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Techno-economic and climate impact analysis of carbon utilization process for methanol production from blast furnace gas over Cu/ZnO/Al_2O_3 catalyst

机译:Cu / ZnO / Al_2O_3催化剂上高炉煤气生产甲醇的碳利用过程的技术经济和气候影响分析

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This paper presents conceptual design, economic evaluation, and sensitivity analysis of a commercial scale carbon-utilization process that produces methanol (MeOH) from blast furnace gas (BFG). Three process cases that use different N_2 compositions in the feed (Case 1: 40%, Case 2: 35%, and Case 3: 30%) are simulated. The kinetic model over a commercial Cu/ZnO/Al_2O_3 catalyst is used to consider the effect of N_2 on the reaction and to find the optimal process synthesis condition. The proposed process yields 78.3-113.3 kt_(MeOH)/y with 32.2-40.2% energy efficiency, and after heat integration it has no requirement for external heat. Case 3 improves energy efficiency by 5.2% compared to the conventional electricity production process from BFG. The process is assessed using techno-economic and environmental metrics. The lowest minimum selling price of US$ 902/t_(MeOH) and the highest potential to reduce CO_2 emissions of 3.9 t_(CO2)/t_(MeOH) are obtained for Case 3. Sensitivity analysis for H_2, electricity price and major economic assumptions shows that Case 3 is the better option in the ranges of H_2 price, except high-priced H_2 produced by solar energy, and in ranges of electricity price using current technology. Case 3 is a techno-economically viable alternative under positive assumptions.
机译:本文介绍了从高炉煤气(BFG)生产甲醇(MeOH)的商业规模碳利用过程的概念设计,经济评估和敏感性分析。模拟了三个在进料中使用不同N_2组成的工艺案例(案例1:40%,案例2:35%和案例3:30%)。利用工业Cu / ZnO / Al_2O_3催化剂的动力学模型考虑了N_2对反应的影响并找到了最佳的工艺合成条件。拟议的过程可产生78.3-113.3 kt_(MeOH)/ y,能量效率为32.2-40.2%,并且在进行热集成后,不需要外部热量。案例3与BFG的常规电力生产过程相比,能效提高了5.2%。使用技术经济和环境指标评估该过程。案例3的最低最低售价为902美元/吨(MeOH),最大的减排潜力为3.9吨(CO2)/ t_(MeOH)。H_2,电价和主要经济假设的敏感性分析结果表明,案例3在H_2价格范围内是更好的选择,除了太阳能生产的高价H_2以及在使用当前技术的电价范围内。在肯定的假设下,案例3是技术上可行的替代方案。

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