西南賽區(qū)-重慶科技學(xué)院tnt團(tuán)隊(duì)作品設(shè)計(jì)集源文件附錄

1、附錄 1 物料一覽表1.1 一氧化碳偶聯(lián)草酸二甲酯工段1.1.1 羰化偶聯(lián)反應(yīng)器（R0101）流進(jìn)物料流出物料1355179141753604.392-67.723476135517499.29456257635.1750745.4746-82.943507溫度 壓力 bar氣相分率摩爾流率 kmol/hr質(zhì)量流量體積流量kg/hrm3/hr質(zhì)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?dú)庖谎趸細(xì)錃庖谎趸?碳酸二甲酯水甲醇 亞硝酸甲酯氧氣 乙二醇乙醇酸甲酯摩爾流率 kmol/hr草酸二甲酯氮?dú)?一氧化碳?xì)錃?一氧化氮 碳酸二甲酯水 甲醇亞硝酸甲酯氧氣乙二醇乙醇酸甲酯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離工段21.2.1 草酸二甲酯分離塔（T0201）流進(jìn)物料流出物料溫度 壓力 bar氣相分率摩爾流率 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質(zhì)量流量體積流量kg/hrm3/hr質(zhì)量流量kg/hr草酸二甲酯氮?dú)庖谎趸細(xì)錃庖谎趸?碳酸二甲酯水甲醇 亞硝酸甲酯氧氣乙二醇乙醇酸甲酯 摩爾流率 kmol/hr草酸二甲酯氮?dú)庖谎趸細(xì)錃庖谎趸?碳酸二甲酯水甲醇 亞硝酸甲酯氧氣 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）流進(jìn)物料流出物料溫度 壓力 bar氣相分率摩爾流率 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質(zhì)量流量體積流量kg/hrm3/hr質(zhì)量流量kg/hr草酸二甲酯氮?dú)庖谎趸細(xì)錃庖谎趸?碳酸二甲酯水甲醇 亞硝酸甲酯氧氣 乙二醇乙醇酸甲酯摩爾流率 kmol/hr草酸二甲酯氮?dú)?一氧化碳?xì)錃?一氧化氮 碳酸二甲酯水 甲醇亞硝酸甲酯氧氣乙二醇乙醇酸甲酯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 草酸二甲酯分離塔（T0202）流進(jìn)物料流出物料溫度 壓力 bar氣相分率摩爾流率 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質(zhì)量流量體積流量kg/hrm3/hr質(zhì)量流量kg/hr草酸二甲酯氮?dú)?8992.921176.48648992.921.02E-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?xì)錃庖谎趸?碳酸二甲酯水甲醇 亞硝酸甲酯氧氣 乙二醇乙醇酸甲酯摩爾流率 kmol/hr草酸二甲酯氮?dú)?一氧化碳?xì)錃?一氧化氮 碳酸二甲酯水 甲醇亞硝酸甲酯氧氣乙二醇乙醇酸甲酯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 氣體回收塔（T0203）流進(jìn)物料流出物料溫度 壓力 bar氣相分率摩爾流率 kmol/hr101.7497574.91704.27550524525.34534313.80399-2.84E+0158.992124.851257.82138050.8241438.769-4.12932111.65194.9090446.454216474.5222.85949-27.6459質(zhì)量流量體積流量kg/hrm3/hr質(zhì)量流量kg/hr草酸二甲酯氮?dú)庖谎趸細(xì)錃庖谎?/p>

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 亞硝酸甲酯氧氣乙二醇乙醇酸甲酯 摩爾流率 kmol/hr草酸二甲酯氮?dú)庖谎趸細(xì)錃庖谎趸?碳酸二甲酯水甲醇 亞硝酸甲酯氧氣 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）流進(jìn)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溫度 壓力 bar氣相分率摩爾流率 kmol/hr質(zhì)量流量體積流量kg/hrm3/hr質(zhì)量流量kg/hr草酸二甲酯氮?dú)庖谎趸細(xì)錃庖谎趸?碳酸二甲酯水甲醇 亞硝酸甲酯氧氣 乙二醇乙醇酸甲酯摩爾流率 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?dú)庖谎趸細(xì)錃庖谎趸?碳酸二甲酯水甲醇 亞硝酸甲酯氧氣 乙二醇乙醇酸甲酯1.2.6 碳酸二甲酯分離塔（T0205）流進(jìn)物料流出物料溫

16、度 壓力 bar氣相分率摩爾流率 kmol/hr138.660410.30500.005818320.3227.13778-30.3452183.95518710.236037.39983453362.572454.26364603-5.17E+00136.8665100462.60614957.7423.26925-25.1424質(zhì)量流量體積流量kg/hrm3/hr質(zhì)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?dú)庖谎趸細(xì)錃庖谎趸?碳酸二甲酯水甲醇 亞硝酸甲酯氧氣乙二醇乙醇酸甲酯 摩爾流率 kmol/hr草酸二甲酯氮?dú)庖谎趸細(xì)錃庖谎趸妓岫柞?.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 甲醇亞硝酸甲酯氧氣乙二醇乙醇酸

18、甲酯1.3 亞硝酸甲酯再生工段1.3.1 反應(yīng)精餾塔（T0301）流進(jìn)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溫度 壓力 bar氣相分率摩爾流率 kmol/hr質(zhì)量流量體積流量kg/hrm3/hr質(zhì)量流量kg/hr草酸二甲酯氮?dú)庖谎趸細(xì)錃庖谎趸?碳酸二甲酯水甲醇 亞硝酸甲酯氧氣乙二醇乙醇酸甲酯 摩爾流率 k

19、mol/hr草酸二甲酯氮?dú)庖谎趸細(xì)錃庖谎趸?碳酸二甲酯水甲醇 亞硝酸甲酯氧氣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 甲醇分離塔（T0302）流進(jìn)物料流出物料溫度 壓力 bar氣相分率摩爾流率 kmol/hr78.865791.30.127943114029964.

21、43268.576-67.629966.776541.10678.362721647.8729.17536-38.0224105.6451.2360461.63738316.5369.116149-30.8401質(zhì)量流量體積流量kg/hrm3/hr質(zhì)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?dú)庖谎趸細(xì)錃庖谎趸?碳酸二甲酯水甲醇 亞硝酸甲酯氧氣 乙二醇乙醇酸甲酯摩爾流率 kmol/hr草酸二甲酯氮?dú)?一氧化碳?xì)錃?一氧化氮 碳酸二甲酯水 甲醇亞硝酸甲酯氧氣乙二醇乙醇酸甲酯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 草酸二甲酯催化加氫工段91.4.1 加氫反應(yīng)器（R0401）流進(jìn)物料流出物料

23、溫度 壓力 bar氣相分率摩爾流率 kmol/hr205201.00E+0021411.6498911.942914.87-50.579120520120604.5998911.941256.24-62.6188質(zhì)量流量體積流量kg/hrm3/hr質(zhì)量流量kg/hr草酸二甲酯氮?dú)庖谎趸細(xì)錃庖谎趸?碳酸二甲酯水甲醇 亞硝酸甲酯氧氣 乙二醇乙醇酸甲酯摩爾流率 kmol/hr草酸二甲酯氮?dú)?一氧化碳?xì)錃?一氧化氮 碳酸二甲酯水 甲醇亞硝酸甲酯氧氣乙二醇乙醇酸甲酯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 閃蒸罐（V0401）流進(jìn)物料流出物料溫度 壓力 bar氣相分率摩爾流率 kmol/hr4019.90.94069420604.594019.89895119382.634019.8989501221.9

25、61098911.925699.05-105.67146663.8525644.53-10.036652248.0455.86699-95.6346質(zhì)量流量體積流量kg/hrm3/hr質(zhì)量流量kg/hr草酸二甲酯氮?dú)庖谎趸細(xì)錃庖谎趸?碳酸二甲酯水甲醇 亞硝酸甲酯氧氣 乙二醇乙醇酸甲酯摩爾流率 kmol/hr草酸二甲酯氮?dú)?一氧化碳?xì)錃?一氧化氮 碳酸二甲酯水 甲醇亞硝酸甲酯氧氣乙二醇乙醇酸甲酯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 乙二醇分離工段1.5.1 乙二醇分離塔（T0501)流進(jìn)物料流出物料溫度 壓力 bar氣相分率摩爾流率 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質(zhì)量流量體積流量kg/hrm3/hr質(zhì)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?dú)庖谎趸細(xì)錃庖谎趸?碳酸二甲酯水甲醇 亞硝酸甲酯氧氣 乙二醇乙醇酸甲酯摩爾流率 kmol/hr草酸二甲酯氮?dú)?一氧化碳?xì)錃?一氧化氮 碳酸二甲酯水 甲醇亞硝酸甲酯氧氣乙二醇乙醇酸甲酯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 乙醇酸甲酯分離塔（T0502）流進(jìn)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溫度 壓力 bar氣相分率摩爾流率 kmol/hr質(zhì)量流量體積流量kg/hrm3/hr質(zhì)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?dú)庖谎趸細(xì)錃庖谎趸妓岫柞?2025858.20.00E+000.00E+000.8467212044.528025857.97001.32E-088.09E-0500.227185000.8467212044.528水 甲醇亞硝酸甲酯氧氣乙二醇 乙醇酸甲酯摩爾流率 kmol/hr草酸二甲酯氮?dú)?一氧化碳?xì)錃?一氧化氮 碳酸二甲酯水 甲醇亞硝酸甲酯氧氣乙二醇乙醇酸甲酯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附錄 2 能量一覽表1.1 一氧化碳偶聯(lián)草酸二甲酯工段1.1.1 羰化偶聯(lián)反應(yīng)器（R0101）溫度 1351355179141753604.392-67.723476517499.29456257635.1750745.4746-82.943507壓力 bar氣相分率摩爾流率 kmol/hr質(zhì)量流量 k

32、g/hr 體積流量 m3/hr能量 Gcal/hr1.2 草酸二甲酯和碳酸二甲酯分離工段1.2.1 草酸二甲酯分離塔（T0201）流進(jìn)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溫度 壓力

33、bar氣相分率摩爾流率 kmol/hr質(zhì)量流量 kg/hr 體積流量 m3/hr能量 Gcal/hr1.2.2 冷凝罐（V0201）流進(jìn)物料流出物料溫度 壓力 bar氣相分率摩爾流率 kmol/hr質(zhì)量流量 kg/hr 體積流量 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 草酸二甲酯分離塔（T0202）流進(jìn)物料流出物料溫度 壓

34、力 bar43.884854.984227.10844.934101.74984.91401119.16373518.9174.46425-107.8020414.887748993.5756.57251-68.50931704.275524525.354313.804-28.3709氣相分率摩爾流率 kmol/hr質(zhì)量流量 kg/hr 體積流量 m3/hr 能量 Gcal/hr1.2.4 氣體回收塔（T0203）流進(jìn)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溫度 壓力 bar氣相分率摩爾流率 kmol/hr質(zhì)量流量 kg/hr 體積流量 m3/hr能量 Gcal/hr1.2.5 甲醇回收塔（T0204）流進(jìn)物料流出物料溫度 壓力 bar氣相分率摩爾流率 kmol/hr質(zhì)量流量 kg/hr 體積流量 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 碳酸二甲酯分離塔（T0205）流進(jìn)物料流出物料溫度 壓力 bar氣相分率摩爾流率 kmol/hr質(zhì)量流量 kg/hr 體積流量 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 亞硝酸甲酯再生工段1.3.1 反應(yīng)精餾塔（T0301）15流進(jìn)物料流出物

37、料溫度 壓力 bar氣相分率摩爾流率 kmol/hr質(zhì)量流量 kg/hr 體積流量 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 甲醇分離塔（T0302）流進(jìn)物料流出物料溫度 壓力 bar氣相分率摩爾流率 kmol/hr質(zhì)量流量 kg/hr 體積流量 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 草酸二甲酯催化加氫工段1.4.1 加氫反應(yīng)器（R0401）流進(jìn)物料流出物料溫度 壓力 bar氣相分率摩爾流率 kmol/hr質(zhì)量流量 kg/hr 體積流量 m3/hr能量 Gcal/hr205201.00E+0021411.6498911.942914.87-50.579120520120604.5998911.941256.

39、24-62.61881.4.2 閃蒸罐（V0401）流進(jìn)物料流出物料溫度 壓力 bar氣相分率摩爾流率 kmol/hr質(zhì)量流量 kg/hr 體積流量 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 乙二醇分離工段1.5.1 乙二醇分離塔（T0501)流進(jìn)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溫度 壓力 bar氣相分率摩爾流率 kmol/hr質(zhì)量流量 kg/hr 體積流量 m3/hr能量 Gcal/hr1.5.2 乙醇酸甲酯分離塔（T0502）流進(jìn)物料流出物料溫度 壓力 bar氣相分率摩爾流率 kmol/hr質(zhì)量流量 kg/hr 體積流量 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附錄 3 設(shè)備選型一覽表表 3-1 塔選型一覽表名稱類型內(nèi)徑（mm）壁厚（mm）高度（mm）設(shè)計(jì)壓力（MPa）設(shè)計(jì)溫度（）封頭形式材料保溫層保護(hù)層總質(zhì)量（kg）1T0201F1Z-4A 浮閥280011230800.5545標(biāo)準(zhǔn)橢圓型封頭Q235-B復(fù)合硅酸鹽卷氈 復(fù)合硅酸鹽卷氈 復(fù)合硅酸鹽卷氈 復(fù)合硅酸鹽卷氈 復(fù)合硅酸鹽卷氈 復(fù)合硅酸鹽卷氈 復(fù)合硅酸鹽卷氈 復(fù)合硅酸鹽卷氈 復(fù)合硅酸鹽卷氈 復(fù)合硅酸鹽

42、卷氈鋁合金板鋁合金板鋁合金板鋁合金板鋁合金板鋁合金板鋁合金板鋁合金板鋁合金板鋁合金板67629.92T0202F1Z-4A 浮閥1600-280012-14324300.11114.4標(biāo)準(zhǔn)橢圓型封頭Q235-B49524.23T0203F1Z-4A 浮閥240010329500.11143.1標(biāo)準(zhǔn)橢圓型封頭Q345-R65906.74T0204F1Z-4A 浮閥240010520800.11142.8Q345-R69031.1標(biāo)準(zhǔn)橢圓型封頭5T0205F1Z-4A 浮閥2800-360012-14601600.11102Q345-R71537.5標(biāo)準(zhǔn)橢圓型封頭6T0301AF1Z-4A 浮閥4

43、80016192800.1191.4標(biāo)準(zhǔn)橢圓型封頭Q235-B34060.37T0301BF1Z-4A 浮閥20001981500.11113.6標(biāo)準(zhǔn)橢圓型封頭Q235-B1038088T0302F1Z-4A 浮閥240016329500.11141.2標(biāo)準(zhǔn)橢圓型封頭Q235-B67569.69T0501F1Z-4A 浮閥300024402300.11141.7Q235-B71539.1標(biāo)準(zhǔn)橢圓型封頭10T0502F1Z-4A 浮閥26006270000.11141.7Q345-R71539.1標(biāo)準(zhǔn)橢圓型封頭18表 3-2 換熱器選型一覽表型號類型內(nèi)徑列管規(guī)格排列方式列管數(shù)管程數(shù)換熱面積管程材

44、料殼程材料重量中心排管數(shù)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 泵選型一覽表20電數(shù)機(jī) 參單泵運(yùn)行參數(shù)運(yùn)行方式泵 編號泵名稱型號電功機(jī) 軸率轉(zhuǎn)速流Q(L/S)量楊程H(m)軸功率總功率效率(%)臺

52、數(shù)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甲醇輸送泵塔頂回流泵塔頂回流泵塔頂回流泵輸送泵塔頂回流泵輸送泵塔頂回流泵甲醇輸送泵塔頂回流泵塔頂回流泵輸送泵塔頂回流泵塔頂回流泵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單泵單泵單泵單泵單泵單泵單泵單泵單泵單泵單泵串聯(lián)單泵單泵4.332.081.826.623.939.895.1627.926.24.211.81372.041.371.91表 3-4 壓縮機(jī)選型一覽表氣量(m3/min)位號型號個(gè)數(shù)吸氣壓力（MP）出口壓力（MP）轉(zhuǎn)速(r.p.m)軸功率（KW）21C0101C0401H600-6/0.8H410-6.7/0.87136504100.080.0870.610.6710258/1272012387/1476924941920表 3-5

55、儲罐選型一覽表位號數(shù)量溫度壓強(qiáng)mpa公稱容積m3公稱直徑mm壁厚mm長度mm封頭厚度mm焊接系數(shù)儲罐重量kg標(biāo)準(zhǔn)序號總長度mm材料備注系數(shù)Q234- A Q234- A Q235- A Q235-A甲醇儲罐 DMC 儲罐 MG 儲罐 EG 儲罐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 回流罐選型一覽表位號數(shù) 溫度壓 強(qiáng)公 稱 公稱 壁長 度 封 頭 焊 接 儲 罐 標(biāo)準(zhǔn)序號總 長材料備注22量mpa系數(shù)容m3積直徑mm厚mmmm厚 度mm系數(shù)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 分離塔回流罐氣體回收塔回流罐甲醇回收塔回流罐 DMC 回收塔回流罐反應(yīng)精餾回流罐甲醇分離塔回流罐EG 分離塔回流罐MG 分離塔回流罐20322552.54200022002200120010001200141610555560076005800400028003200表 3-7 氣液分離器選型一覽表位號V0201V0401氣象密度（kg/m3）5.8171.82封頭直邊高度（mm）4040進(jìn)口氣液體積流量(m3/h)33640.26325699.048浮動流速（m/s）0.6031.16封頭曲面高度（mm）800800溫度（）16.240氣體流速(m/s)0.

59、51.0氣液分離器總高（mm）86006300壓力（MPa）4.81.99分離器直徑（mm）50003200氣液進(jìn)口管徑（mm）9201072010出口液相體積流量(m3/h)14.21255.867高低液位差（mm）120120液體出口管徑（mm）573.51027出口氣相體積流量(m3/h)33626.04725644.527液相總高度（mm）170170氣體出口管徑（mm）7201062010液相密度（kg/m3）811.95935.22氣象總高度 (mm)6650431023表 3-8 反應(yīng)器選型一覽表圖號反應(yīng)器名稱類型數(shù)量材料12R0401 R010123Q345R Q345R加氫反

60、應(yīng)器 羰化偶連反應(yīng)器列管式固定床絕熱固定床24附錄 4 配管一覽表表 4-1 配管一覽表管道代號物流代號氣相分率質(zhì)量流量 kg/h體積流量 m3/h管內(nèi)徑/mm管道尺寸/mm公稱直徑/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