賽區(qū)-32共價(jià)鍵隊(duì)-321設(shè)計(jì)5附錄

第一章物料CO羰化偶聯(lián)工段物料..................................................................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 1.5總 第二章能量總 能量的主要依 能量任 能量..........................................................................................................CO羰化偶聯(lián)工段能量..................................................................酯再生工段能量............................................................................碳酸二甲酯提純工段能量...........................................................乙二醇提純工段能量....................................................................甲醇水雙效精餾工段能量............................................................附錄三設(shè)備一覽 附錄四配管一覽 第一章物料CO羰化偶聯(lián)工段物料物流Temperature-物流Temperature-PressureVpaor111Enthalpy---TotalTotalFlowTotalFlowMassFlow00000000000000000000000000000000000000000表 CO羰化偶聯(lián)反應(yīng)器（R0201）物料物流TemperaturePressureVpaor11EnthalpyTotalFlowTotalFlowTotalFlowMassFlow00000000000000表 CO羰化偶聯(lián)反應(yīng)器（R0202）物料物流TemperaturePressureVpaor11EnthalpyTotalFlowTotalFlowTotalFlowMassFlow0000000000酯再生工1.51.6酯再生工段總物料TemperaturePressureVpaor1100110-------TotalTotalTotalMass00000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000001.7反應(yīng)精餾塔（T0101）物料物流TemperaturePressureVpaor1010Enthalpy-TotalFlowTotalFlowTotalFlowMassFlow0000000000000000000000000000000000000碳酸二甲酯提純工1.9碳酸二甲酯提純工段總物料物流TemperaturePressureVpaor001101Enthalpy-4-4--3-1-3-6Total3TotalFlow2Total7MassFlow00000000000000000000000000000001000600000000000000000001.10預(yù)分離塔（T0301）物料物流Temperature0PressureVpaor0010EnthalpyTotalFlowTotalFlowTotalFlowMassFlow0000000000003.58e-9.0519e-000000001.11吸收塔（T0302）物料物流TemperaturePressureVpaor1010EnthalpyTotalFlowTotalFlowTotalFlowMassFlow00000000000000001.4162e-01.0026e-0000000000001.12高壓共沸精餾塔（T0303）物料物流TemperaturePressureVpaor0001EnthalpyTotalFlowTotalFlowTotalFlowMassFlow00003.4331e-1.2967e-000000002.5784e-5.5072e-00002.2834e-00001.13碳酸酯精制塔（T0304）物料物流TemperaturePressureVpaor000EnthalpyTotalFlowTotalFlowTotalFlowMassFlow000000000000000000000乙二醇提純工1.15乙二醇提純工段總物料物流TemperaturePressureVpaor15.6566e-0100Enthalpy-----TotalFlowTotalFlowTotalFlowMassFlow006.2041e-000001.1426e-000000000000000001.6181e-000001.4855e-9.2882e-0002.2202e-1.2235e-00001.0836e-6.6389e-08.6416e-9.4494e-001.16乙二醇精制塔（T0401）物料物流TemperaturePressureVpaor0100EnthalpyTotalFlowTotalFlowTotalFlowMassFlow7.3759e-000000000000000000001.6807e-1.9846e-1.4308e-1.17甲醇精制回收塔（T0402）物料物流TemperaturePressureVpaor000EnthalpyTotalFlowTotalFlowTotalFlowMassFlow0000000000000001.18草酸酯加氫反應(yīng)器（R0401）物料物流TemperaturePressure22Vpaor11EnthalpyTotalFlowTotalFlowTotalFlowMassFlow6.2041e-1.1426e-00001.6181e-1.4855e-2.2202e-01.0836e-8.6416e-0甲醇水雙效精餾工1.20雙效精餾工段總物料物流TemperaturePressureVpaor00EnthalpyTotalFlowTotalFlowTotalFlowMassFlow000000000000000000000000000001.21高壓塔（T0501）物料物流TemperaturePressureVpaor0010EnthalpyTotalFlowTotalFlowTotalFlowMassFlow00001.0948e-00000006.2207e-0000000000000000000000001.22常壓塔（T0502）物料物流TemperaturePressureVpaor000EnthalpyTotalFlowTotalFlowTotalFlowMassFlow00000000000000000000000001.1941e-000000000000000000001.5總1.23123.6萬(wàn)噸/23.34萬(wàn)噸/36.9萬(wàn)噸/46.9萬(wàn)噸/1.24/質(zhì)量指標(biāo)1.25/第二章能量總擬建一套年產(chǎn)25萬(wàn)噸的乙二醇裝置，在全工藝段中伴隨著物料從一系或單元進(jìn)入另一系或單元在發(fā)生質(zhì)量傳遞的同時(shí)也伴隨著能量的消耗釋放和轉(zhuǎn)化。其中的能量變換數(shù)量關(guān)系可以從能量求得，對(duì)于新設(shè)計(jì)的車間，可以由此確定的設(shè)備?？傊?，通過(guò)下述能量，可以為后續(xù)設(shè)計(jì)工作中提高熱量的利用率，降能量的主要依工程依據(jù)化工設(shè)計(jì)中關(guān)于熱量的基本思想和要求遵循基與實(shí)際工藝相結(jié)合的原則，進(jìn)行熱量書的編制。其中一個(gè)主要依據(jù)是能量平衡方程：Q+W=ΣHout–能量任在進(jìn)行乙二醇裝置的熱量中，主要通過(guò)定量計(jì)算完成下述基本任務(wù)確定工藝單元中物料輸送機(jī)械（如泵）提高熱量集成度，充分利用余熱，提高能量利用率，降低能耗能量CO羰化偶聯(lián)工段能量CO羰化偶聯(lián)反應(yīng)器2.1QHeat 2.2物流TemperaturePressureVpaor11EnthalpyTotalFlowTotalFlowTotalFlow2.3Q-0CO羰化偶聯(lián)反應(yīng)器2.4QHeat 2.5物流TemperaturePressureVpaor11EnthalpyTotalFlowTotalFlowTotalFlow2.6Q酯再生工段能量反應(yīng)精餾塔2.7QHeat 2.8物流TemperaturePressureVpaor1010EnthalpyTotalFlowTotalFlowTotalFlow2.9Q單級(jí)壓縮機(jī)2.10WHeat 2.11物流Temperature-PressureVpaor11EnthalpyTotalFlowTotalFlowTotalFlow2.12W碳酸二甲酯提純工段能量預(yù)分離塔2.13QHeat 2.14物流TemperaturePressureVpaor0010EnthalpyTotalFlowTotalFlowTotalFlow2.15Q吸收塔2.16QHeat 0002.17物流TemperaturePressureVpaor1010EnthalpyTotalFlowTotalFlowTotalFlow2.18Q0高壓共沸精餾塔2.19QHeat 2.20物流TemperaturePressureVpaor0001EnthalpyTotalFlowTotalFlowTotalFlow2.21Q碳酸酯精制塔2.22QHeat 2.23物流TemperaturePressureVpaor000EnthalpyTotalFlowTotalFlowTotalFlow2.24Q氣液分離器2.25QHeat 02.26物流TemperaturePressureVpaor01EnthalpyTotalFlowTotalFlowTotalFlow2.27Q0乙二醇提純工段能量乙二醇精制塔2.28QHeat 2.29物流TemperaturePressureVpaor0100EnthalpyTotalFlowTotalFlowTotalFlow2.30Q甲醇回收精制塔2.31QHeat 2.32物流TemperaturePressureVpaor000EnthalpyTotalFlowTotalFlowTotalFlow2.33Q草酸酯加氫反應(yīng)器2.34QHeat 2.35物流TemperaturePressureVpaor11EnthalpyTotalFlowTotalFlowTotalFlow2.36Q0單級(jí)壓縮機(jī)2.37WHeat 2.38物流TemperaturePressureVpaor11EnthalpyTotalFlowTotalFlowTotalFlow2.39W單級(jí)壓縮機(jī)2.40WHeat 2.41物流TemperaturePressureVpaor11EnthalpyTotalFlowTotalFlowTotalFlow2.42W氣液分離器2.43QHeat 2.44物流TemperaturePressureVpaor10EnthalpyTotalFlowTotalFlowTotalFlow2.45Q甲醇水雙效精餾工段能量高壓塔2.46QHeat 02.47物流TemperaturePressureVpaor0010EnthalpyTotalFlowTotalFlowTotalFlow2.48Q常壓塔2.49QHeat 02.50物流TemperaturePressureVpaor000EnthalpyTotalFlowTotalFlowTotalFlow2.51Q附錄備一覽泵泵 揚(yáng)軸功總軸功率電機(jī)總功率231DMC預(yù)分醇1DMC預(yù)分111DMC精制塔1DMO加氫泵2223215設(shè)計(jì)溫度MNF1Z-4AF1Z-3AF1Z-3AF1Z-3ADMCF1Z-4AF1Z-4AF1Z-4AF1Z-4AF1Z-4A封頭內(nèi)徑 列管壁反應(yīng)溫腐蝕余質(zhì)量反應(yīng)標(biāo)準(zhǔn)62 火反應(yīng)標(biāo)準(zhǔn)62 火反應(yīng)標(biāo)準(zhǔn)62 火尺寸度內(nèi)管列管規(guī)格管數(shù)根管程數(shù)換熱面積重量/BEM600-0.35/0.7-48.8-1.5/19-11BEM1000-2.2/0.7-219.3-3.0/19-11BEM400-0.7/0.35-19.7-2.0/19-11BEM400-1.7/0.7-30.1-3.0/19-11BEM800-2.2/1.1-138.0-3.0/19-11BEM400-0.35/0.7-14.5-1.5/19-11BEM500-0.35-47.5-3.0/19-11BEM1400-0.35-900.5-6.0/19-11BEM450-0.35-28.4-3.0/19-22BEM1600-0.35-1175.9-9.0/19-11BEM219-0.35-2.8-1.5/19-66BEM219-0.35-2.8-1.5/19-11BEM273-0.35-5.4-1.5/19-11BEM273-0.35/9.0-4.7-1.5/19-66BEM450-0.35/9.0-61.3-6.0/19-11BEM219-0.35/9.0-2.8-1.5/19-14BEM1000-0.35/9.0-219.3-3.0/19-11BEM325-2.2/9.0-8