賽區(qū)-理工學(xué)院running隊(duì)伍-設(shè)計(jì)05附錄2007版

附錄一物料衡算一覽 MN再生與DMO合成工 MN再生反應(yīng)精餾塔 甲醇精餾塔 催化偶聯(lián)固定床反應(yīng)器 DMO吸收塔 DMO成品塔 循環(huán)氣冷凝閃蒸罐 脫DMC常壓塔 脫甲醇加壓塔 DMO加氫反應(yīng)工 加氫固定床反應(yīng)器 循環(huán)氫氣冷凝閃蒸罐 乙二醇精制工 甲醇回收塔 脫氫組分塔 DMO-MG回收塔 附錄二能量衡 MN再生與DMO反應(yīng)工 換熱 塔設(shè) 反應(yīng)器設(shè) 分離設(shè) 換熱 塔設(shè) DMO加氫反應(yīng)工 換熱 反應(yīng)設(shè) 表2.13加氫反應(yīng)器的能量衡算 分離設(shè) 乙二醇精制工 換熱 塔設(shè) 附錄三設(shè)備一覽 塔設(shè) 換熱 儲(chǔ) 氣液分離設(shè) 壓縮 反應(yīng) 附錄四配管一覽 附錄一料衡算一覽MN再生與DMO合成工MN再生反應(yīng)精餾塔表 MN再生反應(yīng)精餾塔物料衡進(jìn)料物流 進(jìn)料物流 出料物流 出料物流TemperaturePressureVapor0110MoleFlowMassFlowVolumeFlow MassFlow0000CH3NO-00000003.56E-00000000000000002.83E-6.10E-06.22E-00000000Mass0000CH3NO-002.73E-000002.12E-00001000000000001.46E-02.29E-3.63E-03.70E-00000000甲醇精餾塔1.2進(jìn)料物流進(jìn)料物流 出料物流 出料物流TemperaturePressureVapor000MoleFlowMassFlowVolumeFlowMassFlow000CH3NO-1.08E-0003.56E-000000000006.10E-006.22E-00000000Mass000CH3NO-2.73E-7.89E-9.81E-0002.12E-000000000003.63E-003.70E-00000000催化偶聯(lián)固定床反應(yīng)器1.3進(jìn)料物流進(jìn)料物流 出料物流TemperaturePressureVapor1MoleFlowMassFlowVolumeFlow MassFlow0CH3NO-0000002.83E-2.83E-0000Mass0CH3NO-0000001.13E-1.13E-1.77E-1.77E-0000DMO吸收塔1.4DMOTemperaturePressureVapor010MoleFlowMassFlowVolumeFlowMassFlow09.63E-CH3NO-00000004.17E-0000000002.97E-02.83E-2.83E-1.11E-000000000Mass08.60E-CH3NO-000001.48E-07.49E-03.72E-10000000001.13E-2.65E-1.85E-01.77E-2.53E-1.14E-07.46E-00000000DMO成品塔1.5DMO進(jìn)料物流進(jìn)料物流 出料物流 出料物流TemperaturePressureVapor000MoleFlowMassFlowVolumeFlowMassFlowCH3NO-0005.01E-2.82E-0000001.17E-1.11E-1.11E-5.73E-1.98E-000000MassCH3NO-0001.48E-4.34E-7.78E-7.49E-4.38E-2.00E-2.95E-0000001.85E-5.43E-1.82E-1.14E-3.34E-8.90E-7.46E-3.08E-000000DMC-甲醇采出塔1.6DMC-進(jìn)料物流 出料物流 出料物流TemperaturePressureVapor000MoleFlowMassFlowVolumeFlowMassFlow7.66E-CH3NO-0006.86E-1.02E-0000001.24E-1.11E-1.11E-2.22E-1.63E-000000Mass2.14E-CH3NO-0004.34E-2.09E-3.11E-0000005.43E-3.45E-5.49E-3.34E-3.10E-6.74E-4.95E-000000循環(huán)氣冷凝閃蒸罐1.7進(jìn)料物流 出料物流 出料物流TemperaturePressureVapor101MoleFlowMassFlowVolumeFlow MassFlow9.63E-8.35E-3.69E-0004.17E-1.46E-7.15E-0000002.97E-1.40E-02.83E-2.23E-2.83E-000000Mass8.60E-2.49E-4.71E-0007.97E-3.72E-4.36E-9.12E-0000002.65E-4.18E-02.53E-6.64E-3.61E-000000DMC-甲醇變壓分離工DMC常壓塔1.8DMCTemperaturePressureVapor00MoleFlowMassFlowVolumeFlowMassFlow2.61E-CH3NO-0000000000000000000000000000000Mass4.03E-2.82E-CH3NO-000000000004.16E-3.90E-1.97E-000000000000000000脫甲醇加壓塔1.9TemperaturePressure111Vapor000MoleFlowMassFlowVolumeFlowMassFlow2.61E-1.57E-2.61E-CH3NO-0000000000000000000000000000000Mass2.82E-1.80E-4.54E-000000000003.90E-6.94E-5.24E-000000000000000000DMO加氫反應(yīng)工加氫固定床反應(yīng)器1.10進(jìn)料物流 進(jìn)料物流TemperaturePressureVapor11MoleFlowMassFlowVolumeFlow MassFlowCH3NO-005.01E-02.82E-05.73E-01.98E-0MassCH3NO-003.52E-01.98E-01.02E-1.02E-8.87E-4.02E-01.39E-0循環(huán)氫氣冷凝閃蒸罐1.11進(jìn)料物流進(jìn)料物流 進(jìn)料物流TemperaturePressure22Vapor10MoleFlowMassFlowVolumeFlow MassFlowCH3NO-0000000000MassCH3NO-0000002.26E-1.88E-7.26E-0000乙二醇精制工甲醇回收塔1.12進(jìn)料物流 出料物流 出料物流 出料物流TemperaturePressure2Vapor0100MoleFlowMassFlowVolumeFlow MassFlow2.07E-4.50E-CH3NO-0000000000007.59E-01.83E-4.18E-000000001.21E-1.74E-Mass4.76E-2.10E-CH3NO-0000000000001.88E-1.75E-4.28E-2.73E-7.26E-6.77E-04.22E-1.95E-4.19E-000000002.78E-8.11E-脫氫組分塔1.13TemperaturePressureVapor000MoleFlowMassFlowVolumeFlowMassFlowCH3NO-0000000001.39E-4.40E-0002.19E-0000001.41E-MassCH3NO-0000000002.73E-7.60E-4.65E-1.47E-0003.19E-7.31E-0000004.69E-8.86E-DMO-MG回收塔1.14DMC-MG進(jìn)料物流 出料物流 出料物流TemperaturePressureVapor000MoleFlowMassFlowVolumeFlowMassFlow3.78E-CH3NO-0000000000002.53E-0000001.31E-Mass4.20E-CH3NO-0000000007.60E-5.13E-1.63E-0003.19E-2.81E-6.86E-0000001.45E-附錄二量衡MN再生與DMO反應(yīng)工換熱2.1MNDMODMODMO塔設(shè)2.2MN再生反應(yīng)塔能量衡算TemperaturePressureVapor0110MoleFlowMassFlowVolumeFlow∑H2.3甲醇回收塔能量衡算進(jìn)料物流 出料物流 出料物流TemperaturePressureVapor000MoleFlowMassFlowVolumeFlow∑H2.4DMO吸收塔能量衡算TemperaturePressureVapor010MoleFlowMassFlowVolumeFlow∑H2.5DMO成品塔能量衡算進(jìn)料物流 出料物流 出料物流TemperaturePressureVapor000MoleFlowMassFlowVolumeFlow∑H2.6DMC-甲醇采出塔能量衡算TemperaturePressureVapor000MoleFlowMassFlowVolumeFlow∑H2.7催化氧化偶聯(lián)反應(yīng)器能量衡算進(jìn)料物流 出料物流TemperaturePressureVapor1MoleFlowMassFlowVolumeFlow ∑H分離設(shè)2.8循環(huán)氣冷凝閃蒸罐TemperaturePressureVapor010MoleFlowMassFlowVolumeFlow∑HDMC-甲醇變壓分離工換熱DMC塔設(shè)2.10DMC常壓塔能量衡算進(jìn)料物流 出料物流 出料物流TemperaturePressureVapor00MoleFlowMassFlowVolumeFlow∑H2.11脫甲醇加壓塔能量衡算TemperaturePressure111Vapor000MoleFlowMassFlowVolumeFlow∑HDMO加氫反應(yīng)工換熱2.12DMO反應(yīng)設(shè)2.13加氫反應(yīng)器的能量衡算進(jìn)料物流 進(jìn)料物流TemperaturePressureVapor11MoleFlowMassFlowVolumeFlow --∑H--分離設(shè)2.14循環(huán)氫氣冷凝閃蒸罐能量衡算TemperaturePressure22Vapor10MoleFlowMassFlowVolumeFlow --∑H--乙二醇精制工換熱2.15來(lái) 說(shuō) 熱負(fù)荷DMO-MGDMO-MG塔設(shè)2.16甲醇回收塔能量衡算進(jìn)料物流 出料物流 出料物流 出料物流TemperaturePressure2Vapor0100MoleFlowMassFlowVolumeFlow ∑H2.17脫輕組分塔能量衡算TemperaturePressureVapor000MoleFlowMassFlowVolumeFlow∑H2.18DMO-MG回收塔能量衡算進(jìn)料物流 出料物流 出料物流TemperaturePressureVapor000MoleFlowMassFlowVolumeFlow∑H附錄三備一覽塔設(shè)3.1編設(shè)名類塔內(nèi)塔封形設(shè)計(jì)溫℃設(shè)計(jì)壓殼材保溫單tMNDMODMODMC1DMO-MG換熱3.2圖型類管管規(guī)排列方換熱殼管臺(tái)111111121111111111121111111111121111111111111111111121111111111111121111泵3.3流流軸功率電機(jī)圖類型泵揚(yáng)效轉(zhuǎn)數(shù) m％242424242DMO42DMO2DMO24222622222322EG26222122DMO-MG2DMO-MG2DMO-MG42