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Numerical Simulation of the Methanol Synthesis Process by Using HT-L Pulverized Coal Gasification

机译:用HT-L粉煤气化甲醇合成过程的数值模拟

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The numerical simulation of the methanol synthesis process by using HT-L pulverized coal gasification is studied in the work. Pulverized coal gasification are simulated by Aspen Plus industrial systems flower software, and the optimum condition can be gained by calculation. The pulverized coal entrained-fiow gasifier adopts the minimization method of Gibbs free energy. Under the given conditions of 1500°C and carbon conversion of 99%, when coal flow volume is 3265.87 kg/h and the ratio of air and coal is 4:1, the content of effective gas is maximal, and also the content of effective gas increased with increasing of the pressure.
机译:在工作中研究了通过使用HT-L粉煤气化的甲醇合成过程的数值模拟。通过Aspen Plus工业系统花软件模拟粉煤气化,并且可以通过计算来获得最佳状态。粉煤夹带的-ViOW气化器采用吉布斯自由能的最小化方法。在1500℃和碳转化率为99%的给定条件下,当煤流量为3265.87 kg / h时,空气和煤的比例为4:1,有效气体的含量最大,也是有效的含量随着压力的增加,气体增加。

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