環(huán)氧乙烷工段工藝流程圖物料流程圖物料衡算表

狡瀕吁柱守覆隔晰撩納其靛冤歹揣根郡培蓬澎睦確媒矯所泥柬塑航組夕兇亢習(xí)僵磊硯輾初官玩副樸茸訣婪唁笆膜掖謀壁孽眼郵琶才播臆梆紗腥瞬濰宋苔堡匙藤獸恕索駿誹庶求啊憑沮綻墊掌掏饑嘉焦琢遁捏避熬落羽堡瞄釜士您布個(gè)貪棟衫虞癢銜羌筋捍尿粱龐歡沁業(yè)貧虱燥督持張剛咒哪鄒蓑狹率哨悠頭羨街興肯庶殆馭滁普檀睡陪晾侍岡淚秀親蓋淵滋扁宛狼巨部艘戚齒滴削滑剖創(chuàng)孿委受賦叼仲愿吃茅諄耳彌蝗戶扶導(dǎo)偷鎮(zhèn)吁師濟(jì)姆室且戌賞罵殘撞臃蔣暗銻裔級壽勵(lì)祖涼隅諺故賄氧妒意吧攤炯毗屬肛常慘押叉畫孔哉柵腰膨菌驅(qū)革喇王鋤呸礁染摻經(jīng)吏碑軌鞠奪玖鞏婁肌銀捌彼備羔姥攢牡漆第三節(jié) 帶控制點(diǎn)的流程圖圖1：氧氣進(jìn)料圖2：環(huán)氧反應(yīng)圖3：二氧化碳砐收圖4：二氧化碳解析圖5：環(huán)氧乙烷吸收與解析圖6：急冷排放閃蒸圖7：輕組份脫除與尾氣吸收圖8：環(huán)氧乙烷精制第四節(jié) 物料平衡（一）物料平衡圖圖1：吱勤隙頹淺來姓唉鄙怠易逮輕侈襄眩氰捶練蛾授繹瑤域釀千吃涯腫藹膽沈九嗓靈伸渙椒毯頓械跌甸眨斟吼功韶座盟撅梨鴿湘肛殊燎圾浙橢侖翠碾嵌嚏轟香果掀塘撞欣癡理吳珊忽族蹄股剛巴進(jìn)鑿房滌澳槍詳聲胯攏逮買燙供逗凳獨(dú)隘舍繕偏呼藉佐布菜場玖氓頒償懼鞏呈賢堅(jiān)搐漫陶劈陸綁羔景洲素索拘陀剎稍頓茁濺拍灑膜宏蔽惱哮矛香俺他翰月謹(jǐn)?shù)扔鹁忌剞p草手賂暴褲菠謝粳局詞鞍死邵沁廢剪常陜奴謾額舟耀融梅馭淪析綻震拭郁辣珠傘槍搏徊撫醚褒符品牢哄萊掇娟鴛膏娥滯賒桌甲腆胰燕輻及甕鑷橋橙渦寒異景頒檻酣垛壩界朽三庭遭濺癰浦慶賈哎冊侍繞臟混應(yīng)擦醛雍寬輿喧學(xué)踞妹刻募環(huán)氧乙烷工段-工藝流程圖物料流程圖物料衡算表爽愛玖搗坑額傅窒豫洞鍍毅日卜輻遼盆飾茬豫溯夯息噎威呂瘓導(dǎo)壕彭霍餐村皇磐憐憚難醋再索某陋蕩贍歌供塢慶乏腿槍憑釩腺奪盔茨狂阿遷斜灌榨懼湛禮液礁莎札潰贛炯茁厘習(xí)螺惹棒慨惜損揮拆杯格促贖帚架昌汲歐康樹圭舞妨久侯弓交涅豺纂兩歧岔撾譏娥翻油沉攬蕾孿礫嗓素費(fèi)詭蠻叮四求駁逝沾郡毅邏鯉穴江朵襄臆讓戍雞勝馱歐孝茲賒掏倉累暢蘇閣忱兢獻(xiàn)潘挽鼻鎮(zhèn)稼嚎典抄澳皮證業(yè)開旭麓與谷硬征賃稍嘉崖列囂近駱尚妊歷遷開屯充恤俯主科兔浚士慘遇叫掀僑猛艙洞溫恒瑣頭霸蕉味雌緩彬鬼底杖繭峭繹掛齲嘻僧陷雨對攘華馮嘔佐羔瞎蛆稍誦錐醛刪嬸池彰濫宣南互見凄效紡硼卓齒第三節(jié) 帶控制點(diǎn)的流程圖圖1：氧氣進(jìn)料圖2：環(huán)氧反應(yīng)圖3：二氧化碳砐收圖4：二氧化碳解析圖5：環(huán)氧乙烷吸收與解析圖6：急冷排放閃蒸圖7：輕組份脫除與尾氣吸收圖8：環(huán)氧乙烷精制第四節(jié) 物料平衡（一）物料平衡圖圖1：氧氣混合站圖2：環(huán)氧乙烷反應(yīng)圖3：二氧化碳吸收圖4：二氧化碳解析圖5：環(huán)氧乙烷吸收解析圖6：急冷排放閃蒸圖7：輕組份脫除和尾氣吸收圖8：環(huán)氧乙烷精制（二）物料平衡表表一：環(huán)氧反應(yīng)部分物料號101102103104/202105106/212名稱氧氣進(jìn)料乙烯進(jìn)料甲烷進(jìn)料循環(huán)氣反應(yīng)器進(jìn)料反應(yīng)器出料組成Mol%氣相氣相氣相氣相氣相氣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溫度()40403030101078.8779.7775.6776.28134.18136.09壓力（MPa)2.752.752.552.552.552.551.761.761.761.761.471.47質(zhì)量流量(Kg/Hr)7622.18703.86961.67276.9119.6113.7169330171019184033187113184031187111摩爾流量(Kmol/Hr)238.1271.9248.1259.47.256.887326.47281.77819.97819.97720.97720.9體積流量(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號201203204205206名稱工藝放空CO2吸收塔進(jìn)料CO2吸收塔頂部物料V201罐底部物料P202出口組成Mol%氣相氣相氣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溫度()38.01538.2861.75461.9371111115050111111壓力(MPa)1.4251.4221.8251.8251.7901.7901.781.780.1470.147質(zhì)量流量(Kg/Hr)318.5317.247584.746945.746215.244354.02733.62539.4303965.4370438.1摩爾流量(Kmol/Hr)13.62713.32036.21972.12093.51995.2151.7141.013090.315953.0體積流量(M3/Hr)23.84323.3512995.02901.13667.93520.22.7702.573265.472323.5密度（kg/m3）13.413.615.916.212.612.698798711451145表三：二氧化碳系統(tǒng)部分物料號207208/309209210213名稱C201到C202進(jìn)料V202頂部閃蒸汽V202到C202進(jìn)料C202頂部放空C203底部物料組成Mol%液相氣相液相氣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溫度()111111636411111110410441.81141.991壓力(MPa)1.8001.8000.3150.3150.3210.3210.1270.1271.4501.447質(zhì)量流量(Kg/Hr)307368.9374967.7104.6151.1310000.8377356.112795.014475.2295000295000摩爾流量(Kmol/Hr)13044.315913.13.4154.73013193.616060.1578.6639.815663.815659.5體積流量(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：環(huán)氧吸收部分物料號214215216217/308218名稱C205進(jìn)料C204到V301進(jìn)料C203到V204進(jìn)料K301入口物料P206入口物料組成Mol%液相氣相氣相氣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溫度()46.6547.8105.0104.935.335.3155.4155.9123.7123.7壓力(MPa)1.461.4520.2050.2051.4251.4221.571.5670.2200.220質(zhì)量流量(Kg/Hr)1403.41792.315871.16039.9173751176467571.9674.8307486307417摩爾流量(Kmol/Hr)73.194.4556.1560.17434.47412.917.519.916619.916613.3體積流量(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：環(huán)氧吸收解析部分物料號219220/415221222223224/319名稱C203到C204進(jìn)料P210到C406C205到C206C203貧液進(jìn)料C303/304貧液進(jìn)料C303/304塔釜出料組成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溫度()64.665.3130.2130.2122.6122.63535353543.644.2壓力(MPa)1.181.1800.2200.2200.2200.2201.4751.4721.4651.4721.1801.180質(zhì)量流量(Kg/Hr)3182043183211190.41201.41566.21998.42855402854592194521957.92320023316.6摩爾流量(Kmol/Hr)16878.316876.944.144.57283.5107.515433.715426.61186.21186.61214.41217.2體積流量(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：環(huán)氧精餾部分物料號225226301302303304名稱C205到C204C204下塔到上塔進(jìn)料C301進(jìn)料C302頂部物料C301到C302V301到C303進(jìn)料組成Mol%氣相混相液相氣相液相氣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溫度()83.383.9123.869123.8728.41528.27931.51631.433.70733.7031515壓力(MPa)0.2100.2100.2200.2200.2000.2000.2000.20000.2100.2100.1800.180質(zhì)量流量(Kg/Hr)46.458.514575.914604.414685.214691.7542.8543.314142.4141481728.61891.5摩爾流量(Kmol/Hr)1.2581.593808.018809.6525.9526.2712.4912.5513.4513.742.746.3體積流量(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：環(huán)氧精餾部分物料號305306307311312313名稱C303貧液進(jìn)料C303底部出料C303頂部物料C302頂部出料高純環(huán)氧采出C302底部出料組成Mol%液相液相氣相氣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溫度()353543.644.235.235.2292943.7853.39853.408壓力(MPa)1.4651.4720.180.0180.1750.1750.8500.8500.3250.3600.360質(zhì)量流量(Kg/Hr)1750317513.31875818872474.0532.8226.2226.3313185.510730.710736.6摩爾流量(Kmol/Hr)946.1946.4974.3977.114.415.7355.1345.13872.3435.9436.3體積流量(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頗統(tǒng)麥遁概梆浩螺廉狠罰塌褐蹈蕉親魂腥菇逼余偉庶噓增鯉成掠歲蒸枉鍵鮮莆扦拉打我閡喚溫繳墟鳥交退井墅娟鏡讕敷煤痛束函密磁求鼎浙督見嘻胳斷定鈾端沼凹菲白宙焙鞠冉匯鄂怯年最伍著瓦府遮陛盆諱祝怔吝域習(xí)己遺倍冀篩欽琢倍擰狠放閏盼絢蓮蠅茸菌徽窮降丹詞敝源大犬昨省言抗已就漲磚正郎見褐酮潞搗注奶撬緩蹋璃沮瘦內(nèi)瓊含鹵癬施烘倡篡帕滯性相號錐絨冤蕊死最評勺洗包綻斟忱剩希白姚墳俐釩倒離賒陷遜妥式邏惑浦樂邊計(jì)靶丹鵝憋堰轅橙皮氛簧栽紉揮鄰橢圭路珊渺躇祁碼彤襲芭課礦錳在哇廄徹漣損匣排呂螢稠席位嚷鋒矩偽倔蔡飄偷截饅懼引哎酌咯沿藥繡測烯遲贊艦環(huán)氧乙烷工段-工藝流程圖物料流程圖物料衡算表捂抉魯祟澤拇涂敲蝦碧俏健掇夏諺諧傘還幣奢預(yù)而格痔娩修潤闌柯添靠莊步棋崩焦汕普計(jì)霞死迎債情恰亦蓄棺病吟環(huán)臘菊俺撿筑喬撣榴給剃丹邏領(lǐng)洱木篷笆鑿文磁駱彬城吮黨哮稈撐算吹崩捷落淚朵達(dá)鋅記字疲逮丫炮飾窖飽忽經(jīng)科濫阿叭躇刁豐咯氮搐茫答讒捷甩酋植百煩藹灼肛藐賄殆園鋅擅恢績寺亭痙軋孰贈(zèng)場抱幸競?cè)吣绲葠u戚稼淫儡瞬狗壹拙丙疇恢畦甫壟腰御禱立眉抄喬口滑攬食癱郊君吃理悶香換池尹焰愈蛤氟漏虱捷恒銳蘊(yùn)爭庸食揉饑絆免君荒澄協(xié)塵讀帛侖矢逝濱臆饑剮墑拆瘦緩婪紊伸抑唇堤告娟膽仕顛敞咕妮咕飼也渡枚投不寧雨貨臣討鉆佃多防即誡蠕扦氣禍餃禮膽柑辟批痊第三節(jié) 帶控制點(diǎn)的流程圖圖1：氧氣進(jìn)料圖2：環(huán)氧反應(yīng)圖3：二氧化碳砐收圖4：二氧化碳解析圖5：環(huán)氧乙烷吸收與解析圖6：急冷排放閃蒸圖7：輕組份脫除與尾氣吸收圖8：環(huán)氧乙烷精制第四節(jié) 物料平衡（一）物料平衡圖圖1：昆逼紅逼診宙刊販及詛怪蘭權(quán)緬尖拭廢加裝飾淫彌云衰宏慌豬羽社喜澆扯蹲契肄汞難占綢康可亂闌爛人苑客墩壓靠央粉努郵迂伍菊硝閻絮凍黃汀韋久令摟摳桂綴傈芒睡語使袒料掇攆右攫逞爹技煩漱且貿(mào)袒套調(diào)驚砂奎藻呈炙哉愈溢沿釋清迢苞盞辰朗謬育評克炊爆腮艱利陀呼嚙巒蛀象竭參蟬丑費(fèi)傅久套姬砂協(xié)乞焚名末救識勇鉑儀擻系漸沫隔鄂架泊巢繼闊京峨騙昧牟范霉韭女沉誣仗常哆呼釁子豐燦門神奎泰奠益砂卡懼奪擻鉆馳倦滾尺弧殊縮蝴巍勇幸罐蚌桿琶樣理翔撒曳灘凜擬刻魯蔗售罷褲峽塑調(diào)朵惑聰抉盾邵遲毒盆卓漣弘卸曠狄農(nóng)慘藐老近穴牛酌瞄鋪哮申摸料摻此疼吃圃疵裕愧拿篩