裝配圖網(wǎng) > 圖紙設(shè)計 > 畢設(shè)全套 > 大連理工大學-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-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-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-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,DUTER,化工,原料藥,多功能,車間,初步設(shè)計,CAD,圖紙,PDF,文檔 ?Dalian university of technology?DUTER?2014/9/23?S3?2014/10/3?MWG0454-60/50-PV3MWG0455-60/50-PV3PIPIMWG0452-60/50-PV3MWG0453-60/50-PV3PIPIMWG0461-60/50-PV3MWG0462-60/50-PV3PIPIMWG0456-60/50-PV3MWG0457-60/50-PV3PIPIMWG0459-60/50-PV3MWG0460-60/50-PV3PIPIMWG0458-60/50-PV3PIMWG0451-60/50-PV3PIMWG0464-60/50-PV3MWG0465-60/50-PV3PIPIMWG0466-60/50-PV3MWG0467-60/50-PV3PIPIMWG0463-60/50-PV3PIMWG0469-60/50-PV3MWG0470-60/50-PV3PIPIMWG0471-60/50-PV3MWG0472-60/50-PV3PIPIMWG0473-60/50-PV3MWG0474-60/50-PV3PIPIMWG0475-60/50-PV3MWG0476-60/50-PV3PIPIMWG0489-60/50-PV3MWG0490-60/50-PV3PIPIMWG0487-60/50-PV3MWG0488-60/50-PV3PIPIMWG0485-60/50-PV3MWG0486-60/50-PV3PIPIMWG0483-60/50-PV3MWG0484-60/50-PV3PIPIMWG0481-60/50-PV3MWG0482-60/50-PV3PIPIMWG0468-60/50-PV3PIMWG0447-75/65-PV3PIMWG0445-75/65-PV3MWG0446-75/65-PV3PIPIMWG0443-75/65-PV3MWG0444-75/65-PV3PIPIMWG0491-60/50-PV3MWG0492-110/100-PV3PIPIV001V002V003V004V005V006V007V008V009S002R008AR008BMT012M002AM002BR008BR008AE001BR009E001AR007MT001MT002MT003MT005MT006MT007R006MT009E002AE002BMT008BMT004MT008A?E003AE003BR004AR004BMT001MT002V011?VT?T001?MCSR?MCSW?M?V013?E006? X002?PIWW0442-110/100-PVWG0477-60/50-PV3WG0478-60/50-PV3WG0498-60/50-PV3WG0499-110/100-BAWG0500-110/100-PV3WG0448-75/65-PV3WG0449-75/65-PV3WG0450-75/65-PV3WG0479-110/100-PV3WG0480-75/65-PV3WG493-110/100-PV3WG0494-60/50-PV3WG0495-60/50-PV3WG0496-60/50-PV3WG0497-60/50-PV3MPIS003CSR0501-40/32-BACSW0502-40/32-BA148149150151152153154155156157158159160161162163164165166167168169170171172173174175176177178179180181182183184185186187188189190191192PI194PI195WG0503-60/50-PV3V010MT010MT011PI196WG0506-60/50-PV3WG0507-60/50-PV3MMM工程號版次JOB NO.REV圖號設(shè)計階段DRW NO.DESIGN STAGE設(shè)備型號規(guī)格及附件操作/設(shè)計條件數(shù)量凈重(kg)隔熱EQUIPMENT MAIN SPEC AND ACCESSORIESOPER/DESN COND單重總重INSULATION分類設(shè)備型號規(guī)格面積(m2)附件主要介質(zhì)溫度壓力材料單位本期UNIT TOTAL材料厚度NO. SORT EQUIPMENTSERVICEEQUIPMENT MAIN SPEC或 ORACCESSORIESMEDIATEMPPRESSMATLUNITUNITWEIGHT WEIGHT MATLTHKEQUIPMENTINSTALLATIONREMARKS容積(m3)()(MPa)(kg)(kg)(mm)ORIGINDRW NO.12345678910121314161719202122231V011氫氣鋼瓶21921914500.0415鋼個24501200鋼6.3訂購2R001A(B)氫化反應(yīng)釜不銹鋼攪拌鼓泡釜2防爆電機：4kW低壓蒸汽131.50.3不銹鋼個221004200不銹鋼6訂購D1200/1400 H2150 L2920循環(huán)水180.3攪拌形式：直頁圓盤渦輪式攪拌冷凍鹽水-100.3攪拌轉(zhuǎn)速：40r/min夾套蒸汽：管徑DN40，壓力0.3MPa夾套循環(huán)水：管徑DN40，壓力0.3MPa夾套冷凍鹽水：管徑DN40，壓力0.3MPa3R002A(B)反應(yīng)釜93標搪玻璃開式攪拌容器2防爆電機：4kW低壓蒸汽131.50.3搪玻璃個224104820訂購D1300/1450 H2350 L4035循環(huán)水200.3攪拌形式：折頁槳式攪拌器攪拌轉(zhuǎn)速：40r/min夾套蒸汽：管徑DN40，壓力0.3MPa夾套循環(huán)水：管徑DN40，壓力0.3MPa4R006配料釜立式盆蓋底0.3防爆電機：1.0kW循環(huán)水180.3不銹鋼個1750750不銹鋼5訂購D700 H1130 L1920攪拌形式：折頁槳式攪拌器攪拌轉(zhuǎn)速：40r/min夾套循環(huán)水：管徑DN40，壓力0.3MPa5R007配料釜93標搪玻璃開式攪拌容器0.5防爆電機：1.5kW循環(huán)水180.3搪玻璃個110301030訂購D900/1000 H1490 L3040攪拌形式：渦輪式攪拌器攪拌轉(zhuǎn)速：40r/min夾套循環(huán)水：管徑DN40，壓力0.3MPa6R009配料釜立式盆蓋底0.3防爆電機：1.0kW循環(huán)水180.3不銹鋼個1750750不銹鋼5訂購D700 H1130 L1920攪拌形式：折頁槳式攪拌器攪拌轉(zhuǎn)速：40r/min夾套循環(huán)水：管徑DN40，壓力0.3MPa注： 1.本表中壓力（MPa）系表壓；2.D代表公稱直徑，H代表罐體高度，L代表包括攪拌器等輔助設(shè)備的總高度。設(shè)計王曉睿校核趙靜喃DESNCHKD化工原料藥多功能車間工程名稱設(shè)備一覽表設(shè)備來源安裝圖號備注設(shè)備名稱設(shè)備位號1L02初步設(shè)計一、反應(yīng)區(qū)序號設(shè)備工程號版次JOB NO.REV圖號設(shè)計階段DRW NO.DESIGN STAGE設(shè)備型號規(guī)格及附件操作/設(shè)計條件數(shù)量凈重(kg)隔熱EQUIPMENT MAIN SPEC AND ACCESSORIESOPER/DESN COND單重總重INSULATION分類設(shè)備型號規(guī)格面積(m2)附件主要介質(zhì)溫度壓力材料單位本期UNIT TOTAL材料厚度NO. SORT EQUIPMENTSERVICEEQUIPMENT MAIN SPEC或 ORACCESSORIESMEDIATEMPPRESSMATLUNITUNITWEIGHT WEIGHT MATLTHKEQUIPMENTINSTALLATIONREMARKS容積(m3)()(MPa)(kg)(kg)(mm)ORIGINDRW NO.1234567891012131416171920212223化工原料藥多功能車間工程名稱設(shè)備一覽表設(shè)備來源安裝圖號備注設(shè)備名稱設(shè)備位號1L02初步設(shè)計序號設(shè)備7S001A(B)多級離心萃取器MCTL多級離心萃取機0.02電功率7.50kW不銹鋼個2300600訂購最大流量 2100 L/h型號：LX363（理論級數(shù)3）1050 590 7608F001A(B)板框過濾器SHF-3000.7電功率1.10kW不銹鋼個2訂購0.8 m 300處理量4 t/h700 500 8009E001A(B)冷凝器臥式列管冷凝器18.94冷凍鹽水-100.3不銹鋼臺2訂購D500 L2500傾斜安裝10E002A(B)冷凝器臥式列管冷凝器18.94冷凍鹽水-100.3不銹鋼臺2訂購D500 L2500傾斜安裝11MT001-003計量罐立式盆蓋底0.2不銹鋼個3不銹鋼4訂購D500 H113012MT004計量罐搪玻璃開式儲存容器0.2搪玻璃個1280280搪玻璃8訂購D600 H152013MT005-007計量罐立式盆蓋底0.4不銹鋼個3不銹鋼5訂購D700 H133014MT008A(B)計量罐立式橢圓封頭2玻璃鋼個2170340訂購D1200 H245815MT009/013計量罐立式盆蓋底1.5不銹鋼個2不銹鋼6訂購D1000 H218016FM001真空上料機氣動B型0.246不銹鋼臺1訂購輸送量10-22t/h17FM002真空上料機氣動B型0.019不銹鋼臺1訂購輸送量0.4-1.6t/h18FM003真空上料機氣動B型0.085不銹鋼臺1訂購輸送量1.2-8t/h注： 1.本表中壓力（MPa）系表壓；2.D代表公稱直徑，H代表罐體高度，L代表包括攪拌器等輔助設(shè)備的總高度。設(shè)計王曉睿校核趙靜喃DESNCHKD工程號版次JOB NO.REV圖號設(shè)計階段DRW NO.DESIGN STAGE設(shè)備型號規(guī)格及附件操作/設(shè)計條件數(shù)量凈重(kg)隔熱EQUIPMENT MAIN SPEC AND ACCESSORIESOPER/DESN COND單重總重INSULATION分類設(shè)備型號規(guī)格面積(m2)附件主要介質(zhì)溫度壓力材料單位本期UNIT TOTAL材料厚度NO. SORT EQUIPMENTSERVICEEQUIPMENT MAIN SPEC或 ORACCESSORIESMEDIATEMPPRESSMATLUNITUNITWEIGHT WEIGHT MATLTHKEQUIPMENTINSTALLATIONREMARKS容積(m3)()(MPa)(kg)(kg)(mm)ORIGINDRW NO.1234567891012131416171920212223化工原料藥多功能車間工程名稱設(shè)備一覽表設(shè)備來源安裝圖號備注設(shè)備名稱設(shè)備位號1L02初步設(shè)計序號設(shè)備19FM004真空上料機氣動B型0.054不銹鋼臺1訂購輸送量1-5t/h20X001制冰機FM210電功率：0.55kW不銹鋼臺19898訂購210 kg/h690 620 99021V010暫存罐臥式橢圓封頭2玻璃鋼個1228228訂購D1000 L297022P010輸送泵離心泵防爆電機：2kW不銹鋼個1訂購Q22.7m3/h H26.5m465 240 2921R003A(B)濃縮釜立式盆蓋底1防爆電機：4kW低壓蒸汽131.50.3不銹鋼個214002800不銹鋼6訂購D1000/1200 H1580 L2660攪拌形式：直頁圓盤渦輪式攪拌攪拌轉(zhuǎn)速：40r/min夾套蒸汽：管徑DN40，壓力0.3MPa2E003A(B)冷凝器臥式列管式冷凝器18.94冷凍鹽水-100.3不銹鋼臺2訂購D500 L2500傾斜安裝3MT010計量罐立式盆蓋底0.7不銹鋼個1不銹鋼6訂購D900 H14304R004A(B)結(jié)晶釜立式盆蓋底1防爆電機：4kW冷凍鹽水-100.3不銹鋼個214002800不銹鋼6訂購D1000/1200 H1580 L2660攪拌形式：槳式攪拌器攪拌轉(zhuǎn)速：40r/min夾套冷凍鹽水：管徑DN40，壓力0.3MPa5M001A(B)三合一設(shè)備化工級過濾洗滌干燥機2.8電機功率：11kW 低壓蒸汽131.50.3不銹鋼個2580011600訂購DN1600D1600/1900 H44006MT011計量罐立式盆蓋底0.1不銹鋼個1不銹鋼4訂購D400 H880注： 1.本表中壓力（MPa）系表壓；2.D代表公稱直徑，H代表罐體高度，L代表包括攪拌器等輔助設(shè)備的總高度。設(shè)計王曉睿校核趙靜喃DESNCHKD二、濃縮結(jié)晶區(qū)工程號版次JOB NO.REV圖號設(shè)計階段DRW NO.DESIGN STAGE設(shè)備型號規(guī)格及附件操作/設(shè)計條件數(shù)量凈重(kg)隔熱EQUIPMENT MAIN SPEC AND ACCESSORIESOPER/DESN COND單重總重INSULATION分類設(shè)備型號規(guī)格面積(m2)附件主要介質(zhì)溫度壓力材料單位本期UNIT TOTAL材料厚度NO. SORT EQUIPMENTSERVICEEQUIPMENT MAIN SPEC或 ORACCESSORIESMEDIATEMPPRESSMATLUNITUNITWEIGHT WEIGHT MATLTHKEQUIPMENTINSTALLATIONREMARKS容積(m3)()(MPa)(kg)(kg)(mm)ORIGINDRW NO.1234567891012131416171920212223化工原料藥多功能車間工程名稱設(shè)備一覽表設(shè)備來源安裝圖號備注設(shè)備名稱設(shè)備位號1L02初步設(shè)計序號設(shè)備1R005A(B)脫色釜立式盆蓋底1防爆電機：1.5kW 低壓蒸汽131.50.3不銹鋼個214002800不銹鋼6訂購D1000/1200 H1580 L2660攪拌形式：推進式攪拌器攪拌轉(zhuǎn)速：40r/min夾套蒸汽：管徑DN40，壓力0.3MPa2F002A/B微孔液體大正壓過濾器ZJZ-D5000.05不銹鋼個2訂購0.8m500處理量0.8m /h3FM005真空上料機氣動B型0.125不銹鋼臺1訂購輸送量4-15t/h4E004A(B)冷凝器臥式列管式冷凝器18.94冷凍鹽水-100.3不銹鋼臺2訂購D500 L2500傾斜安裝1F003A/B雙層精濾器YF-4000.6不銹鋼個2訂購上層0.8m，下層0.45m400處理量400kg/h2R008A(B)結(jié)晶釜立式盆蓋底1防爆電機：4kW冷凍鹽水-100.3不銹鋼個214002800不銹鋼6訂購D1000/1200 H1580 L2660攪拌形式：槳式攪拌器攪拌轉(zhuǎn)速：40r/min夾套冷凍鹽水：管徑DN40，壓力0.3MPa3M002A(B)三合一設(shè)備無菌級過濾洗滌干燥機1.2電機功率：7.5kW 低壓蒸汽131.50.3不銹鋼個249009800訂購DN1200D1200/1500 H4000注： 1.本表中壓力（MPa）系表壓；2.D代表公稱直徑，H代表罐體高度，L代表包括攪拌器等輔助設(shè)備的總高度。設(shè)計王曉睿校核趙靜喃DESNCHKD四、D級潔凈區(qū)脫色區(qū)三、工程號版次JOB NO.REV圖號設(shè)計階段DRW NO.DESIGN STAGE設(shè)備型號規(guī)格及附件操作/設(shè)計條件數(shù)量凈重(kg)隔熱EQUIPMENT MAIN SPEC AND ACCESSORIESOPER/DESN COND單重總重INSULATION分類設(shè)備型號規(guī)格面積(m2)附件主要介質(zhì)溫度壓力材料單位本期UNIT TOTAL材料厚度NO. SORT EQUIPMENTSERVICEEQUIPMENT MAIN SPEC或 ORACCESSORIESMEDIATEMPPRESSMATLUNITUNITWEIGHT WEIGHT MATLTHKEQUIPMENTINSTALLATIONREMARKS容積(m3)()(MPa)(kg)(kg)(mm)ORIGINDRW NO.1234567891012131416171920212223化工原料藥多功能車間工程名稱設(shè)備一覽表設(shè)備來源安裝圖號備注設(shè)備名稱設(shè)備位號1L02初步設(shè)計序號設(shè)備4C001A/B振動磨WFM-100型0.1電機功率：11kW冷卻水250.3不銹鋼個215003000訂購粉碎細度200-3000 mum20-60kg/h2850 1500 18005MT012計量罐立式盆蓋底0.1不銹鋼個1不銹鋼4訂購D400 H8806X002電子稱TCS-150功率：0.05 KW常溫常壓鋼個220臺面尺寸400 5001V001B儲罐立式橢圓封頭容器0.2不銹鋼個1不銹鋼4訂購D500 H11302V002二乙基鋅儲罐立式橢圓封頭容器0.2不銹鋼個1不銹鋼4訂購D500 H11303V003儲罐立式橢圓封頭容器0.5不銹鋼個1不銹鋼6訂購D700 H14304V004儲罐立式橢圓封頭容器0.5不銹鋼個1不銹鋼6訂購D700 H14305V005儲罐立式橢圓封頭容器0.5搪玻璃個1搪玻璃10訂購D800 H19366V006儲罐立式橢圓封頭容器1.5不銹鋼個1不銹鋼6訂購D1000 H21807V007儲罐立式橢圓封頭容器4不銹鋼個1不銹鋼8訂購D1400 H29808V008乙酸乙酯回收罐立式橢圓封頭容器4不銹鋼個1不銹鋼8訂購D1400 H29809V009儲罐立式橢圓封頭容器4不銹鋼個1不銹鋼8訂購D1400 H298010P001-009輸送泵離心泵防爆電機：2kW不銹鋼個9訂購Q22.7m3/h H26.5m465 240 292注： 1.本表中壓力（MPa）系表壓；2.D代表公稱直徑，H代表罐體高度，L代表包括攪拌器等輔助設(shè)備的總高度。設(shè)計王曉睿校核趙靜喃DESNCHKD儲罐區(qū)五、工程號版次JOB NO.REV圖號設(shè)計階段DRW NO.DESIGN STAGE設(shè)備型號規(guī)格及附件操作/設(shè)計條件數(shù)量凈重(kg)隔熱EQUIPMENT MAIN SPEC AND ACCESSORIESOPER/DESN COND單重總重INSULATION分類設(shè)備型號規(guī)格面積(m2)附件主要介質(zhì)溫度壓力材料單位本期UNIT TOTAL材料厚度NO. SORT EQUIPMENTSERVICEEQUIPMENT MAIN SPEC或 ORACCESSORIESMEDIATEMPPRESSMATLUNITUNITWEIGHT WEIGHT MATLTHKEQUIPMENTINSTALLATIONREMARKS容積(m3)()(MPa)(kg)(kg)(mm)ORIGINDRW NO.1234567891012131416171920212223化工原料藥多功能車間工程名稱設(shè)備一覽表設(shè)備來源安裝圖號備注設(shè)備名稱設(shè)備位號1L02初步設(shè)計序號設(shè)備1S002分水裝置乙醇滲透汽化膜脫水裝置裝機功率：15 KW 低壓蒸汽131.50.3不銹鋼套1訂購ZMA1-EA 7.8+2 L800循環(huán)水180.31000噸/年冷凍鹽水-100.35000 3500 45002S003分水裝置乙酸乙酯滲透汽化膜脫水裝置裝機功率：15 KW 低壓蒸汽131.50.3不銹鋼套1訂購ZMA1-EAC 7.8+2 L800循環(huán)水180.3冷凍鹽水-100.33X003純化水機組500 L/h電機功率：5.5 KW不銹鋼套12000訂購KRM-DRO 500 L6000 5000 30004X004空調(diào)機組ZKW-70電機功率：30 KW不銹鋼套1訂購額定風量70000m /h3100310027005X005冷水機組中低溫螺桿式冷水機消耗電力：40.1KW不銹鋼套11350訂購水溫-10SCY-60 WL制冷量102.9 KW6X006制氮裝置JSN-60套1訂購產(chǎn)量60Nm /h 有效耗氣量2.9Nm /min進口DN40 出口DN322210 12107X007酸度計PHS-2功率：0.01KW個2訂購8X009電子稱TCS-60功率：0.05 KW常溫常壓鋼個212.625.2訂購臺面尺寸300 4009X010電子稱TCS-150功率：0.05 KW常溫常壓鋼個22040訂購臺面尺寸400 500注： 1.本表中壓力（MPa）系表壓；2.D代表公稱直徑，H代表罐體高度，L代表包括攪拌器等輔助設(shè)備的總高度。設(shè)計王曉睿校核趙靜喃DESNCHKD六、共有系統(tǒng)設(shè)備區(qū)?2014/9/23?S1?WW?WW0091-225/200-P3WW0078-60/50-PVWW0079-60/50-PVWW0080-60/50-PVWW0081-60/50-PVWW0082-60/50-PVWW0083-60/50-PVWW0084-60/50-PVWW0085-60/50-PVWW0086-60/50-PVWW0087-60/50-PVWW0061-60/50-PVWW0062-60/50-PVWW0063-60/50-PVWW0059-60/50-PVWW0060-60/50-PVWW0076-60/50-PVWW0077-60/50-PVWW0075-60/50-PVWW0065-60/50-PVWW0066-60/50-PVWW0067-60/50-PVWW0068-60/50-PVWW0069-60/50-PVWW0072-60/50-PVWW0073-60/50-PVWW0074-60/50-PV?WW0090-225/200-P3TW?TW0006-75/65-P3R001BF001AF001BS001AS001BR002AR002BR003AR003BR004AR004BM001AM001BR005AR005BF002AR009R001A?TW0007-75/65-P3R006R007F002BF003AF003BR008AR008BM002AM002BTW0009-60/50-P3TW0008-60/50-P3TW0010-60/50-P3TW0011-60/50-P3TW0012-60/50-P3TW0014-60/50-P3TW0015-60/50-P3TW0016-60/50-P3TW0017-60/50-P3TW0018-60/50-P3TW0019-60/50-P3TW0020-60/50-P3TW0021-60/50-P3TW0025-40/32-BA1TW0026-40/32-BA1TW0027-40/32-BA1TW0023-40/32-BA1TW0024-40/32-BA1TW0028-40/32-BA1TW0029-40/32-BA1TW0030-40/32-BA1TW0031-40/32-BA1TW0032-40/32-BA1TW0033-40/32-BA1TW0036-40/32-BA1TW0037-40/32-BA1TW0038-40/32-BA1PISW0097-76/65-BA?SW0098-76/65-BAMMMMMMMMMMMMMMMMMMR002BF001AF001BS001AS001B?R003AR003BR004AR004BM001AM001BR005AR005BF002AR007R002AR009R006F002BF003AF003BR008AR008BM002AM002BM MMMMMM MM MM MM MM MM M?M MSW?SW?MPIQIMMMMMMMMMMMMMMMMMMMMMMMMMMMMR001BF001AF001BS001AS001BR002AR002BR003AR003BR004AR004BM001AM001BR005AR005BF002AR009R001AR006R007F002BF003AF003BR008AR008BM002AM002BSW0162-76/65-BASW0161-76/65-BATW0039-40/32-BA1SW0130-76/65-BASW0131-76/65-BASW0132-76/65-BASW0133-76/65-BASW0134-76/65-BASW0135-76/65-BASW0136-76/65-BASW0137-76/65-BASW0138-76/65-BASW0139-76/65-BASW0140-76/65-BASW0141-76/65-BASW0142-76/65-BASW0143-76/65-BASW0144-76/65-BASW0145-76/65-BASW0146-76/65-BASW0147-76/65-BASW0148-76/65-BASW0149-76/65-BASW0150-76/65-BASW0151-76/65-BASW0152-76/65-BASW0153-76/65-BASW0154-76/65-BASW0155-76/65-BASW0156-76/65-BASW0102-57/50-BASW0103-57/50-BASW0104-57/50-BASW1109-57/50-BASW0110-57/50-BASW0105-57/50-BASW0106-57/50-BASW0107-57/50-BASW0108-57/50-BASW0111-57/50-BASW0112-57/50-BASW0113-57/50-BASW0114-57/50-BASW0115-57/50-BASW0116-57/50-BASW0117-57/50-BASW0118-57/50-BASW0119-57/50-BASW0120-57/50-BASW0121-57/50-BASW0122-57/50-BASW0123-57/50-BASW0124-57/50-BASW0125-57/50-BASW0126-57/50-BASW0127-57/50-BASW0128-57/50-BATW0040-40/32-BA1TW0041-40/32-BA1TW0042-40/32-BA1TW0043-40/32-BA1TW0044-40/32-BA1TW0045-40/32-BA1TW0046-40/32-BA1TW0047-40/32-BA1TW0048-40/32-BA1TW0049-40/32-BA1TW0050-40/32-BA1TW0051-40/32-BA1?TW0013-60/50-P3TW0034-40/32-BA1TW0035-40/32-BA1MMWW0064-60/50-PVWW0070-60/50-PVWW0071-60/50-PV?R001BR001ASW0100-57/50-BASW0101-57/50-BAM?TW0022-60/50-P3MMTW0052-40/32-BA1TW0053-40/32-BA1WW0089-60/50-PV?WW0088-60/50-PVSW0129-76/65-BAMMSW0099-76/65-BAM MSW0158-76/65-BAM MSW0160-76/65-BA?QISW0157-76/65-BASW0159-76/65-BA?001?002003004 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(shè)計競賽第四屆“國藥工程杯”全國大學生制藥工程設(shè)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(shè)計說明書初步設(shè)計說明書附件附件 3 Aspen batch 模擬結(jié)果目錄模擬結(jié)果目錄 1 硫辛酸模擬結(jié)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(jié)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(jié)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(shè)計含CAD圖紙PDF文檔.zip

車間立面圖、剖面圖.pdf---(點擊預覽)

車間平布置圖例說明.pdf---(點擊預覽)

設(shè)計說明書.pdf---(點擊預覽)

設(shè)備一覽表.xlsx---(點擊預覽)

蒸汽冷凝水系統(tǒng).pdf---(點擊預覽)

純水、廢水、自來水系統(tǒng).pdf---(點擊預覽)

純化水工藝流程圖.pdf---(點擊預覽)

空調(diào)風口布置及氣流流向平面圖.pdf---(點擊預覽)

真空氮氣系統(tǒng).pdf---(點擊預覽)

潔凈空調(diào)流程圖.pdf---(點擊預覽)

廢氣系統(tǒng).pdf---(點擊預覽)

工藝流程圖例說明.pdf---(點擊預覽)

多功能車間第二層平面布置圖.pdf---(點擊預覽)

多功能車間第三層平面布置圖.pdf---(點擊預覽)

多功能車間第一層平面布置圖.pdf---(點擊預覽)

多功能車間平面布置圖.pdf---(點擊預覽)

多功能車間主要設(shè)備平面、立面布置圖.pdf---(點擊預覽)

多功能車間主要管道平面布置圖.pdf---(點擊預覽)

圖紙目錄.pdf---(點擊預覽)

冷卻水和冷凍鹽水分配系統(tǒng).pdf---(點擊預覽)

3D實物展示圖.pdf---(點擊預覽)

PID圖

纈沙坦生產(chǎn)工藝流程圖3.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1.dwg---(點擊預覽)

硫辛酸生產(chǎn)工藝流程圖4.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2.dwg---(點擊預覽)

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(diào)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(shè)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(shè)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(jié)果目錄.pdf---(點擊預覽)

Aspen batch模擬結(jié)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(jié)果目錄.docx--點擊預覽
    - Aspen batch模擬結(jié)果目錄.pdf--點擊預覽
    - 附件3.pdf--點擊預覽
  - 附件1 設(shè)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(shè)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(diào)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
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