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 Sequence DiagramStep Recipe Sequence DiagramProcess (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:3.89 StartStartTimeTimeEnd TimeEnd TimeOperationOperationTimeTimeSequenceSequenceNumberNumberV002V002VesselVesselLiq+SolLiq+SolVesselVesselLiq+SolLiq+SolVesselVesselTempTempVesselVesselPressurePressureInput StreamsInput StreamsFromFromMassMassVolumeVolumeTempTempMassMassVolumeVolumeMassMassVolumeVolumeTempTempToToOutput StreamsOutput Streams(kg)(kg)(liter)(liter)(C)(C)(min)(min)(min)(min)(min)(min)(kg)(kg)(liter)(liter)(C)(C)(kPa)(kPa)(kg)(kg)(liter)(liter)(C)(C)NITROGEN0.83580.8025.000.003.003.001.1.Purge unit V002. Purge 3 times with NITROGEN between0.000.0025.00101.33high pressure 1.25 atm and low pressure 0.04 atm for 1min each. Then setup blanket to maintain 101325 Papressure in the unit.ZnEt2159.01160.0025.006.008.002.001.3.Charge V002 with 160 liter of ZnEt2. The charge time 159.01160.0025.00101.33is 2 min.8.0013.005.001.4.Transfer contents of unit V002 to MT001. Transfer 72 87.0187.5525.00101.3372.0072.4525.00MT0011.4. Transfer-55kg of vessel contents. The transfer time is 5 min.Transfer using P002.StartStartTimeTimeEnd TimeEnd TimeOperationOperationTimeTimeSequenceSequenceNumberNumberMT001MT001VesselVesselLiq+SolLiq+SolVesselVesselLiq+SolLiq+SolVesselVesselTempTempVesselVesselPressurePressureInput StreamsInput StreamsFromFromMassMassVolumeVolumeTempTempMassMassVolumeVolumeMassMassVolumeVolumeTempTempToToOutput StreamsOutput Streams(kg)(kg)(liter)(liter)(C)(C)(min)(min)(min)(min)(min)(min)(kg)(kg)(liter)(liter)(C)(C)(kPa)(kPa)(kg)(kg)(liter)(liter)(C)(C)NITROGEN0.83580.8025.003.006.003.001.2.Purge unit MT001. Purge 3 times with NITROGEN between 0.000.0025.00101.33high pressure 1.25 atm and low pressure 0.04 atm for 1min each. Then setup blanket to maintain 101325 Papressure in the unit.1.4. Transfer-55V00272.0072.4525.008.0013.005.001.4.Transfer contents of unit V002 to MT001. Transfer 72 72.0072.4525.00101.33 kg of vessel contents. The transfer time is 5 min. Transfer using P002. 15.0020.005.001.21.Transfer contents of unit MT001 to R006. Transfer 720.000.0025.00101.3372.0072.4525.00R0061.21. Transfer-67kg of vessel contents. The transfer time is 5 min.StartStartTimeTimeEnd TimeEnd TimeOperationOperationTimeTimeSequenceSequenceNumberNumberV001V001VesselVesselLiq+SolLiq+SolVesselVesselLiq+SolLiq+SolVesselVesselTempTempVesselVesselPressurePressureInput StreamsInput StreamsFromFromMassMassVolumeVolumeTempTempMassMassVolumeVolumeMassMassVolumeVolumeTempTempToToOutput StreamsOutput Streams(kg)(kg)(liter)(liter)(C)(C)(min)(min)(min)(min)(min)(min)(kg)(kg)(liter)(liter)(C)(C)(kPa)(kPa)(kg)(kg)(liter)(liter)(C)(C)NITROGEN0.83580.8025.000.003.003.001.5.Purge unit V001. Purge 3 times with NITROGEN between0.000.0025.00101.33high pressure 1.25 atm and low pressure 0.04 atm for 1min each. Then setup blanket to maintain 101325 Papressure in the unit.B76.8048.0225.006.007.001.001.7.Charge V001 with 76.8 kg of B. The charge time is 176.8048.0225.00101.33min.7.0012.005.001.8.Transfer contents of unit V001 to MT003. Transfer 76.80.000.0025.00101.3376.8048.0225.00MT0031.8. Transfer-58kg of vessel contents. The transfer time is 5 min.Transfer using P001.StartStartTimeTimeEnd TimeEnd TimeOperationOperationTimeTimeSequenceSequenceNumberNumberMT003MT003VesselVesselLiq+SolLiq+SolVesselVesselLiq+SolLiq+SolVesselVesselTempTempVesselVesselPressurePressureInput StreamsInput StreamsFromFromMassMassVolumeVolumeTempTempMassMassVolumeVolumeMassMassVolumeVolumeTempTempToToOutput StreamsOutput Streams(kg)(kg)(liter)(liter)(C)(C)(min)(min)(min)(min)(min)(min)(kg)(kg)(liter)(liter)(C)(C)(kPa)(kPa)(kg)(kg)(liter)(liter)(C)(C)NITROGEN0.83580.8025.003.006.003.001.6.Purge unit MT003. Purge 3 times with NITROGEN between 0.000.0025.00101.33high pressure 1.25 atm and low pressure 0.04 atm for 1min each. Then setup blanket to maintain 101325 Papressure in the unit.1.8. Transfer-58V00176.8048.0225.007.0012.005.001.8.Transfer contents of unit V001 to MT003. Transfer 76.8 76.8048.0225.00101.33kg of vessel contents. The transfer time is 5 min.Transfer using P001.30.0035.005.001.34.Transfer contents of unit MT003 to R001A. Transfer0.000.0025.00101.3376.8048.0225.00R001A1.34. Transfer-7876.8 kg of vessel contents. The transfer time is 5 min.StartStartTimeTimeEnd TimeEnd TimeOperationOperationTimeTimeSequenceSequenceNumberNumberV003V003VesselVesselLiq+SolLiq+SolVesselVesselLiq+SolLiq+SolVesselVesselTempTempVesselVesselPressurePressureInput StreamsInput StreamsFromFromMassMassVolumeVolumeTempTempMassMassVolumeVolumeMassMassVolumeVolumeTempTempToToOutput StreamsOutput Streams(kg)(kg)(liter)(liter)(C)(C)(min)(min)(min)(min)(min)(min)(kg)(kg)(liter)(liter)(C)(C)(kPa)(kPa)(kg)(kg)(liter)(liter)(C)(C)NITROGEN2.081,452.0025.000.003.003.001.9.Purge unit V003. Purge 3 times with NITROGEN between0.000.0025.00101.33high pressure 1.25 atm and low pressure 0.04 atm for 1min each. Then setup blanket to maintain 101325 Papressure in the unit.ANILINE770.02400.0025.006.0010.004.001.11.Charge V003 with 400 liter of ANILINE. Material is770.02400.0025.00101.33charged using P003. The charge time is 4 min.10.0015.005.001.12.Transfer contents of unit V003 to MT002. Transfer 160610.02316.8825.00101.33160.0083.1225.00MT0021.12. Transfer-61kg of vessel contents. The transfer time is 5 min.StartStartTimeTimeEnd TimeEnd TimeOperationOperationTimeTimeSequenceSequenceNumberNumberMT002MT002VesselVesselLiq+SolLiq+SolVesselVesselLiq+SolLiq+SolVesselVesselTempTempVesselVesselPressurePressureInput StreamsInput StreamsFromFromMassMassVolumeVolumeTempTempMassMassVolumeVolumeMassMassVolumeVolumeTempTempToToOutput StreamsOutput Streams(kg)(kg)(liter)(liter)(C)(C)(min)(min)(min)(min)(min)(min)(kg)(kg)(liter)(liter)(C)(C)(kPa)(kPa)(kg)(kg)(liter)(liter)(C)(C)NITROGEN0.83580.8025.003.006.003.001.10.Purge unit MT002. Purge 3 times with NITROGEN between 0.000.0025.00101.33high pressure 1.25 atm and low pressure 0.04 atm for 1min each. Then setup blanket to maintain 101325 Papressure in the unit.1.12. Transfer-61V003160.0083.1225.0010.0015.005.001.12.Transfer contents of unit V003 to MT002. Transfer 160160.0083.1225.00101.33kg of vessel contents. The transfer time is 5 min.125.00130.005.001.30.Transfer contents of unit MT002 to R007. Transfer 160 0.000.0025.00101.33160.0083.1225.00R0071.30. Transfer-104kg of vessel contents. The transfer time is 5 min.StartStartTimeTimeEnd TimeEnd TimeOperationOperationTimeTimeSequenceSequenceNumberNumberV007V007VesselVesselLiq+SolLiq+SolVesselVesselLiq+SolLiq+SolVesselVesselTempTempVesselVesselPressurePressureInput StreamsInput StreamsFromFromMassMassVolumeVolumeTempTempMassMassVolumeVolumeMassMassVolumeVolumeTempTempToToOutput StreamsOutput Streams(kg)(kg)(liter)(liter)(C)(C)(min)(min)(min)(min)(min)(min)(kg)(kg)(liter)(liter)(C)(C)(kPa)(kPa)(kg)(kg)(liter)(liter)(C)(C)NITROGEN16.6211,616.0025.000.003.003.001.13.Purge unit V007. Purge 3 times with NITROGEN between0.000.0025.00101.33high pressure 1.25 atm and low pressure 0.04 atm for 1min each. Then setup blanket to maintain 101325 Papressure in the unit.ETHYL-ACETATE2,859.573,200.0025.006.0010.004.001.15.Charge V007 with 3200 liter of ETHYL-ACETATE. The2,859.573,200.0025.00101.33charge time is 4 min.10.0015.005.001.16.Transfer contents of unit V007 to MT011. Transfer2,824.723,161.0025.00101.3334.8539.0025.00MT0111.16. Transfer-6434.85 kg of vessel contents. The transfer time is 5min.20.0030.0010.001.33.Transfer contents of unit V007 to R001A. Transfer 320 2,504.722,802.9125.00101.33320.00358.1025.00R001A1.33. Transfer-73kg of vessel contents. The transfer time is 10 min.Transfer using P009.117.00125.008.001.29.Transfer contents of unit V007 to R007. Transfer 1602,344.722,623.8625.00101.33160.00179.0525.00R0071.29. Transfer-101BATCH PLUS - Step_2_Recipe_Sequence_Diagram.xlsConfidential and ProprietaryPage 1 of 8Step Recipe Sequence DiagramStep Recipe Sequence DiagramProcess (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:3.89 kg of vessel contents. The transfer time is 8 min.Transfer using P009.769.77792.7723.001.46.Transfer contents of unit V007 to R001A. Transfer 480 1,864.722,086.7125.00101.33480.00537.1425.00R001A1.46. Transfer-135kg of vessel contents. The transfer time is 23 min.Transfer using P007.1,477.771,492.7715.002.1.Transfer contents of unit V007 to R002A. Transfer1,299.221,453.8925.00101.33565.50632.8225.00R002A2.1. Transfer-193565.5 kg of vessel contents. The transfer time is 15min. Transfer using P009.1,957.771,977.7720.002.9.Transfer contents of unit V007 to S001A. Transfer1,186.121,327.3325.00101.33113.10126.5625.00S001A2.9. Transfer-213113.1 kg of vessel contents. The transfer time is 20min. Transfer using P007.2,820.302,825.305.002.21.Transfer contents of unit V007 to MT011. Transfer1,167.271,306.2325.00101.3318.8521.0925.00MT0112.21. Transfer-24818.85 kg of vessel contents. The transfer time is 5min.2,900.892,910.8910.003.2.Transfer contents of unit V007 to R005A. Transfer 350817.27914.5725.00101.33350.00391.6725.00R005A3.2. Transfer-261kg of vessel contents. The transfer time is 10 min.3,696.473,701.475.003.10.Transfer contents of unit V007 to MT012. Transfer798.75893.8425.00101.3318.5220.7225.00MT0123.10. Transfer-28518.52 kg of vessel contents. The transfer time is 5min. Transfer using Pump metering 1.StartStartTimeTimeEnd TimeEnd TimeOperationOperationTimeTimeSequenceSequenceNumberNumberMT011MT011VesselVesselLiq+SolLiq+SolVesselVesselLiq+SolLiq+SolVesselVesselTempTempVesselVesselPressurePressureInput StreamsInput StreamsFromFromMassMassVolumeVolumeTempTempMassMassVolumeVolumeMassMassVolumeVolumeTempTempToToOutput StreamsOutput Streams(kg)(kg)(liter)(liter)(C)(C)(min)(min)(min)(min)(min)(min)(kg)(kg)(liter)(liter)(C)(C)(kPa)(kPa)(kg)(kg)(liter)(liter)(C)(C)NITROGEN0.42290.4025.003.006.003.001.14.Purge unit MT011. Purge 3 times with NITROGEN between 0.000.0025.00101.33high pressure 1.25 atm and low pressure 0.04 atm for 1min each. Then setup blanket to maintain 101325 Papressure in the unit.1.16. Transfer-64V00734.8539.0025.0010.0015.005.001.16.Transfer contents of unit V007 to MT011. Transfer34.8539.0025.00101.3334.85 kg of vessel contents. The transfer time is 5min.1,367.771,397.7730.001.58.Wash the cake in unit M001A. For each wash, use 16 kg18.8521.0925.00101.3316.0017.9025.00M001A1.58. Wash-Cake-172of the material in MT011. The feed time is 30 min.Wash the cake 1 times. Dissolve the followingcomponents: 41.36% of ETHYL-ACETATE and 2.35% of M1.Spent Wash Stream: The stream is sent to V005.1.62. Transfer-183V00918.8523.9625.001,397.771,402.775.001.62.Transfer contents of unit V009 to MT011. Transfer37.7045.0625.00101.3318.85 kg of vessel contents. The transfer time is 5min. Transfer using P009.2.21. Transfer-248V00718.8521.0925.002,820.302,825.305.002.21.Transfer contents of unit V007 to MT011. Transfer56.5566.1525.00101.3318.85 kg of vessel contents. The transfer time is 5min.2,825.302,825.890.592.22.Wash the cake in unit M001A. For each wash, use 18.8537.7044.1025.00101.3318.8522.0525.00M001A2.22. Wash-Cake-251kg of the material in MT011. Wash the cake 1 times.The moisture content in the final cake is 20%.Dissolve the following components: 100% ofETHYL-ACETATE. Spent Wash Stream: The stream is sentto V005.StartStartTimeTimeEnd TimeEnd TimeOperationOperationTimeTimeSequenceSequenceNumberNumberV009V009VesselVesselLiq+SolLiq+SolVesselVesselLiq+SolLiq+SolVesselVesselTempTempVesselVesselPressurePressureInput StreamsInput StreamsFromFromMassMassVolumeVolumeTempTempMassMassVolumeVolumeMassMassVolumeVolumeTempTempToToOutput StreamsOutput Streams(kg)(kg)(liter)(liter)(C)(C)(min)(min)(min)(min)(min)(min)(kg)(kg)(liter)(liter)(C)(C)(kPa)(kPa)(kg)(kg)(liter)(liter)(C)(C)NITROGEN16.6211,616.0025.000.003.003.001.17.Purge unit V009. Purge 3 times with NITROGEN between0.000.0025.00101.33high pressure 1.25 atm and low pressure 0.04 atm for 1min each. Then setup blanket to maintain 101325 Papressure in the unit.ACETONE3,200.004,068.3125.003.009.006.001.18.Charge V009 with 3200 kg of ACETONE. The charge time3,200.004,068.3125.00101.33is 6 min.20.0025.005.001.22.Transfer contents of unit V009 to R006. Transfer 72 kg3,128.003,976.7725.00101.3372.0091.5425.00R0061.22. Transfer-70of vessel contents. The transfer time is 4 min.Transfer using P009.65.0073.008.001.25.Transfer contents of unit V009 to R007. Transfer 80 kg3,048.003,875.0625.00101.3380.00101.7125.00R0071.25. Transfer-86of vessel contents. The transfer time is 8 min.Transfer using P009.1,397.771,402.775.001.62.Transfer contents of unit V009 to MT011. Transfer3,029.153,851.1025.00101.3318.8523.9625.00MT0111.62. Transfer-18318.85 kg of vessel contents. The transfer time is 5min. Transfer using P009.ETHYL-ACETATE893.621,000.0025.002,885.892,900.8915.003.1.Charge V009 with 1000 liter of ETHYL-ACETATE. The3,922.774,851.1025.00101.33charge time is 15 min.StartStartTimeTimeEnd TimeEnd TimeOperationOperationTimeTimeSequenceSequenceNumberNumberR006R006VesselVesselLiq+SolLiq+SolVesselVesselLiq+SolLiq+SolVesselVesselTempTempVesselVesselPressurePressureInput StreamsInput StreamsFromFromMassMassVolumeVolumeTempTempMassMassVolumeVolumeMassMassVolumeVolumeTempTempToToOutput StreamsOutput Streams(kg)(kg)(liter)(liter)(C)(C)(min)(min)(min)(min)(min)(min)(kg)(kg)(liter)(liter)(C)(C)(kPa)(kPa)(kg)(kg)(liter)(liter)(C)(C)NITROGEN1.25871.2025.000.003.003.001.19.Purge unit R006. Purge 3 times with NITROGEN between0.000.0025.00101.33high pressure 1.25 atm and low pressure 0.04 atm for 1min each. Then setup blanket to maintain 101325 Papressure in the unit.1.21. Transfer-67MT00172.0072.4525.0015.0020.005.001.21.Transfer contents of unit MT001 to R006. Transfer 72 72.0072.4525.00101.33kg of vessel contents. The transfer time is 5 min.1.22. Transfer-70V00972.0091.5425.0020.0025.005.001.22.Transfer contents of unit V009 to R006. Transfer 72 kg 144.00163.9925.00101.33of vessel contents. The transfer time is 4 min.Transfer using P009.25.0055.0030.001.23.Heat unit R006 to 30 C. The heating time is 30 min.144.00165.0130.00101.33Use 131.5 C Steam (Low Pressure).55.0065.0010.001.24.Transfer contents of unit R006 to MT005. Transfer 100%0.000.0030.00101.33144.00165.0130.00MT005Mix 1of vessel contents. The transfer time is 10 min. Thetransfer stream is named Mix 1.StartStartTimeTimeEnd TimeEnd TimeOperationOperationTimeTimeSequenceSequenceNumberNumberMT005MT005VesselVesselLiq+SolLiq+SolVesselVesselLiq+SolLiq+SolVesselVesselTempTempVesselVesselPressurePressureInput StreamsInput StreamsFromFromMassMassVolumeVolumeTempTempMassMassVolumeVolumeMassMassVolumeVolumeTempTempToToOutput StreamsOutput Streams(kg)(kg)(liter)(liter)(C)(C)(min)(min)(min)(min)(min)(min)(kg)(kg)(liter)(liter)(C)(C)(kPa)(kPa)(kg)(kg)(liter)(liter)(C)(C)NITROGEN1.661,161.6025.003.006.003.001.20.Purge unit MT005. Purge 3 times with NITROGEN between 0.000.0025.00101.33high pressure 1.25 atm and low pressure 0.04 atm for 1min each. Then setup blanket to maintain 101325 Papressure in the unit.Mix 1R006144.00165.0130.0055.0065.0010.001.24.Transfer contents of unit R006 to MT005. Transfer 100% 144.00165.0129.99101.33of vessel contents. The transfer time is 10 min. Thetransfer stream is named Mix 1.96.00216.00120.001.37.Transfer contents of unit MT005 to R001A. Transfer0.000.0029.99101.32144.00165.0129.99R001A1.37. Transfer-93BATCH PLUS - Step_2_Recipe_Sequence_Diagram.xlsConfidential and ProprietaryPage 2 of 8Step Recipe Sequence DiagramStep Recipe Sequence DiagramProcess (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:3.89 100% of vessel contents. The transfer time is 2 h.StartStartTimeTimeEnd TimeEnd TimeOperationOperationTimeTimeSequenceSequenceNumberNumberR007R007VesselVesselLiq+SolLiq+SolVesselVesselLiq+SolLiq+SolVesselVesselTempTempVesselVesselPressurePressureInput StreamsInput StreamsFromFromMassMassVolumeVolumeTempTempMassMassVolumeVolumeMassMassVolumeVolumeTempTempToToOutput StreamsOutput Streams(kg)(kg)(liter)(liter)(C)(C)(min)(min)(min)(min)(min)(min)(kg)(kg)(liter)(liter)(C)(C)(kPa)(kPa)(kg)(kg)(liter)(liter)(C)(C)1.25. Transfer-86V00980.00101.7125.0065.0073.008.001.25.Transfer contents of unit V009 to R007. Transfer 80 kg 80.00101.7125.00101.33of vessel contents. The transfer time is 8 min.Transfer using P009.1.29. Transfer-101V007160.00179.0525.00117.00125.008.001.29.Transfer contents of unit V007 to R007. Transfer 160 240.00280.7625.00101.33kg of vessel contents. The transfer time is 8 min.Transfer using P009.1.30. Transfer-104MT002160.0083.1225.00125.00130.005.001.30.Transfer contents of unit MT002 to R007. Transfer 160400.00363.8725.00101.33kg of vessel contents. The transfer time is 5 min.130.00160.0030.001.31.Heat unit R007 to 30 C. The heating time is 30 min.400.00366.1330.00101.33Use 131.5 C Steam (Low Pressure).160.00170.0010.001.32.Transfer contents of unit R007 to MT007. Transfer 100%0.000.0030.00101.32400.00366.1330.00MT007Mix3of vessel contents. The transfer time is 10 min. Thetransfer stream is named Mix3.StartStartTimeTimeEnd TimeEnd TimeOperationOperationTimeTimeSequenceSequenceNumberNumberR009R009VesselVesselLiq+SolLiq+SolVesselVesselLiq+SolLiq+SolVesselVesselTempTempVesselVesselPressurePressureInput StreamsInput StreamsFromFromMassMassVolumeVolumeTempTempMassMassVolumeVolumeMassMassVolumeVolumeTempTempToToOutput StreamsOutput Streams(kg)(kg)(liter)(liter)(C)(C)(min)(min)(min)(min)(min)(min)(kg)(kg)(liter)(liter)(C)(C)(kPa)(kPa)(kg)(kg)(liter)(liter)(C)(C)CA LITHIUM62.5062.8925.0073.0077.004.001.26.Charge R009 with 62.5 kg of CA LITHIUM. Material is62.5062.8925.00101.33charged using FM004. The charge time is 4 min.77.00107.0030.001.27.Heat unit R009 to 30 C. The heating time is 30 min.62.5063.2030.00101.33Use 131.5 C Steam (Low Pressure).107.00117.0010.001.28.Transfer contents of unit R009 to MT006. The transfer 0.000.0030.00101.3362.5063.2030.00MT006Mix2time is 10 min. The transfer stream is named Mix2.StartStartTimeTimeEnd TimeEnd TimeOperationOperationTimeTimeSequenceSequenceNumberNumberMT006MT006VesselVesselLiq+SolLiq+SolVesselVesselLiq+SolLiq+SolVesselVesselTempTempVesselVesselPressurePressureInput StreamsInput StreamsFromFromMassMassVolumeVolumeTempTempMassMassVolumeVolumeMassMassVolumeVolumeTempTempToToOutput StreamsOutput Streams(kg)(kg)(liter)(liter)(C)(C)(min)(min)(min)(min)(min)(min)(kg)(kg)(liter)(liter)(C)(C)(kPa)(kPa)(kg)(kg)(liter)(liter)(C)(C)Mix2R00962.5063.2030.00107.00117.0010.001.28.Transfer contents of unit R009 to MT006. The transfer62.5063.1929.96101.33time is 10 min. The transfer stream is named Mix2.216.00336.00120.001.38.Transfer contents of unit MT006 to R001A. Transfer0.000.0029.96101.3362.5063.1929.96R001A1.38. Transfer-112100% of vessel contents. The transfer time is 2 h.StartStartTimeTimeEnd TimeEnd TimeOperationOperationTimeTimeSequenceSequenceNumberNumberMT007MT007VesselVesselLiq+SolLiq+SolVesselVesselLiq+SolLiq+SolVesselVesselTempTempVesselVesselPressurePressureInput StreamsInput StreamsFromFromMassMassVolumeVolumeTempTempMassMassVolumeVolumeMassMassVolumeVolumeTempTempToToOutput StreamsOutput Streams(kg)(kg)(liter)(liter)(C)(C)(min)(min)(min)(min)(min)(min)(kg)(kg)(liter)(liter)(C)(C)(kPa)(kPa)(kg)(kg)(liter)(liter)(C)(C)Mix3R007400.00366.1330.00160.00170.0010.001.32.Transfer contents of unit R007 to MT007. Transfer 100% 400.00366.1330.00101

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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纈沙坦生產(chǎn)工藝流程圖1.dwg---(點擊預(yù)覽)

硫辛酸生產(chǎn)工藝流程圖4.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2.dwg---(點擊預(yù)覽)

硫辛酸生產(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5.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3.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

編號：83168031 類型：共享資源大小：21.82MB 格式：ZIP 上傳時間：2022-05-01

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