| 焦炉煤气部分氧化制甲醇合成气研究 |
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| 引用本文： | 丁洁. 焦炉煤气部分氧化制甲醇合成气研究[J]. 当代化工, 2017, 46(5). DOI: 10.3969/j.issn.1671-0460.2017.05.005 |
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| 作者姓名： | 丁洁 |
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| 作者单位： | 青岛职业技术学院,山东青岛,266555 |
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| 摘 要： | 应用ChemCAD软件,采用吉布斯反应器模型对转化炉进行模拟,分析了温度、压力、进气量等各工艺条件对反应的影响。模拟结果表明,焦炉煤气部分氧化制取合成气适宜的操作条件为:进气温度500℃,反应压力1.85 MPa,进入转化炉各物流的摩尔流量COG(焦炉煤气):H_2O:O_2:CO_2=1:0.8:0.21:0.095。
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| 关 键 词： | 焦炉煤气 甲醇 合成气 Chem CAD |
Research on Producing Methanol Synthesis Gas From Coke Oven Gas by Partial Oxidation |
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| DING Jie. Research on Producing Methanol Synthesis Gas From Coke Oven Gas by Partial Oxidation[J]. Contemporary Chemical Industry, 2017, 46(5). DOI: 10.3969/j.issn.1671-0460.2017.05.005 |
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| Authors: | DING Jie |
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| Abstract: | Gibbs reactor model of ChemCAD program was used to simulate the conversion furnace.The influences of temperature,pressure and feed flow rate on the reaction were analyzed.The results show that the optimal operating conditions of the reaction are as follows:feed temperature 500 ℃,reaction pressure 1.85 MPa,and feed mole flow ratio COG(coke oven gas):H2O∶ O2∶CO2=1∶ 0.8∶ 0.21∶ 0.095. |
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| Keywords: | Coke oven gas Methanol Synthesis gas Chem CAD |
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