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A novel coke-oven gas-to-natural gas and hydrogen process by integrating chemical looping hydrogen with methanation

机译:通过将化学环化氢气与甲烷化反应相结合的新型焦炉气制天然气制氢工艺

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摘要

The coke-oven gas (COG)-to-natural gas (CGtNG) is a promising process of chemical industry. However, the CGtNG suffers from low hydrogen utilization efficiency and natural gas capacity due to the high ratio of hydrogen to carbon of the COG. The CO2derived from chemical looping hydrogen process can be an effective carbon source to optimize syngas composition for high efficient natural gas production. Therefore, a novel process of COG chemical looping hydrogen assisted COG-to-natural gas (CGCLH-CGtNG) is proposed in this paper. The key parameters are optimized for maximizing COG utilization and natural gas production in the novel process. Results show that the novel process could solve the issues of CO2utilization in the chemical looping hydrogen process and low natural gas production in the CGtNG. At the cost of additional 4.36 t/h COG consumption, the novel process produce about 19% more natural gas and additional 1.39 t/h hydrogen compared with the conventional CGtNG process. The corresponding hydrogen utilization and exergy efficiencies of the novel process are increased from 61.1% to 78.5% in the CGtNG to 82.4% and 87.6% through intensive mass and energy integration, respectively.
机译:焦炉气(COG)转换为天然气(CGtNG)是化学工业的一个有前途的过程。但是,由于COG的氢碳比高,因此CGtNG的氢利用效率和天然气容量低。来自化学循环氢工艺的二氧化碳可以是有效的碳源,可以优化合成气的组成,从而实现高效的天然气生产。因此,本文提出了一种新的COG化学环化氢气辅助COG制天然气的工艺(CGCLH-CGtNG)。对关键参数进行了优化,以在新工艺中最大程度地提高COG利用率和天然气产量。结果表明,该新方法可以解决化学循环制氢过程中二氧化碳利用和CGtNG天然气产量低的问题。与传统的CGtNG工艺相比,该新工艺以增加4.36 t / h的COG消耗为代价,可生产约19%的天然气和额外的1.39 t / h氢气。通过密集的质量和能量整合,新工艺的相应氢气利用率和火用效率分别从CGtNG中的61.1%提高到78.5%,分别提高到82.4%和87.6%。

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