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

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

大連理工大學(xué)-DUTER隊化工原料藥多功能車間初步設(shè)計【含CAD圖紙+PDF文檔】,含CAD圖紙+PDF文檔,大連理工大學(xué)-DUTER隊,化工原料藥多功能車間初步設(shè)計【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,CAD,圖紙,PDF,文檔 Step Recipe DescriptionStep Recipe DescriptionProcess (Version):Process (Version):Efavirenz (1.0)Key Input Intermediate:Key Input Intermediate:ANILINE Step (Version):Step (Version):Step1 (1.0)Key Output Intermediate:Key Output Intermediate: M1 Simulation Date:Simulation Date:#Number of Batches:Number of Batches:1 Plan Quantity:Plan Quantity:3.89kg Unit IDUnit IDSequenceSequenceNumberNumberOperationOperationOperationOperationLiquid+SoliLiquid+Solid Massd MassVesselVesselLiquid+SoliLiquid+Solid Massd MassOperationOperationLiquid+SoliLiquid+Solid Volumed VolumeVesselVesselLiquid+SoliLiquid+Solid dVolumeVolumeOperationOperationTimeTimeVesselVesselOccupancyOccupancyTimeTimeBatch TimeBatch Time(kg)(kg)(kg)(kg)(liter)(liter)(liter)(liter)(min)(min)(min)(min)(min)(min)V0021.1.Purge unit V002. Purge 3 times withNITROGEN between high pressure 1.25atm and low pressure 0.04 atm for 1min each. Then0.000.000.000.003.003.003.00setup blanket to maintain 101325 Papressure in the unit.1.3.Charge V002 with 160 liter of ZnEt2.The charge time is 2 min.159.01159.01160.00160.002.008.008.001.4.Transfer contents of unit V002 toMT001. Transfer 72 kg of vesselcontents. The transfer time is 5min. Transfer using P002.-72.0087.01-72.4587.555.0013.0013.00MT0011.2.Purge unit MT001. Purge 3 times withNITROGEN between high pressure 1.25atm and low pressure 0.04 atm for 1min each. Then0.000.000.000.003.003.006.00setup blanket to maintain 101325 Papressure in the unit.1.4.Transfer contents of unit V002 toMT001. Transfer 72 kg of vesselcontents. The transfer time is 5min. Transfer using P002.72.0072.0072.4572.455.0010.0013.001.21.Transfer contents of unit MT001 toR006. Transfer 72 kg of vesselcontents. The transfer time is 5min.-72.000.00-72.450.005.0017.0020.00V0011.5.Purge unit V001. Purge 3 times withNITROGEN between high pressure 1.25atm and low pressure 0.04 atm for 1min each. Then0.000.000.000.003.003.003.00setup blanket to maintain 101325 Papressure in the unit.BATCH PLUS - Step_2_Recipe_Description.xlsConfidential and ProprietaryPage 1 of 29Step Recipe DescriptionStep Recipe DescriptionProcess (Version):Process (Version):Efavirenz (1.0)Key Input Intermediate:Key Input Intermediate:ANILINE Step (Version):Step (Version):Step1 (1.0)Key Output Intermediate:Key Output Intermediate: M1 Simulation Date:Simulation Date:#Number of Batches:Number of Batches:1 Plan Quantity:Plan Quantity:3.89kg Unit IDUnit IDSequenceSequenceNumberNumberOperationOperationOperationOperationLiquid+SoliLiquid+Solid Massd MassVesselVesselLiquid+SoliLiquid+Solid Massd MassOperationOperationLiquid+SoliLiquid+Solid Volumed VolumeVesselVesselLiquid+SoliLiquid+Solid dVolumeVolumeOperationOperationTimeTimeVesselVesselOccupancyOccupancyTimeTimeBatch TimeBatch Time(kg)(kg)(kg)(kg)(liter)(liter)(liter)(liter)(min)(min)(min)(min)(min)(min)1.7.Charge V001 with 76.8 kg of B. Thecharge time is 1 min.76.8076.8048.0248.021.007.007.001.8.Transfer contents of unit V001 toMT003. Transfer 76.8 kg of vesselcontents. The transfer time is 5min. Transfer using P001.-76.800.00-48.020.005.0012.0012.00MT0031.6.Purge unit MT003. Purge 3 times withNITROGEN between high pressure 1.25atm and low pressure 0.04 atm for 1min each. Then0.000.000.000.003.003.006.00setup blanket to maintain 101325 Papressure in the unit.1.8.Transfer contents of unit V001 toMT003. Transfer 76.8 kg of vesselcontents. The transfer time is 5min. Transfer using P001.76.8076.8048.0248.025.009.0012.001.34.Transfer contents of unit MT003 toR001A. Transfer 76.8 kg of vesselcontents. The transfer time is 5min.-76.800.00-48.020.005.0032.0035.00V0031.9.Purge unit V003. Purge 3 times withNITROGEN between high pressure 1.25atm and low pressure 0.04 atm for 1min each. Then0.000.000.000.003.003.003.00setup blanket to maintain 101325 Papressure in the unit.1.11.Charge V003 with 400 liter ofANILINE. Material is charged usingP003. The charge time is 4 min.770.02770.02400.00400.004.0010.0010.00BATCH PLUS - Step_2_Recipe_Description.xlsConfidential and ProprietaryPage 2 of 29Step Recipe DescriptionStep Recipe DescriptionProcess (Version):Process (Version):Efavirenz (1.0)Key Input Intermediate:Key Input Intermediate:ANILINE Step (Version):Step (Version):Step1 (1.0)Key Output Intermediate:Key Output Intermediate: M1 Simulation Date:Simulation Date:#Number of Batches:Number of Batches:1 Plan Quantity:Plan Quantity:3.89kg Unit IDUnit IDSequenceSequenceNumberNumberOperationOperationOperationOperationLiquid+SoliLiquid+Solid Massd MassVesselVesselLiquid+SoliLiquid+Solid Massd MassOperationOperationLiquid+SoliLiquid+Solid Volumed VolumeVesselVesselLiquid+SoliLiquid+Solid dVolumeVolumeOperationOperationTimeTimeVesselVesselOccupancyOccupancyTimeTimeBatch TimeBatch Time(kg)(kg)(kg)(kg)(liter)(liter)(liter)(liter)(min)(min)(min)(min)(min)(min)1.12.Transfer contents of unit V003 toMT002. Transfer 160 kg of vesselcontents. The transfer time is 5min.-160.00610.02-83.12316.885.0015.0015.00MT0021.10.Purge unit MT002. Purge 3 times withNITROGEN between high pressure 1.25atm and low pressure 0.04 atm for 1min each. Then0.000.000.000.003.003.006.00setup blanket to maintain 101325 Papressure in the unit.1.12.Transfer contents of unit V003 toMT002. Transfer 160 kg of vesselcontents. The transfer time is 5min.160.00160.0083.1283.125.0012.0015.001.30.Transfer contents of unit MT002 toR007. Transfer 160 kg of vesselcontents. The transfer time is 5min.-160.000.00-83.120.005.00127.00130.00V0071.13.Purge unit V007. Purge 3 times withNITROGEN between high pressure 1.25atm and low pressure 0.04 atm for 1min each. Then0.000.000.000.003.003.003.00setup blanket to maintain 101325 Papressure in the unit.1.15.Charge V007 with 3200 liter ofETHYL-ACETATE. The charge time is 4min.2,859.572,859.573,200.003,200.004.0010.0010.001.16.Transfer contents of unit V007 toMT011. Transfer 34.85 kg of vesselcontents. The transfer time is 5min.-34.852,824.72-39.003,161.005.0015.0015.00BATCH PLUS - Step_2_Recipe_Description.xlsConfidential and ProprietaryPage 3 of 29Step Recipe DescriptionStep Recipe DescriptionProcess (Version):Process (Version):Efavirenz (1.0)Key Input Intermediate:Key Input Intermediate:ANILINE Step (Version):Step (Version):Step1 (1.0)Key Output Intermediate:Key Output Intermediate: M1 Simulation Date:Simulation Date:#Number of Batches:Number of Batches:1 Plan Quantity:Plan Quantity:3.89kg Unit IDUnit IDSequenceSequenceNumberNumberOperationOperationOperationOperationLiquid+SoliLiquid+Solid Massd MassVesselVesselLiquid+SoliLiquid+Solid Massd MassOperationOperationLiquid+SoliLiquid+Solid Volumed VolumeVesselVesselLiquid+SoliLiquid+Solid dVolumeVolumeOperationOperationTimeTimeVesselVesselOccupancyOccupancyTimeTimeBatch TimeBatch Time(kg)(kg)(kg)(kg)(liter)(liter)(liter)(liter)(min)(min)(min)(min)(min)(min)1.33.Transfer contents of unit V007 toR001A. Transfer 320 kg of vesselcontents. The transfer time is 10min. Transfer using P009.-320.002,504.72-358.102,802.9110.0030.0030.001.29.Transfer contents of unit V007 toR007. Transfer 160 kg of vesselcontents. The transfer time is 8min. Transfer using P009.-160.002,344.72-179.052,623.868.00125.00125.001.46.Transfer contents of unit V007 toR001A. Transfer 480 kg of vesselcontents. The transfer time is 23min. Transfer using P007.-480.001,864.72-537.142,086.7123.00792.77792.772.1.Transfer contents of unit V007 toR002A. Transfer 565.5 kg of vesselcontents. The transfer time is 15min. Transfer using-565.501,299.22-632.821,453.8915.001,492.771,492.77P009.2.9.Transfer contents of unit V007 toS001A. Transfer 113.1 kg of vesselcontents. The transfer time is 20min. Transfer using-113.101,186.12-126.561,327.3320.001,977.771,977.77P007.2.21.Transfer contents of unit V007 toMT011. Transfer 18.85 kg of vesselcontents. The transfer time is 5min.-18.851,167.27-21.091,306.235.002,825.302,825.303.2.Transfer contents of unit V007 toR005A. Transfer 350 kg of vesselcontents. The transfer time is 10min.-350.00817.27-391.67914.5710.002,910.892,910.89BATCH PLUS - Step_2_Recipe_Description.xlsConfidential and ProprietaryPage 4 of 29Step Recipe DescriptionStep Recipe DescriptionProcess (Version):Process (Version):Efavirenz (1.0)Key Input Intermediate:Key Input Intermediate:ANILINE Step (Version):Step (Version):Step1 (1.0)Key Output Intermediate:Key Output Intermediate: M1 Simulation Date:Simulation Date:#Number of Batches:Number of Batches:1 Plan Quantity:Plan Quantity:3.89kg Unit IDUnit IDSequenceSequenceNumberNumberOperationOperationOperationOperationLiquid+SoliLiquid+Solid Massd MassVesselVesselLiquid+SoliLiquid+Solid Massd MassOperationOperationLiquid+SoliLiquid+Solid Volumed VolumeVesselVesselLiquid+SoliLiquid+Solid dVolumeVolumeOperationOperationTimeTimeVesselVesselOccupancyOccupancyTimeTimeBatch TimeBatch Time(kg)(kg)(kg)(kg)(liter)(liter)(liter)(liter)(min)(min)(min)(min)(min)(min)3.10.Transfer contents of unit V007 toMT012. Transfer 18.52 kg of vesselcontents. The transfer time is 5min. Transfer using Pump-18.52798.75-20.72893.845.003,701.473,701.47metering 1.MT0111.14.Purge unit MT011. Purge 3 times withNITROGEN between high pressure 1.25atm and low pressure 0.04 atm for 1min each. Then0.000.000.000.003.003.006.00setup blanket to maintain 101325 Papressure in the unit.1.16.Transfer contents of unit V007 toMT011. Transfer 34.85 kg of vesselcontents. The transfer time is 5min.34.8534.8539.0039.005.0012.0015.001.58.Wash the cake in unit M001A. Foreach wash, use 16 kg of the materialin MT011. The feed time is 30 min.Wash the cake 1-16.0018.85-17.9021.0930.001,394.771,397.77times. Dissolve the followingcomponents: 41.36% of ETHYL-ACETATEand 2.35% of M1. Spent Wash Stream:The stream is sent toV005.1.62.Transfer contents of unit V009 toMT011. Transfer 18.85 kg of vesselcontents. The transfer time is 5min. Transfer using P009.18.8537.7023.9645.065.001,399.771,402.772.21.Transfer contents of unit V007 toMT011. Transfer 18.85 kg of vesselcontents. The transfer time is 5min.18.8556.5521.0966.155.002,822.302,825.30BATCH PLUS - Step_2_Recipe_Description.xlsConfidential and ProprietaryPage 5 of 29Step Recipe DescriptionStep Recipe DescriptionProcess (Version):Process (Version):Efavirenz (1.0)Key Input Intermediate:Key Input Intermediate:ANILINE Step (Version):Step (Version):Step1 (1.0)Key Output Intermediate:Key Output Intermediate: M1 Simulation Date:Simulation Date:#Number of Batches:Number of Batches:1 Plan Quantity:Plan Quantity:3.89kg Unit IDUnit IDSequenceSequenceNumberNumberOperationOperationOperationOperationLiquid+SoliLiquid+Solid Massd MassVesselVesselLiquid+SoliLiquid+Solid Massd MassOperationOperationLiquid+SoliLiquid+Solid Volumed VolumeVesselVesselLiquid+SoliLiquid+Solid dVolumeVolumeOperationOperationTimeTimeVesselVesselOccupancyOccupancyTimeTimeBatch TimeBatch Time(kg)(kg)(kg)(kg)(liter)(liter)(liter)(liter)(min)(min)(min)(min)(min)(min)2.22.Wash the cake in unit M001A. Foreach wash, use 18.85 kg of thematerial in MT011. Wash the cake 1times. The moisture content-18.8537.70-22.0544.100.592,822.892,825.89in the final cake is 20%. Dissolvethe following components: 100% ofETHYL-ACETATE. Spent Wash Stream:The stream is sent toV005.V0091.17.Purge unit V009. Purge 3 times withNITROGEN between high pressure 1.25atm and low pressure 0.04 atm for 1min each. Then0.000.000.000.003.003.003.00setup blanket to maintain 101325 Papressure in the unit.1.18.Charge V009 with 3200 kg of ACETONE.The charge time is 6 min.3,200.003,200.004,068.314,068.316.009.009.001.22.Transfer contents of unit V009 toR006. Transfer 72 kg of vesselcontents. The transfer time is 4min. Transfer using P009.-72.003,128.00-91.543,976.775.0025.0025.001.25.Transfer contents of unit V009 toR007. Transfer 80 kg of vesselcontents. The transfer time is 8min. Transfer using P009.-80.003,048.00-101.713,875.068.0073.0073.001.62.Transfer contents of unit V009 toMT011. Transfer 18.85 kg of vesselcontents. The transfer time is 5min. Transfer using P009.-18.853,029.15-23.963,851.105.001,402.771,402.773.1.Charge V009 with 1000 liter ofETHYL-ACETATE. The charge time is 15min.893.623,922.771,000.004,851.1015.002,900.892,900.89BATCH PLUS - Step_2_Recipe_Description.xlsConfidential and ProprietaryPage 6 of 29Step Recipe DescriptionStep Recipe DescriptionProcess (Version):Process (Version):Efavirenz (1.0)Key Input Intermediate:Key Input Intermediate:ANILINE Step (Version):Step (Version):Step1 (1.0)Key Output Intermediate:Key Output Intermediate: M1 Simulation Date:Simulation Date:#Number of Batches:Number of Batches:1 Plan Quantity:Plan Quantity:3.89kg Unit IDUnit IDSequenceSequenceNumberNumberOperationOperationOperationOperationLiquid+SoliLiquid+Solid Massd MassVesselVesselLiquid+SoliLiquid+Solid Massd MassOperationOperationLiquid+SoliLiquid+Solid Volumed VolumeVesselVesselLiquid+SoliLiquid+Solid dVolumeVolumeOperationOperationTimeTimeVesselVesselOccupancyOccupancyTimeTimeBatch TimeBatch Time(kg)(kg)(kg)(kg)(liter)(liter)(liter)(liter)(min)(min)(min)(min)(min)(min)R0061.19.Purge unit R006. Purge 3 times withNITROGEN between high pressure 1.25atm and low pressure 0.04 atm for 1min each. Then0.000.000.000.003.003.003.00setup blanket to maintain 101325 Papressure in the unit.1.21.Transfer contents of unit MT001 toR006. Transfer 72 kg of vesselcontents. The transfer time is 5min.72.0072.0072.4572.455.0020.0020.001.22.Transfer contents of unit V009 toR006. Transfer 72 kg of vesselcontents. The transfer time is 4min. Transfer using P009.72.00144.0091.54163.995.0025.0025.001.23.Heat unit R006 to 30 C. The heatingtime is 30 min. Use 131.5 C Steam(Low Pressure).0.00144.001.03165.0130.0055.0055.001.24.Transfer contents of unit R006 toMT005. Transfer 100% of vesselcontents. The transfer time is 10min. The transfer stream is-144.000.00-165.010.0010.0065.0065.00named Mix 1.MT0051.20.Purge unit MT005. Purge 3 times withNITROGEN between high pressure 1.25atm and low pressure 0.04 atm for 1min each. Then0.000.000.000.003.003.006.00setup blanket to maintain 101325 Papressure in the unit.1.24.Transfer contents of unit R006 toMT005. Transfer 100% of vesselcontents. The transfer time is 10min. The transfer stream is144.00144.00165.01165.0110.0062.0065.00BATCH PLUS - Step_2_Recipe_Description.xlsConfidential and ProprietaryPage 7 of 29Step Recipe DescriptionStep Recipe DescriptionProcess (Version):Process (Version):Efavirenz (1.0)Key Input Intermediate:Key Input Intermediate:ANILINE Step (Version):Step (Version):Step1 (1.0)Key Output Intermediate:Key Output Intermediate: M1 Simulation Date:Simulation Date:#Number of Batches:Number of Batches:1 Plan Quantity:Plan Quantity:3.89kg Unit IDUnit IDSequenceSequenceNumberNumberOperationOperationOperationOperationLiquid+SoliLiquid+Solid Massd MassVesselVesselLiquid+SoliLiquid+Solid Massd MassOperationOperationLiquid+SoliLiquid+Solid Volumed VolumeVesselVesselLiquid+SoliLiquid+Solid dVolumeVolumeOperationOperationTimeTimeVesselVesselOccupancyOccupancyTimeTimeBatch TimeBatch Time(kg)(kg)(kg)(kg)(liter)(liter)(liter)(liter)(min)(min)(min)(min)(min)(min)named Mix 1.1.37.Transfer contents of unit MT005 toR001A. Transfer 100% of vesselcontents. The transfer time is 2 h.-144.000.00-165.010.00120.00213.00216.00R0071.25.Transfer contents of unit V009 toR007. Transfer 80 kg of vesselcontents. The transfer time is 8min. Transfer using P009.80.0080.00101.71101.718.008.0073.001.29.Transfer contents of unit V007 toR007. Transfer 160 kg of vesselcontents. The transfer time is 8min. Transfer using P009.160.00240.00179.05280.768.0060.00125.001.30.Transfer contents of unit MT002 toR007. Transfer 160 kg of vesselcontents. The transfer time is 5min.160.00400.0083.12363.875.0065.00130.001.31.Heat unit R007 to 30 C. The heatingtime is 30 min. Use 131.5 C Steam(Low Pressure).0.00400.002.26366.1330.0095.00160.001.32.Transfer contents of unit R007 toMT007. Transfer 100% of vesselcontents. The transfer time is 10min. The transfer stream is-400.000.00-366.130.0010.00105.00170.00named Mix3.R0091.26.Charge R009 with 62.5 kg of CALITHIUM. Material is charged usingFM004. The charge time is 4 min.62.5062.5062.8962.894.004.0077.001.27.Heat unit R009 to 30 C. The heatingtime is 30 min. Use 131.5 C Steam(Low Pressure).0.0062.500.3163.2030.0034.00107.00BATCH PLUS - Step_2_Recipe_Description.xlsConfidential and ProprietaryPage 8 of 29Step Recipe DescriptionStep Recipe DescriptionProcess (Version):Process (Version):Efavirenz (1.0)Key Input Intermediate:Key Input Intermediate:ANILINE Step (Version):Step (Version):Step1 (1.0)Key Output Intermediate:Key Output Intermediate: M1 Simulation Date:Simulation Date:#Number of Batches:Number of Batches:1 Plan Quantity:Plan Quantity:3.89kg Unit IDUnit IDSequenceSequenceNumberNumberOperationOperationOperationOperationLiquid+SoliLiquid+Solid Massd MassVesselVesselLiquid+SoliLiquid+Solid Massd MassOperationOperationLiquid+SoliLiquid+Solid Volumed VolumeVesselVesselLiquid+SoliLiquid+Solid dVolumeVolumeOperationOperationTimeTimeVesselVesselOccupancyOccupancyTimeTimeBatch TimeBatch Time(kg)(kg)(kg)(kg)(liter)(liter)(liter)(liter)(min)(min)(min)(min)(min)(min)1.28.Transfer contents of unit R009 toMT006. The transfer time is 10 min.The transfer stream is named Mix2.-62.500.00-63.200.0010.0044.00117.00MT0061.28.Transfer contents of unit R009 toMT006. The transfer time is 10 min.The transfer stream is named Mix2.62.5062.5063.1963.1910.0010.00117.001.38.Transfer contents of unit MT006 toR001A. Transfer 100% of vesselcontents. The transfer time is 2 h.-62.500.00-63.190.00120.00229.00336.00MT0071.32.Transfer contents of unit R007 toMT007. Transfer 100% of vesselcontents. The transfer time is 10min. The transfer stream is400.00400.00366.13366.1310.0010.00170.00named Mix3.1.39.Transfer contents of unit MT007 toR001A. Maintain the temperature at40 C. Transfer 320 kg of vesselcontents. The transfer-320.0080.00-292.9073.23180.00356.00516.00time is 3 h.R001A1.33.Transfer contents of unit V007 toR001A. Transfer 320 kg of vesselcontents. The transfer time is 10min. Transfer using P009.320.00320.00358.10358.1010.0010.0030.001.34.Transfer contents of unit MT003 toR001A. Transfer 76.8 kg of vesselcontents. The transfer time is 5min.76.80396.8048.02406.125.0015.0035.001.35.Charge R001A with 11 kg of A. Thecharge time is 1 min.11.00407.806.76412.881.0016.0036.001.36.Cool unit R001A to 0 C. The coolingtime is 1 h. Use -10 C Brine.0.00407.80-13.32399.5660.0076.0096.00BATCH PLUS - Step_2_Recipe_Description.xlsConfidential and ProprietaryPage 9 of 29Step Recipe DescriptionStep Recipe DescriptionProcess (Version):Process (Version):Efavirenz (1.0)Key Input Intermediate:Key Input Intermediate:ANILINE Step (Version):Step (Version):Step1 (1.0)Key Output Intermediate:Key Output Intermediate: M1 Simulation Date:Simulation Date:#Number of Batches:Number of Batches:1 Plan Quantity:Plan Quantity:3.89kg Unit IDUnit IDSequenceSequenceNumberNumberOperationOperationOperationOperationLiquid+SoliLiquid+Solid Massd MassVesselVesselLiquid+SoliLiquid+Solid Massd MassOperationOperationLiquid+SoliLiquid+Solid Volumed VolumeVesselVesselLiquid+SoliLiquid+Solid dVolumeVolumeOperationOperationTimeTimeVesselVesselOccupancyOccupancyTimeTimeBatch TimeBatch Time(kg)(kg)(kg)(kg)(liter)(liter)(liter)(liter)(min)(min)(min)(min)(min)(min)1.37.Transfer contents of unit MT005 toR001A. Transfer 100% of vesselcontents. The transfer time is 2 h.144.00551.80163.60563.16120.00196.00216.001.38.Transfer contents of unit MT006 toR001A. Transfer 100% of vesselcontents. The transfer time is 2 h.62.50614.3062.96626.12120.00316.00336.001.39.Transfer contents of unit MT007 toR001A. Maintain the temperature at40 C. Transfer 320 kg of vesselcontents. The transfer320.00934.30323.12949.24180.00496.00516.00time is 3 h.1.40.Charge R001A with 40 kg of WATER.The charge time is 1 min.40.00974.3039.04988.281.00497.00517.001.41.React in unit R001A via Reaction 1.Reaction occurs over 2 h. Use 131.5C Steam (Low Pressure).0.00974.30-37.55950.73120.00617.00637.001.42.Charge R001A with 40 kg of WATER.The charge time is 1 h.40.001,014.3039.15989.8860.00677.00697.001.43.Concentrate the

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

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依非韋倫生產(chǎn)工藝流程圖2.dwg---(點擊預(yù)覽)

依非韋倫生產(chǎn)工藝流程圖1.dwg---(點擊預(yù)覽)

PID圖總.dwg---(點擊預(yù)覽)

PID圖.dwg---(點擊預(yù)覽)

附件

附件7 USP標(biāo)準(zhǔn).pdf---(點擊預(yù)覽)

附件6-9空調(diào)風(fēng)口布置及氣流流向平面圖.pdf---(點擊預(yù)覽)

附件6-8真空、氮氣系統(tǒng).pdf---(點擊預(yù)覽)

附件6-7冷卻水分配系統(tǒng).pdf---(點擊預(yù)覽)

附件6-6冷卻水和冷凍鹽水分配系統(tǒng).pdf---(點擊預(yù)覽)

附件6-5蒸汽冷凝水系統(tǒng).pdf---(點擊預(yù)覽)

附件6-4廢氣系統(tǒng).pdf---(點擊預(yù)覽)

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

附件6-1管道布置圖.pdf---(點擊預(yù)覽)

附件6-10純化水流程圖.pdf---(點擊預(yù)覽)

附件5 主要設(shè)備平面、立面布置圖.pdf---(點擊預(yù)覽)

附件4 物料平衡框圖.pdf---(點擊預(yù)覽)

附件1 設(shè)備一覽表.pdf---(點擊預(yù)覽)

附件3 PDF docs

附件3.pdf---(點擊預(yù)覽)

Aspen batch模擬結(jié)果目錄.pdf---(點擊預(yù)覽)

Aspen batch模擬結(jié)果目錄.docx---(點擊預(yù)覽)

Aspen Batch模擬.pdf---(點擊預(yù)覽)

Aspen Batch模擬.docm

依非韋倫Aspen

Waste_Stream_Table.pdf---(點擊預(yù)覽)

Utility_Stream_Table.pdf---(點擊預(yù)覽)

Stream_Table.pdf---(點擊預(yù)覽)

Recipe_Sequence_Diagram.pdf---(點擊預(yù)覽)

Recipe_Description.pdf---(點擊預(yù)覽)

Material_Balance.pdf---(點擊預(yù)覽)

utive_Summary.pdf---(點擊預(yù)覽)

Equipment_Ratings.pdf---(點擊預(yù)覽)

Equipment_Contents.pdf---(點擊預(yù)覽)

Energy_Balance.pdf---(點擊預(yù)覽)

Composite_Utility_Streams.pdf---(點擊預(yù)覽)

Composite_Output_Streams.pdf---(點擊預(yù)覽)

Composite__Streams.pdf---(點擊預(yù)覽)

Bpstep_2.tif

Bpstep_2_PFD.vsd

Step_2_Block_Diagram.vsd

硫辛酸 Aspen

Waste_Stream_Detail.pdf---(點擊預(yù)覽)

Equipment_Capacity.pdf---(點擊預(yù)覽)

Bpstep_3_PFD.jpg---(點擊預(yù)覽)

Bpstep_3_PFD.vsd

Step_3_Block_Diagram.vsd

纈沙坦Aspen

壓縮包目錄

預(yù)覽區(qū)

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

請點擊導(dǎo)航文件預(yù)覽

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