西南赛区-重庆科技学院tnt团队作品设计集源文件附录

1、附录 1 物料一览表1.1 一氧化碳偶联草酸二甲酯工段1.1.1 羰化偶联反应器（R0101）流进物料流出物料1355179141753604.392-67.723476135517499.29456257635.1750745.4746-82.943507温度 压力 bar气相分率摩尔流率 kmol/hr质量流量体积流量kg/hrm3/hr质量流量kg/hr0115521.82156430.2064013584.36450.009182440.132897699569.1223262529.51449.32E-250048992.9195115521.8213214

2、0.9487040726.17443368.098650.132897699569.122327315.95318000草酸二甲酯氮气一氧化碳氢气一氧化氮 碳酸二甲酯水甲醇 亚硝酸甲酯氧气 乙二醇乙醇酸甲酯摩尔流率 kmol/hr草酸二甲酯氮气 一氧化碳氢气 一氧化氮 碳酸二甲酯水 甲醇亚硝酸甲酯氧气乙二醇乙醇酸甲酯04123.7942014.616230452.7194931.02E-047.38E-03298.6416121024.396232.91E-2600414.8804714123.7941147.4648201357.2613637.39056427.38E-03298.6416

3、12119.8543580001.2 草酸二甲酯和碳酸二甲酯分离工段21.2.1 草酸二甲酯分离塔（T0201）流进物料流出物料温度 压力 bar气相分率摩尔流率 kmol/hr155.10358.170511476.5414.26179-20.49736750.9275197499.295257635.239286.24-94.243116.211964250353.40862911539.494814.2118625-1.97E+0138.52724.917091.735207133.137320.63-26.601643.884854.98401119.16373518.9174.464

4、25-107.802质量流量体积流量kg/hrm3/hr质量流量kg/hr草酸二甲酯氮气一氧化碳氢气一氧化氮 碳酸二甲酯水甲醇 亚硝酸甲酯氧气乙二醇乙醇酸甲酯 摩尔流率 kmol/hr草酸二甲酯氮气一氧化碳氢气一氧化氮 碳酸二甲酯水甲醇 亚硝酸甲酯氧气 乙二醇乙醇酸甲酯0000000.018015.53000048992.92115521.832140.95040726.173368.0990.1328989569.1227315.953000081.467558932.1116863030.42583850.030591950.0045991810903.0904492.364163000.

5、00E+001.68E-33114426.831228.42038526.140.0426140.00513515660.867290.81900048992.921176.486944.645102230.4653368.0870.16288.62517.5360000000001.00E-03358.16950000414.88054123.7941147.46501357.26137.390567.38E-03298.6416119.854400002.908155611.1464201301.013987093.40E-042.55E-04340.2732648.06620673000

6、1.42E-354084.7051114.88701283.9424.73E-042.85E-04488.7579119.4426000414.880541.9971533.7248074.3336337.390438.35E-03508.34988.4785870001.2.2 冷凝罐（V0201）流进物料流出物料温度 压力 bar气相分率摩尔流率 kmol/hr16.24.80.9501667091.73516.24.8000010353.408616.24.80000116738.3263207133.133640.26-30.908211539.4914.21161-19.661719

7、5593.633626.05-11.2465质量流量体积流量kg/hrm3/hr质量流量kg/hr草酸二甲酯氮气一氧化碳氢气一氧化氮 碳酸二甲酯水甲醇 亚硝酸甲酯氧气 乙二醇乙醇酸甲酯摩尔流率 kmol/hr草酸二甲酯氮气 一氧化碳氢气 一氧化氮 碳酸二甲酯水 甲醇亚硝酸甲酯氧气乙二醇乙醇酸甲酯1.68E-33114426.831228.42038526.140.0426140.00513515660.867290.819000081.4675632.11169030.425840.0305920.00459910903.09492.36420000114345.331196.31038495

8、.710.0120225.36E-044757.7696798.4550001.42E-354084.7051114.88701283.9424.73E-042.85E-04488.7579119.442600002.9081561.1464201.01E3.40E-042.55E-04340.27338.06620700004081.7971113.740.928 1.33E-042.98E-05148.4847111.37640001.2.3 草酸二甲酯分离塔（T0202）流进物料流出物料温度 压力 bar气相分率摩尔流率 kmol/hr43.884854.98401119.1637351

9、8.9174.46425-107.802227.10844.9340414.887748993.5756.57251-68.5093101.74984.91704.275524525.354313.804-28.3709质量流量体积流量kg/hrm3/hr质量流量kg/hr草酸二甲酯氮气48992.921176.48648992.921.02E-279.18E-041176.48649.45E+020.00E+002230.4653.37E+031.50E-011.63E+04517.5360001.64E-3103.31E-230.6499643.39E-211.74E-089.37E-11

10、000.00E+00944.645102230.4653367.437062517.536000一氧化碳氢气一氧化氮 碳酸二甲酯水甲醇 亚硝酸甲酯氧气 乙二醇乙醇酸甲酯摩尔流率 kmol/hr草酸二甲酯氮气 一氧化碳氢气 一氧化氮 碳酸二甲酯水 甲醇亚硝酸甲酯氧气乙二醇乙醇酸甲酯414.880541.997153.37E+010.00E+0074.333633.74E+018.35E-035.08E+028.478587000414.88053.65E-295.84E-3301.10E-247.22E-031.88E-225.44E-101.53E-120007.78

11、E-0641.9971533.7248074.3336337.383218.35E-03508.34988.4785870001.2.4 气体回收塔（T0203）流进物料流出物料温度 压力 bar气相分率摩尔流率 kmol/hr101.7497574.91704.27550524525.34534313.80399-2.84E+0158.992124.851257.82138050.8241438.769-4.12932111.65194.9090446.454216474.5222.85949-27.6459质量流量体积流量kg/hrm3/hr质量流量kg/hr草酸二甲酯氮气一氧化碳氢气一氧

12、化氮 碳酸二甲酯水9.18E-041176.48644944.64505302.23E3.37E+031.50E-011.96E-231.18E+039.45E+020.4650.490646.58E-129.18E-047.83E-172.97E-2307.60E-213366.9460.150375516288.6246517.535991000.00E+003.18E5.18E+02000.00E+00.42 7.86E-05000甲醇 亚硝酸甲酯氧气乙二醇乙醇酸甲酯 摩尔流率 kmol/hr草酸二甲酯氮气一氧化碳氢气一氧化氮 碳酸二甲酯水甲醇 亚硝酸甲酯氧气 乙二醇乙醇酸甲酯7.78E

13、-0641.997154133.72479707.43E+013.74E+018.35E-03508.3497698.478586810001.66E-254.20E+013.37E+01074.333635.45E-033.65E-139.93E8.48E+000007.78E-062.80E-181.06E-2402.53E-2237.377778.35E-03.0681 1.29E-060001.2.5甲醇回收塔（T0204）流进物料流出物料106.622410.30909.101531433.6944.32259-53.2755138.65615310.2360500.00580818

14、320.316127.-3.03E+01136.8153101409.095713113.37.403-19.1942温度 压力 bar气相分率摩尔流率 kmol/hr质量流量体积流量kg/hrm3/hr质量流量kg/hr草酸二甲酯氮气一氧化碳氢气一氧化氮 碳酸二甲酯水甲醇 亚硝酸甲酯氧气 乙二醇乙醇酸甲酯摩尔流率 kmol/hr9.75E-033.52E-181.30E-1701.37E-203576.3921.51E-0127857.147.87E-05000.00E+009.75E-030000.00E+003568.530841.51E-0114751.62492.00E-08000.

15、00E+002.67E-2500007.8609793.50E-1013105.517.86E-0500068.26E-051.26E-194.63E-1904.58E-2239.702918.36E-03869.39011.29E-060008.26E-050000.00E+0039.61563938.36E-03460.3817263.28E-100002.26E-2700000.0872681.94E-11409.00841.29E-06000草酸二甲酯氮气一氧化碳氢气一氧化氮 碳酸二甲酯水甲醇 亚硝酸甲酯氧气 乙二醇乙醇酸甲酯1.2.6 碳酸二甲酯分离塔（T0205）流进物料流出物料温

16、度 压力 bar气相分率摩尔流率 kmol/hr138.660410.30500.005818320.3227.13778-30.3452183.95518710.236037.39983453362.572454.26364603-5.17E+00136.8665100462.60614957.7423.26925-25.1424质量流量体积流量kg/hrm3/hr质量流量kg/hr9.75E-0300003568.5311.51E-0114751.622.00E-08000.00E+009.75E-0300003359.231081.50E-013.181246651.60E-17000.

17、00E+002.93E-090000209.29982.36E-0414748.442.00E-08000草酸二甲酯氮气一氧化碳氢气一氧化氮 碳酸二甲酯水甲醇 亚硝酸甲酯氧气乙二醇乙醇酸甲酯 摩尔流率 kmol/hr草酸二甲酯氮气一氧化碳氢气一氧化氮碳酸二甲酯8.26E-05000039.615648.26E-050000.00E+0037.29212192.48E-1100002.32351778.36E-03460.38173.28E-100008.35E-030.099283152.63E-190001.31E-05460.28243.28E-10000水 甲醇亚硝酸甲酯氧气乙二醇乙醇酸

18、甲酯1.3 亚硝酸甲酯再生工段1.3.1 反应精馏塔（T0301）流进物料流出物料45517643.946224374.640225.41-33.3154355.101239.93839556.3750.60664-70.4987119.08354.850114029964.441.67413-67.629930.86784.8517059.884233966.636496.93-52.0262温度 压力 bar气相分率摩尔流率 kmol/hr质量流量体积流量kg/hrm3/hr质量流量kg/hr草酸二甲酯氮气一氧化碳氢气一氧化氮 碳酸二甲酯水甲醇 亚硝酸甲酯氧气乙二醇乙醇酸甲酯 摩尔流率 k

19、mol/hr草酸二甲酯氮气一氧化碳氢气一氧化氮 碳酸二甲酯水甲醇 亚硝酸甲酯氧气6.49E-22115521.832140.72041048.48.3634055.36E-04.587316.0057295.726000.00E+0000.00E+00000223.37833.93E000001.83E-104.48E-1005.11E-138.3541568438.213.662.176232.81E-16000115521.832140.72013682.80.0092490.9638.46562982.649.39E-25005.49E-244123.7941147.457013689.

20、28E-022.97E-05656.7467119.85522280.00E+0000.00E+0000012.399381.23E0006.54E-121.60E-110.00E+001.70E-149.27E-02468.392.4796 3.57E-028.78E-1804123.7941147.4570456.00011.03E-047.43E-03300.80571031.822.93E-26800000000乙二醇乙醇酸甲酯1.3.2 甲醇分离塔（T0302）流进物料流出物料温度 压力 bar气相分率摩尔流率 kmol/hr78.865791.30.127943114029964.

21、43268.576-67.629966.776541.10678.362721647.8729.17536-38.0224105.6451.2360461.63738316.5369.116149-30.8401质量流量体积流量kg/hrm3/hr质量流量kg/hr01.83E-104.48E-1005.11E-138.3541568438.21321515.662.176232.81E-160001.83E-104.48E-10008.3538071.22E21515.632.1762300001.29E-351.29E-35003.49E-04.5110.0241363.21E-13000

22、草酸二甲酯氮气一氧化碳氢气一氧化氮 碳酸二甲酯水甲醇 亚硝酸甲酯氧气 乙二醇乙醇酸甲酯摩尔流率 kmol/hr草酸二甲酯氮气 一氧化碳氢气 一氧化氮 碳酸二甲酯水 甲醇亚硝酸甲酯氧气乙二醇乙醇酸甲酯06.54E-121.60E-1101.70E-149.27E-02468.392671.47963.57E-028.78E-06.54E-121.60E-11000.0927396.76E671.47893.57E-0204.62E-374.62E-37003.88E-06.6365 7.53E-045.26E-15.4 草酸二甲酯催化加氢工段91.4.1 加氢反应器（R0401）流进物料流出物料

23、温度 压力 bar气相分率摩尔流率 kmol/hr205201.00E+0021411.6498911.942914.87-50.579120520120604.5998911.941256.24-62.6188质量流量体积流量kg/hrm3/hr质量流量kg/hr草酸二甲酯氮气一氧化碳氢气一氧化氮 碳酸二甲酯水甲醇 亚硝酸甲酯氧气 乙二醇乙醇酸甲酯摩尔流率 kmol/hr草酸二甲酯氮气 一氧化碳氢气 一氧化氮 碳酸二甲酯水 甲醇亚硝酸甲酯氧气乙二醇乙醇酸甲酯48992.921.02E-271.64E-3141818.063.31E-230.7411893.39E-218080.049.37E

24、-1109.10056711.0408200038564.2207.41E-01033939.72002.44E+042.06E+03414.88053.65E-295.84E-332.07E1.10E-248.23E-031.88E-22252.1691.53E-1200.1466210.122568000.2108.23E-0301059.221003.92E+0222.83171.4.2 闪蒸罐（V0401）流进物料流出物料温度 压力 bar气相分率摩尔流率 kmol/hr4019.90.94069420604.594019.89895119382.634019.8989501221.9

25、61098911.925699.05-105.67146663.8525644.53-10.036652248.0455.86699-95.6346质量流量体积流量kg/hrm3/hr质量流量kg/hr草酸二甲酯氮气一氧化碳氢气一氧化氮 碳酸二甲酯水甲醇 亚硝酸甲酯氧气 乙二醇乙醇酸甲酯摩尔流率 kmol/hr草酸二甲酯氮气 一氧化碳氢气 一氧化氮 碳酸二甲酯水 甲醇亚硝酸甲酯氧气乙二醇乙醇酸甲酯0003.86E07.41E-0103.39E0024350.562056.6530000001.75E-0300.649971025860.320024341.462045.614.2100.091

26、2180.407009.09971211.039930001.91E08.23E-0301.06E00392.31792.28E+010000008.66E-0407.22E-030807.0716003.92E+0222.70915.2100.0010130.1493000.1466080.1225591.5 乙二醇分离工段1.5.1 乙二醇分离塔（T0501)流进物料流出物料温度 压力 bar气相分率摩尔流率 kmol/hr40.109771.38.27E-071221.9652248.0455.89428-95.6346671.110.0670072.1248631.69821-0.00

27、315671.10829.723427904.2236.64524-48.3738203.54111.2260392.169724341.725.86395-40.1353质量流量体积流量kg/hrm3/hr质量流量kg/hr110001.75E-0306.50E-01025860.320.00E+00024341.462045.61400.00E+0000.00174504.52E-0502.1172004.00E-060.00586800.00E+000.00E+004.06E-070.00E+006.50E-010.00E+0025858.20.00E+0000.8467212044.5

28、280005.26E-2702.21E-1405.06E-170024340.621.079576草酸二甲酯氮气一氧化碳氢气一氧化氮 碳酸二甲酯水甲醇 亚硝酸甲酯氧气 乙二醇乙醇酸甲酯摩尔流率 kmol/hr草酸二甲酯氮气 一氧化碳氢气 一氧化氮 碳酸二甲酯水 甲醇亚硝酸甲酯氧气乙二醇乙醇酸甲酯0008.66E-0407.22E-030807.07160.00E+000.00E+00392.171322.7091500.00E+0000.00086605.02E-0700.066075006.45E-086.51E-0500.00E+000.00E+002.01E-070.00E+007.22

29、E-030.00E+00807.00550.00E+0001.36E-022.27E+010002.61E-2702.45E-1601.58E-1800392.15770.0119851.5.2 乙醇酸甲酯分离塔（T0502）流进物料流出物料671.10829.723427904.2236.64524-48.373863.5523910807.005625858.6234.69629-45.2025152.70691.072022.717832045.6022.072206-3.1834温度 压力 bar气相分率摩尔流率 kmol/hr质量流量体积流量kg/hrm3/hr质量流量kg/hr00

30、.00E+0004.06E-0700.64992600.00E+0004.06E-0700.6498410001.06E-3108.48E-05草酸二甲酯氮气一氧化碳氢气一氧化氮碳酸二甲酯12025858.20.00E+000.00E+000.8467212044.528025857.97001.32E-088.09E-0500.227185000.8467212044.528水 甲醇亚硝酸甲酯氧气乙二醇 乙醇酸甲酯摩尔流率 kmol/hr草酸二甲酯氮气 一氧化碳氢气 一氧化氮 碳酸二甲酯水 甲醇亚硝酸甲酯氧气乙二醇乙醇酸甲酯00.00E+0002.01E-0707.22E-030807.00

31、550.00E+000.00E+000.01364222.697100.00E+0002.01E-0707.21E-030806.9984002.12E-108.98E-070005.26E-3209.41E-0700.00709000.01364222.6970913附录 2 能量一览表1.1 一氧化碳偶联草酸二甲酯工段1.1.1 羰化偶联反应器（R0101）温度 1351355179141753604.392-67.723476517499.29456257635.1750745.4746-82.943507压力 bar气相分率摩尔流率 kmol/hr质量流量 k

32、g/hr 体积流量 m3/hr能量 Gcal/hr1.2 草酸二甲酯和碳酸二甲酯分离工段1.2.1 草酸二甲酯分离塔（T0201）流进物料流出物料155.10358.170511476.5414.26179-20.49736750.9275197499.295257635.239286.24-94.243116.211964250353.40862911539.494814.2118625-1.97E+0138.52724.917091.735207133.137320.63-26.601643.884854.98401119.16373518.9174.46425-107.802温度 压力

33、bar气相分率摩尔流率 kmol/hr质量流量 kg/hr 体积流量 m3/hr能量 Gcal/hr1.2.2 冷凝罐（V0201）流进物料流出物料温度 压力 bar气相分率摩尔流率 kmol/hr质量流量 kg/hr 体积流量 m3/hr能量 Gcal/hr16.24.80.9501667091.735207133.133640.26-30.908216.24.8000010353.408611539.4914.21161-19.661716.24.80000116738.326195593.633626.05-11.24651.2.3 草酸二甲酯分离塔（T0202）流进物料流出物料温度 压

34、力 bar43.884854.984227.10844.934101.74984.91401119.16373518.9174.46425-107.8020414.887748993.5756.57251-68.50931704.275524525.354313.804-28.3709气相分率摩尔流率 kmol/hr质量流量 kg/hr 体积流量 m3/hr 能量 Gcal/hr1.2.4 气体回收塔（T0203）流进物料流出物料101.7497574.91704.27550524525.34534313.80399-2.84E+0158.992124.851257.82138050.8241

35、438.769-4.12932111.65194.9090446.454216474.5222.85949-27.6459温度 压力 bar气相分率摩尔流率 kmol/hr质量流量 kg/hr 体积流量 m3/hr能量 Gcal/hr1.2.5 甲醇回收塔（T0204）流进物料流出物料温度 压力 bar气相分率摩尔流率 kmol/hr质量流量 kg/hr 体积流量 m3/hr能量 Gcal/hr106.622410.30909.101531433.6944.32259-53.2755138.65615310.2360500.00580818320.316127.-3.03E+01136.815

36、3101409.095713113.37.403-19.19421.2.6 碳酸二甲酯分离塔（T0205）流进物料流出物料温度 压力 bar气相分率摩尔流率 kmol/hr质量流量 kg/hr 体积流量 m3/hr能量 Gcal/hr138.660410.30500.005818320.3227.13778-30.3452183.95518710.236037.39983453362.572454.26364603-5.17E+00136.8665100462.60614957.7423.26925-25.14241.3 亚硝酸甲酯再生工段1.3.1 反应精馏塔（T0301）15流进物料流出物

37、料温度 压力 bar气相分率摩尔流率 kmol/hr质量流量 kg/hr 体积流量 m3/hr能量 Gcal/hr45517643.946224374.640225.41-33.3154355.101239.93839556.3750.60664-70.4987119.08354.850114029964.441.67413-67.629930.86784.8517059.884233966.636496.93-52.02621.3.2 甲醇分离塔（T0302）流进物料流出物料温度 压力 bar气相分率摩尔流率 kmol/hr质量流量 kg/hr 体积流量 m3/hr能量 Gcal/hr78.

38、865791.30.127943114029964.43268.576-67.629966.776541.10678.362721647.8729.17536-38.0224105.6451.2360461.63738316.5369.116149-30.84011.4 草酸二甲酯催化加氢工段1.4.1 加氢反应器（R0401）流进物料流出物料温度 压力 bar气相分率摩尔流率 kmol/hr质量流量 kg/hr 体积流量 m3/hr能量 Gcal/hr205201.00E+0021411.6498911.942914.87-50.579120520120604.5998911.941256.

39、24-62.61881.4.2 闪蒸罐（V0401）流进物料流出物料温度 压力 bar气相分率摩尔流率 kmol/hr质量流量 kg/hr 体积流量 m3/hr能量 Gcal/hr4019.90.94069420604.5998911.925699.05-105.6714019.89895119382.6346663.8525644.53-10.03664019.8989501221.9652248.0455.86699-95.6346161.5 乙二醇分离工段1.5.1 乙二醇分离塔（T0501)流进物料流出物料40.109771.38.27E-071221.9652248.0455.894

40、28-95.6346671.110.0670072.1248631.69821-0.00315671.10829.723427904.2236.64524-48.3738203.54111.2260392.169724341.725.86395-40.1353温度 压力 bar气相分率摩尔流率 kmol/hr质量流量 kg/hr 体积流量 m3/hr能量 Gcal/hr1.5.2 乙醇酸甲酯分离塔（T0502）流进物料流出物料温度 压力 bar气相分率摩尔流率 kmol/hr质量流量 kg/hr 体积流量 m3/hr能量 Gcal/hr671.10829.723427904.2236.6452

41、4-48.373863.5523910807.005625858.6234.69629-45.2025152.70691.072022.717832045.6022.072206-3.183417附录 3 设备选型一览表表 3-1 塔选型一览表名称类型内径（mm）壁厚（mm）高度（mm）设计压力（MPa）设计温度（）封头形式材料保温层保护层总质量（kg）1T0201F1Z-4A 浮阀280011230800.5545标准椭圆型封头Q235-B复合硅酸盐卷毡 复合硅酸盐卷毡 复合硅酸盐卷毡 复合硅酸盐卷毡 复合硅酸盐卷毡 复合硅酸盐卷毡 复合硅酸盐卷毡 复合硅酸盐卷毡 复合硅酸盐卷毡 复合硅酸盐

42、卷毡铝合金板铝合金板铝合金板铝合金板铝合金板铝合金板铝合金板铝合金板铝合金板铝合金板67629.92T0202F1Z-4A 浮阀1600-280012-14324300.11114.4标准椭圆型封头Q235-B49524.23T0203F1Z-4A 浮阀240010329500.11143.1标准椭圆型封头Q345-R65906.74T0204F1Z-4A 浮阀240010520800.11142.8Q345-R69031.1标准椭圆型封头5T0205F1Z-4A 浮阀2800-360012-14601600.11102Q345-R71537.5标准椭圆型封头6T0301AF1Z-4A 浮阀4

43、80016192800.1191.4标准椭圆型封头Q235-B34060.37T0301BF1Z-4A 浮阀20001981500.11113.6标准椭圆型封头Q235-B1038088T0302F1Z-4A 浮阀240016329500.11141.2标准椭圆型封头Q235-B67569.69T0501F1Z-4A 浮阀300024402300.11141.7Q235-B71539.1标准椭圆型封头10T0502F1Z-4A 浮阀26006270000.11141.7Q345-R71539.1标准椭圆型封头18表 3-2 换热器选型一览表型号类型内径列管规格排列方式列管数管程数换热面积管程材

44、料壳程材料重量中心排管数E-0101 E-0102 E-0201 E-0202 E-0203 E-0204E-0205BEM-900-0.66-259.5-4.5/19-2 I BEM-1400-2.42-900.5-6/19-1 I BEM-273-0.33-6.4-2/19-2 I BEM-900-0.33-355.3-6/19-1 IBEM-900-0.33-524.9-9/19-2 I固定管板式 固定管板式 固定管板式 固定管板式 固定管板式 固定管板式 立式虹吸式再沸器固定管板式 立式虹吸式再沸器固定管板式 固定管板式 立式虹吸式再沸器立式虹吸式再沸器固定管板式立式虹吸式再90014

45、0027390090032518004500600020006000900060003000192 192 192 192 192 192 192正三角形正三角形正三角形正三角形正三角形正三角形正三角形98825575610099886811772121241259.5900.56.4355.3524.923.940820202020202020Q345R Q345R Q345R Q345R Q345R Q345RQ345R6948.722310386.98315.6117901160.4152403555835351135BEM-325-0.33-23.9-6/19-4BEM-1800-3.

46、63-408-3/19-1IIE-0206E-0207BEM-700-0.33-93.8-3/19-4BEM-1600-2.42-937-9/19-1II700160030009000192 192正三角形正三角形54220234193.89372020Q345RQ345R2821.9311492747E-0208 E-0209 E-0210 AE-0210 BE-0211E-0212BEM-500-0.55-29-2/19-2 IBEM-600-1.32-126.8-6/19-1 I BEM-1000-3.63-404.3-6/19-6 I5006001000200060006000192

47、192 192正三角形正三角形正三角形256360114821629126.8404.3202020Q345RQ345R Q345R762.13570.911301182038BEM-1400-2.42-1263.3-9/19-6 三角形237861263.3151.4417.720Q345R1539554BEM-600-1.32-151.4-6/19-1 IBEM-1000-3.41-417.7-6/19-4 I600100060006000192 192正三角形正三角形4301186142020Q345RQ345R387111327223919沸器固定管板式固定管

48、板式E-0301E-0302BEM-900-0.66-355.3-6/19-1 IBEM-1400-2.42-900.5-6/19-1 I900140060006000192 192正三角形正三角形1009255711355.3900.52020Q345RQ345R8315.622521.96398.165855245.35914.83555E-0303 E-0304 E-0305E-0306BEM-800-0.33-186.5-6/19-6 I BEM-800-1.32-254.3-6/19-4 I BEM-800-0.33-203.8-4.5/19-2 IBEM-1000-0.33-213

49、.6-3/19-2 I固定管板式 固定管板式 固定管板式 立式虹吸式再沸器固定管板式 固定管板式 固定管板式 立式虹吸式再沸器立式虹吸式再沸器固定管板式 立式虹吸式再沸器立式虹吸式再沸器80080080010006000600045003000192 192 192 192正三角形正三角形正三角形正三角形71072277612346422186.5254.3203.8213.620202020Q345R Q345R Q345RQ345R30313139E-0401 E-0402 E-0501 E-0502 AE-0502 BE-0503 E-0504 AE-0504BBEM-900-3.63-

50、174.7-3/19-1 I9009008009003000450030004500192 192 192 192正三角形正三角形正三角形正三角形10099887979881212174.7259.5138259.520202020Q345R Q345R Q345RQ345R6172.27028.33676.88080.735353135BEM-900-2.42-259.5-4.5/19-2 BEM-800-0.33-138-3/19-1 IBEM-900-3.63-259.5-4.5/19-2IIBEM-900-3.63-259.5-4.5/19-2I9004500192正三角形988225

51、9.520Q345R8080.735BEM-1000-0.33-332.8-4.5/19-1IBEM-1000-3.63-332.8-4.5/19-1I1000100045004500192 192正三角形正三角形1267126711332.8332.82020Q345RQ345R8247.510404.610404.63939BEM-1000-3.63-332.8-4.5/19-1I10004500192正三角形12671332.820Q345R39表 3-3 泵选型一览表20电数机 参单泵运行参数运行方式泵 编号泵名称型号电功机 轴率转速流Q(L/S)量杨程H(m)轴功率总功率效率(%)台

52、数方式n(r/min)P(KW)P(KW)(KW)5.532.2117.5115.5377.55.538001.52.2P0201 P0202 P0203 P0204 P0205 P0206 P0207 P0208 P0301 P0302 P0303 P0401 P0501P0502甲醇输送泵塔顶回流泵塔顶回流泵塔顶回流泵输送泵塔顶回流泵输送泵塔顶回流泵甲醇输送泵塔顶回流泵塔顶回流泵输送泵塔顶回流泵塔顶回流泵50D-8 XA40/26 50D-8IS100-80-160B XA40/16 IS100-80-160A IS65-40-200A 6SA-8100D-16 XA50/13A XA40

53、/13B 500S98IS50-32-160B50D-829501450295029002900290029002950295029002900970290029503.793.993.58319.356.1728.447.5640.4513.7417.576.84566.833.124.8365.7123.3628.9525.9838.2926.5841.8855.4233.0818.1317.3297.9223.726.014.332.081.826.623.939.895.1627.926.24.211.8686.021.371.9159.2543.9255.874.4258.8374.

54、8860.0478.6971.8273.8964.3579.3252.5163.9511111111111211单泵单泵单泵单泵单泵单泵单泵单泵单泵单泵单泵串联单泵单泵4.332.081.826.623.939.895.1627.926.24.211.81372.041.371.91表 3-4 压缩机选型一览表气量(m3/min)位号型号个数吸气压力（MP）出口压力（MP）转速(r.p.m)轴功率（KW）21C0101C0401H600-6/0.8H410-6.7/0.87136504100.080.0870.610.6710258/1272012387/1476924941920表 3-5

55、储罐选型一览表位号数量温度压强mpa公称容积m3公称直径mm壁厚mm长度mm封头厚度mm焊接系数储罐重量kg标准序号总长度mm材料备注系数Q234- A Q234- A Q235- A Q235-A甲醇储罐 DMC 储罐 MG 储罐 EG 储罐v06011250.150.910001150061200012540.939430HG21502.1-92-11713254v06022250.150.910001150061200012540.939430HG21502.1-92-11813254v06031250.150.910001150061200012540.939430HG21502.1-

56、92-11913254v06044250.150.9300017000101585018410.989485HG21502.1-92-12317691表 3-6 回流罐选型一览表位号数 温度压 强公 称 公称 壁长 度 封 头 焊 接 储 罐 标准序号总 长材料备注22量mpa系数容m3积直径mm厚mmmm厚 度mm系数重 量kg度 mmv0202 v0203 v0204 v0205 v0301 v0302 v0501v050211111111105.41105.76136.83136.8971.3167.06373.0565.270.490.48110.480.110.110.10.850.

57、850.850.850.850.850.850.8531000534005101416108680.850.850.850.850.850.850.850.856402930558086904670935565815HG 5-1580-85-74HG 5-1580-85-86 HG5-1580-85-222 HG5-1580-85-226 HG5-1580-85-8 HG5-1580-85-9 HG5-1580-85-6 HG 5-1580-85-839626600691288127000466633623866Q235-B Q235-B Q235-B Q235-B Q235-B Q235-B

58、 Q235-BQ235-BDMO 分离塔回流罐气体回收塔回流罐甲醇回收塔回流罐 DMC 回收塔回流罐反应精馏回流罐甲醇分离塔回流罐EG 分离塔回流罐MG 分离塔回流罐20322552.54200022002200120010001200141610555560076005800400028003200表 3-7 气液分离器选型一览表位号V0201V0401气象密度（kg/m3）5.8171.82封头直边高度（mm）4040进口气液体积流量(m3/h)33640.26325699.048浮动流速（m/s）0.6031.16封头曲面高度（mm）800800温度（）16.240气体流速(m/s)0.

59、51.0气液分离器总高（mm）86006300压力（MPa）4.81.99分离器直径（mm）50003200气液进口管径（mm）9201072010出口液相体积流量(m3/h)14.21255.867高低液位差（mm）120120液体出口管径（mm）573.51027出口气相体积流量(m3/h)33626.04725644.527液相总高度（mm）170170气体出口管径（mm）7201062010液相密度（kg/m3）811.95935.22气象总高度 (mm)6650431023表 3-8 反应器选型一览表图号反应器名称类型数量材料12R0401 R010123Q345R Q345R加氢反

60、应器 羰化偶连反应器列管式固定床绝热固定床24附录 4 配管一览表表 4-1 配管一览表管道代号物流代号气相分率质量流量 kg/h体积流量 m3/h管内径/mm管道尺寸/mm公称直径/mm厚度/mmPG0101-900-K1C-H PG0102-900-K1C-H N0101-200-K1C PG0101-350-K1C PG0103-900-K1C-H PG0101-1000-K1C-H PG0102-1000-K2C-H PL0201-50-H1C PL0202-50-K1C PL0203-50-K1C-H PLG0201-800-K1C-H PG0201-700-K1C PG0202-7