周口师范学院设计集版h

2.2.2水洗塔 2.2.3CO2吸收塔 2.3第三工段能量衡 2.2.2水洗塔 2.2.3CO2吸收塔 2.3第三工段能量衡 2.3.1醋酸乙烯粗分塔 2.3.2三出口闪蒸罐 2.3.3VAC粗分塔 2.3.4VAC精制塔 2.3.5醋酸精制塔 附录三设备一览 3.1塔设备一览 3.2反应器一览 3.3换热器一览 泵一览 3.5储罐一览 3.6压缩机一览 3.7气液分离器一览 3.8管道一览 ~2Penta12物料衡算一览第一工段物料衡醋酸乙烯合成反应混合器~1Penta温度12物料衡算一览第一工段物料衡醋酸乙烯合成反应混合器~1Penta温度压力888111000000102030405 醋酸乙烯合成反应器~~Penta温度压力88100069.98669e-102030 醋酸乙烯合成反应器~~Penta温度压力88100069.98669e-102030454.995E-2.77E-3.38E-60111~3Penta123456701234~3Penta12345670123453.38E-607.58E-7111.1.3产物气液分离罐~4Penta温度压力8881001000123451.1.3产物气液分离罐~4Penta温度压力88810010001234567第二工段物料衡1.2.1酸洗塔~5Penta温度压力181118011110100001000000102012第二工段物料衡1.2.1酸洗塔~5Penta温度压力181118011110100001000000102012345671111.2.2水洗塔~6Penta3045060710206.848E-31.5304E-04501.2.2水洗塔~6Penta3045060710206.848E-31.5304E-04505.49E-8.63E-65.51E-07111111~7Penta温度压力11110111100000001020304.38E-4.382E-45060710203~7Penta温度压力11110111100000001020304.38E-4.382E-4506071020306.34E-6.343E-41505.49E-5.56E-5.56E-60吸收塔~8Penta温度压力10110100100001020304.385E-00450601.09E-1.70E-吸收塔~8Penta温度压力10110100100001020304.385E-00450601.09E-1.70E-70900005.79E-002.557E-701111~9Penta000000000000000-00010204.595E-306.348E-004505.562E-5.530E-2.27E-601.571E-3.497E-70~9Penta000000000000000-00010204.595E-306.348E-004505.562E-5.530E-2.27E-601.571E-3.497E-702.702E-800900+1.123E-5.256E-001.3.2三出口闪蒸罐~10Penta温度压力11110100010110000011.053E-23.8765E-34.355E-451.2E-653.61.8E-71.154E-1.3.2三出口闪蒸罐~10Penta温度压力11110100010110000011.053E-23.8765E-34.355E-451.2E-653.61.8E-71.154E--02.409E-011111.3.3VAC粗分塔~11Penta序组分名质量流量温度压力111100101101000016.092E-11.0875E-23.99E-1.724E-3.628E-1.3.3VAC粗分塔~11Penta序组分名质量流量温度压力111100101101000016.092E-11.0875E-23.99E-1.724E-3.628E-36.34305E-451.335E-5.56812E-61.95E-1.606E-3.3E-71.191E-1.3596E-2.86E-111111.3.4VAC精制塔~12Penta温度242.26.091E-34563.9E-71.06E-序组分名质量分11.3.4VAC精制塔~12Penta温度242.26.091E-34563.9E-71.06E-序组分名质量分11.172E-21.676E-3.9191E-6.8489E-1.123E-31.534E-42.20E-561.56E-3.32E-5.517E-7.31E-71.327E-2.6569E-1.963E-111~13Penta压力11000011110000101.430E-203.106E-308.84E-4050601.4001E-708.48E-802.4863E-103.08E-~13Penta压力11000011110000101.430E-203.106E-308.84E-4050601.4001E-708.48E-802.4863E-103.08E-23.9E-04.09E-6.8E-306.16E-405063.389E-03.4710704E-3.012E-1.3.5醋酸精制塔~14Penta温度压力110001110001002003451.263E-2.016E-60071.3.5醋酸精制塔~14Penta温度压力110001110001002003451.263E-2.016E-60070072.6685E-02.761E-1.87E-8011.6871E-1111~15Penta10021.75E-003457.343E-2.52E-~15Penta10021.75E-003457.343E-2.52E-61.6469E-0071.36482E-00111能量衡算一览第一工段能量衡醋酸乙烯合成反应混合2.2 醋酸乙烯合成反应器能量衡算一览第一工段能量衡醋酸乙烯合成反应混合2.2 醋酸乙烯合成反应器~16Penta∑Hin ∑Q ∑W ∑Hout --项 进料流股 出料流温度压力888111质量流量焓 -∑H2.4产物气液分离罐2.5~17Penta温度压力88110质量流量焓值-2.4产物气液分离罐2.5~17Penta温度压力88110质量流量焓值--∑Hin ∑Q ∑W ∑Hout ---项 进料流 出料流温度压力881质量流量焓值--∑H--2.6第二工段能量衡2.2.1酸洗塔2.72.8~18Penta∑Hin ∑Q ∑W ∑Hout 温度2.6第二工段能量衡2.2.1酸洗塔2.72.8~18Penta∑Hin ∑Q ∑W ∑Hout 温度压力181118011110质量流量491.焓 ---∑H∑Hin ∑Q ∑W ∑Hout ---∑H--2.2.2水洗塔2.92.102.2.3CO2吸收塔2.11~19Penta项进料流股进料流股出料出料温度压力1气相分02.2.2水洗塔2.92.102.2.3CO2吸收塔2.11~19Penta项进料流股进料流股出料出料温度压力1气相分0110∑Hin ∑Q ∑W ∑Hout 误---温度压力11110110质量流量焓 --∑H--2.12第三工段能量衡醋酸乙烯粗分塔2.132.14~20Penta温度116.压力800010质量流量2.12第三工段能量衡醋酸乙烯粗分塔2.132.14~20Penta温度116.压力800010质量流量焓值-----∑H--∑Hin ∑Q ∑W ∑Hout 误--质量流量焓值--∑H--2.3.2三出口闪蒸罐2.152.162.3.3VAC粗分塔2.17~21Penta∑Hin ∑Q ∑W ∑Hout --2.3.2三出口闪蒸罐2.152.162.3.3VAC粗分塔2.17~21Penta∑Hin ∑Q ∑W ∑Hout --温度压力11110100质量流量焓值---∑H--∑Hin ∑Q ∑W ∑Hout 误---2.182.3.4VAC精制塔2.19~22Penta温度242.压力110000质量流量焓值----∑H--∑Hin2.182.3.4VAC精制塔2.19~22Penta温度242.压力110000质量流量焓值----∑H--∑Hin ∑Q ∑W ∑Hout 误--温度压力11110100质量流量焓值----∑H--2.20醋酸精制塔2.22~23Penta∑Hin ∑Q ∑W ∑Hout 误温度2.20醋酸精制塔2.22~23Penta∑Hin ∑Q ∑W ∑Hout 误温度压力11000质量流量焓值---∑H--∑Hin ∑Q ∑W ∑Hout 误---~24Penta-~24Penta--设备一览3.1塔设备一览~25Penta设筒 设设 压 图 a设备一览3.1塔设备一览~25Penta设筒 设设 压 图 a头9棉1─头9棉1—头棉1─1-8-头棉1─VAC2-9-头棉1─3.2反应器一览3.23.3换热器一览~26Penta 图号型式公称 管长管数 排列方式3.2反应器一览3.23.3换热器一览~26Penta 图号型式公称 管长管数 排列方式换热面管程壳程个位 压 直 / 积 数 设 设设备 封头 1—VAC1-17-头9棉1─VAC2-10-31-1─3.4泵一览~27Penta1AEM1800-2.5-2223.8-9/19-—2112AEM1100-1.6-308.8-4.5/25-—2113AEM1700-2.5-1284-6/19-—2114AEM1300-1.6-832.8-9/25-—6115AEM1300-1.6-411.7-4.5/25-—6116AEM1800-2.5-2256.2-9/19-—1117AEM1100-1-292.9-4.5/25-—14118AEM1300-1.6-411.7-4.5/25-—6119AEM1300-1-440-4.5/25-—1211AEM450-1-38.1-3/19-—1211AEM1800-2.5-1755.1-9/25-—211AEM700-4-105-4.5/25-—4611AEM1400-1.6-716.5-6/25-—111AEM1100-1.6-308.8-4.5/25-—3.4泵一览~27Penta1AEM1800-2.5-2223.8-9/19-—2112AEM1100-1.6-308.8-4.5/25-—2113AEM1700-2.5-1284-6/19-—2114AEM1300-1.6-832.8-9/25-—6115AEM1300-1.6-411.7-4.5/25-—6116AEM1800-2.5-2256.2-9/19-—1117AEM1100-1-292.9-4.5/25-—14118AEM1300-1.6-411.7-4.5/25-—6119AEM1300-1-440-4.5/25-—1211AEM450-1-38.1-3/19-—1211AEM1800-2.5-1755.1-9/25-—211AEM700-4-105-4.5/25-—4611AEM1400-1.6-716.5-6/25-—111AEM1100-1.6-308.8-4.5/25-—211AEM450-1-34.6-3/19-—1411AEM1700-2.5-1284-6/19-—211~28Penta序 设备位 设备名 流 扬 转 电 型 材 个数/ 机 1P-泵EAP300-22P-CQB100-80-23P-CQB80-65-24P-3EHG65-40-25P-~28Penta序 设备位 设备名 流 扬 转 电 型 材 个数/ 机 1P-泵EAP300-22P-CQB100-80-23P-CQB80-65-24P-3EHG65-40-25P-26P-EDS600-27P-3EHG100-65-28P-3EHG80-50-29P-82P-4EHG65-40-23.5储罐一览~29Penta设备位 名 内径 高 设计 设计 材 介 安装 个 度 力 /1Q235-12Q235-13Q235-1P-泵42P-泵3.5储罐一览~29Penta设备位 名 内径 高 设计 设计 材 介 安装 个 度 力 /1Q235-12Q235-13Q235-1P-泵42P-泵42P-泵2P-32P-8ZX50-32-2P-2P-VAC2~30Penta4醋酸VACQ235-15VAC粗分塔回罐16VAC精制塔回罐17罐1819Q235-3Q235-2~30Penta4醋酸VACQ235-15VAC粗分塔回罐16VAC精制塔回罐17罐1819Q235-3Q235-2Q235-3Q235-4VAC13.6压缩机一览~31Penta 进口气体温出3.6压缩机一览~31Penta 进口气体温出口气体量 1181850/0.1-1143.7气液分离器一览~32Penta 1VAC3.7气液分离器一览~32Penta 1VAC1-21─31─41─5VAC分离1-3.8管道一览~33Penta管道编体积流率壁厚管气相摩尔率管PG0101-LIB-81PG0102-LIB-1PG0103-LIB-3.8管道一览~33Penta管道编体积流率壁厚管气相摩尔率管PG0101-LIB-81PG0102-LIB-1PG0103-LIB-1PG0103-LIB-61PG0104-LIB-1PG0105-LIE-管PG0106-LIE-1管PG0106-LIE-1管PG0107-1~34PentaLIB-PG0108-LIB-1PG0109-LIB-1LIB-1HLIB-LIB-1H80H8~34PentaLIB-PG0108-LIB-1PG0109-LIB-1LIB-1HLIB-LIB-1H80H80管PIE-0管PG0202-PIB-1~35PentaPIB-60PIB-60H40PG0205-LIB-1PIB-40PIB-40H0PG0208-LIB-1~35PentaPIB-60PIB-60H40PG0205-LIB-1PIB-40PIB-40H0PG0208-LIB-1H0PG0202-LIB-140~36PentaHPG0204-LIB-61PG0205-LIB-61PG0206-LIB-61H0PG0208-LIB-61PIB-5PG0301-LIB-1PIB-~36PentaHPG0204-LIB-61PG0205-LIB-61PG0206-LIB-61H0PG0208-LIB-61PIB-5PG0301-LIB-1PIB-60PIB-50PIE-50管~37PentaPG0305-L