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潮汐式嗜氢型甲烷化性能及其用于CO2富液再生可行性

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碳捕集与转化利用是应对气候变暖、实现"双碳"目标的重要技术手段之一.化学吸收法是目前发展成熟的碳捕集技术之一,但面临CO2富液再生能耗高的问题.为降低碳捕集成本,提出了一种基于嗜氢型甲烷化的CO2富液生物再生方法,即以Na2CO3和微生物营养液配制pH为10的溶液作为CO2吸收剂,同时利用嗜氢型甲烷化过程将吸收富液中的CO2转化为CH4,实现CO2富液再生和吸收剂循环利用.为提高CO2生物转化速率,构建了一种潮汐式嗜氢型甲烷化反应器,在完成该反应器启动阶段运行性能研究的基础上,考察了该反应器用于CO2富液生物再生的可行性.结果表明:潮汐式嗜氢型甲烷化反应器在第33天时的气体停留时间(Gas Residence Time,GRT)达到23 min,反应器出口 CH4体积分数为95%左右,CO2转化速率是常规滴流床和固定床的10倍左右;启动阶段的pH、碱度基本保持稳定,未出现明显的有机酸积累现象,有机酸总浓度平均值为0.2~2.3 mmol/L.在随后5个周期的CO2富液生物再生试验中,再生后吸收剂的CO2吸收量平均值为55 mmol/L,标准差为1.1 mmol/L,再生后吸收剂的pH稳定在9.53±0.05,说明基于嗜氢型甲烷化的CO2富液生物再生可基本实现吸收剂的循环利用;CO2富液生物再生试验结束后,反应器内耐碱性细菌属Proteiniborus、Acinetobacter以及古菌属Methanobacterium的相对丰度增加,说明微生物通过群落结构调整逐步适应在弱碱性条件下开展CO2甲烷化等代谢活动.
Performance of tidal hydrogenotrophic methanation and its feasibility for regenerating CO2-loaded solutions
To counteract global warming and reach the"double carbon"target,carbon capture,conversion,and utilization(CCCU)is a crucial technical strategy.One of the most recognizable carbon capture techniques,chemical absorption requires a lot of energy to regenerate CO2-loaded solutions.Bio-regeneration of CO2-loaded solutions using hydrogenotrophic methanation was proposed here for reducing carbon capture costs.In this method,a solution with a pH of 10 was prepared with Na2CO3 and microbial nutrient solutions as CO2 absorbents,and hydrogenotrophic methanation was used to convert CO2 to CH4 so that the solution could be regenerated and the absorbent reused.Initially,a tidal hydrogenotrophic methanation reactor was developed in order to increase the rate of CO2 bioconversion.Its viability for bio-regeneration of CO2-loaded solutions was determined after examining its startup performance.The results showed that on day 33,the gas residence time(GRT)of the tidal hydrogenotrophic methanation reactor had reached 23 minutes and the CH4 content at the reactor outlet was about 95% ,indicating a CO2 conversion rate about 10 times higher than that of the conventional trickling bed and fixed bed.During the start-up phase,pH and alkalinity were essentially stable,there was no obvious accumulation of organic acids,and the average total organic acid concentration ranged from 0.2 to 2.3 mmol/L.In the subsequent 5 cycles of CO2-loaded solution bio-regeneration experiments,the regenerated absorbent's mean CO2 uptake was 55 mmol/L with a standard deviation of 1.1 mmol/L.The pH of the regenerated absorbent remained stable at 9.53±0.05,indicating that a CO2-loaded solution based on hydrogenotrophic methanation could effectively recycle absorbent.In the reactor,the relative abundance of the alkali-tolerant bacterial genera Proteiniborus and Acinetobacter and the archaeon Methanobacterium increased after the CO2-loaded solution bio-regeneration experiment.Results indicate that microorganisms have progressively adapted to weakly alkaline environments by reorganizing their communities to conduct metabolic processes such as CO2 methanation.

carbon capturehydrogenotrophic methanationCO2 bioconversionbio-regenerationchemical absorption

苗佳慧、王建城、代雅男、徐恒、张佳音、赵敏楠

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中国矿业大学(北京)化学与环境工程学院,北京 100083

滨州魏桥国科高等技术研究院,山东滨州 256606

碳捕集 嗜氢型甲烷化 CO2生物转化 生物再生 化学吸收

2024

洁净煤技术
煤炭科学研究总院 煤炭工业洁净煤工程技术研究中心

洁净煤技术

CSTPCD北大核心
影响因子:0.893
ISSN:1006-6772
年,卷(期):2024.30(11)