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1、目第一章 .CO.酯再生工碳酸二甲酯提純工乙二醇提純工甲醇水雙效精餾工總第二能.總的主要依目第一章 .CO.酯再生工碳酸二甲酯提純工乙二醇提純工甲醇水雙效精餾工總第二能.總的主要依任.CO.第一章 物CO 羰化偶聯(lián)工段物1.1COTemperature reVpaor111lpyTotalFlowTotalFlowTotalFlowMassFlow00000000000000000000000000000000000000000TOTALCO羰化偶聯(lián)反應器（R0201）Temperature re Vpaor11lpyTotalFlowTotalFlowTotalFlowMassFlow000

2、000第一章 物CO 羰化偶聯(lián)工段物1.1COTemperature reVpaor111lpyTotalFlowTotalFlowTotalFlowMassFlow00000000000000000000000000000000000000000TOTALCO羰化偶聯(lián)反應器（R0201）Temperature re Vpaor11lpyTotalFlowTotalFlowTotalFlowMassFlow000000CO羰化偶聯(lián)反應器（R0202）Temperature re Vpaor11lpyTotalFlowTotalFlowTotalFlowMassFlow0000000000TOT

3、AL酯再生工1.5 Temperature re Vpaor110011000000000TOTALCO羰化偶聯(lián)反應器（R0202）Temperature re Vpaor11lpyTotalFlowTotalFlowTotalFlowMassFlow0000000000TOTAL酯再生工1.5 Temperature re Vpaor110011000000000TOTALTemperature re Vpaor1010lpy-TotalFlowTotalFlowTotalFlowMassFlow0000000000000000000000000000000000000TOTALTotalF

4、low TotalFlow TotalFlow MassFlow 0000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000TOTALTemperature re Vpaor1010lpy-TotalFlowTotalFlowTotalFlowMassFlow0000000000000000000000000000000000000TOTALTotalFlow TotalFlow TotalFlow MassFlow 000000000000000000000000

5、0000000000000000000000000000000000000000000000000000000000000000000000TOTAL碳酸二甲酯提純工0Temperature re Vpaor0010lpyTotalFlowTotalFlowTotalFlowMassFlow0000Temperature re Vpaor001101lpy443136TotalFlow 3TotalFlow2TotalFlow 7MassFlow0000000000000000000000000000000100060000碳酸二甲酯提純工0Temperature re Vpaor0010lp

6、yTotalFlowTotalFlowTotalFlowMassFlow0000Temperature re Vpaor001101lpy443136TotalFlow 3TotalFlow2TotalFlow 7MassFlow0000000000000000000000000000000100060000000000000000000TOTAL1.9吸收塔（T0302）Temperature re Vpaor1010lpyTotalFlowTotalFlowTotalFlowMassFlow00000000000000001.4162e-01.0026e-000000000000TOTAL

7、1.10高壓共沸精餾塔（T0303）Temperature re Vpaor0001lpyTotalFlowTotalFlow000000003.58e-9.0519e-00000000TOTAL1.9吸收塔（T0302）Temperature re Vpaor1010lpyTotalFlowTotalFlowTotalFlowMassFlow00000000000000001.4162e-01.0026e-000000000000TOTAL1.10高壓共沸精餾塔（T0303）Temperature re Vpaor0001lpyTotalFlowTotalFlow000000003.58e-

8、9.0519e-00000000TOTAL1.11碳酸酯精制塔（T0304）Temperature re Vpaor000lpyTotalFlowTotalFlowTotalFlowMassFlow000000000000000000000TOTAL乙二醇提純工1.12TotalFlowMassFlow00003.4331e-1.2967e-000000002.5784e-5.5072e-00002.2834e-0000TOTAL1.11碳酸酯精制塔（T0304）Temperature re Vpaor000lpyTotalFlowTotalFlowTotalFlowMassFlow00000

9、0000000000000000TOTAL乙二醇提純工1.12TotalFlowMassFlow00003.4331e-1.2967e-000000002.5784e-5.5072e-00002.2834e-0000TOTALTemperature re Vpaor15.6566e-0100lpyTotalFlowTotalFlowTotalFlowMassFlow006.2041e-000001.1426e-000000000000000001.6181e-000001.4855e-0002.2202e-00001.0836e-08.6416e-00TOTALTemperature re V

10、paor0100lpyTotalFlowTotalFlowTotalFlowMassFlow7.3759e-000000000000000000001.6807e-1.9846e-1.4308e-Temperature re Vpaor15.6566e-0100lpyTotalFlowTotalFlowTotalFlowMassFlow006.2041e-000001.1426e-000000000000000001.6181e-000001.4855e-0002.2202e-00001.0836e-08.6416e-00TOTALTemperature re Vpaor0100lpyTota

11、lFlowTotalFlowTotalFlowMassFlow7.3759e-000000000000000000001.6807e-1.9846e-1.4308e-Temperature re Vpaor000lpyTotalFlowTotalFlowTotalFlowMassFlow000000000000000TOTAL1.15草酸酯加氫反應器（R0401）Temperature re 22Vpaor11lpyTotalFlowTotalFlowTotalFlowMassFlow6.2041e-1.1426e-00001.6181e-1.4855e-TOTALTemperature re

12、 Vpaor000lpyTotalFlowTotalFlowTotalFlowMassFlow000000000000000TOTAL1.15草酸酯加氫反應器（R0401）Temperature re 22Vpaor11lpyTotalFlowTotalFlowTotalFlowMassFlow6.2041e-1.1426e-00001.6181e-1.4855e-TOTAL甲醇水雙效精餾工1.16Temperature re Vpaor00lpyTotalFlowTotalFlowTotalFlowMassFlow00000000000000000000000000000TOTAL1.17高

13、壓塔（T0501）Temperature re Vpaor0010lpyTotalFlowTotalFlowTotalFlow2.2202e-01.0836e-8.6416e-0TOTAL甲醇水雙效精餾工1.16Temperature re Vpaor00lpyTotalFlowTotalFlowTotalFlowMassFlow00000000000000000000000000000TOTAL1.17高壓塔（T0501）Temperature re Vpaor0010lpyTotalFlowTotalFlowTotalFlow2.2202e-01.0836e-8.6416e-0TOTAL1

14、.18常壓塔（T0502）Temperature re Vpaor000lpyTotalFlowTotalFlowTotalFlowMassFlow00000000000000000000000001.1941e-00000000000000000000TOTAL總MassFlow00001.0948e-6.8011e-00000006.2207e-000000000000000000000000TOTAL1.18常壓塔（T0502）Temperature re Vpaor000lpyTotalFlowTotalFlowTotalFlowMassFlow00000000000000000000

15、000001.1941e-00000000000000000000TOTAL總MassFlow00001.0948e-6.8011e-00000006.2207e-000000000000000000000000TOTAL1.191.201.21 /產量 萬噸/質量指標 123.61.191.201.21 /產量 萬噸/質量指標 123.6萬噸/23.34萬噸/34第二第二能總 能的主要依第二第二能總 能的主要依2.2Temperature re Vpaor11lpyTotalFlowTotalFlowTotalFlow2.3CO 羰化偶聯(lián)反應器2.4 2.5Temperature re Vp

16、aor11lpyTotalFlowTotalFlowTotalFlow2.62.4.2.酯再生工段能QQHeatQ02.2Temperature re Vpaor11lpyTotalFlowTotalFlowTotalFlow2.3CO 羰化偶聯(lián)反應器2.4 2.5Temperature re Vpaor11lpyTotalFlowTotalFlowTotalFlow2.62.4.2.酯再生工段能QQHeatQ0反應精餾塔2.72.8Temperature re Vpaor1010lpyTotalFlowTotalFlowTotalFlow2.9單級壓縮機2.102.11-Temperatur

17、e re Vpaor11lpyTotalFlowTotalFlowTotalFlow2.12WWHeatQQHeat反應精餾塔2.72.8Temperature re Vpaor1010lpyTotalFlowTotalFlowTotalFlow2.9單級壓縮機2.102.11-Temperature re Vpaor11lpyTotalFlowTotalFlowTotalFlow2.12WWHeatQQHeat2.4.3. 碳酸二甲酯提純工段能預分離塔2.132.14Temperature re Vpaor0010lpyTotalFlowTotalFlowTotalFlow2.15吸收塔2.

18、162.17Temperature re Vpaor1010lpyTotalFlowTotalFlowTotalFlowQHeat000QQHeat2.4.3. 碳酸二甲酯提純工段能預分離塔2.132.14Temperature re Vpaor0010lpyTotalFlowTotalFlowTotalFlow2.15吸收塔2.162.17Temperature re Vpaor1010lpyTotalFlowTotalFlowTotalFlowQHeat000QQHeat2.18高壓共沸精餾塔2.192.20Temperature re Vpaor0001lpyTotalFlowTotal

19、FlowTotalFlow2.21碳酸酯精制塔2.222.23Temperature re Vpaor000lpyTotalFlowTotalFlowTotalFlowQHeatQQHeatQ02.18高壓共沸精餾塔2.192.20Temperature re Vpaor0001lpyTotalFlowTotalFlowTotalFlow2.21碳酸酯精制塔2.222.23Temperature re Vpaor000lpyTotalFlowTotalFlowTotalFlowQHeatQQHeatQ02.24氣液分離器2.252.26Temperature re Vpaor01lpyTota

20、lFlowTotalFlowTotalFlow2.272.4.4. 乙二醇提純工段乙二醇精制塔2.282.29Temperature re Vpaor0100lpyQHeatQ0QHeat0Q2.24氣液分離器2.252.26Temperature re Vpaor01lpyTotalFlowTotalFlowTotalFlow2.272.4.4. 乙二醇提純工段乙二醇精制塔2.282.29Temperature re Vpaor0100lpyQHeatQ0QHeat0Q2.30甲醇回收精制塔2.312.32Temperature re Vpaor000lpyTotalFlowTotalFlo

21、wTotalFlow2.33草酸酯加氫反應器2.342.35Temperature re Vpaor11QHeatQQHeatQTotalFlow2.30甲醇回收精制塔2.312.32Temperature re Vpaor000lpyTotalFlowTotalFlowTotalFlow2.33草酸酯加氫反應器2.342.35Temperature re Vpaor11QHeatQQHeatQTotalFlowTotalFlowTotalFlowlpyTotalFlowTotalFlowTotalFlow2.36單級壓縮機2.372.38Temperature re Vpaor11lpyTotalFlowTotalFlowTotalFlow2.39單級壓縮機2.402.41Temperature re WHeatWWHeatQ0lpyTotalFlowTotalFlow

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