重慶chem-magic團(tuán)隊(duì)設(shè)計(jì)版附錄

1、附錄 1物料一覽表MN 再生工段MN 再生塔（T0101）1流入物料 1流入物料 2流出物料 1流出物料 2Temperature C35.040.15119.4744.07Prere bar5.55.55.55Vapor Frac0101Mole Flow kmol/hr3365.1338898.4362330.0789123.488Mass Flow kg/hr107840.219256681.63767145.51297376.3Volume Flow cum/hr137.97904242144.172496.798748125.33EnlpyGcal/hr-191.243-9.539-

2、133.481-74.1661Mass Flow kg/hrH20000N23.576146384.80180146388.4CO4.99738378.236038383.15O208639.67600NO3.90152437.251020034.4MN0.93468.8250.00034369393.31ME107409.4657287.19656930.6123160.57ET0000DMC239.04885.035307.92516.16H2O178.3320.5859906.9430.225MG0000DMO00.03170.03170EG0000DEG0000Mass FracH20

3、000N200.5700.4923CO00.14900.129O200.033700NO00.204300.0674MN00.013500.233ME0.9960.02840.8480.078ET0000DMC0.0020.00030.004601.1.2. 甲醇回收塔（T0102）2流入物料流出物料 1流出物料 2Temperature C119.47147.34111.6Prere bar5.55.25Vapor Frac000Mole Flow kmol/hr2330.078568.541761.539Mass Flow kg/hr67145.5110756.44156389.065Vo

4、lume Flow cum/hr96.79912.740882.927EnlpyGcal/hr-133.481-37.352-96.313Mass Flow kg/hrH2000N2000CO000O2000NO000MN0.000300.00034ME56930.606769.30756161.299ET000DMC307.925221.5686.365H2O9906.9439765.542141.4005H2O0.00200.1470MG0000DMO0000EG0000DEG0000Mole Flow kmol/hrH20000N20.1285225.512905225.643CO0.1

5、781370.1423701370.318O2027000NO0.131747.550710667.677MN0.01556.8283801136.843ME3352.129227.425241776.741722.8154ET0000DMC2.6540.9443.4183950.179H2O9.8990.0325549.9190.0125MG0000DMO00.00030.00030EG0000DEG00003MG000DMO0.03170.03170EG000DEG000Mass FracH2000N2000CO000O2000NO000MN000ME0.8480.07150.996ET0

6、00DMC0.00460.02060.0015H2O0.1480.9080.00251MG000DMO000EG000DEG000Mole Flow kmol/hrH2000N2000CO000O2000NO000MN000ME1776.7424.0091752.73ET000DMC3.41842.460.959H2O549.92542.077.849MG000DMO0.000270.000270EG000DEG0001.2. 羰基化反應(yīng)工段1.2.1羰基化反應(yīng)器（R0201）4流入物料流出物料Temperature C135135Prere bar55Vapor Frac11Mole Flo

7、w kmol/hr10149.6939663.68Mass Flow kg/hr326122.125326122.125Volume Flow cum/hr68885.87265587.277EnlpyGcal/hr-93.316-111.403Mass Flow kg/hrH200N2146391.31146391.31CO67123.71238384.007O200NO20034.452442.2MN69395.7513469.788ME23160.56723160.567ET00DMC16.1584880.591H2O0.2250.225MG00DMO057393.44EG00DEG00

8、Mass FracH200N20.4490.449CO0.2060.118O200NO0.06143220.161MN0.2130.01063953ME0.0710.071ET00DMC00.015H2O00MG00DMO00.176EG00DEG001.2.2 氣體回收塔（0201）5流入物料 1流入物料 2流入物料 3流出物料 1流出物料 2Temperature C1352025.372.6120.02Prere bar54.854.85Vapor Frac10010Mole Flow kmol/hr9663.683191.66470011820.261735.084Mass Flow

9、kg/hr326122.1103717.522380.42351764100456Volume Flow cum/hr65587.28129.8727.870790.58113.62Enlpy Gcal/hr-111.403-181.67-40.098-158.737-155.615Mass Flow kg/hrH200000N2146391.3319.4940146707.23.58CO38384.0197.101038476.15.004O200000NO52442.270.16052508.463.9MN3469.7881539.53105008.420.9ME23160.5710041

10、5.622317.36107702.638191ET00000DMC4880.5911230.45101315.4934795.549H2O0.22528.29563.05328.8862.69MG00000DMO57393.4416.839016.8757393.4EG00000Mole Flow kmol/hrH200N25225.7455225.745CO2396.3851370.348O200NO667.6771747.716MN1136.88356.844ME722.815722.815ET00DMC0.17954.181H2O0.01250.0125MG00DMO0486.018E

11、G00DEG001.2.氣液分離器（V0201）6流入物料流出物料 1流出物料 2Temperature C72.62020Prere bar4.84.84.8Vapor Frac110Mole Flow kmol/hr11820.268628.6093191.664Mass Flow kg/hr351764.02248046.92103717.5Volume Flow cum/hr70790.58243814.383129.867EnlpyGcal/hr-158.737-10.811-181.67DEG00000Mass FracH200000N20.4490.003100.4170CO0.

12、1180.000900.1090O200000NO0.1610.000700.1490MN0.01060.014800.0140ME0.0710.9680.9970.3060.38ET00000DMC0.0150.01200.003740.0477H2O00.0002730.0028200.000624MG00000DMO0.1760.000162000.571EG00000DEG00000Mole Flow kmol/hrH200000N25225.74511.40505237.0220.128CO1370.3483.46701373.6360.179O200000NO1747.7162.3

13、3801749.9240.13MN56.84425.222082.0510.0147ME722.8153133.86696.53361.2771191.898ET00000DMC54.18113.66014.60453.237H2O0.01251.5713.51.60313.48MG00000DMO486.01750.142600.143486.017EG00000DEG000007Mass Flow kg/hrH2000N2146707.22146387.73319.494CO38476.10438379.00397.1O2000NO52508.4652438.370.16MN5008.41

14、93468.8941539.531ME107702.577287.342100415.63ET000DMC1315.49385.0371230.451H2O28.880.58528.295MG000DMO16.8720.031716.839EG000DEG000Mass FracH2000N20.4170.590.0031CO0.1090.15470.00094O2000NO0.14930.2110.0007MN0.01420.0140.0148ME0.3060.02940.968ET000DMC0.003740.0003430.0119H2O000.000273MG000DMO000.000

15、16EG000DEG000Mole Flow kmol/hrH2000N25237.0225225.61711.405CO1373.6361370.173.467O2000NO1749.9241747.5862.338MN82.05156.82925.221ME3361.277227.433133.86ET000DMC14.6040.94413.66羰基化分離工段分離塔（0301）8流入物流流出物流 1流出物流 2Temperature C120.02166.155.8Prere bar51.11.1Vapor Frac000Mole Flow kmol/hr1735.084486.16112

16、48.923Mass Flow kg/hr10045657405.2843050.75Volume Flow cum/hr113.62457.04355.3EnlpyGcal/hr-155.615-81.989-74.823Mass Flow kg/hrH2000N23.58403.584CO5.003505.0035O2000NO3.903.9MN0.900.9ME381910.01738190.98ET000DMC4795.54916.2464779.303H2O62.6940.0074262.686MG000DMO57393.457389.014.4EG000DEG000Mass Fra

17、cH2000N2000CO000.00012O2000NO000MN000ME0.3800.887H2O1.6030.03251.5706MG000DMO0.14290.000270.1426EG000DEG0001.3.2. 甲醇常壓分離塔（0302）9流入物料 1流入物料 1流出物料 1流出物料 2Temperature C55.8136.19865.80346.4Prere bar1.19.811Vapor Frac0000Mole Flow kmol/hr1248.923196.267251.1741194.016Mass Flow kg/hr43050.756441.21611135

18、.6438356.33Volume Flow cum/hr55.2999.93813.19850.011EnlpyGcal/hr-74.823-10.776-18.803-67.502Mass Flow kg/hrH20000N23.584003.584CO5.004005.004O20000NO3.899003.899MN0.9000.9ME38190.986203.9756204.96538189.99ET000DMC0.04770.000280.111H2O0.000600.00146MG000DMO0.57110.0001EG000DEG000Mole Flow kmol/hrH200

19、0N20.12800.128CO0.17900.179O2000NO0.1300.13MN0.01500.015ME1191.8980.0005231191.898ET000DMC53.2370.1853.057H2O3.480.00043.48MG000DMO486.017485.980.037EG000DEG00010ET0000DMC4779.303236.9134863.264152.953H2O62.6860.32863.01460MG0000DMO4.39604.3960EG0000DEG0000Mass FracH20000N20000CO0.00012000.00013O200

20、00NO0000.0001MN0000ME0.8870.9630.5570.996ET0000DMC0.1110.03680.4370.004H2O0.0014600.00570MG0000DMO0.000100.00040EG0000DEG0000Mole Flow kmol/hrH20000N20.128000.128CO0.179000.179O20000NO0.13000.13MN0.01474000.01474ME1191.898193.619193.651191.867ET0000DMC53.0572.6353.9891.698H2O3.480.01823.4980MG0000DM

21、O0.03700.0370EG0000DEG00001.3.3. DMC 分離塔（0303）11流入物料流出物料 1流出物料 2Temperature C66.6136.2183Prere bar109.810Vapor Frac000Mole Flow kmol/hr251.174196.26754.907Mass Flow kg/hr11135.646441.2164694.423Volume Flow cum/hr13.2169.9385.923EnlpyGcal/hr-18.797-10.776-7.329Mass Flow kg/hrH2000N2000CO000O2000NO000

22、MN000ME6204.9656203.9750.99ET000DMC4863.264236.9134626.351H2O63.01460.32862.686MG000DMO4.39604.396EG000DEG000Mass FracH2000N2000CO000O2000NO000MN000ME0.5570.9630.000211ET000DMC0.4370.03680.9855H2O0.0056600.0134MG000DMO0.000400.00094EG000DEG000Mole Flow kmol/hr加氫工段汽化塔（0401）12流入物料 1流入物料 2流入物料 3流出物料Tem

23、perature C167.6938300163.6200Prere bar25252525Vapor Frac0101Mole Flow kmol/hr486.161818059.7811.2292718557.17Mass Flow kg/hr57405.3238704.481088.68397198.47Volume Flow cum/hr57.1798234424.541.11429829201.01EnlpyGcal/hr-81.938331.08259-1.63768-59.4147Mass Flow kg/hrH2036252.170.37136252.55N20000CO000

24、0O20000NO0000MN0000ME0.01692445.0280.0008212445.046ET02.73802.74DMC16.2890.7912017.08H2O0.00751.33620.0003711.344MG00.2825431.232431.54DMO57389.010.3422566.30857955.67EG01.781590.74992.489DEG000.021420.02145H2000N2000CO000O2000NO000MN000ME193.65193.6190.0309ET000DMC53.9892.630151.359H2O3.4980.01823.

25、48MG000DMO0.037200.0372EG000DEG0001.4.2. 加氫反應(yīng)器（0401）13輸入物料輸出物料Temperature C200193Prere bar2525Vapor Frac11Mole Flow kmol/hr18557.1717585.55Mass Flow kg/hr97198.4797198.47Volume Flow cum/hr29201.0127262.7EnlpyGcal/hr-59.4147-74.7823Mass FracH200.93670.0003410.373N20000CO0000O20000NO0000MN0000ME00.063

26、200.0252ET0000DMC0.000284000.000176H2O0000MG000.39610.00444DMO100.52020.5963EG000.08340.000952DEG0000Mole Flow kmol/hrH2017983.30.48N20000CO0000O20000NO0000MN0000ME0.0005376.307076.3072ET00.05900.059DMC0.1810.008800.1896H2O0.0004160.074200.075MG00.003144.78734.791DMO485.980.00294.7956490.779EG00.028

27、71.46211.49DEG000.0002020.00020214Mass Flow kg/hrH236252.5532329.29N200CO00O200NO00MN00ME2445.04633578.03ET2.7385137.4199DMC17.0802517.08H2O1.34475.824MG431.535441.982DMO57955.67579.557EG92.48929910.77DEG0.02145128.514Mass FracH20.3730.333N200CO00O200NO00MN00ME0.025160.3455ET00.0014DMC0.0001760.0001

28、76H2O00.00078MG0.004440.00455DMO0.5962610.005963EG0.0009520.308DEG00.00132Mole Flow kmol/hrH217983.4816037.31N200CO00O200NO00MN00ME76.30721047.933ET0.05942.983DMC0.190.19H2O0.07464.209MG4.79064.9071.4.3. 氣液分離器（V0401）15流入物料流出物料流出物料Temperature C252525Prere bar252424Vapor Frac110Mole Flow kmol/hr17585.

29、5516102.531483.021Mass Flow kg/hr97198.4734758.9362439.54Volume Flow cum/hr16029.8316632.0266.40337EnlpyGcal/hr-114.153-3.6747-110.449Mass Flow kg/hrH232329.2932306.5822.7115N2000CO000O2000NO000MN000ME33578.032445.07831132.95ET137.422.74134.6814DMC17.080.791216.2891H2O75.8241.33674.488MG441.9820.282

30、5441.7DMO579.5570.3422579.215EG29910.771.78229908.99DEG128.5140128.514Mass FracH20.33260.929450.000364N2000CO000O2000NO000MN000ME0.34550.07030.499ET0.00141400.00216DMC0.0001800.000261H2O0.0007800.00119MG0.00454700.007074DMO0.0059600.00928EG0.30800.479DMO490.7794.908EG1.49481.9DEG0.0002021.2111.5. 乙二

31、醇提純工段.5.1 乙二醇粗制塔（0501）16流入物料流出物料 1流出物料 2流出物料 3Temperature C25199.925423.0466623.04666Prere bar241.111Vapor Frac0001Mole Flow kmol/hr1483.021481.6851988.318113.01736Mass Flow kg/hr62439.5429954.4232400.3884.73944Volume Flow cum/hr66.4033731.6961740.2284320.5755EnlpyGcal/hr-110.449-49.4092-57.5208-0.0

32、9371Mass Flow kg/hrH222.7114800.39252322.31896N20000CO0000O20000NO0000MN0000ME31132.95031070.8262.129ET134.68140134.52140.1599DMC16.2891016.25730.03181H2O74.488074.4440.04426MG441.69960.03052441.64970.0194DMO579.21467.6551571.5240.035516DEG0.00132200.0021Mole Flow kmol/hrH216037.3116026.0411.266N200

33、0CO000O2000NO000MN000ME1047.93376.308971.625ET2.9830.0592.9235DMC0.18960.00880.1808H2O4.20890.07424.1347MG4.90660.003144.9035DMO4.9080.00294.9049EG481.90.0287481.871DEG1.2111.211.5.2原料回收塔（0502）17流入物料流出物料 1流出物料 2Temperature C23.05159.8560.83Prere bar111Vapor Frac000Mole Flow kmol/hr988.31811.23977.08

34、9Mass Flow kg/hr32400.381088.68331311.7EG29908.9929818.2490.749150.000139DEG128.514128.49240.021420Mass FracH20.000364000.263383N20000CO0000O20000NO0000MN0000ME0.49900.9590.733182ET0.0021600.0041520.001887DMC0.00026100.0005020.000375H2O0.00119300.0022980.000522MG0.007100.0136310.000229DMO0.00930.000

35、2560.0176390.000419EG0.4790.9954540.0028010DEG0.002060.0042900Mole Flow kmol/hrH211.266300.19471511.07157N20000CO0000O20000NO0000MN0000ME971.62470969.68571.93899ET2.923502.9199960.003472DMC0.180800.18050.000353H2O4.134704.1322510.002457MG4.90350.0003394.9030.000215DMO4.904890.06484.83980.000301EG481

36、.8712480.40911.4620822.24E-06DEG1.2111.21080.0002023.01E-1218Volume Flow cum/hr40.22841.10841.7823EnlpyGcal/hr-57.5208-1.64-54.8813Mass Flow kg/hrH20.3925230.3710730.02145N2000CO000O2000NO000MN000ME31070.820.00082131070.82ET134.52140134.5214DMC16.25728016.25722H2O74.443650.00037174.44328MG441.649743

37、1.231810.41791DMO571.524566.30835.215637EG90.7491590.748980.000168DEG0.0214170.0214170Mass FracH200.0003410N2000CO000O2000NO000MN000ME0.95896500.992307ET0.00415200.004296DMC0.00050200.000519H2O0.00229800.002377MG0.0136310.3961040.000333DMO0.0176390.5201780.000167EG0.0028010.0833570DEG000Mole Flow km

38、ol/hrH20.1947150.1840750.01064N2000CO000O2000NO000MN000ME969.68570969.6857ET2.91999602.919996DMC0.18047800.180478.5.3 乙二醇精制塔（0503）19流入物料流出物料流出物料Temperature C199.9254196.6389247.793Prere bar1.111.1Vapor Frac000Mole Flow kmol/hr481.6851480.47511.209993Mass Flow kg/hr29954.4229826.07128.3531Volume Flow

39、 cum/hr31.6961731.433470.14371EnlpyGcal/hr-49.4092-49.3129-0.16333Mass Flow kg/hrH2000N2000CO000O2000NO000MN000ME000ET000DMC000H2O000MG0.0305180.0305180DMO7.655087.655080EG29818.2429818.170.075103DEG128.49240.214451128.278Mass FracH2000N2000CO000O2000NO000MN000ME000ET000DMC000H2O4.13225104.13223MG4.

40、9029244.7872710.115653DMO4.8397634.7955960.044167EG1.4620821.4620790DEG0.0002020.000202020H2O000MG000DMO0.0002560.0002570EG0.9954540.9997350.000585DEG0.0042900.999415Mole Flow kmol/hrH2000N2000CO000O2000NO000MN000ME000ET000DMC000H2O000MG0.0003390.0003390DMO0.0648250.0648250EG480.4091480.40790.00121D

41、EG1.2108040.0020211.208783附錄 22.1 MN 再生工段能量能量一覽表2.1.1MN 再生塔(T0101)表 2-1反應(yīng)精餾塔焓變計(jì)算表表 2-2反應(yīng)精餾塔負(fù)荷計(jì)算表表 2-3反應(yīng)精餾塔能量平衡計(jì)算表21Q(Gcal/hr)W(Gcal/hr)Hin(Gcal/hr)Hout(Gcal/hr)Errcal/hr)-6.86434360-200.782-207.6470.00006564CONDENSERREBOILERHeat duty(Gcal/hr)-31.42722724.5628834Q=-6.8643436Gcal/hrW=0流入物料 1流入物料 2流出物料

42、 1流出物料 2Temperature ()3540.144.1119.5Prere(bar)5.55.555.5Vapor Frac0110Mole Flow(kmol/hr)3365.1338898.4369123.4882330.078Mass Flow(kg/hr)107840.219256681.637297376.25167145.506Volume Flow(cum/hr)137.97942144.17248125.32596.799Enlpy(Gcal/hr)-191.243-9.539-74.166-133.481H(Gcal/hr)Hin =-200.782Hout =-2

43、07.6472.1.2 甲醇回收塔（T0102）表 2-4甲醇回收塔物流焓變計(jì)算表表 2-5甲醇回收塔負(fù)荷計(jì)算表表 2-6甲醇回收塔能量平衡計(jì)算表22Q(Gcal/hr)W(Gcal/hr)Hin(Gcal/hr)Hout(Gcal/hr)Errcal/hr)-0.1840-133.481-133.6650CONDENSERREBOILERHeat duty(Gcal/hr)-32.21432.03Q=-0.184Gcal/hrW=0流入物料流出物料 1流出物料 2Temperature ()119.5147.3111.6Prere(bar)5.55.25Vapor Frac000Mole F

44、low(kmol/hr)2330.078568.5391761.539Mass Flow(kg/hr)67145.50610756.44156389.065Volume Flow(cum/hr)96.79912.74182.927Enlpy(Gcal/hr)-133.481-37.352-96.313H(Gcal/hr)Hin =-133.481Hout =-133.665羰基化反應(yīng)工段羰基化反應(yīng)器（R0201）表 2-7 羰化反應(yīng)器焓變計(jì)算表表 2-8 羰化反應(yīng)器負(fù)荷計(jì)算表表 2-9 羰化反應(yīng)器能量平衡計(jì)算表23Q(Gcal/hr)W(Gcal/hr)Hin(Gcal/hr)Hout(Gca

45、l/hr)Errcal/hr)-18.0864050-93.316-111.403-0.0000595Heating dutyHeat duty(Gcal/hr)-18.086405Q=-18.086405 Gcal/hrW=0流入物料流出物料Temperature ()135135Prere(bar)55Vapor Frac11Mole Flow(kmol/hr)10149.79663.68Mass Flow(kg/hr)326122.125326122.125Volume Flow(cum/hr)68885.87265587.277Enlpy(Gcal/hr)-93.316-111.403

46、H(Gcal/hr)Hin =-93.316Hout =-111.4032.2.2氣體回收塔（T0201）表 2-10 氣體回收塔物流焓變計(jì)算表表 2-11 氣體回收塔負(fù)荷計(jì)算表表 2-12 氣體回收塔能量平衡計(jì)算表24Q(Gcal/hr)W(Gcal/hr)Hin(Gcal/hr)Hout(Gcal/hr)Errcal/hr)18.820-333.171-314.3510CONDENSERREBOILERHeat duty(Gcal/hr)018.82Q=18.82Gcal/hrW=0流入物料 1流入物料 2流入物料 3流出物料 1流出物料 2Temperature ()1352025.37

47、2.6120Prere(bar)54.854.85Vapor Frac10010Mole Flow(kmol/hr)9663.683191.66470011820.261735.084Mass Flow(kg/hr)326122.125103717.50322380.418351764.017100456.03Volume Flow(cum/hr)65587.277129.86727.870790.582113.624Enlpy(Gcal/hr)-111.403-181.67-40.098-158.737-155.6145H(Gcal/hr)Hin =-333.171Hout =-314.35

48、12.2.3氣液分離器（V0201）表 2-13 氣液分離器焓變計(jì)算表表 2-14 氣液分離器負(fù)荷計(jì)算表表 2-15 氣液分離器能量平衡計(jì)算表25Q(Gcal/hr)W(Gcal/hr)Hin(Gcal/hr)Hout(Gcal/hr)Errcal/hr)-33.7430-158.737-192.480Heating dutyHeat duty(Gcal/hr)-33.743Q=-33.743Gcal/hrW=0流入物料流出物料 1流出物料 2Temperature ()72.62020Prere(bar)4.84.84.8Vapor Frac110Mole Flow(kmol/hr)1182

49、0.268628.6093191.664Mass Flow(kg/hr)351764.017248046.921103717.503Volume Flow(cum/hr)70790.58243814.3834129.867Enlpy(Gcal/hr)-158.737-10.811-181.67H(Gcal/hr)Hin =-158.737Hout =-192.48羰基化分離工段分離塔（0301）表 2-16DMO 分離塔物流焓變計(jì)算表表 2-17DMO 分離塔負(fù)荷計(jì)算表表 2-18DMO 分離塔能量平衡計(jì)算表26Q(Gcal/hr)W(Gcal/hr)Hin(Gcal/hr)Hout(Gcal

50、/hr)Errcal/hr)-1.1980-155.6145-156.812-0.000764CONDENSERREBOILERHeat duty(Gcal/hr)-13.80712.609Q=-1.198Gcal/hrW=0流入物料流出物料 1流出物料 2Temperature ()120166.155.8Prere(bar)51.11.1Vapor Frac000Mole Flow(kmol/hr)1735.084486.1611248.923Mass Flow(kg/hr)100456.0357405.27843050.751Volume Flow(cum/hr)113.62457.04

51、355.299Enlpy(Gcal/hr)-155.6145-81.989-74.823H(Gcal/hr)Hin =-155.6145Hout =-156.8122.3.2甲醇常壓分離塔（0302）表 2-19甲醇常壓分離塔物流焓變計(jì)算表表 2-20 甲醇常壓分離塔負(fù)荷計(jì)算表表 2-21 甲醇常壓分離塔能量平衡計(jì)算表27Q(Gcal/hr)W(Gcal/hr)Hin(Gcal/hr)Hout(Gcal/hr)Errcal/hr)-0.7050-85.599464-86.304965-0.0000501CONDENSERREBOILERHeat duty(Gcal/hr)-96.78996.0

52、84Q=-0.705Gcal/hrW=0流入物料 1流入物料 2流出物料 1流出物料 2Temperature ()55.8136.265.846.4Prere(bar)1.19.811Vapor Frac0000Mole Flow(kmol/hr)1248.923196.267251.1741194.016Mass Flow(kg/hr)43050.7516441.21611135.63938356.328Volume Flow(cum/hr)55.2999.93813.19850.011Enlpy(Gcal/hr)-74.823-10.776-18.803-67.502H(Gcal/hr)

53、Hin =-85.599464Hout =-86.3049652.3.3DMC 分離塔（0303）表 2-22甲醇加壓分離塔物流焓變計(jì)算表表 2-23 甲醇加壓分離塔負(fù)荷計(jì)算表表 2-24 甲醇加壓分離塔能量平衡計(jì)算表28Q(Gcal/hr)W(Gcal/hr)Hin(Gcal/hr)Hout(Gcal/hr)Errcal/hr)0.69190-18.796667-18.104797-0.00003CONDENSERREBOILERHeat duty(Gcal/hr)-5.51997246.2118418Q=0.6919Gcal/hrW=0流入物料流出物料 1流出物料 2Temperature

54、 ()66.6136.2182.9Prere(bar)109.810Vapor Frac000Mole Flow(kmol/hr)251.174196.26754.907Mass Flow(kg/hr)11135.6396441.2164694.423Volume Flow(cum/hr)13.2169.9385.923Enlpy(Gcal/hr)-18.797-10.776-7.329H(Gcal/hr)Hin =-18.796667Hout =-18.1047972.加氫工段2.4.1汽化塔（0401）表 2-25DMO 汽化塔焓變計(jì)算表表 2-26DMO 汽化塔負(fù)荷計(jì)算表表 2-27DM

55、O 汽化塔能量平衡計(jì)算表29Q(Gcal/hr)W(Gcal/hr)Hin(Gcal/hr)Hout(Gcal/hr)Errcal/hr)-6.92136160-52.493391-59.4147-0.000034Heating dutyHeat duty(Gcal/hr)-6.9213616Q=-6.8986 Gcal/hrW=0流入物料 1流入物料 2流入物料 3流出物料Temperature ()167.7300163.57200Prere(bar)25252525Vapor Frac0101Mole Flow(kmol/hr)486.161818059.7811.2292718557.

56、17Mass Flow(kg/hr)57405.3238704.481088.68397198.47Volume Flow(cum/hr)57.1798234424.541.11429829201.01Enlpy(Gcal/hr)-81.938331.08259-1.63768-59.4147H(Gcal/hr)Hin =-52.493391Hout=-59.41472.4.2加氫反應(yīng)器（0401）表 2-28DMO 加氫反應(yīng)器焓變計(jì)算表表 2-29 DMO 加氫反應(yīng)器負(fù)荷計(jì)算表表 2-30DMO 加氫反應(yīng)器能量平衡計(jì)算表30Q(Gcal/hr)W(Gcal/hr)Hin(Gcal/hr)Ho

57、ut(Gcal/hr)Errcal/hr)-15.3675190-59.4147-74.78230.000055Heating dutyHeat duty(Gcal/hr)-15.367519Q=-15.367519Gcal/hrW=0流入物料流出物料Temperature ()200193Prere(bar)2525Vapor Frac11Mole Flow(kmol/hr)18557.1717585.55Mass Flow(kg/hr)97198.4797198.47Volume Flow(cum/hr)29201.0127262.7Enlpy(Gcal/hr)-59.4147-74.78

58、23H(Gcal/hr)Hin =-59.4147Hout =-74.78232.4.3氣液分離器（V0401）表 2-31 氣液分離器焓變計(jì)算表表 2-32 氣液分離器負(fù)荷計(jì)算表表 2-33 氣液分離器能量平衡計(jì)算表31Q(Gcal/hr)W(Gcal/hr)Hin(Gcal/hr)Hout(Gcal/hr)Errcal/hr)0.028742960-114.153-114.123920.0000053Heating dutyHeat duty(Gcal/hr)0.02874296Q=0.02874296Gcal/hrW=0流入物料流出物料 1流出物料 2Temperature ()2525

59、25Prere(bar)252424Vapor Frac110Mole Flow(kmol/hr)17585.5516102.531483.021Mass Flow(kg/hr)97198.4734758.9362439.54Volume Flow(cum/hr)16029.8316632.0266.40337Enlpy(Gcal/hr)-114.153-3.6747-110.449H(Gcal/hr)Hin =-114.153Hout =-114.12392乙二醇提純工段乙二醇粗制塔（0501）表 2-34乙二醇粗制塔物流焓變計(jì)算表表 2-35 乙二醇粗制塔負(fù)荷計(jì)算表表 2-36 乙二醇粗制

60、塔能量平衡計(jì)算表32Q(Gcal/hr)W(Gcal/hr)Hin(Gcal/hr)Hout(Gcal/hr)Errcal/hr)3.4254770-110.449-107.023740.000023CONDENSERREBOILERHeat duty(Gcal/hr)-22.40660725.832084Q=3.425477Gcal/hrW=0流入物料流出物料 1流出物料 2流出物料 3Temperature ()25199.925423.0466623.04666Prere(bar)241.111Vapor Frac0001Mole Flow(kmol/hr)1483.021481.685