【毕业设计】用chemcad模拟年产15,000吨甲乙酮工艺过程-精品(5)

2019-03-09 16:29

安徽工程科技学院毕业设计

Heat Absorbed MJ/h Fuel Usage(SCF) 1488.1289 2089.5830 表3-6 加热炉数据框

Equip. No. Name Thermal mode Pressure Drop MPa Temperature K Heat duty MJ/h Reaction phase No of Reactions Calc Ht of Rxn MJ/h 6 REACTOR SYS. 2 0.0100 673.1500 1369.2838 1 1 1361.3002 表3-7 化学计量反应器数据框

Equip. No. Name Output pressure MPa Efficiency Calculated power kW Calculated Pout MPa Head m Vol. flow rate m3/h Mass flow rate kg/h 9 0.4666 0.1254 0.4666 21.3007 2.7070 2159.6606 10 0.4333 0.7500 0.0329 0.4333 46.1842 0.2704 195.8326 14 0.4000 0.7500 0.0269 0.4000 37.8072 0.2431 195.8326 19 0.3566 0.7500 0.0036 0.3566 33.2336 0.0378 29.6122 21 0.4000 0.7500 0.2583 0.4000 37.7869 2.3334 1880.5293 表3-8 泵数据框

混合器数据:11,18为混合器代号。

Equip. No. Name Mode Stream no. adjusted Variable No. Sign Flag Tolerance Measured variables: Number Variable Constant Units 12 2 1 6 0 1.0000e-006 16 -201 2070.0000 1 表3-9 控制器数据框

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罗胜:用chemcad模拟年产15,000吨甲乙酮工艺过程

Equip. No. Name Split Destination Press Drop MPa Component No. 3 15 ROCKSALT BED 1 0.0100 1.0000 表3-10 组分分离器数据框

Stream No. Stream Name 1 SBA 2 HYDROGEN GAS 300.4193 0.3000 -87.278 1.0000 25.2171 0.2401 0.0056 0.0145 24.9567 7 CUT 3 673.1500 0.3966 -5337.3 1.0000 54.3380 2.7733 26.3354 0.2669 24.9625 12 MEK 352.1925 0.1013 -6633.6 0.00000 3 4 5 Temp K Pres MPa Enth MJ/h Vapor mole fraction Total kmol/h Flowrates in kmol/h Sec-Butanol MEK Water Hydrogen Stream No. Stream Name Temp K Pres MPa Enth MJ/h Vapor mole fraction Total kmol/h Flowrates in kmol/h Sec-Butanol MEK Water Hydrogen Stream No. Stream Name Temp K Pres MPa Enth MJ/h Vapor mole fraction 298.1500 0.1013 -8731.4 0.00000 25.5620 25.3089 0.0000 0.2531 0.0000 6 673.1500 0.4066 -6706.5 1.0000 29.3784 27.7330 1.3757 0.2669 0.0028 11 359.6336 0.1240 -7467.0 0.00000 305.8197 0.3000 -9895.8 0.00000 29.3784 27.7330 1.3757 0.2669 0.0028 8 373.1500 0.3866 -7037.9 0.90716 54.3380 2.7733 26.3354 0.2669 24.9625 13 373.2365 0.1053 -855.63 0.00000 305.8956 0.4666 -9895.3 0.00000 29.3784 27.7330 1.3757 0.2669 0.0028 9 308.1500 0.3566 -8117.9 0.48568 54.3380 2.7733 26.3354 0.2669 24.9625 14 351.1500 0.1213 -142.10 1.0000 419.7222 0.4566 -8194.7 0.79400 29.3784 27.7330 1.3757 0.2669 0.0028 10 308.1500 0.3566 -776.6 0.00000 27.9473 2.7267 24.9791 0.2385 0.0030 15 CUT 2 308.1500 0.3566 -350.27 1.0000 - 22 -

安徽工程科技学院毕业设计

Total kmol/h Flowrates in kmol/h Sec-Butanol MEK Water Hydrogen Stream No. Stream Name Temp K Pres MPa Enth MJ/h Vapor mole fraction Total kmol/h Flowrates in kmol/h Sec-Butanol MEK Water Hydrogen Stream No. Stream Name 27.7509 2.7267 24.9781 0.0459 0.0000 16 298.3376 0.4000 -9632.8 0.00000 28.2046 27.9265 0.0250 0.2531 0.0000 21 CUT 1 25.1089 0.1091 24.9532 0.0459 0.0000 17 298.3376 0.4000 -9632.8 0.00000 28.2046 27.9265 0.0250 0.2531 0.0000 22 TO TREATMENT 351.1500 0.1113 -54.265 0.00000 0.1926 0.0000 0.0000 0.1926 0.0000 27 313.1500 0.1013 -111.08 0.00000 0.4146 - 23 -

2.6427 2.6177 0.0250 0.0000 0.0000 18 373.3896 0.4333 -855.52 0.00000 2.6427 2.6177 0.0250 0.0000 0.0000 23 0.6072 0.0012 0.4104 0.1926 0.0030 19 308.1500 0.4000 -897.15 0.00000 2.6427 2.6177 0.0250 0.0000 0.0000 24 26.3907 0.0466 1.3563 0.0283 24.9596 20 298.1500 0.1013 -902.42 0.00000 2.6427 2.6177 0.0250 0.0000 0.0000 25 Temp K Pres MPa Enth MJ/h Vapor mole fraction Total kmol/h Flowrates in kmol/h Sec-Butanol MEK Water Hydrogen Stream No. Stream Name Temp K Pres MPa Enth MJ/h Vapor mole fraction Total kmol/h Flowrates in kmol/h 298.3384 0.4000 -902.32 0.00000 2.6427 2.6177 0.0250 0.0000 0.0000 26 CUT 4 313.3444 0.3566 -111.07 0.00000 0.4146 351.1500 0.1113 -108.07 0.060291 0.4146 0.0012 0.4104 0.0000 0.0030 28 313.1500 0.1013 -0.22677 1.00000 0.0039 313.1500 0.1013 -111.31 0.4146 0.0012 0.4104 0.0000 0.0030 29 298.3376 0.4000 -8730.5 0.00000 25.5620 308.2238 0.3566 -7878.7 28.3580 2.7279 25.3886 0.2385 0.0030 0.0094704 0.00000 OFF-GAS 罗胜:用chemcad模拟年产15,000吨甲乙酮工艺过程

Sec-Butanol MEK Water Hydrogen

0.0012 0.4095 0.0000 0.0000 0.0012 0.4095 0.0000 0.0000 0.0000 0.0010 0.0000 0.0030 0.0000 0.0000 0.2531 0.0000 表3-11 所有流股性质数据框

图3-1 TPXY

图3-2 Binodal Plot

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安徽工程科技学院毕业设计

图3-3 7号塔Tower Profiles

图3-4 8号塔Tower Profiles

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