裝配圖網(wǎng) > 圖紙設計 > 畢設全套 > 大連理工大學-DUTER隊化工原料藥多功能車間初步設計【含CAD圖紙+PDF文檔】

大連理工大學-DUTER隊化工原料藥多功能車間初步設計【含CAD圖紙+PDF文檔】

大連理工大學-DUTER隊化工原料藥多功能車間初步設計【含CAD圖紙+PDF文檔】,含CAD圖紙+PDF文檔,大連理工大學-DUTER隊,化工原料藥多功能車間初步設計【含CAD圖紙+PDF文檔】,大連理工大學,DUTER,化工,原料藥,多功能,車間,初步設計,CAD,圖紙,PDF,文檔化工原料藥多功能車間 Aspen Batch 工藝模擬第四屆“國藥工程杯”全國大學生制藥工程設計競賽第四屆“國藥工程杯”全國大學生制藥工程設計競賽化工原料藥多功能車間化工原料藥多功能車間化工原料藥多功能車間化工原料藥多功能車間初步設計說明書初步設計說明書附件附件 3 Aspen batch 模擬結果目錄模擬結果目錄 1 硫辛酸模擬結果 1.1 Bpstep_3 1.2 Composite_Input_Streams 1.3 Composite_Output_Streams 1.4 Composite_Utility_Streams 1.5 Energy_Balance 1.6 Equipment_Capacity 1.7 Equipment_Contents 1.8 Equipment_Ratings 1.9 Executive_Summary 1.10 Material_Balance 1.11 Recipe_Description 1.12 Recipe_Sequence_Diagram 1.13 Step_3_Block_Diagram 1.14 Stream_Table 1.15 Utility_Stream_Table 1.16 Waste_Stream_Detail 1.17 Waste_Stream_Table 2 依非韋倫模擬結果 2.1 Bpstep_2 2.2 Composite_Input_Streams 2.3 Composite_Output_Streams 2.4 Composite_Utility_Streams 2.5 Energy_Balance 2.6 Equipment_Contents 2.7 Equipment_Ratings 2.8 Executive_Summary 2.9 Material_Balance 2.10 Recipe_Description 2.11 Recipe_Sequence_Diagram 2.12 Step_2_Block_Diagram 2.13 Stream_Table 2.14 Utility_Stream_Table 2.15 Waste_Stream_Table 3 纈沙坦模擬結果 3.1 Bpstep_2 3.2 Composite_Input_Streams 3.3 Composite_Output_Streams 3.4 Composite_Utility_Streams 3.5 Energy_Balance 3.6 Equipment_Capacity 3.7 Equipment_Contents 3.8 Equipment_Ratings 3.9 Executive_Summary 3.10 Material_Balance 3.11 Recipe_Description 3.12 Recipe_Sequence_Diagram 3.13 Step_2_Block_Diagram 3.14 Stream_Table 3.15 Utility_Stream_Table 3.16 Waste_Stream_Table Step Composite Input StreamsStep Composite Input StreamsProcess (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 21:33Number of Batches:Number of Batches:1Plan Quantity:Plan Quantity:125.77kgAll ComponentsAll ComponentsInitial Mass (kg):Initial Mass (kg): 0Initial Volume (liter):Initial Volume (liter): 0Initial Moles (kmole):Initial Moles (kmole): 0Constant Inflow (kg/min):Constant Inflow (kg/min): 0Constant Inflow (liter/min):Constant Inflow (liter/min): 0Constant Inflow (kmole/min):Constant Inflow (kmole/min): 00100200300400500600700050010001500200025003000Flowrate (kg/min)Flowrate (kg/min) Time (min)Time (min) Mass Flow from Unspecified LocationMass Flow from Unspecified Location 02000400060008000100001200014000050010001500200025003000Flowrate (liter/min)Flowrate (liter/min) Time (min)Time (min) Volume Flow from Unspecified LocationVolume Flow from Unspecified Location 0246810050010001500200025003000Flowrate (kmole/min)Flowrate (kmole/min) Time (min)Time (min) Mole Flow from Unspecified LocationMole Flow from Unspecified Location -10000-8000-6000-4000-20000050010001500200025003000Mass (kg)Mass (kg) Time (min)Time (min) Total Mass in Unspecified LocationTotal Mass in Unspecified Location -200000-150000-100000-500000050010001500200025003000Volume (liter)Volume (liter) Time (min)Time (min) Total Volume in Unspecified LocationTotal Volume in Unspecified Location -200-150-100-500050010001500200025003000Moles (kmole)Moles (kmole) Time (min)Time (min) Total Moles in Unspecified LocationTotal Moles in Unspecified Location 012345050010001500200025003000Flowrate (kg/min)Flowrate (kg/min) Time (min)Time (min) Mass Flow from StorageMass Flow from Storage 00.511.522.5050010001500200025003000Flowrate (liter/min)Flowrate (liter/min) Time (min)Time (min) Volume Flow from StorageVolume Flow from Storage 00.020.040.060.080.1050010001500200025003000Flowrate (kmole/min)Flowrate (kmole/min) Time (min)Time (min) Mole Flow from StorageMole Flow from Storage BATCH PLUS - Step_3_Composite_Input_Streams.xlsConfidential and ProprietaryPage 1 of 2Step Composite Input StreamsStep Composite Input StreamsProcess (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 21:33Number of Batches:Number of Batches:1Plan Quantity:Plan Quantity:125.77kgAll ComponentsAll ComponentsInitial Mass :Initial Mass : 0Initial Volume (liter):Initial Volume (liter): 0Initial Moles (kmole):Initial Moles (kmole): 0Constant Inflow (kg/min):Constant Inflow (kg/min): 0Constant Inflow (liter/min):Constant Inflow (liter/min): 0Constant Inflow (kmole/min):Constant Inflow (kmole/min): 0-140-120-100-80-60-40-200050010001500200025003000Mass (kg)Mass (kg) Time (min)Time (min) Total Mass in StorageTotal Mass in Storage -100-80-60-40-200050010001500200025003000Volume (liter)Volume (liter) Time (min)Time (min) Total Volume in StorageTotal Volume in Storage -3-2.5-2-1.5-1-0.50050010001500200025003000Moles (kmole)Moles (kmole) Time (min)Time (min) Total Moles in StorageTotal Moles in Storage BATCH PLUS - Step_3_Composite_Input_Streams.xlsConfidential and ProprietaryPage 2 of 2Step Composite Output StreamsStep Composite Output StreamsProcess (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 21:33Number of Batches:Number of Batches:1Plan Quantity:Plan Quantity:125.77kgAll ComponentsAll ComponentsInitial Mass (kg):Initial Mass (kg): 0Initial Volume (liter):Initial Volume (liter): 0Initial Moles (kmole):Initial Moles (kmole): 0Constant Outflow (kg/min):Constant Outflow (kg/min): 0Constant Outflow (liter/min):Constant Outflow (liter/min): 0Constant Outflow (kmole/min):Constant Outflow (kmole/min): 000.10.20.30.40.50.60.70.8050010001500200025003000Flowrate (kg/min)Flowrate (kg/min) Time (min)Time (min) Mass Flow to Unspecified LocationMass Flow to Unspecified Location 0100200300400500600700800050010001500200025003000Flowrate (liter/min)Flowrate (liter/min) Time (min)Time (min) Volume Flow to Unspecified LocationVolume Flow to Unspecified Location 00.0050.010.0150.020.0250.03050010001500200025003000Flowrate (kmole/min)Flowrate (kmole/min) Time (min)Time (min) Mole Flow to Unspecified LocationMole Flow to Unspecified Location 012345678050010001500200025003000Mass (kg)Mass (kg) Time (min)Time (min) Total Mass in Unspecified LocationTotal Mass in Unspecified Location 010002000300040005000600070008000050010001500200025003000Volume (liter)Volume (liter) Time (min)Time (min) Total Volume in Unspecified LocationTotal Volume in Unspecified Location 00.050.10.150.20.250.3050010001500200025003000Moles (kmole)Moles (kmole) Time (min)Time (min) Total Moles in Unspecified LocationTotal Moles in Unspecified Location 012345678050010001500200025003000Flowrate (kg/min)Flowrate (kg/min) Time (min)Time (min) Mass Flow to Waste WaterMass Flow to Waste Water 012345678050010001500200025003000Flowrate (liter/min)Flowrate (liter/min) Time (min)Time (min) Volume Flow to Waste WaterVolume Flow to Waste Water 00.050.10.150.20.250.30.35050010001500200025003000Flowrate (kmole/min)Flowrate (kmole/min) Time (min)Time (min) Mole Flow to Waste WaterMole Flow to Waste Water BATCH PLUS - Step_3_Composite_Output_Streams.xlsConfidential and ProprietaryPage 1 of 3Step Composite Output StreamsStep Composite Output StreamsProcess (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 21:33Number of Batches:Number of Batches:1Plan Quantity:Plan Quantity:125.77kgAll ComponentsAll ComponentsInitial Mass :Initial Mass : 0Initial Volume (liter):Initial Volume (liter): 0Initial Moles (kmole):Initial Moles (kmole): 0Constant Outflow (kg/min):Constant Outflow (kg/min): 0Constant Outflow (liter/min):Constant Outflow (liter/min): 0Constant Outflow (kmole/min):Constant Outflow (kmole/min): 0Initial Mass :Initial Mass : 0Initial Volume (liter):Initial Volume (liter): 0Initial Moles (kmole):Initial Moles (kmole): 0Constant Outflow (kg/min):Constant Outflow (kg/min): 0Constant Outflow (liter/min):Constant Outflow (liter/min): 0Constant Outflow (kmole/min):Constant Outflow (kmole/min): 00102030405060050010001500200025003000Mass (kg)Mass (kg) Time (min)Time (min) Total Mass in Waste WaterTotal Mass in Waste Water 010203040506070050010001500200025003000Volume (liter)Volume (liter) Time (min)Time (min) Total Volume in Waste WaterTotal Volume in Waste Water 00.511.522.53050010001500200025003000Moles (kmole)Moles (kmole) Time (min)Time (min) Total Moles in Waste WaterTotal Moles in Waste Water 00.20.40.60.81050010001500200025003000Flowrate (kg/min)Flowrate (kg/min) Time (min)Time (min) Mass Flow to BagsMass Flow to Bags 00.20.40.60.81050010001500200025003000Flowrate (liter/min)Flowrate (liter/min) Time (min)Time (min) Volume Flow to BagsVolume Flow to Bags 00.0010.0020.0030.0040.005050010001500200025003000Flowrate (kmole/min)Flowrate (kmole/min) Time (min)Time (min) Mole Flow to BagsMole Flow to Bags 020406080100120140050010001500200025003000Mass (kg)Mass (kg) Time (min)Time (min) Total Mass in BagsTotal Mass in Bags 020406080100120140050010001500200025003000Volume (liter)Volume (liter) Time (min)Time (min) Total Volume in BagsTotal Volume in Bags 00.10.20.30.40.50.60.7050010001500200025003000Moles (kmole)Moles (kmole) Time (min)Time (min) Total Moles in BagsTotal Moles in Bags BATCH PLUS - Step_3_Composite_Output_Streams.xlsConfidential and ProprietaryPage 2 of 3Step Composite Output StreamsStep Composite Output StreamsProcess (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 21:33Number of Batches:Number of Batches:1Plan Quantity:Plan Quantity:125.77kgAll ComponentsAll ComponentsInitial Mass :Initial Mass : 0Initial Volume (liter):Initial Volume (liter): 0Initial Moles (kmole):Initial Moles (kmole): 0Constant Outflow (kg/min):Constant Outflow (kg/min): 0Constant Outflow (liter/min):Constant Outflow (liter/min): 0Constant Outflow (kmole/min):Constant Outflow (kmole/min): 0Time (min)Time (min) Time (min)Time (min) Time (min)Time (min) 0510152025303540050010001500200025003000Flowrate (kg/min)Flowrate (kg/min) Time (min)Time (min) Mass Flow to Waste TreatmentMass Flow to Waste Treatment 0510152025303540050010001500200025003000Flowrate (liter/min)Flowrate (liter/min) Time (min)Time (min) Volume Flow to Waste TreatmentVolume Flow to Waste Treatment 00.511.52050010001500200025003000Flowrate (kmole/min)Flowrate (kmole/min) Time (min)Time (min) Mole Flow to Waste TreatmentMole Flow to Waste Treatment 02004006008001000120014001600050010001500200025003000Mass (kg)Mass (kg) Time (min)Time (min) Total Mass in Waste TreatmentTotal Mass in Waste Treatment 02004006008001000120014001600050010001500200025003000Volume (liter)Volume (liter) Time (min)Time (min) Total Volume in Waste TreatmentTotal Volume in Waste Treatment 01020304050607080050010001500200025003000Moles (kmole)Moles (kmole) Time (min)Time (min) Total Moles in Waste TreatmentTotal Moles in Waste Treatment BATCH PLUS - Step_3_Composite_Output_Streams.xlsConfidential and ProprietaryPage 3 of 3Step Composite Utility StreamsStep Composite Utility StreamsProcess (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 21:33Number of Batches:Number of Batches:1Plan Quantity:Plan Quantity:125.77kgUtilityUtilityTotalTotalTotalTotalTotalTotalAverage MassAverage MassAverage Vol.Average Vol.Average DutyAverage DutyPeak MassPeak MassPeak VolumePeak VolumePeak DutyPeak DutyMassMassVolumeVolumeHeat DutyHeat DutyFlowrateFlowrateFlowrateFlowrateFlowrateFlowrateFlowrateFlowrateFlowrateFlowrateFlowrateFlowrate(kg)(kg)(Cubic m)(Cubic m)(kJ)(kJ)(kg/min)(kg/min)(Cubic m/min)(Cubic m/min)(kJ/min)(kJ/min)(kg/min)(kg/min)(Cubic m/min)(Cubic m/min)(kJ/min)(kJ/min)Brine87,331.9540.371,786,164.9929.070.01594.60415.170.1916,056.49Steam (Low Pressure)1,053.92393.542,293,997.530.350.13763.657.232.7015,731.61WATER23,247.4723.28966,058.857.740.01321.59179.440.186,003.14Step Composite Utility StreamsStep Composite Utility StreamsProcess (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 21:33Number of Batches:Number of Batches:10 00Plan Quantity:Plan Quantity:125.77kg0 00BrineBrine0100200300400500050010001500200025003000Flowrate (kg/min)Flowrate (kg/min) Time (min)Time (min) Mass Flow TotalMass Flow Total 00.050.10.150.20.25050010001500200025003000Flowrate (Cubic m/min)Flowrate (Cubic m/min) Time (min)Time (min) Volume Flow TotalVolume Flow Total 05000100001500020000050010001500200025003000Flowrate (kJ/min)Flowrate (kJ/min) Time (min)Time (min) Heat Duty Flow TotalHeat Duty Flow Total BATCH PLUS - Step_3_Composite_Utility_Streams.xlsConfidential and ProprietaryPage 1 of 3Step Composite Utility StreamsStep Composite Utility StreamsProcess (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 21:33Number of Batches:Number of Batches:1Plan Quantity:Plan Quantity:125.77kgUtilityUtilityTotalTotalTotalTotalTotalTotalAverage MassAverage MassAverage Vol.Average Vol.Average DutyAverage DutyPeak MassPeak MassPeak VolumePeak VolumePeak DutyPeak DutyMassMassVolumeVolumeHeat DutyHeat DutyFlowrateFlowrateFlowrateFlowrateFlowrateFlowrateFlowrateFlowrateFlowrateFlowrateFlowrateFlowrate(kg)(kg)(Cubic m)(Cubic m)(kJ)(kJ)(kg/min)(kg/min)(Cubic m/min)(Cubic m/min)(kJ/min)(kJ/min)(kg/min)(kg/min)(Cubic m/min)(Cubic m/min)(kJ/min)(kJ/min)Step Composite Utility StreamsStep Composite Utility StreamsProcess (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 21:33Number of Batches:Number of Batches:10 00Plan Quantity:Plan Quantity:125.77kg0 00Steam (Low Pressure)Steam (Low Pressure)Step Composite Utility StreamsStep Composite Utility StreamsProcess (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 21:33Number of Batches:Number of Batches:10 00012345678050010001500200025003000Flowrate (kg/min)Flowrate (kg/min) Time (min)Time (min) Mass Flow TotalMass Flow Total 00.511.522.530100020003000Flowrate (Cubic m/min)Flowrate (Cubic m/min) Time (min)Time (min) Volume Flow TotalVolume Flow Total 05000100001500020000050010001500200025003000Flowrate (kJ/min)Flowrate (kJ/min) Time (min)Time (min) Heat Duty Flow TotalHeat Duty Flow Total BATCH PLUS - Step_3_Composite_Utility_Streams.xlsConfidential and ProprietaryPage 2 of 3Step Composite Utility StreamsStep Composite Utility StreamsProcess (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 21:33Number of Batches:Number of Batches:1Plan Quantity:Plan Quantity:125.77kgUtilityUtilityTotalTotalTotalTotalTotalTotalAverage MassAverage MassAverage Vol.Average Vol.Average DutyAverage DutyPeak MassPeak MassPeak VolumePeak VolumePeak DutyPeak DutyMassMassVolumeVolumeHeat DutyHeat DutyFlowrateFlowrateFlowrateFlowrateFlowrateFlowrateFlowrateFlowrateFlowrateFlowrateFlowrateFlowrate(kg)(kg)(Cubic m)(Cubic m)(kJ)(kJ)(kg/min)(kg/min)(Cubic m/min)(Cubic m/min)(kJ/min)(kJ/min)(kg/min)(kg/min)(Cubic m/min)(Cubic m/min)(kJ/min)(kJ/min)Plan Quantity:Plan Quantity:125.77kg0 00WATERWATER050100150200050010001500200025003000Flowrate (kg/min)Flowrate (kg/min) Time (min)Time (min) Mass Flow TotalMass Flow Total 00.050.10.150.2050010001500200025003000Flowrate (Cubic m/min)Flowrate (Cubic m/min) Time (min)Time (min) Volume Flow TotalVolume Flow Total 01000200030004000500060007000050010001500200025003000Flowrate (kJ/min)Flowrate (kJ/min) Time (min)Time (min) Heat Duty Flow TotalHeat Duty Flow Total BATCH PLUS - Step_3_Composite_Utility_Streams.xlsConfidential and ProprietaryPage 3 of 3Step Energy BalanceStep Energy BalanceProcess (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 21:33Number of Batches:Number of Batches:1Plan Quantity:Plan Quantity:125.77kgOperationOperationOperation TimeOperation TimeUnit IDUnit IDTotalTotalHeat DutyHeat Duty(min)(min)(kJ)(kJ)2.3. Heat10.00R001A(B)2.56E+042.5. React65.00R001A(B)-3.06E+052.8. Heat10.00R001A(B)1.21E+052.9. Transfer120.00R001A(B)2.52E+042.10. React480.00R001A(B)8.04E+042.11. Cool30.00R001A(B)-1.80E+052.16. Cool10.00R006-5.24E+042.20. Cool30.00R002A(B)-9.85E+043.2. Heat15.00R001A(B)1.49E+053.3. React180.00R001A(B)1.64E+053.4. Concentrate80.00R001A(B)1.26E+06E001A(B)-1.28E+063.5. Cool40.00R001A(B)-1.30E+053.8. pH-Adjust40.00R002A(B)-1.99E+053.29. Concentrate20.00R003A(B)2.60E+05E001A(B)-2.05E+053.33. Cool120.00R004A(B)-4.33E+043.40. Dry5.35M001A(B)2.88E+034.4. Heat-To-Reflux-And-Age120.00R005A(B)2.05E+05E004A(B)-1.97E+054.7. Crystallize360.00R008A(B)-5.65E+044.8. Filter-Dry234.08M002A(B)2.46E+03BATCH PLUS - Step_3_Energy_Balance.xlsConfidential and ProprietaryPage 1 of 1Step 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 - Press10,000.0

大連理工大學-DUTER隊化工原料藥多功能車間初步設計含CAD圖紙PDF文檔.zip

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硫辛酸生產(chǎn)工藝流程圖1.dwg---(點擊預覽)

依非韋倫生產(chǎn)工藝流程圖5.dwg---(點擊預覽)

依非韋倫生產(chǎn)工藝流程圖4.dwg---(點擊預覽)

依非韋倫生產(chǎn)工藝流程圖3.dwg---(點擊預覽)

依非韋倫生產(chǎn)工藝流程圖2.dwg---(點擊預覽)

依非韋倫生產(chǎn)工藝流程圖1.dwg---(點擊預覽)

PID圖總.dwg---(點擊預覽)

PID圖.dwg---(點擊預覽)

附件

附件7 USP標準.pdf---(點擊預覽)

附件6-9空調風口布置及氣流流向平面圖.pdf---(點擊預覽)

附件6-8真空、氮氣系統(tǒng).pdf---(點擊預覽)

附件6-7冷卻水分配系統(tǒng).pdf---(點擊預覽)

附件6-6冷卻水和冷凍鹽水分配系統(tǒng).pdf---(點擊預覽)

附件6-5蒸汽冷凝水系統(tǒng).pdf---(點擊預覽)

附件6-4廢氣系統(tǒng).pdf---(點擊預覽)

附件6-2.3.4純水、廢水、自來水系統(tǒng)1003.pdf---(點擊預覽)

附件6-1管道布置圖.pdf---(點擊預覽)

附件6-10純化水流程圖.pdf---(點擊預覽)

附件5 主要設備平面、立面布置圖.pdf---(點擊預覽)

附件4 物料平衡框圖.pdf---(點擊預覽)

附件1 設備一覽表.pdf---(點擊預覽)

附件3 PDF docs

附件3.pdf---(點擊預覽)

Aspen batch模擬結果目錄.pdf---(點擊預覽)

Aspen batch模擬結果目錄.docx---(點擊預覽)

Aspen Batch模擬.pdf---(點擊預覽)

Aspen Batch模擬.docm

依非韋倫Aspen

Waste_Stream_Table.pdf---(點擊預覽)

Utility_Stream_Table.pdf---(點擊預覽)

Stream_Table.pdf---(點擊預覽)

Recipe_Sequence_Diagram.pdf---(點擊預覽)

Recipe_Description.pdf---(點擊預覽)

Material_Balance.pdf---(點擊預覽)

utive_Summary.pdf---(點擊預覽)

Equipment_Ratings.pdf---(點擊預覽)

Equipment_Contents.pdf---(點擊預覽)

Energy_Balance.pdf---(點擊預覽)

Composite_Utility_Streams.pdf---(點擊預覽)

Composite_Output_Streams.pdf---(點擊預覽)

Composite__Streams.pdf---(點擊預覽)

Bpstep_2.tif

Bpstep_2_PFD.vsd

Step_2_Block_Diagram.vsd

硫辛酸 Aspen

Waste_Stream_Detail.pdf---(點擊預覽)

Equipment_Capacity.pdf---(點擊預覽)

Bpstep_3_PFD.jpg---(點擊預覽)

Bpstep_3_PFD.vsd

Step_3_Block_Diagram.vsd

纈沙坦Aspen

壓縮包目錄

預覽區(qū)

全部
- PID圖
  - PID圖.dwg--點擊預覽
  - PID圖總.dwg--點擊預覽
  - 依非韋倫生產(chǎn)工藝流程圖1.dwg--點擊預覽
  - 依非韋倫生產(chǎn)工藝流程圖2.dwg--點擊預覽
  - 依非韋倫生產(chǎn)工藝流程圖3.dwg--點擊預覽
  - 依非韋倫生產(chǎn)工藝流程圖4.dwg--點擊預覽
  - 依非韋倫生產(chǎn)工藝流程圖5.dwg--點擊預覽
  - 硫辛酸生產(chǎn)工藝流程圖1.dwg--點擊預覽
  - 硫辛酸生產(chǎn)工藝流程圖2.dwg--點擊預覽
  - 硫辛酸生產(chǎn)工藝流程圖3.dwg--點擊預覽
  - 硫辛酸生產(chǎn)工藝流程圖4.dwg--點擊預覽
  - 纈沙坦生產(chǎn)工藝流程圖1.dwg--點擊預覽
  - 纈沙坦生產(chǎn)工藝流程圖2.dwg--點擊預覽
  - 纈沙坦生產(chǎn)工藝流程圖3.dwg--點擊預覽
- 附件
  - 附件3 PDF docs
    - 依非韋倫Aspen
      - Bpstep_2.tif
      - Bpstep_2_PFD.vsd
      - Composite__Streams.pdf--點擊預覽
      - Composite_Output_Streams.pdf--點擊預覽
      - Composite_Utility_Streams.pdf--點擊預覽
      - Energy_Balance.pdf--點擊預覽
      - Equipment_Contents.pdf--點擊預覽
      - Equipment_Ratings.pdf--點擊預覽
      - utive_Summary.pdf--點擊預覽
      - Material_Balance.pdf--點擊預覽
      - Recipe_Description.pdf--點擊預覽
      - Recipe_Sequence_Diagram.pdf--點擊預覽
      - Step_2_Block_Diagram.vsd
      - Stream_Table.pdf--點擊預覽
      - Utility_Stream_Table.pdf--點擊預覽
      - Waste_Stream_Table.pdf--點擊預覽
    - 硫辛酸 Aspen
      - Bpstep_3_PFD.jpg--點擊預覽
      - Bpstep_3_PFD.vsd
      - Equipment_Capacity.pdf--點擊預覽
      - Step_3_Block_Diagram.vsd
      - Waste_Stream_Detail.pdf--點擊預覽
    - 纈沙坦Aspen
    - Aspen Batch模擬.docm
    - Aspen Batch模擬.pdf--點擊預覽
    - Aspen batch模擬結果目錄.docx--點擊預覽
    - Aspen batch模擬結果目錄.pdf--點擊預覽
    - 附件3.pdf--點擊預覽
  - 附件1 設備一覽表.pdf--點擊預覽
  - 附件4 物料平衡框圖.pdf--點擊預覽
  - 附件5 主要設備平面、立面布置圖.pdf--點擊預覽
  - 附件6-10純化水流程圖.pdf--點擊預覽
  - 附件6-1管道布置圖.pdf--點擊預覽
  - 附件6-2.3.4純水、廢水、自來水系統(tǒng)1003.pdf--點擊預覽
  - 附件6-4廢氣系統(tǒng).pdf--點擊預覽
  - 附件6-5蒸汽冷凝水系統(tǒng).pdf--點擊預覽
  - 附件6-6冷卻水和冷凍鹽水分配系統(tǒng).pdf--點擊預覽
  - 附件6-7冷卻水分配系統(tǒng).pdf--點擊預覽
  - 附件6-8真空、氮氣系統(tǒng).pdf--點擊預覽
  - 附件6-9空調風口布置及氣流流向平面圖.pdf--點擊預覽
  - 附件7 USP標準.pdf--點擊預覽
- 3D實物展示圖.pdf--點擊預覽
- 冷卻水和冷凍鹽水分配系統(tǒng).pdf--點擊預覽
- 圖紙目錄.pdf--點擊預覽
- 多功能車間主要管道平面布置圖.pdf--點擊預覽
- 多功能車間主要設備平面、立面布置圖.pdf--點擊預覽
- 多功能車間平面布置圖.pdf--點擊預覽
- 多功能車間第一層平面布置圖.pdf--點擊預覽
- 多功能車間第三層平面布置圖.pdf--點擊預覽
- 多功能車間第二層平面布置圖.pdf--點擊預覽
- 工藝流程圖例說明.pdf--點擊預覽
- 廢氣系統(tǒng).pdf--點擊預覽
- 潔凈空調流程圖.pdf--點擊預覽
- 真空氮氣系統(tǒng).pdf--點擊預覽
- 空調風口布置及氣流流向平面圖.pdf--點擊預覽
- 純化水工藝流程圖.pdf--點擊預覽
- 純水、廢水、自來水系統(tǒng).pdf--點擊預覽
- 蒸汽冷凝水系統(tǒng).pdf--點擊預覽
- 設備一覽表.xlsx--點擊預覽
- 設計說明書.pdf--點擊預覽
- 車間平布置圖例說明.pdf--點擊預覽
- 車間立面圖、剖面圖.pdf--點擊預覽

請點擊導航文件預覽

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