en-plus專業(yè)軟件實訓(xùn)題目加答案

1、?專業(yè)軟件實訓(xùn)?上機報告要求上機報告一、利用Flash2模型，以靈敏度分析為工具，模擬CO2在水中的溶解度與溫度的變化曲線壓力1atm，其中起始溫度為學(xué)生本人的學(xué)號最后兩位，終點溫度為80。并以抓圖的方式把“stream、“blocks、“sensitivity的“input中輸入的內(nèi)容粘貼到Word中，并給出CO2水的溶解度隨溫度變化的Plot圖。注：物性方法選NRTL上機報告二、利用Flash2模型，以靈敏度分析為工具，模擬絕對濕度一定時，空氣的露點溫度壓力1atm，其中絕對濕度為學(xué)生本人的學(xué)號最后兩位除以100如學(xué)號最后兩位為15，那么絕對濕度為水/Kg空氣。并以抓圖的方式把“strea

2、m、“blocks、“sensitivity的“input中輸入的內(nèi)容粘貼到Word中，并給出結(jié)果即絕對濕度為*時空氣的露點溫度為*。注：物性方法選NRTL上機報告三、利用DSTWU模型，模擬苯甲苯對二甲苯異丙苯的簡捷計算，其中進料為飽和液體，壓力1.0atm，組成依次為0.3、0.3、0.3、0.1摩爾分率，流量為學(xué)生學(xué)號后兩位單位為km atm。以三線表給出“stream和“blocks的結(jié)果，其中“stream應(yīng)給出all和Full的結(jié)果。注：物性方法選NRTL-RK上機報告四、根據(jù)上題結(jié)果，利用RacFrac模型對結(jié)果校核操作回流比為最小回流比的1.5倍。給出溫度塔盤、組成汽液塔盤、流

3、量汽液塔盤的關(guān)系曲線圖。并以三線表給出“blocks 中“Results Summary的“Summary、“Blance、“Split Fraction結(jié)果。上機報告五、在上題根底上，對篩板式塔盤進行設(shè)計計算，然后根據(jù)結(jié)果，進行校核計算。將兩種計算結(jié)果以三線表的形式給出，即“Tray Sizing、“Tray Rating的“Results和“Profiles。上機報告六、利用RacFrac模型，模擬甲烷乙烷丙烷正丁烷正戊烷正葵烷的氣體吸收過程，其中原料氣進料溫度50，壓力5atm，組成甲烷0.8、乙烷0.1、丙烷0.05、正丁烷0.03、正戊烷0.02摩爾分率，進料流量為學(xué)生學(xué)號后兩位單位

4、為kmol/sec；吸收液進料溫度50，壓力5atm，組成正戊烷0.01、正葵烷0.99摩爾分率，進料流量為學(xué)生學(xué)號后兩位的兩倍單位為kmol/sec。以三線表給出“blocks中“Results Summary的“Summary、“Blance、“Split Fraction結(jié)果。注：物性方法選NRTL-RK上機報告七、上題中，假設(shè)尾氣中丙烷的組成為0.001摩爾分率，那么吸收液用量為多少。利用“Design Specs和“Vary進行計算。以抓圖的方式把“Design Specs的“Specification、“Components、“Feed/Product Stream的內(nèi)容，以及“V

5、ary的“Results粘貼到Word中。上機報告八、利用HeatX模型，模擬水壓力1atm，溫度20，流量10tonne/hr冷卻熱空氣壓力1atm，溫度120，流量為學(xué)生學(xué)號后兩位的開平方tonne/hr的計算。換熱器“Setup采用“Shortcut和“Design，出口溫度110。以三線表給出“Stream的“Results“Display：All Stream，“Format：Full。并給出“blocks中“Thermal Results下的所有結(jié)果，指出換熱器的面積和對數(shù)平均溫度值。注：物性方法選IDEAL上機報告九、上題中，假設(shè)換熱器“Setup采用“Hetran-Rigoro

6、us和“Design，出口溫度110。指出兩種不同情況下，“blocks中“Thermal Results下結(jié)果的異同，并以三線表給出“blocks中“Hetran Thermal Results下的所有結(jié)果。上機報告十、利用ASPEN Plus的“B-JAC模塊，模擬計算20的水，將70的煤油冷卻至50的過程，冷熱流體操作壓力均為1atm，冷流體流量為10tonne/hr，熱流體流量為10+學(xué)生學(xué)號后兩位tonne/hr。以普通表格形式給出“Thermal Summary下的所有結(jié)果。并以“Export to DXP將“Mechanical Summary 下“Setting Plan &

7、Tubesheet Layout的換熱器圖輸出，并插入到Word中。注意：報告封面打印必須用A4紙張，標(biāo)題寫“?專業(yè)軟件實訓(xùn)?上機報告，一號，黑體，加粗。寫明姓名、班級及學(xué)號標(biāo)題下方，三號宋體加粗居中。報告正文一律使用標(biāo)準(zhǔn)簡化漢字，采用Word文檔格式，用計算機打印在A42129.7紙上。采用單面打印，右側(cè)裝訂。每題的標(biāo)題如上機報告一、上機報告二以三號宋體加粗居左；正文根本用字為小四號宋體，數(shù)字及英文字體均為Times New Roman，字符間距：標(biāo)準(zhǔn)，行距：單倍。頁面上、下、左、右頁邊距的設(shè)定分別為：3.0、2.5、3.0、2.0。除封面不編排頁碼外，報告正文局部請編排頁碼，起始頁碼為1，

8、頁碼格式為“第*頁 共*頁，字體用五號宋體，數(shù)字用Times New Roman。?專業(yè)軟件實訓(xùn)?上機報告班級：化工102班姓名：曾懿學(xué)號：1011034044上機報告一1.1 Stream中的input:1.2 Block中的input:1.3 Sensitivity中的input:CO2溶解度隨溫度T變化關(guān)系圖由上圖可知，當(dāng)溫度為44，CO25。上機報告二2.1 Stream中的input:2.2 Block中的input: Sensitivity中的input: Sensitivity中的result：由上圖可得當(dāng)絕對濕度為水/kg空氣時，空氣的露點溫度為39。上機報告三3.1 Stre

9、am中的reasult:DFWSubstream:MIXED Mole Flow:kmol/hr BENZE-01TOLUE-01P-XYL-01ISOPR-01Total Flow:kmol/hrTotal Flow:kg/hr2734898Total Flow:cum/hrTemperature:C0Pressure:barVapor Frac000Liquid Frac111Solid Frac000Enthalpy:kcal/molEnthalpy:kcal/kgEnthalpy:MMkcal/hrEntropy:cal/mol-KEntropy:cal/gm-KDensity:kmo

10、l/cumDensity:kg/cumAverage MWLiq Vol 60F:cum/hr3.2 block中的result:Parameter resultMinimum reflux ratio:Actual reflux ratio:Minimum number of stages:Number of actual stages:Feed stage:Number of actual stages above feed:Reboiler heating required:MMkcal/hrCondenser cooling required:MMkcal/hrDistillate t

11、emperature:Bottom temperature:Distillate to feed fraction:HETP:上機報告四 各變量與塔板數(shù)的關(guān)系圖汽液組成與塔盤數(shù)關(guān)系圖汽液流量與塔盤數(shù)關(guān)系圖摩爾流率與塔盤數(shù)關(guān)系圖4.2 Block中result summary: Summary:Condenser/top stage performanceResultTemperature:Heat duty:MMkcal/hrDisitilate rate: kmol/hrReflux rate: kmol/hrReflux ratio4 Blance:TotalInOutRMole-flow

12、: kmol/hr4444Mass-flow: kg/hrenthalpy :MMkcal/hr Split Fraction:ComponentDWBENZE-01TOLUE-01P-XYL-01ISOPR-01上機報告五： Tray sizing 中的result:Section starting stageSectionending stageStage with maximum diameterColumn diameter:meterDowncomer area/colum area:sqmSide downcomer velocity:m/secSide weir length:m

13、eter288 Tray sizing 中的profiles:Stage2345678Diameter:meterTotal area:sqmActivearea:sqm98Sidedowncomer area: sqm5.2 Tray rating中的reasult: Tray rating summaryParameterResultSection starting stage:2Section ending stage:8Maximum flooding factor:Stage:8Panel:Section pressure drop:bar Downcome result:Param

14、eterResultMaximum backup / Tray spacing:Stage:8Backup:Stage:8Velocity:/sec Tray rating中的profiles:StageFlooding factorDowncomer velocityDowncomer backupBackup / Tray spacePressure dropm/secmeterbar2345678上機報告六:6.1 Results summary中的summary:Temperature:FHeat duty:btu/hrDistillate rate:ibmol/hrReflux ra

15、te:ibmol/hrReflux ratio:06.2 Results summary中的balance: TotalInOutRel. diffMole-flow:lbmol/hr0Mass-flow:lb/hr106299984106299984Enthalpy:Btu/hr-9.95E+10-9.95E+106.3 Results summary中的split fraction:Component12METHA-01ETHAN-01PROPA-01N-BUT-01N-PEN-01N-DEC-01上機報告七: Design specs中的specification: Design spe

16、cs中的components: Design specs中的feed/product streams:7.2 Vary中的reasult:上機報告八：8.1 Stream中的results：LCLJRCRJSubstream: MIXED Mole Flow kmol/hr WATER00 AIR00Total Flow kmol/hrTotal Flow kg/hr100001000066006600Total Flow cum/hr681Temperature C20110120Pressure bar11Vapor Frac0011Liquid Frac1100Solid Frac000

17、0Enthalpy kcal/molEnthalpy kcal/kgEnthalpy MMkcal/hrEntropy cal/mol-KEntropy cal/gm-KDensity kmol/cumDensity kg/cumAverage MWLiq Vol 60F cum/hr8.2 Thermal results: Summary:inletoutletHot stream: RJRCtemperature:c120110pressure: barvapor fraction:11cold stream:LJLCtemperature:c20pressure: barvapor fr

18、action:00heat duty: MMkcal/h Balance: TotalInOutRel. diffMole-flow:kmol/hr0Mass-flow:kg/hr16600166000Enthalpy:MMkcal/hr0 Exchanger details:ParameterresultCalculated heat duty:MMkcal/hrRequired exchanger area:sqmActual exchanger area:sqmPercent over design:0Avg.heat transfer coefficient dirty: kcal/h

19、r-sqm-kLMTD(corrected):LMTD corrected factor1number of shells1換熱器的面積為0.2310183sqm，對數(shù)平均溫度為。上機報告九：9.1 Shoutcut與hetran-rigorous的比較：shortcutHetran-rigorousInletOutletInletOutletHot streamRJRCRJRCtemperature120110120110Pressure:barVapor fraction:1111Cold streamLJLCLJLCTemperature:2020Pressure:barVapor fr

20、action0000Heatduty:MMkcal/hr通過比較可知，這兩種方法除了冷流體的出口溫度有細微差異，其余的變量都相同。 Hetran thermal results中的overall:ParameterresultHot stream location:SHELLHeat duty:MMkcal/hrRequired exchanger area:sqmActual exchanger area:sqm%excess surface area clean:%excess surface area dity:Avg.heat transfer coefficient(dirty):k

21、cal/hr-sqm-kAvg.heat transfer coefficient(clean):kcal/hr-sqm-kLMTD(corrected):cLMTD correction factor:Vibration indication:YESHigh rhov2 indication:YES Hetran thermal results中的Shellside thermal:parameterresultWall temperature:Average skill temperature:Bulk film coefficient:kcal/hr-sqm-kWall film coe

22、fficient: kcal/hr-sqm-kThermal resistance:cal/sec/-sqcm-kFilm % overall resistance: Hetran thermal results中的shellside delta p:parameterresultClean pressure drop:barDity pressure drop: barWindow pressure drop: barPressure drop in ends: bar barCrossflow pressure drop: barCrossflow velocity:m/secWindow

23、 flow velocity: m/secMidpoint velocity: m/secShell entrance rho-v2:kg/m-sqsecShell exit rho-v2: kg/m-sqsecBundle entrance rho-v2: kg/m-sqsecBundle exit rho-v2: kg/m-sqsec Hetran thermal results中的tubeside thermal:parameterresultWall temperature:Average skin temperature:bulk film coefficient: kcal/hr-

24、sqm-kWall film coefficient:kcal/hr-sqm-kThermal resistance:sec-sqcm-k/calFilm%overall resistance: Hetran thermal results中的tubeside delta p:parameterresultClean pressure drop:barDirty pressure drop:barInlet velocity: m/sec Outlet velocity: m/secMidpoint velocity:m/sec上機報告十：以下圖為thermal summary的所有結(jié)果：Th

25、ermal Details - GeneralShell SideTube SideGases (in/out)lb/hLiquids (in/out)lb/h2204622046119048119048Temperature (in/out)F15812268Dew point or bubble pointFFilm coefficientBTU/(h*ft2*F)Fouling resistanceft2*h*F/BTUVelocityft/sPressure drop (allow./calc.)psi.469Total heat exchanged BTU/h402234TypeBE

26、Mhor1ser1parOverall coef. - dirtyBTU/(h*ft2*F)Shell size8/48inEffective surface areaft242Tube No-OD55/.75inMTD correctedFBafflessingle seg39%horMTD correction factor1Tube passes1Thermal Details - Thermal ResistancesCleanSpecified FoulMax. FoulArea reqd.ft2343442Excess surfaceOverall coefficientBTU/(

27、h*ft2*F)Overall resistanceft2*h*F/BTU.0058.0058.0072Shell side foulingft2*h*F/BTUTube side fouling (at tube ID)Distribution of overall resistanceShell side film%Shell side fouling%Tube wall%Tube side fouling%Tube side film%Thermal Details - CoefficientsShell SideTube SideFilm coefficientsBTU/(h*ft2*

28、F)As calculated by programAs specified by user in inputUser specified multiplier11As used in designDesuperheating coefficientCondensing coefficientVapor sensible coefficientLiquid sensible coefficientBoiling coefficientLiquid cooling coefficientReynolds numberFin efficiency factor1Mean metal temperatureFThermal Details - MTD and FluxMean temperature differenceFFluxBTU/(h*ft2)Corrected MTD used in designActual flux9612LMTDBoiling fl