng)六甲基二硅氮烷的含量為0.05時結(jié)束精餾我一直在惦記著

6、還有兩個問題沒解決，一個是進料的事后屬于間歇進料需要設(shè)置間歇進料的時間昨天在實驗室看書剛剛找到了這方面的內(nèi)容-勺SatupSpe:iia-a.13ans母SiirnjlationOpticiLS涉StreamClass0-:衲Subetrs-iTisn|Cosiing,Dp11ons閉二JStreamFrice出Uniic-SfiteffjCusiorriUrtLisBtpitfrtD叭i.廿iiw匚ompoLentE尊ISp4difiC-a.t3dTiE|Assiy/BltiL-lLdgM-EndTropertieslJFatroCtiaracteriEaticinpESsudoCOTiJ-

7、JLQTiSAttr-CompsHenryCoinpsMoistureCorapEUNIFACGrDupeConp-Grnij.p3Culili-LiEtEPolyncorsA+r-Sa-iliagFropertiesGgneralFlowsheetBlock%/lre：LimProperly|ADA|麗世口國口1.二忠1.口巴匕|空住衛(wèi)忠減*Include?bmdcciiption?Itemstobeinductedinstieannreporl在全局設(shè)置reportoptions中有一個batchoperation選項設(shè)置進料時間。躲得好深還有一個問題是設(shè)置成絲網(wǎng)填料塔，前面所設(shè)置的板數(shù)只

8、是理論板要換算成填料高度1.15EtUP對rketHeatrcPressurc/HoHipsIntetnafcSpccfiratonPachrqHwdrpg-Section-乳丸站;日OcfrieterrEndstagefiratiunt、BLorkUpt:ocisEOVirJvhlasB.A510Llt母ReceiversCantrolers0JtiHeICcndtnrg申EternChwgtSiJCpwabna宜cpsFheJCcricttnri5HETPYuki3；&Specifcsu-face最后終于找到了，在blocks的internals選項里面packing代表填料塔tray代表

9、篩板塔。運行完成之后出來結(jié)果Material|Display:AllstreamsFormat:GEN_MStreamTable1TerriperatureC120.0120.1100.EPressurebar1.0131.1591.013VaporFrac1.0000.190o.aooMoleFlowkrmalZhr393.000262.948136.053MassFlowkg/hiG45E3.G07424E1.62922092.071VolumeFlowcum/hr12871.8751489.60432.717EnthalpyMMkcal/hr54.680-31.81025.653Mole

10、Flowkmol/hrC6H19-01233.400239.3330.068C6H18-01153.60023.615135.9B511i2113ToBlSutstream:KIKEDYapoJLiquidConipoxLentMoLeFljvtcentg-oiKMOL/KR259.40259.S3LI.I：l7CE-Hl8-01KMOL/Jffi159.&029.62135-98Mu1yJLlit.7XMOL/HE399.LIU282.95136-OSM：iEEILoiffKG/HE64553.6142461.63221132.0701UJTi已F1QT.TCUK/Effi.12S71.8S

11、14旳日032.72Tenipt：ratnirec120.Liu128.131i：ii：i_50FrezEnifeBAR.1.011.lb-1.i：iiV：=LTi-1Fiction1ULILi19Li.i：h：iLiquidFiactloilLI.ULILi311.i：h：iSolidFractionLI.ULILiULILi.i：h：iMqlarEnthalpyKCAL/MDL-13?.0+-120.?：?-18S.55M：=lEEIEntlullJi7kcal/k&-s4r.o4-743.15-1161.20En+h：1pvFlewccal/hr-54.&S-：=：i.：=：i-25.65Mi-ErL+fijii7cal/mol-k-P99.IE-22T.13-2i：n：i.79MaEntlupyCAL/&M-K-1.23-1.41-1.