西南賽區(qū)重慶super young隊(duì)伍-設(shè)計(jì)集

1、重慶大學(xué)super young2015年乙二醇職責(zé)簽字首頁(yè)圖設(shè)計(jì)項(xiàng)目20萬(wàn)噸乙二醇生產(chǎn)項(xiàng)目設(shè)計(jì)super young設(shè)計(jì)階段初步設(shè)計(jì)階段制圖圖號(hào)校對(duì)審核羨小超審定比例不按第 1 張共 1 張字母第一字母后繼字母被測(cè)變量修飾詞功能A B C D E F G H I L O P Q R S T VW Y成分分析噴嘴火焰電導(dǎo)率 密度電壓流量尺度手動(dòng)液面（或界面）壓力（或真空）速度或頻率溫度重量差比（分?jǐn)?shù)）掃描供選用控制檢出原件玻璃高限指示低限限流積算或打印聯(lián)鎖變送 調(diào)節(jié)閥輔助功能自循環(huán)甲醇儲(chǔ)罐0106至T01020108E0103自原料甲醇儲(chǔ)罐 01050107V0101P01010103R0101

2、自V01020120E0101P0102C0101010T010101110102自原料氣0101E01020110D0101至T0201C0101P0101R0101E0102T0101E0103V0101循環(huán)壓縮機(jī)甲醇進(jìn)料泵列管式反應(yīng)器塔底再沸器 吸收精餾塔塔頂冷凝器塔頂回流罐 E0101P0102D0101預(yù)熱器塔頂回流泵透平機(jī)物料平衡表物流號(hào)010101020103010010501060107010801101110120溫度（）25.0001.519130.000130.00025.0002.20025.0762.11112 . 5725.00036.857壓力（bar）5.200

3、5.2005.1505.1001.0005.1005.1005.1005.0801.050.900汽相分率1.0001.0001.0001.0000.0000.0000.0000.0000.0000.0001.000摩爾流量（kmol/hr）102 .86812698.28112698.28112197.6 110.0001890.6710.0001900.671 00.000632.30011673. 13質(zhì)量流量（kg/hr）28706.96912022.02012022.02012022.020320.17260 87.087320.17260807.25989071.35120259.

4、822383315.051體積流量（cum/hr）872.92663182.20782293.56079857.3 70. 078.3110. 078.715100.26625.55160669.558熱焓（Gcal/hr）-27.007-102.078-92. 39-109.909-0.570-107.016-0.570-107.586-136.380-36.035-75.639組分流量（kg/hr）H20.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.000CO286 5.06058821.83758821.83730187.3670.

5、0000.0000.0000.0000.0260.00030176.777O20.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.000N261.910218713.653218713.653218713.6530.0000.0000.0000.0000.0000.000218651.7 3NO0.00015652. 0915652. 096957.2130.0000.0000.0000.0000.0000.00015652. 09MN0.00097109.5997109.5933 27. 110.0000.0000.0000.0000.00

6、00.00097109.59重慶大學(xué)super young2015年乙二醇CH3OH0.00021712.53321712.53321712.533319.85260366.113319.85260685.96527950.29620259.26121712.533C2H5OH0.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.000設(shè)計(jì)super young偶聯(lián)反應(yīng)和原料再生工段物料流程圖設(shè)計(jì)項(xiàng)目20萬(wàn)噸乙二醇項(xiàng)目DMC0.0000.0000.0001891.6560.0000.0000.0000.0001891.6550.0000.000

7、制圖設(shè)計(jì)階段初步設(shè)計(jì)階段MG0.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.000校核圖號(hào)CQU-SY-0101-01DMO0.0000.0000.00059120.190.0000.0000.0000.00059120.1680.0000.000審核羨小超EG0.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.000審定比例不按第1張共5張H2O0.560至C01010119去火炬自循環(huán)甲醇儲(chǔ)罐 01230117E0107011E0105自原料甲醇儲(chǔ)罐 01120113V0102T01

8、03V0103 P0103至循環(huán)甲醇儲(chǔ)罐P0104P0105一氧化氮0115T01020122氧氣0116自V01010109E0104012廢水處理0118D0102P0103E0104T0102E0105V0102E0106T0103E0107V0103甲醇進(jìn)料泵塔底再沸器 再生反應(yīng)精餾塔塔頂冷凝器塔頂回流罐塔底再沸器 甲醇精餾塔塔頂冷凝器塔頂回流罐物料平衡表P0104D0102P0105塔頂回流泵透平機(jī)塔頂回流泵物流號(hào)0109011201130110115011601170118011901220123012溫度（）5 .05325.00025.00125.07625.00025.000

9、36.857119.33836.85776.26665. 56102.29壓力（bar）5.0001.0001.0005.0005.0008.000.900.900.9001.1501.0501.100汽相分率1.0000.0000.0000.0001.0001.0001.0000.0001.0000.1220.0000.000摩爾流量（kmol/hr）12698.31522.10065 . 0065 . 000.739261. 8211677.500115 .559.087115 .559632.300522.259質(zhì)量流量（kg/hr）383757.928707.58120967. 022

10、0967. 0222.1758365.026383 9.22829663.30313 .20729663.30320252.9669 10.337體積流量（cum/hr）68517.3070.89226. 326. 63.6805. 7360690.7960.86621.2 23532.8927.26310.276熱焓（Gcal/hr）-82.899-1.260-37.295-37.2920.016-0.00-75.666-69.303-0.026-69.303-35.391-3 .922組分流量（kg/hr）H20.0000.0000.0000.0000.0000.0000.0000.000

11、0.0000.0000.0000.000CO30187.3 10.0000.0000.0000.0000.00030187.3 10.00010.5660.0000.0000.000O20.0000.0000.0000.0000.0008350.3760.0000.0000.0000.0000.0000.000N2218713.6530.0000.0000.0000.0001 .650218728.3030.00076.5550.0000.0000.000NO6957.2130.0000.0000.00022.1750.00015657.890.0005. 800.0000.0000.000M

12、N33 27. 110.0000.0000.0000.0000.000971 3.530.0113 .0000.0110.0110.000重慶大學(xué)super young2015年乙二醇CH3OH5 8.202706.87320966.13520966.1350.0000.00021720.158202 7. 17.602202 7. 1202 3.583.831C2H5OH0.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.000設(shè)計(jì)super young偶聯(lián)反應(yīng)和原料再生工段物料流程圖設(shè)計(jì)項(xiàng)目20萬(wàn)噸乙二醇項(xiàng)目DMC0.0000.

13、0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.000制圖設(shè)計(jì)階段初步設(shè)計(jì)階段MG0.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.000校核圖號(hào)CQU-SY-0101-02DMO0.0250.0000.0000.0000.0000.0000.0000.0250.0000.0250.0000.025審核羨小超EG0.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.000審定比例不按第2張共5張H2O2 .0830.70

14、81.2680.0000.00011.9989 15.8520.009 15.8529.3729 06. 81E01060207020至循環(huán)甲醇儲(chǔ)罐E0202E02040203P0206T0201T0202V0202V0201E0206P0201V0203T02040202P0203自D010102010206P0205P0204E0201020502E0203E02050208至DMC儲(chǔ)罐至管路0304E0201T0201E0202V0201E0203T0202E0204V0202E0205T0203P0206V0203塔底再沸器DMO分離塔塔頂冷凝器 塔頂回流罐塔底再沸器 共沸精餾塔 塔頂

15、冷凝器 塔頂回流罐 塔底再沸器 循環(huán)精餾塔循環(huán)泵塔頂回流罐P0201P0202P0203P0204E0206塔頂回流泵加壓泵塔頂回流泵 加壓進(jìn)料泵塔頂冷凝器物料平衡表P0205塔頂回流泵物流號(hào)02010202020302002050206020702080209溫度（）78.69366.2506 .2826 .37670.53270.729138.766183.15816 .517壓力（bar）1.1001.0501.0005.1001.00010.05010.00010.0001.050汽相分率0.2090.0000.0000.0000.0000.0000.0000.0000.000摩爾流量

16、（kmol/hr）1 00.000899.365877.629877.629215.309215.309193.57221.737500.635質(zhì)量流量（kg/hr）89071.35129951.801280 1.395280 1.395823 .636823 .636632 .2301910. 3659119.550體積流量（cum/hr）7756.33639.6 937.6 837.6510.27910.2829.6662. 2061.397熱焓（Gcal/hr）-136.380-52. 09- 9.208- 9.20-1 .5 7-1 .5 5-10.973-2.952-8 .51組分流

17、量（kg/hr）H20.0000.0000.0000.0000.0000.0000.0000.0000.000CO0.0260.0260.0260.0260.0000.0000.0000.0000.000O20.0000.0000.0000.0000.0000.0000.0000.0000.000N20.0000.0000.0000.0000.0000.0000.0000.0000.000NO0.0000.0000.0000.0000.0000.0000.0000.0000.000MN0.0000.0000.0000.0000.0000.0000.0000.0000.000重慶大學(xué)super

18、young2015年乙二醇CH3OH27950.29627950.29627938.91627938.91657 2.98557 2.9855731.60511.3730.000C2H5OH0.0000.0000.0000.0000.0000.0000.0000.0000.000設(shè)計(jì)super young草酸二甲酯和甲醇 分離工段物料流程圖設(shè)計(jì)項(xiàng)目20萬(wàn)噸乙二醇項(xiàng)目DMC1891.6551891.650.0220.0222301. 782301. 7809.8 61891.6670.001制圖設(shè)計(jì)階段初步設(shè)計(jì)階段MG0.0000.0000.0000.0000.0000.0000.0000.00

19、00.000校核圖號(hào)CQU-SY-0201-01DMO59120.1680.6200.0020.0020.6200.6200.0030.61759119.5 9審核羨小超EG0.0000.0000.0000.0000.0000.0000.0000.0000.000審定比例不按第3張共5張H2O109.206109.206102. 29102. 29189.553189.553182.7766.7780.000P02020903110306自P02020300305R0301V03030 11V03020309自T04030 10至T0401P0301C0302V0301P03020308031

20、031203030313氫氣0301C0300310C0302C0301P0301V0301R0301V0302V0303P0302循環(huán)增壓機(jī) 氫氣增壓機(jī)循環(huán)加壓泵閃蒸罐加氫反應(yīng)器閃蒸罐閃蒸罐減壓泵物料平衡表物流號(hào)030103020303030030503060308030903100311031203130310 100 11溫度（）25.000178.33826.036165.38616 .831200.000200.0000.0000.00010.00012.65510.0001.617153.36215 . 57壓力（bar）8.50025.20025.20025.20025.2002

21、5.10025.0002 .8002 .8002 .60025.2002 .6002 .6001.05025.200汽相分率1.0001.0001.0000.0000.0001.0001.0001.0000.0001.0001.0000.0000.0000.0000.000摩爾流量（kmol/hr）2010.2010.25102.663500.6355 2.36256 5.0272 6 . 29232 7.7081396.72123092.21923092.219155. 81552.1691.7291.729質(zhì)量流量（kg/hr）058.0 1058.0 153566.7259119.550

22、63157.167116723.891116723.8915 513.09862210.7939508.689508.68500 .3267215.117037.617037.617體積流量（cum/hr）5893.2213027.91325153.65761. 7665.6 20622.00391 1.852 751.22665.26622 36.58122113.9706.16071.717.11.120熱焓（Gcal/hr）0.002.160-3.221-8 . 75-90.612-56.9 8-71.980-8.502-113.317-5.806-5.380-8.955-122.272

23、-6.1 0-6.137組分流量（kg/hr）H2052. 09052. 0950397. 380.0000.00050397. 3863 5.11563 5.1100.0063 5.03063 5.0300.0000.000.0000.000CO0.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.000O20.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.000N25.6325.632801.2800.000

24、0.000801.280801.280796.0795.202795.6 8795.6 80. 255.6270.0000.000NO0.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.000MN0.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.000重慶大學(xué)super young2015年乙二醇CH3OH0.0000.0002358.520.0000.0002358.523 19.8597282.958271

25、36.9002358.522358.5292 . 3032061.3300.0000.000C2H5OH0.0000.0008.3170.0000.0008.31723.12552. 66370.6598.3178.317.1 91 .8080.0000.000設(shè)計(jì)super young加氫反應(yīng)和預(yù)分離工段物料流程圖設(shè)計(jì)項(xiàng)目20萬(wàn)噸乙二醇項(xiàng)目DMC0.0000.0000.0000.0010.0010.0010.0010.0000.0010.0000.0000.0000.0010.0000.000制圖設(shè)計(jì)階段初步設(shè)計(jì)階段MG0.0000.0000.1210.0002862. 732862.593

26、2876.112. 062863.7380.1210.12112.2862876.022862. 732862. 73校核圖號(hào)CQU-SY-0301-01DMO0.0000.0000.08859119.5 96029 .6 16029 .7291205.8955.3091200.5860.0880.0885.2211205.8071175.0931175.093審核羨小超EG0.0000.0000.0000.0000.0510.05130 89.3069.67230 79.6350.0000.0009.67130 89.3060.0510.051審定比例不按第4張共5張H2O0.0000.00

27、00.9550.0000.0000.955163.1669.09815 .0680.9550.9558.1 3162.2100.0000.000103020 02去火炬V0401E0402E0406T0401至循環(huán)甲醇儲(chǔ)罐E0404T04030 00 03V0403T04020 09去廢液處理P0403自P03020 01V04020 07P0405P04010 06P0404E0405E04010 05E0403至P0301P04020 08去EG儲(chǔ)罐E0401T0401E0402V0401P0403E0403T0402E0404V0402E0405T0403E0406V0403塔底再沸器板

28、式精餾塔塔頂冷凝器 塔頂回流罐循環(huán)加壓泵塔底再沸器EG精餾塔塔頂冷凝器 塔頂回流罐塔底再沸器 板式精餾塔塔頂冷凝器塔頂回流罐 P0401P0402P0404P0405塔頂回流泵升壓泵塔頂回流泵塔頂回流泵物流號(hào)0 010 020 030 00 050 060 070 080 09溫度（）1.57322.00022.00022.081 6.0011 6.013108.29201.36579.607壓力（bar）1.0000.5000.5005.1000.5501.2001.1001.1501.000汽相分率0.0001.0000.0000.0000.0000.0000.0000.0000.000摩

29、爾流量（kmol/hr）1552.1690.001001.7261001.726550. 0550. 059.1 291.29717. 15質(zhì)量流量（kg/hr）67215.1170.0553211 .9 53211 .9 535100.11735100.117601.71730 98. 0056 .300體積流量（cum/hr）71.7130.180.3230.32835.11735.118.5632.3220.705熱焓（Gcal/hr）-122.3090.000-57.165-57.160-58.87-58.873-7.379-50.33-1.175組分流量（kg/hr）H20.000.

30、000.0000.0000.0000.0000.0000.0000.000CO0.0000.0000.0000.0000.0000.0000.0000.0000.000O20.0000.0000.0000.0000.0000.0000.0000.0000.000N25.6270.0175.6105.6100.0000.0000.0000.0000.000NO0.0000.0000.0000.0000.0000.0000.0000.0000.000MN0.0000.0000.0000.0000.0000.0000.0000.0000.000重慶大學(xué)super young2015年乙二醇CH3OH

31、32061.3300.035320 2.976320 2.97618.32018.32018.3200.00018.320C2H5OH1 .8080.0006 .6026 .602350.206350.206350.2060.000350.207設(shè)計(jì)super young乙二醇提純工段物料流程圖設(shè)計(jì)項(xiàng)目20萬(wàn)噸乙二醇項(xiàng)目DMC0.0010.0000.0000.0000.0010.0010.0010.0000.001制圖設(shè)計(jì)階段初步設(shè)計(jì)階段MG2876.020.0000.0000.0002876.022876.022876.0110.01313.7 9校核圖號(hào)CQU-SY-0401-01DMO1

32、205.8070.0000.0000.0001205.8071205.8071196.6769.13021.569審核羨小超EG30 89.3060.0000.0000.00030 89.30630 89.3060.0 930 89.2570.000審定比例不按第5張共5張H2O162.2100.0001.7571.757160. 53160. 53160. 530.000160. 5FT 0101FIC 0101自循環(huán)甲醇儲(chǔ)罐PG01006-250-L1B至T0101PL01008-250-L1BFT 0102FIC 0102PL01007-25-L1BPI 0101自原料甲醇儲(chǔ)罐PI 01

33、02P0101A/BPG01003-2000-L1B-HC.S.OPG01005-25-L1BR0101自R0301TIA 0101 FIC 010TIA 0102FIC 0103TIC 0101TIA 0103FT 010LT 0101LIA 0101PT 0101PIC 0101自原料氣PG01001-700-L1BFT 0103TT 0101FT 0105FIC 0105E0101至T0101PT 0102 PIC0102C.S.O自V0102PG01020-2000-L1BPG 0101PG 0102TG 0101TG 0102至V0302C0101甲醇進(jìn)料泵換熱器E0101列管式反應(yīng)

34、器P0101A/BR0101循環(huán)壓縮機(jī)重慶大學(xué)super young2015年乙二醇C0101設(shè)計(jì)項(xiàng)目 20萬(wàn)噸乙二醇項(xiàng)目設(shè)計(jì)super young制圖偶聯(lián)反應(yīng)和 原料再生工段設(shè)計(jì)階段初步設(shè)計(jì)階段校核圖號(hào)CQU-SY-0101-01審核羨小超第1張共16張審定比例不按PG01002-2000-L1BPL01011-150-L1B壓縮空氣回管壓縮空氣上管PG0101-2000-L1BFIC 0110TIC 0103T0101C.S.OPI 0110FT 0107FIC 0107自管路PG01008-250-L1BTI 0103PI 0105FT 0110E0103至T0102PG01009-20

35、00-L1B103 T103PI 0106V0101TI 010PDI 0101FIC 0109LICA 0101LT 0103TI 0102PI 010自R0101TE 0101FT 0109PL0101-150-L1BPI 0108 TTPI0102 0103TI 0101TIC 0102PI 0107PG0101-600-L1BP0102A/BLG 0101LT 0102LIA 0102 FT0106FIC 0106E0102PI 0109至T0201FT 0108FIC 0108C.S.OPG 0103TG 010TG 0103PL0101-350-L1BD0101中壓飽和蒸汽上管蒸汽

36、冷凝水回管再沸器吸收精餾塔冷凝器回流罐E0102T0101E0103V0101重慶大學(xué)super young2015年乙二醇設(shè)計(jì)項(xiàng)目 20萬(wàn)噸乙二醇項(xiàng)目設(shè)計(jì)super young回流泵透平機(jī)制圖偶聯(lián)反應(yīng)和 原料再生工段設(shè)計(jì)階段初步設(shè)計(jì)階段P0102A/BD0101校核圖號(hào)CQU-SY-0101-02審核羨小超第2張共16張審定比例不按MS0101-1600-L1BSC0101-1600-L1BPGL0101-2000-L1BPL01010-350-L1BPG 010PL0101-200-L1BPG01004-2000-L1BTT 010325循環(huán)冷卻水回水25循環(huán)冷卻水上水PL01012-40

37、-L1B自原料甲醇儲(chǔ)罐自V0103PG0102-2000-L1BFIC 0115TIC 0105至C0101T0102PI 0116C.S.OFT 0111FIC 0111TIPI0115FT 0115PL01014-125-L1B0105E0105PG01019-50-L1B 廢氣處理PL01014-125-L1BPIC 0106PT 0106PI 0112PI 0111P0103A/BTT 0105PGL0102-2000-L1BV0102PI 0117PDI 0102FIC 0113LICA 0102LT 0105FT 0113TI 0108PL0102-300-L1BTE 0102TI

38、 0106PI 0113PL01013-200-L1BPT 0105PIC 0105NOPG01015-20-L1BPI 0119TIC 010TT 010TI 0107PI 011PI 0118自T0101PG0102-600-L1BP0104A/BLIA 0103LG 0102LT 010FIC 0112FT 0112E0104PT 010PIC 010O2PI 0120PG01016-500-L1BPL0102-400-L1B至T0103PG01022-200-L1BFIC 011FT 011C.S.OPL01018-200-L1BTG 0106TG 0105PL0102-250-L1B

39、D0102中壓飽和蒸汽上管蒸汽冷凝水回管甲醇進(jìn)料泵再沸器冷凝器回流罐V0102再生反應(yīng)精餾塔E0104E0105P0103A/BT0102重慶大學(xué)super young2015年乙二醇透平機(jī) D0102回流泵設(shè)計(jì)項(xiàng)目 20萬(wàn)噸乙二醇項(xiàng)目設(shè)計(jì)super youngP0104A/B制圖偶聯(lián)反應(yīng)和 原料再生工段設(shè)計(jì)階段初步設(shè)計(jì)階段校核圖號(hào)CQU-SY-0101-03審核羨小超第3張共16張審定比例不按MS0102-450-L1BSC0102-450-L1BPG01017-2000-L1BPG 0105PG 010625循環(huán)冷卻水回水25循環(huán)冷卻水上水PG0103-1800-L1BFIC 0120TI

40、C 0108T0103C.S.OPI 0123FT 0120E0108TT 0108PI 012 FIC 0116FT 0116PGL0103-300-L1BPDI 0103 FIC 0118TI 0111TI 0110PI 0121V0103自D0102TE 0103FT 0118PL0103-200-L1BLT 0107LIC 0103TIC 0107至管路PL01013-200-L1BPL01023-200-L1B自E0203PI 0126TT 0106TIC 0106PI 0122TI 0109FIC 0117FT 0117PG0103-1600-L1BPI 0125P0105A/BL

41、G 0103LT 0106LIA 010E0107E0106PI0127PL0103-250-L1BPL0103-200-L1BFIC 0119FT 0119TT 0107PL01024-125-L1B廢水處理至V0203高壓飽和蒸汽上管蒸汽冷凝水回管再沸器冷凝器回流罐再沸器甲醇精餾塔E0106T0103E0108V0103E0107重慶大學(xué)super young2015年乙二醇回流泵設(shè)計(jì)項(xiàng)目 20萬(wàn)噸乙二醇項(xiàng)目設(shè)計(jì)super youngP0105A/B制圖偶聯(lián)反應(yīng)和 原料再生工段設(shè)計(jì)階段初步設(shè)計(jì)階段校核圖號(hào)CQU-SY-0101-0審核羨小超第4張共16張審定比例不按HS0103-1600-

42、L1BSC0103-1600-L1B25循環(huán)冷卻水上水25循環(huán)冷卻水回水PG0201-1800-L1BFIC 0205TIC 0202T0201C.S.OPI 0205FT 0205E0202TT 0202PI 020FIC 0201FT 0201PDI 0201 FIC 020TI 0203TE 0201TI 0201PI 0201V0201自D0101FT 020PGL02001-300-L1BPL0201-200-L1BLT 0202LIC 0201PL02002-250-L1B至T0202PI 0207TIC 0201TT 0201PI 0202TI 0202P0201A/BPI 02

43、03PG0201-1800-L1BLG 0201LT 0201LIA 0201FIC 0202FT 0202E0201PI 0206PL0201-250-L1BPI 0208PI 0209P0202A/BFIC 0203FT 0203PL02009-350-L1BPG0201-450-L1B高壓飽和蒸汽上管蒸汽冷凝水回管再沸器DMO分離塔加壓泵回流泵冷凝器E0201T0201P0201A/BE0202P0202A/B重慶大學(xué)super young2015年乙二醇設(shè)計(jì)項(xiàng)目 20萬(wàn)噸乙二醇項(xiàng)目設(shè)計(jì)super young回流罐草酸二甲酯和甲醇分離工段制圖設(shè)計(jì)階段初步設(shè)計(jì)階段V0201校核圖號(hào)CQU-

44、SY-0201-01審核羨小超第5張共16張審定比例不按HS0201-600-L1BSC0201-600-L1BPGL0201-300-L1B25循環(huán)冷卻水回水25循環(huán)冷卻水上水PG0202-1600-L1BFIC 0209TIC 020T0202C.S.OPI 0212FT 0209E0204至V0203TT 020PI 0213PDI 0202 FIC 0208TI 0206TI 0205PI 0211V0202TE 0202至V0201FT 0208PL0202-150-L1BLT 020LIC 0202至循環(huán)甲醇儲(chǔ)罐PI 0216PI 0218TIC 0203TTPI0203 0210

45、TI 020P0203A/BPI 021PG0202-1400-L1BLG 0202LT 0203LIA 0202FIC 0206FT 0206E0203P0204A/BPI至T02030215PL0202-200-L1BPI0217PL02004-200-L1BFIC 0207FT 0207至P0204PL02005-125-L1BPL0202-250-L1B至E0107再沸器共沸精餾塔回流泵冷凝器循環(huán)泵重慶大學(xué)super young2015年乙二醇E0203T0202P0203A/BE0204P0204A/B設(shè)計(jì)項(xiàng)目 20萬(wàn)噸乙二醇項(xiàng)目設(shè)計(jì)super young回流罐 V0202制圖草酸二

46、甲酯和甲醇分離工段設(shè)計(jì)階段初步設(shè)計(jì)階段校核圖號(hào)CQU-SY-0201-02審核羨小超第6張共16張審定比例不按PGL0202-250-L1BPL02003-250-L1B至E0203PG0203-500-L1BC.S.OPI 0222自E0107FT 0210FIC 0210自T0202TI 0207PI 0221PL02006-80-L1BPI 0219PI 0220PI 0223P0205A/BLT 0206LIC 0203PDI 0203 FIC 0213TI 0208TE 0203至T0202FT 0213PL02007-100-L1BPL0203-200-L1BPI 0226TIC

47、0205TTPI0205 0227TI 0209PI 022P0206A/BPG0203-500-L1BLG 0203LT 0205LIA 0203FT 0211FIC 0211E0205PI0225PL0203-250-L1BFT 0212FIC 0212自V0102PL02008-65-L1BPL0203-350-L1B高壓飽和蒸汽上管蒸汽冷凝水回管加壓進(jìn)料泵再沸器循環(huán)精餾塔回流泵回流罐E0205T0203P0106A/BV0203P0205A/B重慶大學(xué)super young2015年乙二醇設(shè)計(jì)項(xiàng)目 20萬(wàn)噸乙二醇項(xiàng)目設(shè)計(jì)super young草酸二甲酯和甲醇分離工段制圖設(shè)計(jì)階段初步設(shè)計(jì)

48、階段校核圖號(hào)CQU-SY-0201-03審核羨小超第7張共16張審定比例不按HS0203-600-L1BSC0203-600-L1BPGL0203-200-L1BV0203T0203PG03005-200-L1BFTFIC03010301自P0202A/BPG03004-200-L1BFTFIC03020302PL04011-50-L1BPI 0301自T0403P0301A/BPI0302PG03006-2000-L1B至R0301PL04010-65-L1B自E0404V0301C.S.OC0301TGTG03010302PGPGFICTIC自V03030301030203030301C.

49、S.OFT 0303TTPG03003-2000-L1B0301主產(chǎn)物EGPG03011-2000-L1BE0301PG03002-900-L1BPTPIC03010301C.S.OH2PG03001-800-L1BPGPG0303030FICTIC0300301TGTG0303030TTFT0301030C0302至V0403E0302自T0403閃蒸罐V0301循環(huán)加壓泵P0301A/B換熱器E0301循環(huán)增壓機(jī)C0301氫氣增壓機(jī)換熱器C0302E0302重慶大學(xué)super young2015年乙二醇設(shè)計(jì)super young加氫反應(yīng)和預(yù)分離工段設(shè)計(jì)項(xiàng)目20萬(wàn)噸乙二醇項(xiàng)目制圖設(shè)計(jì)階段初步

50、設(shè)計(jì)階段校核圖號(hào)CQU-SY-0301-01審核羨小超審定比例不按第8張共16張PG03012-100-L1BPTPIC030030至C0301PG03010-2000-L1BV0303PTPIC03030303PG03008-2000-L1BFTFIC03050305自E0101V0302FT 0308PTPIC03020302自V0301FIC0308FTFIC03060306PG03009-300-L1B至T0401R0301PI 0303PIP0302A/B030TI 0301TIA 0302TIALTLIA030303010301PG03013-300-L1BFTFIC0307030

51、7PG03007-2000-L1B至E0101加氫反應(yīng)器閃蒸罐閃蒸罐減壓泵R0301V0302V0303P0302A/B重慶大學(xué)super young2015年乙二醇設(shè)計(jì)super young加氫反應(yīng)和預(yù)分離工段設(shè)計(jì)項(xiàng)目20萬(wàn)噸乙二醇項(xiàng)目制圖設(shè)計(jì)階段初步設(shè)計(jì)階段校核圖號(hào)CQU-SY-0301-02審核羨小超審定比例不按第9張共16張-25制冷劑回管-25制冷劑上管PG0401-2000-L1BTIC 0 03FIC 0 0T0401C.S.OPI0 03FT0 0E0403至火炬PG04002-10-L1B PIC 0 02V0401PT0 02TT0 03PGL0401-400-L1BPI0

52、 0PT0 01PIC 0 01PDI 0 01 FIC 0 03LT0 02LICA 0 01TI0 03TI0 01PI0 01自P0302A/BTE0 01FT0 03PL0401-250-L1BTIC 0 01自T0402PI0 06TIC 0 02TT0 02PI0 02TI0 02PI0 05PG0401-2000-L1BP0401A/BFIC 0 01FT0 01LG0 01LT0 01LIA 0 01E0402E0401PI0 08至循環(huán)甲醇儲(chǔ)罐PI0 07P0402A/BPL0401-400-L1BPI0 09PL04004-150-L1BFIC 0 02FT0 02至P04

53、02TT0 01PL04005-250-L1B至V0402高壓飽和蒸汽上管蒸汽冷凝水回管再沸器再沸器板式精餾塔冷凝器回流罐循環(huán)加壓泵E0401E0402E0403T0401V0401P0402A/B重慶大學(xué)super young2015年乙二醇回流泵設(shè)計(jì)項(xiàng)目 20萬(wàn)噸乙二醇項(xiàng)目P0401A/B設(shè)計(jì)super young制圖設(shè)計(jì)階段初步設(shè)計(jì)階段乙二醇提純工段校核圖號(hào)CQU-SY-0 01-01審核羨小超第10張共16張審定比例不按HS0401-450-L1BSC0401-450-L1BPL04003-250-L1BPL0401-350-L1BPL04001-200-L1B至E0402PG0402

54、-1600-L1BC.S.OPI自T0401自E0402PGL0402-300-L1BPI FIC 0 05FT0 05PI0 10PDIFIC 0 07TI0 06TI0 0PI0 12TEFT0 07PL0402-250-L1BP0403A/BLT0 0LICA 0 03至T0403PL04007-65-L1B-CPI0 11PI 0PL04006-150-L1BTIC 0TT0 0PI 0TI0 05P0404A/BPIPG0402-1600-L1BLG0 02FIC 0 06FT0 06PIE0404PL0402-300-L1BLT0 03LICA 0 02PL0402-350-L1B

55、至E0301PL04008-200-L1B高壓飽和蒸汽上管蒸汽冷凝水回管釜式換熱器回流泵加壓泵EG精餾塔回流罐E0404T0402V0402P0403A/BP0404A/B重慶大學(xué)super young2015年乙二醇設(shè)計(jì)項(xiàng)目 20萬(wàn)噸乙二醇項(xiàng)目設(shè)計(jì)super young制圖設(shè)計(jì)階段初步設(shè)計(jì)階段乙二醇提純工段校核圖號(hào)CQU-SY-0 01-02審核羨小超第11張共16張審定比例不按HS0402-1600-L1BSC0402-1600-L1BV0402T0402至E0302PG0403-600-L1BT0403C.S.OPI自E0302PGL0403-100-L1BPIPDI 0 0 FIC 0

56、 09TI0 09PI 0TI0 07TE0 03自V0402FT0 09PL0403-65-L1BLT0 06LICA 0 0PL04009-25-L1B 廢液處理PI0 2TIC 0 05TT0 05PITI0 08P0405A/BPI0 23PG0403-700-L1BLG0 03LT0 05LI 0 02FIC 0 08FT0 08E0405PI0 25PL0403-100-L1BFIC 0 10FT0 10至PO3O1A/BPL0403-150-L1B高壓飽和蒸汽上管蒸汽冷凝水回管再沸器板式精餾塔回流泵回流罐E0405T0403P0405A/BV0403重慶大學(xué)super young

57、2015年乙二醇設(shè)計(jì)項(xiàng)目 20萬(wàn)噸乙二醇項(xiàng)目設(shè)計(jì)super young制圖設(shè)計(jì)階段初步設(shè)計(jì)階段乙二醇提純工段校核圖號(hào)CQU-SY-0 01-03審核羨小超第12張共16張審定比例不按HS0403-900-L1BSC0403-900-L1BV0403N2自真空系統(tǒng)來(lái)噴淋水至火炬系統(tǒng)至火炬系統(tǒng)PI PICA 0501 0501PIPICA0502 0502LI 0502LIA 0502V0501BLI 0501LIA 0501V0501A LIC 0501FT 0501FIC 0501自E0301FT 0502 LIC 0502主產(chǎn)物乙二醇產(chǎn)品罐主產(chǎn)物乙二醇產(chǎn)品罐重慶大學(xué)super young20

58、15年乙二醇V0501AV0501B設(shè)計(jì)super young設(shè)計(jì)項(xiàng)目 20萬(wàn)噸乙二醇項(xiàng)目制圖設(shè)計(jì)階段初步設(shè)計(jì)階段罐區(qū)校核圖號(hào)CQU-SY-0501-01審核羨小超第13張共16張審定比例不按C.S.OC.S.OFIC0502C.S.ON2自真空系統(tǒng)來(lái)噴淋水至火炬系統(tǒng)PI PICA 0503 0503V0502LG 0501LI LIA0503 0503LG 0502LG 0503LIC自P0 02A/B0503FT FIC 05030503至管路自P020 A/BPG-01006-250-L1B循環(huán)甲醇儲(chǔ)罐 V0502重慶大學(xué)super young2015年乙二醇設(shè)計(jì)super young罐

59、區(qū)設(shè)計(jì)項(xiàng)目20萬(wàn)噸乙二醇項(xiàng)目制圖設(shè)計(jì)階段初步設(shè)計(jì)階段校核圖號(hào)CQU-SY-0501-02審核羨小超審定比例不按第14張共16張N2自真空系統(tǒng)來(lái)噴淋水至火炬系統(tǒng)至火炬系統(tǒng)PI PICA 050050PI PICA0505 0505V0503AV0503BLG 050LG 0507LI 050LIA 050LI LIA0505 0505LG 0505LG 0508LG 0506LG 0509LIC 050 FIC 050FT 050自原料廠至P0103A/B LIC 0505FT 0505FIC 0505至P0101A/B自原料廠原料甲醇儲(chǔ)罐原料甲醇儲(chǔ)罐V0503BV0503A重慶大學(xué)super

60、young2015年乙二醇設(shè)計(jì)super young設(shè)計(jì)項(xiàng)目 20萬(wàn)噸乙二醇項(xiàng)目制圖設(shè)計(jì)階段初步設(shè)計(jì)階段罐區(qū)校核圖號(hào)CQU-SY-0501-03審核羨小超第15張共16張審定比例不按C.S.OC.S.ON2自真空系統(tǒng)來(lái)噴淋水至火炬系統(tǒng)至火炬系統(tǒng)PI PICA0506 0506PI PICA0507 0507V0504AV0504BLG 0510LG 0513LI LIA0506 0506LI LIA0507 0507LG 0511LG 051LG 0512LG 0515LIC 0506FT 0506FIC 0506自E0301 LIC 0507FT 0507FIC 0507次產(chǎn)品DMC產(chǎn)品罐次