大連理工大學(xué)-DUTER隊(duì) 化工原料藥多功能車間初步設(shè)計(jì)【含CAD圖紙+PDF文檔】
大連理工大學(xué)-DUTER隊(duì) 化工原料藥多功能車間初步設(shè)計(jì)【含CAD圖紙+PDF文檔】,含CAD圖紙+PDF文檔,大連理工大學(xué)-DUTER隊(duì),化工原料藥多功能車間初步設(shè)計(jì)【含CAD圖紙+PDF文檔】,大連理工大學(xué),DUTER,化工,原料藥,多功能,車間,初步設(shè)計(jì),CAD,圖紙,PDF,文檔
Step Equipment CapacityStep Equipment CapacityProcess (Version):Process (Version):Thioctic (1.0)Key Input Intermediate:Key Input Intermediate:NA2S 9WSecond Input:Second Input:Ethyl-6,8-dichlorooctanoteStep (Version):Step (Version):Step 1 (1.0 )Key Output Intermediate:Key Output Intermediate:M3Second Output:Second Output:M2Simulation Date:Simulation Date:2014-10-4 20:28Number of Batches:Number of Batches:1Plan Quantity:Plan Quantity:125.77kgUnit IDUnit IDClassClassCapacityCapacityMax CapacityMax CapacitySize UtilizedSize UtilizedUnits ofUnits ofMeasureMeasureSizeSizeUtilizationUtilizationOccupancy TimeOccupancy TimeTimeTimeUtilizationUtilization(% Max)(% Max)(min)(min)(%)(%)R001A(B)Reactor2,000.002,000.001,930.62liter96.531,102.0036.68MT005Tank400.00400.00236.41liter59.10254.008.46V006Tank1,500.001,500.00945.63liter63.0410.000.33V009Tank4,000.004,000.003,200.00liter80.00128.004.26V005Tank500.00500.00182.61liter36.52302.0010.05R002A(B)Reactor2,000.002,000.001,769.79liter88.49348.0011.58MT008Tank2,000.002,000.00914.95liter45.75812.0027.03V007Tank4,000.004,000.003,200.00liter80.002,011.0066.94MT006Tank400.00400.00246.66liter61.67507.0016.88MT009Tank1,500.001,500.001,013.87liter67.5983.002.76F002AFilter - Press10,000.0010,000.004.64liter0.0548.001.60F003AFilter - Press10,000.0010,000.00567.53liter5.68128.004.26R008A(B)Reactor1,000.001,000.00574.37liter57.44383.1312.75M002A(B)Filter - Dryer10,000.0010,000.00251.54liter2.52393.0013.08Reactor 1Reactor2,000.002,000.000.00liter0.0025.000.83MT011Tank100.00100.0067.14liter67.141,640.7754.62MT012Tank100.00100.0053.72liter53.722,370.9278.93R006Reactor300.00300.00258.96liter86.3223.000.77V010Tank2,000.002,000.001,700.89liter85.0429.800.99S001A(B)Extractor10,000.0010,000.002,542.73liter25.4360.002.00R007Reactor500.00500.00273.69liter54.7429.000.97MT007Tank400.00400.0057.05liter14.2646.001.53R003A(B)Reactor2,000.002,000.001,069.65liter53.481,246.9141.51MT010Tank700.00700.00425.27liter60.7528.000.93R004A(B)Reactor1,000.001,000.00683.51liter68.35408.0013.58M001A(B)Filter - Dryer10,000.0010,000.00683.64liter6.84198.666.61R005A(B)Reactor1,000.001,000.00573.18liter57.32191.006.36F001AFilter - Press10,000.0010,000.0018.27liter0.1835.001.17S003Column10,000.0010,000.00425.22liter4.2516.340.54V008Tank4,000.004,000.00425.20liter10.6311.340.38P006Pump0.000.00FM001Conveyor - Pneumatic0.000.00P007Pump0.000.00BATCH PLUS - Step_3_Equipment_Capacity.xlsConfidential and ProprietaryPage 1 of 2Step Equipment CapacityStep Equipment CapacityProcess (Version):Process (Version):Thioctic (1.0)Key Input Intermediate:Key Input Intermediate:NA2S 9WSecond Input:Second Input:Ethyl-6,8-dichlorooctanoteStep (Version):Step (Version):Step 1 (1.0 )Key Output Intermediate:Key Output Intermediate:M3Second Output:Second Output:M2Simulation Date:Simulation Date:2014-10-4 20:28Number of Batches:Number of Batches:1Plan Quantity:Plan Quantity:125.77kgFM003Conveyor - Pneumatic0.000.00FM004Conveyor - Pneumatic0.000.00FM002Conveyor - Pneumatic0.000.00FM005Conveyor - Pneumatic0.000.00C001AMill - Continuous150.004.990.0020.0040.0060.0080.00100.00120.00Utilization (%)Utilization (%) Unit IDUnit ID Size UtilizationSize Utilization 0.00500.001,000.001,500.002,000.002,500.00R001A(B)MT005V006V009V005R002A(B)MT008V007MT006MT009F002AF003AR008A(B)M002A(B)Reactor 1MT011MT012R006V010S001A(B)R007MT007R003A(B)MT010R004A(B)M001A(B)R005A(B)F001AS003V008P006FM001P007FM003FM004FM002FM005C001AOccupancy Time (min)Occupancy Time (min) Unit IDUnit ID Cycle Time OverviewCycle Time Overview BATCH PLUS - Step_3_Equipment_Capacity.xlsConfidential and ProprietaryPage 2 of 2
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