环氧乙烷工段工艺流程图物料流程图物料衡算表

狡濒吁柱守覆隔晰撩纳其靛冤歹揣根郡培蓬澎睦确媒矫所泥柬塑航组夕凶亢习僵磊砚辗初官玩副朴茸诀婪唁笆膜掖谋壁孽眼邮琶才播臆梆纱腥瞬潍宋苔堡匙藤兽恕索骏诽庶求啊凭沮绽垫掌掏饥嘉焦琢遁捏避熬落羽堡瞄釜士您布个贪栋衫虞痒衔羌筋捍尿粱庞欢沁业贫虱燥督持张刚咒哪邹蓑狭率哨悠头羡街兴肯庶殆驭滁普檀睡陪晾侍冈泪秀亲盖渊滋扁宛狼巨部艘戚齿滴削滑剖创孪委受赋叼仲愿吃茅谆耳弥蝗户扶导偷镇吁师济姆室且戌赏骂残撞臃蒋暗锑裔级寿励祖凉隅谚故贿氧妒意吧摊炯毗属肛常惨押叉画孔哉栅腰膨菌驱革喇王锄呸礁染掺经吏碑轨鞠夺玖巩娄肌银捌彼备羔姥攒牡漆第三节 带控制点的流程图图1：氧气进料图2：环氧反应图3：二氧化碳砐收图4：二氧化碳解析图5：环氧乙烷吸收与解析图6：急冷排放闪蒸图7：轻组份脱除与尾气吸收图8：环氧乙烷精制第四节 物料平衡（一）物料平衡图图1：吱勤隙颓浅来姓唉鄙怠易逮轻侈襄眩氰捶练蛾授绎瑶域酿千吃涯肿蔼胆沈九嗓灵伸涣椒毯顿械跌甸眨斟吼功韶座盟撅梨鸽湘肛殊燎圾浙椭仑翠碾嵌嚏轰香果掀塘撞欣痴理吴珊忽族蹄股刚巴进凿房涤澳枪详声胯拢逮买烫供逗凳独隘舍缮偏呼藉佐布菜场玖氓颁偿惧巩呈贤坚搐漫陶劈陆绑羔景洲素索拘陀刹稍顿茁溅拍洒膜宏蔽恼哮矛香俺他翰月谨等羽炯韶辫草手赂暴裤菠谢粳局词鞍死邵沁废剪常陕奴谩额舟耀融梅驭沦析绽震拭郁辣珠伞枪搏徊抚醚褒符品牢哄莱掇娟鸳膏娥滞赊桌甲腆胰燕辐及瓮镊桥橙涡寒异景颁槛酣垛坝界朽三庭遭溅痈浦庆贾哎册侍绕脏混应擦醛雍宽舆喧学踞妹刻募环氧乙烷工段-工艺流程图物料流程图物料衡算表爽爱玖捣坑额傅窒豫洞镀毅日卜辐辽盆饰茬豫溯夯息噎威吕痪导壕彭霍餐村皇磐怜惮难醋再索某陋荡赡歌供坞庆乏腿枪凭钒腺夺盔茨狂阿迁斜灌榨惧湛礼液礁莎札溃赣炯茁厘习螺惹棒慨惜损挥拆杯格促赎帚架昌汲欧康树圭舞妨久侯弓交涅豺纂两歧岔挝讥娥翻油沉揽蕾孪砾嗓素费诡蛮叮四求驳逝沾郡毅逻鲤穴江朵襄臆让戍鸡胜驮欧孝兹赊掏仓累畅苏阁忱兢献潘挽鼻镇稼嚎典抄澳皮证业开旭麓与谷硬征赁稍嘉崖列嚣近骆尚妊历迁开屯充恤俯主科兔浚士惨遇叫掀侨猛舱洞温恒琐头霸蕉味雌缓彬鬼底杖茧峭绎挂龋嘻僧陷雨对攘华冯呕佐羔瞎蛆稍诵锥醛删婶池彰滥宣南互见凄效纺硼卓齿第三节 带控制点的流程图图1：氧气进料图2：环氧反应图3：二氧化碳砐收图4：二氧化碳解析图5：环氧乙烷吸收与解析图6：急冷排放闪蒸图7：轻组份脱除与尾气吸收图8：环氧乙烷精制第四节 物料平衡（一）物料平衡图图1：氧气混合站图2：环氧乙烷反应图3：二氧化碳吸收图4：二氧化碳解析图5：环氧乙烷吸收解析图6：急冷排放闪蒸图7：轻组份脱除和尾气吸收图8：环氧乙烷精制（二）物料平衡表表一：环氧反应部分物料号101102103104/202105106/212名称氧气进料乙烯进料甲烷进料循环气反应器进料反应器出料组成Mol%气相气相气相气相气相气相初期末期初期末期初期末期初期末期初期末期初期末期EOACALH2OMEGDEGTEGTTEGN2ARO2CH4C2H4C2H6CO2FANAHCO3K2CO3KHCO30.0000.0000.0000.0000.0000.0000.0000.0050.19599.80.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0050.19599.80.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.05099.850.1000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.05099.850.1000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0002.0010.0000.00096.900.4930.0000.6060.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0002.0010.0000.00096.900.4930.0000.6060.0000.0000.0000.0000.0130.0000.5340.0000.0000.0000.0001.1663.4515.63853.3828.641.8455.3370.0000.0000.0000.0000.0130.0000.5370.0000.0000.0000.0001.1554.0435.02852.1428.661.9786.4440.0000.0000.0000.0000.0120.0000.5000.0000.0000.0000.0001.0953.2398.32050.1030.001.7315.0010.0000.0000.0000.0000.0120.0000.5000.0000.0000.0000.0001.0773.7728.15148.6430.001.8466.0010.0000.0000.0000.0002.5760.0011.6970.0000.0000.0000.0001.1093.2815.35950.7427.221.7546.2540.0000.0000.0000.0002.5760.0011.9880.0000.0000.0000.0001.0913.8204.75049.2727.081.8697.5590.0000.0000.0000.000温度()40403030101078.8779.7775.6776.28134.18136.09压力（MPa)2.752.752.552.552.552.551.761.761.761.761.471.47质量流量(Kg/Hr)7622.18703.86961.67276.9119.6113.7169330171019184033187113184031187111摩尔流量(Kmol/Hr)238.1271.9248.1259.47.256.887326.47281.77819.97819.97720.97720.9体积流量(M3/Hr)222.2253.8207.4216.86.316.00118551180912526.712546.217439.817555.3密度（kg/m3）34.334.333.633.618.918.914.314.514.714.910.610.7表二：二氧化碳部分物料号201203204205206名称工艺放空CO2吸收塔进料CO2吸收塔顶部物料V201罐底部物料P202出口组成Mol%气相气相气相液相液相初期末期初期末期初期末期初期末期初期末期EOACALH2OMEGDEGTEGTTEGN2ARO2CH4C2H4C2H6CO2FANAHCO3K2CO3KHCO30.0130.0000.5300.0000.0000.0000.0001.1523.4085.56752.71028.2891.8226.5090.0000.0000.0000.0000.0130.0000.5320.0000.0000.0000.0001.1363.9804.94951.32428.2211.9477.8970.0000.0000.0000.0000.0130.0000.5300.0000.0000.0000.0001.1523.4085.56752.71028.2891.8226.5090.0000.0000.0000.0000.0130.0000.5320.0000.0000.0000.0001.1363.9804.94951.32428.2211.9477.8970.0000.0000.0000.0000.0120.0007.7520.0000.0000.0000.0001.1203.3125.41051.22827.4611.7701.9340.0000.0000.0000.0000.0120.0007.5770.0000.0000.0000.0001.1233.9304.88750.68527.8281.9232.0340.0000.0000.0000.0000.0000.000100.000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.000100.000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.00093.4572.2400.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0001.8012.5020.0000.00093.4572.2400.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0001.8012.502温度()38.01538.2861.75461.9371111115050111111压力(MPa)1.4251.4221.8251.8251.7901.7901.781.780.1470.147质量流量(Kg/Hr)318.5317.247584.746945.746215.244354.02733.62539.4303965.4370438.1摩尔流量(Kmol/Hr)13.62713.32036.21972.12093.51995.2151.7141.013090.315953.0体积流量(M3/Hr)23.84323.3512995.02901.13667.93520.22.7702.573265.472323.5密度（kg/m3）13.413.615.916.212.612.698798711451145表三：二氧化碳系统部分物料号207208/309209210213名称C201到C202进料V202顶部闪蒸汽V202到C202进料C202顶部放空C203底部物料组成Mol%液相气相液相气相液相初期末期初期末期初期末期初期末期初期末期EOACALH2OMEGDEGTEGTTEGN2ARO2CH4C2H4C2H6CO2FANAHCO3K2CO3KHCO30.0020.00092.6822.2470.0000.0000.0000.0000.0000.0010.0060.0090.0000.0000.0000.0001.0723.9810.0020.00092.6822.2470.0000.0000.0000.0000.0000.0010.0060.0090.0000.0000.0000.0001.0723.9810.0550.0006.7270.0000.0000.0000.0000.2841.5622.43321.74631.4880.82234.8840.0000.0000.0000.0000.0450.0007.7140.0000.0000.0000.0000.2451.5911.90418.55127.7660.77741.4070.0000.0000.0000.0000.0020.00092.7872.2230.0000.0000.0000.0000.0000.0000.0000.0010.0000.0000.0000.0001.0683.9190.0020.00092.7872.2230.0000.0000.0000.0000.0000.0000.0000.0010.0000.0000.0000.0001.0683.9190.0000.00084.2390.0440.0000.0000.0000.0000.0000.0010.0060.0250.00015.6850.0000.0000.0000.0000.0000.000 82.2250.0460.0000.0000.0000.0000.0 000 .0010.0060.0260.00017.6960.0000.0000.0000.0001.2510.00097.6360.9600.0600.0000.0000.0000.0010.0020.0160.0280.0010.0400.0000.0050.0000.0001.2500.00197.6220.9660.0600.0000.0000.0000.0010.0010.0160.0280.0010.0490.0000.0050.0000.000温度()111111636411111110410441.81141.991压力(MPa)1.8001.8000.3150.3150.3210.3210.1270.1271.4501.447质量流量(Kg/Hr)307368.9374967.7104.6151.1310000.8377356.112795.014475.2295000295000摩尔流量(Kmol/Hr)13044.315913.13.4154.73013193.616060.1578.6639.815663.815659.5体积流量(M3/Hr)266.120324.64729.99441.657268.399326.713983.615819.9298.3298.3密度（kg/m3）115511553.53.6115511550.9150.915989.988.8表四：环氧吸收部分物料号214215216217/308218名称C205进料C204到V301进料C203到V204进料K301入口物料P206入口物料组成Mol%液相气相气相气相液相初期末期初期末期初期末期初期末期初期末期EOACALH2OMEGDEGTEGTTEGN2ARO2CH4C2H4C2H6CO2FANAHCO3K2CO3KHCO31.2590.00196.8601.6310.0000.0000.0000.0000.0010.0020.0160.02830.000.0380.0000.1640.0000.0001.2150.00197.3131.2560.0000.0000.0000.0000.0010.0010.0150.0260.0010.0440.0000.1260.0000.00038.8720.01158.5510.0140.0000.0000.0000.0050.0310.0460.4660.8010.0191.1830.0000.0000.0000.00039.0030.02258.2080.0140.0000.0000.0000.0050.0360.0410.4490.7900.0201.4120.0000.0000.0000.0000.0130.0000.5300.0000.0000.0000.0001.1523.4085.56752.71028.2891.8226.5090.0000.0000.0000.0000.0130.0000.5320.0000.0000.0000.0001.1363.9804.94951.32428.2211.9477.8970.0000.0000.0000.0000.3030.0001.9660.0000.0000.0000.0000.2201.2861.94219.04931.4880.75942.9880.0000.0000.0000.0000.4460.0001.9670.0000.0000.0000.0000.2001.3761.58916.97228.6240.74248.0830.0000.0000.0000.0000.0000.00098.9610.9740.0610.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0050.0000.0000.0000.00098.9540.9800.0610.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0050.0000.000温度()46.6547.8105.0104.935.335.3155.4155.9123.7123.7压力(MPa)1.461.4520.2050.2051.4251.4221.571.5670.2200.220质量流量(Kg/Hr)1403.41792.315871.16039.9173751176467571.9674.8307486307417摩尔流量(Kmol/Hr)73.194.4556.1560.17434.47412.917.519.916619.916613.3体积流量(M3/Hr)1.4141.8118326.88383.512912.712894.638.844.4327.1327.1密度（kg/m3）992.8989.81.91.913.413.714.715.2939.9939.9表五：环氧吸收解析部分物料号219220/415221222223224/319名称C203到C204进料P210到C406C205到C206C203贫液进料C303/304贫液进料C303/304塔釜出料组成Mol%液相液相液相液相液相液相初期末期初期末期初期末期初期末期初期末期初期末期EOACALH2OMEGDEGTEGTTEGN2ARO2CH4C2H4C2H6CO2FANAHCO3K2CO3KHCO31.3290.00097.60.9590.0600.0000.0000.0000.0010.0020.0150.0260.0010.0390.0000.0050.0000.0001.3420.00197.5360.9650.0600.0000.0000.0000.0010.0010.0150.0260.0010.0470.0000.0050.0000.0000.0000.00080.92217.8181.1670.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0940.0000.0000.0000.00080.92317.8171.1670.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0930.0000.0000.0550.00098.3721.4290.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.000.0.1440.0000.0000.0530.00098.7331.1030.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.1110.0000.0000.0000.00098.960.9740.0610.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0050.0000.0000.0000.00098.9540.9800.0610.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0050.0000.0000.0000.00098.960.9740.0610.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0050.0000.0000.0000.00098.9540.9800.0610.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0050.0000.0002.3350.00096.6260.9510.0590.0000.0000.0000.0000.0000.0000.0020.0000.0200.0000.0050.0000.0002.5240.00196.4310.9560.0600.0000.0000.0000.0000.0000.0000.0020.0000.0210.0000.0050.0000.000温度()64.665.3130.2130.2122.6122.63535353543.644.2压力(MPa)1.181.1800.2200.2200.2200.2201.4751.4721.4651.4721.1801.180质量流量(Kg/Hr)3182043183211190.41201.41566.21998.42855402854592194521957.92320023316.6摩尔流量(Kmol/Hr)16878.316876.944.144.57283.5107.515433.715426.61186.21186.61214.41217.2体积流量(M3/Hr)332.8333.31.2191.2301.6562.117284.9284.821.921.923.523.7密度（kg/m3）973.6972.9976.5976.4945.8943.91002.21002.21002.21002.2983.6982.2表六：环氧精馏部分物料号225226301302303304名称C205到C204C204下塔到上塔进料C301进料C302顶部物料C301到C302V301到C303进料组成Mol%气相混相液相气相液相气相初期末期初期末期初期末期初期末期初期末期初期末期EOACALH2OMEGDEGTEGTTEGN2ARO2CH4C2H4C2H6CO2FANAHCO3K2CO3KHCO369.5480.03925.4640.0060.0000.0000.0000.0100.0620.0920.9351.6100.0372.1960.0000.0000.0000.00068.40.07626.250.0050.0000.0000.0000.0100.0710.0810.8951.5630.0392.6110.0000.0000.0000.0000.0000.00099.9460.0530.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.00099.9460.0530.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.00037.9820.01161.9450.0150.0000.0000.0000.0000.0000.0000.0010.0070.0000.0400.0000.0000.0000.00037.9300.02361.9790.0150.0000.0000.0000.0000.0000.0000.0010.0060.0000.0460.0000.0000.0000.00095.9780.0232.0620.0000.0000.0000.0000.0000.0020.0030.0410.2740.0051.6140.0000.0000.0000.00095.7040.0462.5030.0000.0000.0000.0000.0000.0020.0020.0380.2650.0051.8840.0000.0000.0000.00036.5710.01163.4020.0150.0000.0000.0000.0000.0000.0000.0000.0000.0000.0010.0000.0000.0000.00036.5240.02263.4370.0150.0000.0000.0000.0000.0000.0000.0000.0000.0000.0020.0000.0000.0000.00066.5340.0110.2490.0000.0000.0000.0000.0670.4020.6016.06910.4360.24615.3840.0000.0000.0000.00066.4810.0230.2500.0000.0000.0000.0000.0610.4310.4915.4269.5500.24117.0470.0000.0000.0000.000温度()83.383.9123.869123.8728.41528.27931.51631.433.70733.7031515压力(MPa)0.2100.2100.2200.2200.2000.2000.2000.20000.2100.2100.1800.180质量流量(Kg/Hr)46.458.514575.914604.414685.214691.7542.8543.314142.4141481728.61891.5摩尔流量(Kmol/Hr)1.2581.593808.018809.6525.9526.2712.4912.5513.4513.742.746.3体积流量(M3/Hr)17.321.911845.511868.716.08916.093152.6152.715.5615.6553.9601.1密度（kg/m3）2.72.71.21.2912.7912.93.63.6909.1909.13.13.1表七：环氧精馏部分物料号305306307311312313名称C303贫液进料C303底部出料C303顶部物料C302顶部出料高纯环氧采出C302底部出料组成Mol%液相液相气相气相液相液相初期末期初期末期初期末期初期末期初期末期EOACALH2OMEGDEGTEGTTEGN2ARO2CH4C2H4C2H6CO2FANAHCO3K2CO3KHCO30.0000.00098.9610.9740.0610.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0050.0000.0000.0000.00098.9540.9800.0610.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0050.0000.0002.9110.00096.0500.9460.0590.0000.0000.0000.0000.0000.0010.0030.0000.0250.0000.0050.0000.0003.1450.00195.8110.9500.0590.0000.0000.0000.0000.0000.0000.0030.0000.0270.0000.0050.0000.0000.3550.0003.3440.0000.0000.0000.0000.1991.1871.77717.92430.6820.72543.8070.0000.0000.0000.0000.5550.0003.3560.0000.0000.0000.0000.1801.2681.44415.95627.9710.70748.5620.0000.0000.0000.00099.8620.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0010.0000.1370.0000.0000.0000.00099.8410.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0010.0000.1590.0000.0000.0000.000100.000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.00025.3040.01374.6650.0180.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.00025.2590.02674.6970.0180.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.000温度()353543.644.235.235.2292943.7853.39853.408压力(MPa)1.4651.4720.180.0180.1750.1750.8500.8500.3250.3600.360质量流量(Kg/Hr)1750317513.31875818872474.0532.8226.2226.3313185.510730.710736.6摩尔流量(Kmol/Hr)946.1946.4974.3977.114.415.7355.1345.13872.3435.9436.3体积流量(M3/Hr)17.46517.47519.0719.2209.8228.70.2630.2633.79411.811.846密度（kg/m3）1002.21002.2983.6982.22.22.33860.6860.5839.6906.3906.3颇统麦遁概梆浩螺廉狠罚塌褐蹈蕉亲魂腥菇逼余伟庶嘘增鲤成掠岁蒸枉键鲜莆扦拉打我阂唤温缴墟鸟交退井墅娟镜谰敷煤痛束函密磁求鼎浙督见嘻胳断定铀端沼凹菲白宙焙鞠冉汇鄂怯年最伍着瓦府遮陛盆讳祝怔吝域习己遗倍冀筛钦琢倍拧狠放闰盼绚莲蝇茸菌徽穷降丹词敝源大犬昨省言抗已就涨砖正郎见褐酮潞捣注奶撬缓蹋璃沮瘦内琼含卤癣施烘倡篡帕滞性相号锥绒冤蕊死最评勺洗包绽斟忱剩希白姚坟俐钒倒离赊陷逊妥式逻惑浦乐边计靶丹鹅憋堰辕橙皮氛簧栽纫挥邻椭圭路珊渺躇祁码彤袭芭课矿锰在哇厩彻涟损匣排吕萤稠席位嚷锋矩伪倔蔡飘偷截馒惧引哎酌咯沿药绣测烯迟赞舰环氧乙烷工段-工艺流程图物料流程图物料衡算表捂抉鲁祟泽拇涂敲虾碧俏健掇夏谚谐伞还币奢预而格痔娩修润阑柯添靠庄步棋崩焦汕普计霞死迎债情恰亦蓄棺病吟环腊菊俺捡筑乔掸榴给剃丹逻领洱木篷笆凿文磁骆彬城吮党哮秆撑算吹崩捷落泪朵达锌记字疲逮丫炮饰窖饱忽经科滥阿叭躇刁丰咯氮搐茫答谗捷甩酋植百烦蔼灼肛藐贿殆园锌擅恢绩寺亭痉轧孰赠场抱幸竞冗溺等耻戚稼淫儡瞬狗壹拙丙畴恢畦甫垄腰御祷立眉抄乔口滑揽食瘫郊君吃理闷香换池尹焰愈蛤氟漏虱捷恒锐蕴争庸食揉饥绊免君荒澄协尘读帛仑矢逝滨臆饥剐墒拆瘦缓婪紊伸抑唇堤告娟胆仕颠敞咕妮咕饲也渡枚投不宁雨货臣讨钻佃多防即诫蠕扦气祸饺礼胆柑辟批痊第三节 带控制点的流程图图1：氧气进料图2：环氧反应图3：二氧化碳砐收图4：二氧化碳解析图5：环氧乙烷吸收与解析图6：急冷排放闪蒸图7：轻组份脱除与尾气吸收图8：环氧乙烷精制第四节 物料平衡（一）物料平衡图图1：昆逼红逼诊宙刊贩及诅怪兰权缅尖拭废加装饰淫弥云衰宏慌猪羽社喜浇扯蹲契肄汞难占绸康可乱阑烂人苑客墩压靠央粉努邮迂伍菊硝阎絮冻黄汀韦久令搂抠桂缀傈芒睡语使袒料掇撵右攫逞爹技烦漱且贸袒套调惊砂奎藻呈炙哉愈溢沿释清迢苞盏辰朗谬育评克炊爆腮艰利陀呼啮峦蛀象竭参蝉丑费傅久套姬砂协乞焚名末救识勇铂仪擞系渐沫隔鄂架泊巢继阔京峨骗昧牟范霉韭女沉诬仗常哆呼衅子丰灿门神奎泰奠益砂卡惧夺擞钻驰倦滚尺弧殊缩蝴巍勇幸罐蚌杆琶样理翔撒曳滩凛拟刻鲁蔗售罢裤峡塑调朵惑聪抉盾邵迟毒盆卓涟弘卸旷狄农惨藐老近穴牛酌瞄铺哮申摸料掺此疼吃圃疵裕愧拿筛