丙二醇项目初步设计说明书附录

45kt/a1,3-丙二醇项目初步设计说明书-附录一物料衡算一览表1-第一章物料衡算一览表1.1丙烯醛合成工段1.1.1丙烯醛合成车间流入1流入2流入3流入4流入5流入6流出1流出2流出3温度C252525133.594952252589.951807387.921481731.406154压力MPa013250.30.1013250.1013250.311气相分率10.933282271100001摩尔流量kmol/hr88.6223.5105338529.771.262501203274.8452681419.51556473.462861质量流量kg/hr3725.421061034.812615156.88891283.768854503.8221672.38185146.7618828541.251813689.0685体积流量l/min12204.5372888.05477215985.29113388.216875.5200333363.402492.8742579531.61944819981.5558热焓Gcal/hr0.40907404-0.0640646-0.0241137-4.0530552-17.058044-82.083308-18.409959-91.943693-0.6032163质量分率C3H60.993002610.780929635.3206e-050.000316290.07176098C3H80.004034940.000635103.342e-081.7797e-075.6922e-05C2H46.6734e-052.0345e-066.7508e-103.6693e-099.0785e-07C2H23.0969e-061.957e-073.5451e-101.882e-093.8823e-08CO3.3315e-065.1875e-0502.4906e-079.8945e-070.00641360CO21.0469e-050.036040070.000461416.932e-050.000315420.01594439O27.6118e-060.001501540.234057648.5137e-050.000343060.04214244N20.002882120.763921222.4614e-059.8469e-050.84583653HE2.5778e-080.001370843.9348e-081.5881e-070.00151749H2O1.0028e-053.7582e-070.000188871.0001.0001.0000.947089640.846520140.00284464C3H4O0.177799670.020623070.152192270.01344274C3H4O20.028066550.000212681.5186e-34C2H4O20.003988112.1291e-072.3475e-423-C3H6O2H2C3H8O2C6H14O3C2H60.002861170.000157332.1605e-081.0412e-073.9302e-0原料混合器（M0101）流入1流入2流入3流入4流出1温度C133.59495225174.59853525122.375673压力MPa0.30.3气相分率1110.933282271摩尔流量kmol/hr71.2688.62529.723.5105338713.090298质量流量kg/hr1283.768853725.4210615156.88891034.812621200.8804体积流量l/min13388.216812204.537109551.6432888.05477130278.836热焓Gcal/hr-4.05305520.409074040.53003094-0.0640646-3.1779957质量分率C3H60.993002610.780929630.21260745C3H80.004034940.000635100.00074002C2H46.6734e-052.0345e-061.1826e-05C2H23.0969e-061.957e-075.5375e-07CO3.3315e-065.1875e-053.1173e-06CO21.0469e-050.000461410.036040070.00209070O27.6118e-060.234057640.001501540.16740663N20.763921220.002882120.54628162HE0.001370842.5778e-080.00098004H2O1.0001.0028e-050.000188873.7582e-070.06068943C3H4O0.177799670.00867815C3H4O2C2H4O23-C3H6O2H2C3H8O2C6H14O3C2H60.002861170.000157330.0005104丙烯氧化反应器（R0101）流入1流出1温度C280320压力MPa0.30.3气相分率11摩尔流量kmol/hr713.090298714.82369质量流量kg/hr21200.880421200.8804体积流量l/min182197.407195847.585热焓Gcal/hr-2.1099699-9.5396675质量分率C3H60.212607450.04677364C3H80.000740023.7001e-05C2H41.1826e-055.9129e-07C2H25.5375e-072.7687e-08CO3.1173e-060.00414255CO20.002090700.01073650O20.167406630.02769320N20.546281620.54628162HE0.000980040.00098004H2O0.060689430.13668904C3H4O0.008678150.21857199C3H4O20.00709980C2H4O20.000968443-C3H6O2H2C3H8O2C6H14O3C2H60.000510442.5522e-0废酸吸收塔（T0101）流入1流入2流出1流出2温度C9525.176564386.567705789.9518073压力MPa0.3气相分率1010摩尔流量kmol/hr714.82369250689.978422274.845268质量流量kg/hr21200.88044503.8220557.93855146.76188体积流量l/min121556.58575.5329773114644.19692.8742579热焓Gcal/hr-11.119413-17.057317-9.7667712-18.409959质量分率C3H60.046773640.048223145.3206e-05C3H83.7001e-053.815e-053.342e-08C2H45.9129e-076.0961e-076.7508e-10C2H22.7687e-082.8464e-083.5451e-10CO0.004142550.004272042.4906e-07CO20.010736500.011054936.932e-05O20.027693200.028537988.5137e-05N20.546281620.563360212.4614e-05HE0.000980040.001010683.9348e-08H2O0.136689041.0000.122935630.94708964C3H4O0.218571990.220244680.02062307C3H4O20.007099800.000295270.02806655C2H4O20.000968442.9559e-070.003988113-C3H6O2H2C3H8O2C6H14O3C2H62.5522e-0502.6315e-052.1605e-0气液分离器（V0101）流入1流出1流出2温度C100100100压力MPa111气相分率0.8806866610摩尔流量kmol/hr689.978422608.19817181.7802508质量流量kg/hr20557.938519014.24441543.69408体积流量l/min31449.590631448.834728.5124654热焓Gcal/hr-10.475128-5.0778623-5.3945661质量分率C3H60.048223140.052121680.00020341C3H83.815e-054.1237e-051.2068e-07C2H46.0961e-076.5889e-072.6311e-09C2H22.8464e-083.0674e-081.2513e-09CO0.004272040.004618809.5938e-07CO20.011054930.011932940.00024016O20.028537980.030830000.00030636N20.563360210.609089519.5711e-05HE0.001010680.001092721.6035e-07H2O0.122935630.057183990.93282261C3H4O0.220244680.232925510.0640503C3H4O20.000295270.000134390.00227696C2H4O22.9559e-076.4203e-083.1457e-063-C3H6O2H2C3H8O2C6H14O3C2H62.6315e-052.8445e-057.8736e-0丙烯醛吸收塔（T0102）流入1流入2流出1流出2温度C25.445298710031.40615487.1916666压力MPa1111气相分率0110摩尔流量kmol/hr1203608.198171473.4628611337.73531质量流量kg/hr21672.381819014.244413689.068526997.5578体积流量l/min363.55955231448.834719981.5558503.058844热焓Gcal/hr-82.07448-5.0778623-0.6032163-86.549126质量分率C3H60.052121680.071760980.00032274C3H84.1237e-055.6922e-051.8125e-07C2H46.5889e-079.0785e-073.7287e-09C2H23.0674e-083.8823e-081.9181e-09CO0.004618800.006413609.9117e-07CO20.011932940.015944390.00031973O20.030830000.042142440.00034516N20.609089510.845836539.8627e-05HE0.001092720.001517491.5872e-07H2O1.0000.057183990.002844640.84158545C3H4O0.232925510.013442740.15723214C3H4O20.000134391.5186e-349.4651e-05C2H4O26.4203e-082.3475e-424.5218e-083-C3H6O2H2C3H8O2C6H14O3C2H62.8445e-053.9302e-051.0557e-0混合器（M0102）流入1流入2流出1温度C87.191666610087.9214817压力MPa111气相分率000摩尔流量kmol/hr1337.7353181.78025081419.51556质量流量kg/hr26997.55781543.6940828541.2518体积流量l/min503.05884428.5124654531.619448热焓Gcal/hr-86.549126-5.3945661-91.943693质量分率C3H60.000322740.000203410.00031629C3H81.8125e-071.2068e-071.7797e-07C2H43.7287e-092.6311e-093.6693e-09C2H21.9181e-091.2513e-091.882e-09CO9.9117e-079.5938e-079.8945e-07CO20.000319730.000240160.00031542O20.000345160.000306360.00034306N29.8627e-059.5711e-059.8469e-05HE1.5872e-071.6035e-071.5881e-07H2O0.841585450.932822610.84652014C3H4O0.157232140.06405030.15219227C3H4O29.4651e-050.002276960.00021268C2H4O24.5218e-083.1457e-062.1291e-073-C3H6O2H2C3H8O2C6H14O3C2H61.0557e-077.8736e-081.0412e-071.1.2废酸处理车间流入1流入2流出1流出2温度C89.9518073251029.4253641压力MPa0.30.1013250.1013250.101325气相分率0110摩尔流量kmol/hr274.8452682227.262226.85074278.534271质量流量kg/hr5146.7618863731.04163807.20575070.59716体积流量l/min92.8742579908165.754862317.23285.4060218热焓Gcal/hr-18.409959-0.1013924-1.7057443-18.764617质量分率C3H65.3206e-054.2806e-061.3972e-07C3H83.342e-082.6895e-097.8668e-11C2H46.7508e-105.4316e-111.713e-12C2H23.5451e-102.7519e-111.3548e-11CO2.4906e-072.0087e-082.8077e-11CO26.932e-050.000461410.008805810.00205301O28.5137e-050.234057640.225528680.02015396N22.4614e-050.763921220.762951320.00075521HE3.9348e-080.001370840.001369121.0754e-06H2O0.947089640.000188870.001335910.97688349C3H4O0.020623074.6848e-062.4779e-05C3H4O20.028066551.3785e-070.00011221C2H4O20.003988116.8201e-091.6106e-053-C3H6O2H2C3H8O2C6H14O3C2H62.1605e-081.739e-094.5886e-废酸氧化反应器（R0102）流入1流入2流出1温度C4095.1046338270压力MPa777气相分率101摩尔流量kmol/hr2227.26274.8452682505.38501质量流量kg/hr63731.0415146.7618868877.8029体积流量l/min13807.062793.431858726938.4263热焓Gcal/hr0.13085665-18.382899-12.96423质量分率C3H65.3206e-053.9757e-06C3H83.342e-082.4973e-09C2H46.7508e-105.0444e-11C2H23.5451e-102.649e-11CO2.4906e-071.861e-08CO20.000461416.932e-050.00830869O20.234057648.5137e-050.21040955N20.763921222.4614e-050.70684051HE0.001370843.9348e-080.00126841H2O0.000188870.947089640.07315308C3H4O0.020623076.1641e-06C3H4O20.028066558.3889e-06C2H4O20.003988111.192e-063-C3H6O2H2C3H8O2C6H14O3C2H62.1605e-081.6144e-0气液分离器（V0103）流入1流出1流出2温度C54.25376754.063612654.0636126压力MPa777气相分率0.884979710摩尔流量kmol/hr2505.385012226.85074278.534271质量流量kg/hr68877.802963807.20575070.59716体积流量l/min14464.866814424.488987.6086602热焓Gcal/hr-19.671023-1.0223752-18.648647质量分率C3H63.9757e-064.2806e-061.3972e-07C3H82.4973e-092.6895e-097.8668e-11C2H45.0444e-115.4316e-111.713e-12C2H22.649e-112.7519e-111.3548e-11CO1.861e-082.0087e-082.8077e-11CO20.008308690.008805810.00205301O20.210409550.225528680.02015396N20.706840510.762951320.00075521HE0.001268410.001369121.0754e-06H2O0.073153080.001335910.97688349C3H4O6.1641e-064.6848e-062.4779e-05C3H4O28.3889e-061.3785e-070.00011221C2H4O21.192e-066.8201e-091.6106e-053-C3H6O2H2C3H8O2C6H14O3C2H61.6144e-091.739e-094.5886e-111.1.3丙烯回收车间流入1流出1流出2流出3流出4温度C31.40615431.40615421.04618781025压力MPa110.1013250.30.3气相分率10110.93328227摩尔流量kmol/hr473.4628612.16150374447.4667750.324048523.5105338质量流量kg/hr13689.068538.940095112605.87579.440143871034.8126体积流量l/min19981.55580.65704646180010.18142.32406872888.05477热焓Gcal/hr-0.6032163-0.1472547-0.4618076-0.0009066-0.0640646质量分率C3H60.071760980.013792660.037774900.78092963C3H85.6922e-059.6571e-062.6128e-050.00063510C2H49.0785e-078.1708e-072.3672e-062.0345e-06C2H23.8823e-082.6039e-087.4446e-081.957e-07CO0.006413600.006953890.008755345.1875e-05CO20.015944390.014325040.041258670.03604007O20.042142440.045571240.092315740.00150154N20.845836530.917666840.819652050.00288212HE0.001517490.001647780.000124632.5778e-08H2O0.002844641.0003.9431e-111.0277e-103.7582e-07C3H4O0.013442742.3191e-065.4713e-060.17779967C3H4O21.5186e-34C2H4O22.3475e-423-C3H6O2H2C3H8O2C6H14O3C2H63.9302e-052.97e-058.4597e-050.0001573干燥器（V0105）流入1流出1流出2温度C31.40615431.40615431.406154压力MPa111气相分率101摩尔流量kmol/hr473.4628612.16150374471.301357质量流量kg/hr13689.068538.940095113650.1284体积流量l/min19981.55580.6570464619890.3338热焓Gcal/hr-0.6032163-0.1472547-0.4784869质量分率C3H60.071760980.07196570C3H85.6922e-055.7084e-05C2H49.0785e-079.1044e-07C2H23.8823e-083.8934e-08CO0.006413600.00643190CO20.015944390.01598988O20.042142440.04226266N20.845836530.84824947HE0.001517490.00152181H2O0.002844641.0002.8528e-08C3H4O0.013442740.01348109C3H4O21.5186e-34C2H4O22.3475e-423-C3H6O2H2C3H8O2C6H14O3C2H63.9302e-053.9414e-0气液分离器（V0104）流入1流出1流出2温度C-90-90-90压力MPa111气相分率0.9494281510摩尔流量kmol/hr471.301357447.46677523.8345823质量流量kg/hr13650.128412605.87571044.25274体积流量l/min11023.659610999.224.4595508热焓Gcal/hr-1.042779-0.8282186-0.2145604质量分率C3H60.071965700.013792660.77421144C3H85.7084e-059.6571e-060.00062960C2H49.1044e-078.1708e-072.0375e-06C2H23.8934e-082.6039e-081.946e-07CO0.006431900.006953890.00013055CO20.015989880.014325040.03608725O20.042262660.045571240.00232251N20.848249470.917666840.01026580HE0.001521810.001647781.1523e-06H2O2.8528e-083.9431e-113.7243e-07C3H4O0.013481092.3191e-060.17619239C3H4O2C2H4O23-C3H6O2H2C3H8O2C6H14O3C2H63.9414e-052.97e-050.0001566闪蒸罐（V0102）流入1流出1流出2温度C-90-90.014683-90.014683压力MPa10.30.3气相分率010摩尔流量kmol/hr23.83458230.324048523.5105338质量流量kg/hr1044.252749.440143871034.8126体积流量l/min24.459550827.094450324.2255454热焓Gcal/hr-0.2145604-0.0011408-0.2134199质量分率C3H60.774211440.037774900.78092963C3H80.000629602.6128e-050.00063510C2H42.0375e-062.3672e-062.0345e-06C2H21.946e-077.4446e-081.957e-07CO0.000130550.008755345.1875e-05CO20.036087250.041258670.03604007O20.002322510.092315740.00150154N20.010265800.819652050.00288212HE1.1523e-060.000124632.5778e-08H2O3.7243e-071.0277e-103.7582e-07C3H4O0.176192395.4713e-060.17779967C3H4O2C2H4O23-C3H6O2H2C3H8O2C6H14O3C2H60.000156688.4597e-050.000157331.2丙二醇合成车间流入1流入2流入3流出1流出2流出3流出4流出5流出6温度C87.9214817252539.7481523524.99999974745.484009825.1215549压力MPa10.10132560.0280.02860.010.1013250.101325气相分率001111100摩尔流量kmol/hr1419.51556145.0686.75373711.170179020.513718150.26555288804.9937614.51051876.0283268质量流量kg/hr28541.25142613.29652174.88512442.842077124.25015420.5374719514390.059711076.31835795.44144体积流量l/min531.61943543.8197441597.3759821812.06294707.1669351.828565723571264.28189.52221791.768127热焓Gcal/hr-91.943695-9.89775957.7191e-17-0.0310230-0.0156970-7.746e-06-45.82593-41.721273-8.740483质量分率C3H60.000316270.174476690.06400289C3H81.7797e-079.9099e-053.439e-05C2H43.6693e-092.0517e-066.939e-07C2H21.882e-096.1931e-071.121e-06CO9.8946e-070.000654568.1373e-06CO20.000315410.10466130.18632442O20.000343050.160128230.12086982N29.8469e-050.065278840.00056703HE1.5881e-070.000105397.111e-07H2O0.846520171.0000.122241050.011294640.004492760.994923970.999314495.7634e-07C3H4O0.152192280.36653390.616872563.198e-068.2347e-061.2167e-075.7131e-17C3H4O20.000212681.1455e-051.5729e-084.916e-070.000139260.000367001.1504e-07C2H4O22.1291e-077.8082e-092.2592e-112.078e-108.1321e-084.4293e-072.1034e-113-C3H6O20.005747066.575e-06H21.0000.995498240.001340671.8587e-083.3822e-27C3H8O25.3056e-060.003587720.000317910.99599222C6H14O32.3999e-115.0572e-082.0102e-190.00400708C2H61.0412e-075.974e-051.7001e-051.2.1混合器（M0201）流入1流入2流出1温度C87.921481721.630910680.9398736压力MPa111气相分率000摩尔流量kmol/hr1419.51556176.9757611596.49134质量流量kg/hr28541.25143688.4404332229.6919体积流量l/min531.61943564.2560267595.913641热焓Gcal/hr-91.943695-11.541261-103.48496质量分率C3H60.000316270.000115380.00029328C3H81.7797e-073.1234e-081.6118e-07C2H43.6693e-095.7071e-103.3147e-09C2H21.882e-091.5198e-083.4059e-09CO9.8946e-074.8866e-118.7623e-07CO20.000315410.000595660.00034748O20.000343054.4694e-050.00030891N29.8469e-052.5853e-098.72e-05HE1.5881e-071.5573e-121.4063e-07H2O0.846520170.800197020.84121885C3H4O0.152192280.198005410.15743523C3H4O20.000212689.0979e-060.00018938C2H4O22.1291e-073.311e-091.8892e-073-C3H6O20.001032670.00011818H2C3H8O2C6H14O3C2H61.0412e-076.5531e-099.2953e-081.2.2水合反应器（R0201）流入1流出1温度C4040压力MPa11气相分率00摩尔流量kmol/hr1596.491341519.56205质量流量kg/hr32229.691932229.735体积流量l/min568.124431543.748769热焓Gcal/hr-104.69403-102.4487质量分率C3H60.000293280.00029328C3H81.6118e-071.6118e-07C2H43.3147e-093.3147e-09C2H23.4059e-093.4059e-09CO8.7623e-078.7623e-07CO20.000347480.00034748O20.000308910.00030891N28.72e-058.72e-05HE1.4063e-071.4063e-07H2O0.841218850.79821698C3H4O0.157435230.02361525C3H4O20.000189380.00018938C2H4O21.8892e-071.8892e-073-C3H6O20.000118180.17694003H2C3H8O2C6H14O3C2H69.2953e-089.2953e-081.2.3气液分离器（V0201）流入1流出1流出2温度C39.762616339.748152339.7481523压力MPa0.0280.0280.028气相分率0.0007240601摩尔流量kmol/hr1519.562051518.391881.17017902质量流量kg/hr32229.73532186.892942.8420771体积流量l/min2246.65155542.731841812.06294热焓Gcal/hr-102.4487-102.41768-0.0310230质量分率C3H60.000293286.1443e-050.17447669C3H81.6118e-072.9489e-089.9099e-05C2H43.3147e-095.882e-102.0517e-06C2H23.4059e-092.5861e-096.1931e-07CO8.7623e-076.1364e-090.00065456CO20.000347480.000208640.1046613O20.000308919.6187e-050.16012823N28.72e-054.2751e-070.06527884HE1.4063e-075.3593e-100.00010539H2O0.798216980.799116730.12224105C3H4O0.023615250.023158810.3665339C3H4O20.000189380.000189621.1455e-05C2H4O21.8892e-071.8916e-077.8082e-093-C3H6O20.176940030.177167890.00574706H2C3H8O2C6H14O3C2H69.2953e-081.356e-085.974e-051.2.4丙烯醛回收塔（T0201）流入1流出1流出2流出3温度C39.7481523568.32891775压力MPa0.0280.0280.0280.028气相分率0001摩尔流量kmol/hr1518.3918831.91576151485.96240.51371815质量流量kg/hr32186.89291075.1439231087.498924.2501542体积流量l/min542.7318420.0307437538.022902707.166935热焓Gcal/hr-102.41768-1.6463689-100.22612-0.0156970质量分率C3H66.1443e-050.000395836.2235e-230.06400289C3H82.9489e-081.0715e-076.443e-273.439e-05C2H45.882e-101.9579e-092.3447e-286.939e-07C2H22.5861e-095.2138e-082.5614e-201.121e-06CO6.1364e-091.6764e-103.0375e-378.1373e-06CO20.000208640.002043532.3383e-170.18632442O29.6187e-050.000153331.1781e-200.12086982N24.2751e-078.8693e-0900.00056703HE5.3593e-105.3425e-122.4596e-317.111e-07H2O0.799116730.314546270.816489880.01129464C3H4O0.023158810.679286893.8551e-060.61687256C3H4O20.000189623.1212e-050.000195241.5729e-08C2H4O21.8916e-071.1359e-081.9546e-072.2592e-113-C3H6O20.177167890.003542730.183310826.575e-06H2C3H8O2C6H14O3C2H61.356e-082.2481e-087.794e-281.7001e-051.2.5混合器（M0202）流入1流入2流出1温度C5.107502052520.7190733压力MPa0.1013250.1013250.101325气相分率000摩尔流量kmol/hr31.9157615145.06176.975761质量流量kg/hr1075.143922613.296523688.44043体积流量l/min20.033544643.819744164.192534热焓Gcal/hr-1.6462977-9.8977595-11.544057质量分率C3H60.000395830.00011538C3H81.0715e-073.1234e-08C2H41.9579e-095.7071e-10C2H25.2138e-081.5198e-08CO1.6764e-104.8866e-11CO20.002043530.00059566O20.000153334.4694e-05N28.8693e-092.5853e-09HE5.3425e-121.5573e-12H2O0.3145462710.80019702C3H4O0.679286890.19800541C3H4O23.1212e-059.0979e-06C2H4O21.1359e-083.311e-093-C3H6O20.003542730.00103267H2C3H8O2C6H14O3C2H62.2481e-086.5531e-091.2.6一段加氢反应器（R0202）流入1流入2流出1温度C3525.000000135压力MPa666气相分率010.17089687摩尔流量kmol/hr1485.9624352.0489811803.3947质量流量kg/hr31087.4989711.8356531799.3151体积流量l/min518.7882772424.167792711.67592热焓Gcal/hr-100.87333-0.0077386-102.58962质量分率C3H66.2235e-23C3H86.443e-27C2H42.3447e-28C2H22.5614e-20CO3.0375e-37CO22.3383e-17O21.1781e-20N2HE2.4596e-31H2O0.816489880.003388990.79828891C3H4O3.8551e-062.4124e-063.8228e-06C3H4O20.000195243.7083e-070.00019088C2H4O21.9546e-071.5675e-101.9109e-073-C3H6O20.183310820.09856410H20.996604220.02011475C3H8O24.0021e-060.08283732C6H14O31.8103e-114.0524e-13C2H67.794e-281.2.7二段加氢反应器（R0203）流入1流出1温度C35120压力MPa66气相分率0.170896870.15605714摩尔流量kmol/hr1803.39471761.08542质量流量kg/hr31799.315131799.2914体积流量l/min2711.675923052.61721热焓Gcal/hr-102.58962-101.97116质量分率C3H6C3H8C2H4C2H2COCO2O2N2HEH2O0.798288910.79838756C3H4O3.8228e-063.8228e-06C3H4O20.000190880.00019088C2H4O21.9109e-071.9109e-073-C3H6O20.098564100H20.020114750.01743261C3H8O20.082837320.1832546C6H14O34.0524e-130.00073031C2H61.2.8混合器（M0203）流入1流入2流出1温度C2524.999999725.0000001压力MPa666气相分率111摩尔流量kmol/hr86.7537371265.287323352.048981质量流量kg/hr174.885124536.934478711.83565体积流量l/min597.3759821826.737162424.16779热焓Gcal/hr7.7191e-17-0.0077383-0.0077386质量分率C3H6C3H8C2H4C2H2COCO2O2N2HEH2O0.004492760.00338899C3H4O3.198e-062.4124e-06C3H4O24.916e-073.7083e-07C2H4O22.078e-101.5675e-103-C3H6O2H21.0000.995498240.99660422C3H8O25.3056e-064.0021e-06C6H14O32.3999e-111.8103e-11C2H61.2.9气液分离器（V0202）流入1流出1流出2温度C2524.999999724.9999997压力MPa666气相分率0.1507893210摩尔流量kmol/hr1761.08542265.5528761495.53254质量流量kg/hr31799.2914537.4719531261.8195体积流量l/min2333.80351828.56572505.237778热焓Gcal/hr-105.0001-0.0077460-104.99236质量分率C3H6C3H8C2H4C2H2COCO2O2N2HEH2O0.798387560.004492760.81203668C3H4O3.8228e-063.198e-063.8336e-06C3H4O20.000190884.916e-070.00019416C2H4O21.9109e-072.078e-101.9437e-073-C3H6O2000H20.017432610.995498240.00061712C3H8O20.18325465.3056e-060.18640513C6H14O30.000730312.3999e-110.00074287C2H61.2.10物流分割器（M0204）流入1流出1流出2温度C24.999999724.999999724.9999997压力MPa666气相分率111摩尔流量kmol/hr265.5528760.26555288265.287323质量流量kg/hr537.471950.53747195536.934478体积流量l/min1828.565721.828565721826.73716热焓Gcal/hr-0.0077460-7.746e-06-0.0077383质量分率C3H6C3H8C2H4C2H2COCO2O2N2HEH2O0.004492760.004492760.00449276C3H4O3.198e-063.198e-063.198e-06C3H4O24.916e-074.916e-074.916e-07C2H4O22.078e-102.078e-102.078e-103-C3H6O2000H20.995498240.995498240.99549824C3H8O25.3056e-065.3056e-065.3056e-06C6H14O32.3999e-112.3999e-112.3999e-11C2H61.2.11脱水釜（F0201）流入1流出1流出2温度C23.50028524747压力MPa0.010.010.01气相分率0.0088572710摩尔流量kmol/hr1495.53254804.9937690.538845质量流量kg/hr31261.819514390.059716871.7598体积流量l/min54950.02133571264.28264.899616热焓Gcal/hr-104.99236-45.82593-50.388497质量分率C3H6C3H8C2H4C2H2COCO2O2N2HEH2O0.812036680.994923970.65605064C3H4O3.8336e-068.2347e-067.9877e-08C3H4O20.000194160.000139260.00024097C2H4O21.9437e-078.1321e-082.9079e-073-C3H6O2000H20.000617120.001340671.2202e-08C3H8O20.186405130.003587720.34233157C6H14O30.000742875.0572e-080.00137643C2H61.2.12丙二醇精制塔（T0202）流入1流出1流出2温度C4745.4304334146.445003压力MPa0.010.010.01气相分率000摩尔流量kmol/hr690.538845614.51051876.0283268质量流量kg/hr16871.759811076.31835795.44144体积流量l/min264.899616189.511928100.595118热焓Gcal/hr-50.388497-41.721836-8.3309312质量分率C3H6C3H8C2H4C2H2COCO2O2N2HEH2O0.656050640.999314495.7634e-07C3H4O7.9877e-081.2167e-075.7131e-17C3H4O20.000240970.000367001.1504e-07C2H4O22.9079e-074.4293e-072.1034e-113-C3H6O2000H21.2202e-081.8587e-083.3822e-27C3H8O20.342331570.000317910.99599222C6H14O30.001376432.0102e-190.00400708C2H6 45kt/a1,3-丙二醇项目初步设计说明书-附录二能量衡算一览表第二章能量衡算一览表2.1丙烯醛合成车间2.1.1压缩机（C0101）物流焓变计算表流入流出温度C25174.598535压力MPa0.1013250.3气相分率11质量流量kg/hr15156.888915156.8889热焓Gcal/hr-0.02411370.53003094ΣHGcal/hr-0.02411370.53003094能量平衡计算表Q总（Gcal/hr）W总（Gcal/hr）ΣHin（Gcal/hr）ΣHout（Gcal/hr）Error00.55414466-0.02411370.530030942E-082.1.2原料预热器（E0101）负荷计算表HeatingDutyHeatduty（Gcal/hr）1.06802578Q=1.06802578Gcal/hr物流焓变计算表流入流出温度C122.375673280压力MPa0.30.3气相分率11质量流量kg/hr21200.880421200.8804热焓Gcal/hr-3.1779957-2.1099699ΣHGcal/hr-3.1779957-2.1099699能量平衡计算表Q总（Gcal/hr）W总（Gcal/hr）ΣHin（Gcal/hr）ΣHout（Gcal/hr）Error1.068025780-3.1779957-2.10996992E-082.1.3丙烯氧化反应器（R0101）负荷计算表HeatingDutyHeatduty（Gcal/hr）-7.4296976Q=-7.4296976Gcal/hr物流焓变计算表流入流出温度C280320压力MPa0.30.3气相分率11质量流量kg/hr21200.880421200.8804热焓Gcal/hr-2.1099699-9.5396675ΣHGcal/hr-2.1099699-9.5396675能量平衡计算表Q总（Gcal/hr）W总（Gcal/hr）ΣHin（Gcal/hr）ΣHout（Gcal/hr）Error-7.42969760-2.1099699-9.539667502.1.4废酸吸收塔（T0101）物流焓变计算表流入1流入2流出1流出2温度C9525.176564386.567705789.9518073压力MPa0.3气相分率1010质量流量kg/hr21200.88044503.8220557.93855146.76188热焓Gcal/hr-11.119413-17.057317-9.7667712-18.409959ΣHGcal/hr-11.119413-17.057317-9.7667712-18.409959能量平衡计算表Q总（Gcal/hr）W总（Gcal/hr）ΣHin1（Gcal/hr）ΣHin2（Gcal/hr）ΣHout1（Gcal/hr）ΣHout2（Gcal/hr）Error00-11.119413-17.057317-9.7667712-18.4099592E-072.1.5压缩机（C0102）物流焓变计算表流入流出温度C86.5677057230.296925压力MPa0.31气相分率11质量流量kg/hr20557.938520557.9385热焓Gcal/hr-9.7667712-8.8262184ΣHGcal/hr-9.7667712-8.8262184能量平衡计算表Q总（Gcal/hr）W总（Gcal/hr）ΣHin（Gcal/hr）ΣHout（Gcal/hr）Error00.94055277-9.7667712-8.82621843E-082.1.6冷却器（E0103）负荷计算表HeatingDutyHeatduty（Gcal/hr）-1.6489098Q=-1.6489098Gcal/hr物流焓变计算表流入流出温度C230.296925100压力MPa11气相分率10.88068666质量流量kg/hr20557.938520557.9385热焓Gcal/hr-8.8262184-10.475128ΣHGcal/hr-8.8262184-10.475128能量平衡计算表Q总（Gcal/hr）W总（Gcal/hr）ΣHin（Gcal/hr）ΣHout（Gcal/hr）Error-1.64890980-8.8262184-10.4751282E-072.1.7丙烯醛吸收塔（T0102）物流焓变计算表流入1流入2流出1流出2温度C25.445298710031.40615487.1916666压力MPa1111气相分率0110质量流量kg/hr21672.381819014.244413689.068526997.5578热焓Gcal/hr-82.07448-5.0778623-0.6032163-86.549126ΣHGcal/hr-82.07448-5.0778623-0.6032163-86.549126能量平衡计算表Q总（Gcal/hr）W总（Gcal/hr）ΣHin1（Gcal/hr）ΣHin2（Gcal/hr）ΣHout1（Gcal/hr）ΣHout2（Gcal/hr）Error00-82.07448-5.0778623-0.6032163-86.54912602.2废水处理车间2.2.1空气压缩机（C0104）物流焓变计算表流入流出温度C2540压力MPa0.1013257气相分率11质量流量kg/hr63731.04163731.041热焓Gcal/hr-0.10139240.13085665ΣHGcal/hr-0.10139240.13085665能量平衡计算表Q总（Gcal/hr）W总（Gcal/hr）ΣHin（Gcal/hr）ΣHout（Gcal/hr）Error-8.89471989.12696883-0.10139240.130856652E-082.2.2废酸氧化反应器（R0102）负荷计算表HeatingDutyHeatduty（Gcal/hr）5.28781281Q=5.28781281Gcal/hr物流焓变计算表流入1流入2流出温度C4095.1046338270压力MPa777气相分率101质量流量kg/hr63731.0415146.7618868877.8029热焓Gcal/hr0.13085665-18.382899-12.96423ΣHGcal/hr0.13085665-18.382899-12.96423能量平衡计算表Q总（Gcal/hr）W总（Gcal/hr）ΣHin1（Gcal/hr）ΣHin2（Gcal/hr）ΣHout（Gcal/hr）Error5.2878128100.13085665-18.382899-12.964234.6E-072.2.3冷凝器（E0110）负荷计算表HeatingDutyHeatdutyGcal/hr-6.7067927Q=-6.7067927Gcal/hr物流焓变计算表流入1流出1温度C27054.253767压力MPa77气相分率10.8849797质量流量kg/hr68877.802968877.8029热焓Gcal/hr-12.96423-19.671023ΣHGcal/hr-12.96423-19.671023能量平衡计算表Q总（Gcal/hr）W总（Gcal/hr）ΣHin（Gcal/hr）ΣHout（Gcal/hr）Error-6.70679270-12.96423-19.6710233E-072.2.4汽轮机（C0105）物流焓变计算表流入流出温度C54.0636126-109.66981压力MPa70.101325气相分率10.99783964质量流量kg/hr63807.205763807.2057热焓Gcal/hr-1.0223752-3.6106982ΣHGcal/hr-1.0223752-3.6106982能量平衡计算表Q总（Gcal/hr）W总（Gcal/hr）ΣHin（Gcal/hr）ΣHout（Gcal/hr）Error0-2.588323-1.0223752-3.610698202.2.5冷却器（E0107）负荷计算表HeatingDutyHeatduty（Gcal/hr）-0.1133007Q=-0.1133007Gcal/hr物流焓变计算表流入流出温度C54.063612630压力MPa77气相分率00质量流量kg/hr5070.597165070.59716热焓Gcal/hr-18.648647-18.761948ΣHGcal/hr-18.648647-18.761948能量平衡计算表Q总（Gcal/hr）W总（Gcal/hr）ΣHin（Gcal/hr）ΣHout（Gcal/hr）Error-0.11330070-18.648647-18.7619483E-072.2.6加热器（E0109）负荷计算表HeatingDutyHeatduty（Gcal/hr）1.90495391Q=1.90495391Gcal/hr物流焓变计算表流入流出温度C-109.6698110压力MPa0.1013250.101325气相分率0.997839641质量流量kg/hr63807.205763807.2057热焓Gcal/hr-3.6106982-1.7057443ΣHGcal/hr-3.6106982-1.7057443能量平衡计算表Q总（Gcal/hr）W总（Gcal/hr）ΣHin（Gcal/hr）ΣHout（Gcal/hr）Error1.904953910-3.6106982-1.70574431E-082.3丙烯回收车间2.3.1冷凝器（E0104）负荷计算表HeatingDutyHeatduty（Gcal/hr）-0.564292Q=-0.564292Gcal/hr物流焓变计算表流入流出温度C31.406154-90压力MPa11气相分率10.94942815质量流量kg/hr13650.128413650.1284热焓Gcal/hr-0.4784869-1.042779ΣHGcal/hr-0.4784869-1.042779能量平衡计算表Q总（Gcal/hr）W总（Gcal/hr）ΣHin（Gcal/hr）ΣHout（Gcal/hr）Error-0.5642920-0.4784869-1.0427791E-072.3.2汽轮机（C0103）物流焓变计算表流入流出温度C-90-148.41986压力MPa10.101325气相分率10.98530849质量流量kg/hr12605.875712605.8757热焓Gcal/hr-0.8282186-1.0260996ΣHGcal/hr-0.8282186-1.0260996能量平衡计算表Q总（Gcal/hr）W总（Gcal/hr）ΣHin（Gcal/hr）ΣHout（Gcal/hr）Error0-0.197881-0.8282186-1.026099602.3.3加热器（E0105）负荷计算表HeatingDutyHeatduty（Gcal/hr）0.56429204Q=0.56429204Gcal/hr物流焓变计算表流入流出温度C-148.4198621.0461878压力MPa0.1013250.101325气相分率0.985308491质量流量kg/hr12605.875712605.8757热焓Gcal/hr-1.0260996-0.4618076ΣHGcal/hr-1.0260996-0.4618076能量平衡计算表Q总（Gcal/hr）W总（Gcal/hr）ΣHin（Gcal/hr）ΣHout（Gcal/hr）Error0.564292040-1.0260996-0.46180764E-082.3.4加热器（E0106）负荷计算表HeatingDutyHeatduty（Gcal/hr）0.1493552Q=0.1493552Gcal/hr物流焓变计算表流入流出温度C-90.01468325压力MPa0.30.3气相分率00.93328227质量流量kg/hr1034.81261034.8126热焓Gcal/hr-0.2134199-0.0640646ΣHGcal/hr-0.2134199-0.0640646能量平衡计算表Q总（Gcal/hr）W总（Gcal/hr）ΣHin（Gcal/hr）ΣHout（Gcal/hr）Error0.14935520-0.2134199-0.06406461E-072.4丙二醇合成车间2.4.1冷却器（E0201）负荷计算表HeatingDutyHeatduty（Gcal/hr）-1.2090771Q=-1.2090771Gcal/hr物流焓变计算表流入流出温度C80.939873640压力MPa11气相分率00质量流量kg/hr32229.691932229.6919热焓Gcal/hr-103.48496-104.69403能量平衡计算表Q总（Gcal/hr）W总（Gcal/hr）ΣHin（Gcal/hr）ΣHout（Gcal/hr）Error-1.20907710-103.48496-104.694037.1E-062.4.2水合反应器（R0201）负荷计算表HeatingDutyHeatduty（Gcal/hr）2.2454717Q=2.2454717Gcal/hr物流焓变计算表流入流出温度C4040压力MPa11气相分率00质量流量kg/hr32229.691932229.735热焓Gcal/hr-104.69403-102.4487ΣHGcal/hr-104.69403-102.4487能量平衡计算表Q总（Gcal/hr）W总（Gcal/hr）ΣHin（Gcal/hr）ΣHout（Gcal/hr）Error2.24547170-104.69403-102.44870.00014172.4.3丙烯醛回收塔（T0201）负荷计算表CondenserReboilerHeatduty（Gcal/hr）-0.36897640.8984715Q（Gcal/hr）-0.36897640.8984715物流焓变计算表流入1流出1流出2流出3温度C39.7481523568.32891775压力MPa0.0280.0280.0280.028气相分率0001质量流量kg/hr32186.89291075.1439231087.498924.2501542热焓Gcal/hr-102.41768-1.6463689-100.22612-0.0156970ΣHGcal/hr-102.41768-1.6463689-100.22612-0.0156970能量平衡计算表Q1（Gcal/hr）Q2（Gcal/hr）W总（Gcal/hr）ΣHin1（Gcal/hr）ΣHout1（Gcal/hr）ΣHout2（Gcal/hr）ΣHout3（Gcal/hr）Error-0.36897640.89847150-102.41768-1.6463689-100.22612-0.01569701E-062.4.4冷却器（E0202）负荷计算表HeatingDutyHeatduty（Gcal/hr）-0.7266639Q=-0.7266639Gcal/hr物流焓变计算表流入流出温度C72.737688735压力MPa66气相分率00质量流量kg/hr31087.498931087.4989热焓Gcal/hr-100.14667-100.87333ΣHGcal/hr-100.14667-100.87333能量平衡计算表Q总（Gcal/hr）W总（Gcal/hr）ΣHin（Gcal/hr）ΣHout（Gcal/hr）Error-0.72666390-100.14667-100.873333.9E-062.4.5一段加氢反应器（R0202）负荷计算表HeatingDutyHeatduty（Gcal/hr）-1.7086122Q=-1.7086122Gcal/hr物流焓变计算表流入1流入2流出温度C-1.7086122-1.7086122-1.7086122压力MPa-1.7086122-1.7086122-1.7086122气相分率-1.7086122-1.7086122-1.7086122质量流量kg/hr31087.4989711.8356531799.3151热焓Gcal/hr-100.87333-0.0077386-102.58962ΣHGcal/hr-100.87333-0.0077386-102.58962能量平衡计算表Q总（Gcal/hr）W总（Gcal/hr）ΣHin1（Gcal/hr）ΣHin2（Gcal/hr）ΣHout（Gcal/hr）Error-1.70861220-100.87333-0.0077386-102.589626.08E-052.4.6二段加氢反应器（R0203）负荷计算表HeatingDutyHeatduty（Gcal/hr）0.61838497Q=0.61838497Gcal/hr物流焓变计算表流入流出温度C35120压力MPa66气相分率0.170896870.15605714质量流量kg/hr31799.315131799.2914热焓Gcal/hr-102.58962-101.97116ΣHGcal/hr-102.58962-101.97116能量平衡计算表Q总（Gcal/hr）W总（Gcal/hr）ΣHin（Gcal/hr）ΣHout（Gcal/hr）Error0.618384970-102.58962-101.971167.503E-052.4.7冷却器（E0203）负荷计算表HeatingDutyHeatduty（Gcal/hr）-3.02894Q=-3.02894Gcal/hr物流焓变计算表流入流出温度C12025压力MPa66气相分率0.156057140.15078932质量流量kg/hr31799.291431799.2914热焓Gcal/hr-101.97116-105.0001ΣHGcal/hr-101.97116-105.0001能量平衡计算表Q总（Gcal