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 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
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