Optimizing methanol synthesis combining steelworks off-gases and renewable hydrogen

被引:10
作者
Bampaou, M. [1 ,2 ]
Haag, S. [3 ]
Kyriakides, A. -S [1 ]
Panopoulos, K. D. [1 ]
Seferlis, P. [1 ,2 ]
机构
[1] Ctr Res & Technol Hellas CERTH, Chem Proc & Energy Resources Inst CPERI, Thessaloniki 57001, Greece
[2] Aristotle Univ Thessaloniki, Dept Mech Engn, Thessaloniki 54124, Greece
[3] Air Liquide Forsch & Entwicklung GmbH, D-60388 Frankfurt, Germany
关键词
Methanol; Steelworks; Renewable hydrogen; Hydrogen utilization; Optimization; COKE-OVEN GAS; DYNAMIC OPTIMIZATION; SHELL TEMPERATURE; CO2; RECYCLE; CONVERSION;
D O I
10.1016/j.rser.2022.113035
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Renewable hydrogen improves the carbon balance of the methanol synthesis process but raises the production costs rendering a suitable hydrogen utilization strategy necessary. This work proposes different operating maps and reactor configurations that lead to improved hydrogen utilization and thus lower production costs. A mixture of steelworks off-gases is investigated as feedstock for the synthesis. At first, the conventional single-reactor loop operation is investigated, whereas in the second part, multi-reactor configurations are proposed to improve the process performance. Crucial operating variables are optimized to achieve optimum hydrogen utilization con-ditions for the investigated reactor setups. Results showed that recycling improved the performance in the single -reactor but no substantial improvements are observed for the multi-reactor setups. Overall, the four-reactor concept improves significantly the process efficiency that consequently could reduce the associated produc-tion costs: 13% lower hydrogen, 30% lower feedstock, 27% lower compression requirements and higher CO2 conversion (63%) per produced methanol unit.
引用
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页数:13
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