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弱碱性吸收剂碳捕集及CO2富液生物再生性能

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碳捕集转化一体化工艺能利用CO2转化过程同步实现CO2富液再生,有望降低碳捕集转化整体成本.为评价生物甲烷化与碳捕集耦合的可行性,首先,在填料塔中考察了以 4.2 g/L NaHCO3、6 g/L Na2CO3、微生物营养液配制的弱碱性吸收剂(pH=10)对模拟烟气中CO2的吸收性能;其次,在厌氧瓶内利用生物甲烷化过程对CO2富液开展 5 个周期的循环再生试验.结果表明,填料塔气体流量≤1.0 L/min时,随液体流量增加,所有试验组CO2去除率逐渐上升并能稳定在80%以上,该填料塔液体流量宜≤0.9 L/min;不同气体流量(0.4~1.2 L/min)下填料塔体积总传质系数基本稳定在 17~19 mol/(h·kPa·m3);CO2吸收导致吸收液中NaHCO3增加、Na2CO3减少,二者变量比值在 1.2~1.9.气体流量为0.6 L/min、液体流量为0.7 L/min时,在维持 80%以上CO2去除率的前提下,该弱碱性吸收剂可循环使用 6 次,此时活性组分 CO2-3 利用率达 89.5%,形成的 CO2 富液中总无机碳量为0.127 mol/L,pH为8.82,能为生物甲烷化微生物提供适宜的生长环境.CO2富液循环生物再生试验表明,每次再生后的吸收剂CO2吸收量基本稳定在69.6~78.6 mmol/L,且再生期间CH4产生过程具有良好的重复性;再生试验后,Firmicutes、Actinobacteriota等耐碱性门水平细菌得到一定富集;氢营养型产甲烷菌在再生前后古菌属中占比均接近 99%,但再生试验期间弱碱性环境导致Methanobrevibacter相对丰度降低了19.5%,unclassified f Methanobacteriaceae增加了 18.7%.初步证实了碳捕集耦合生物甲烷化工艺的可行性.
Performance of carbon capture by a weakly alkaline absorbent and bio-regeneration of the CO2-rich solution
It is expected that integrated carbon capture and conversion(iCCC)will reduce the overall cost of carbon capture & conversion by leveraging the CO2 conversion process to simultaneously regenerate CO2-rich solutions.To assess the feasibility of coupling biomethana-tion and carbon capture,the absorption performance of a slightly alkaline absorbent(pH=10)prepared with 4.2 g/L NaHCO3,6 g/L Na2CO3 and a microbial nutrient solution for CO2 in simulated flue gas in a packed column was investigated.Second,the CO2-rich solu-tion was subjected to a five-cycle regeneration experiment using the biomethanation process in anaerobic bottles.The results show that in the flow-through mode,when the gas flow rate of packed column is≤1.0 L/min,with the increase of liquid flow rate,CO2 removal rates of all experimental groups gradually increase and can be stabilized above 80%,and the liquid flow rate of this packed column is suitable to be≤0.9 L/min.Overall volumetric mass transfer coefficients of the packed column at different gas flow rates(0.4-1.2 L/min)are gen-erally stable between 17-19 mol/(h·kPa·m3).As a result of CO2 absorption,NaHCO3 in the absorption solution increases and Na2 CO3 decreases,with a ratio between 1.2 and 1.9.Under the condition that the CO2 removal rate is greater than 80%,the slightly alka-line absorbent can be recycled 6 times at a gas flow rate of 0.6 L/min and liquid flow rate of 0.7 L/min.The utilization rate of the ac-tive component CO2-3 reaches 89.5%,and the total inorganic carbon(TIC)of the formed CO2-rich solution is 0.127 mol/L at a pH of 8.82,creating an environment conducive to the growth of biomethanation microorganisms.The results of the cyclic experiments on the bio-regeneration of the CO2-rich solution reveal that the absorbed CO2 of the absorbent is basically stable in the range of 69.6-78.6 mmol/L after each regeneration and the CH4 production is reproducible during the regeneration process.As a result of the regeneration experiment,alkali-resistant bacteria at the phylum level,such as Firmicutes and Actinobacteriota,are somewhat enriched.Approximately 99%of ar-chaeal genera are dominated by hydrogenotrophic methanogens before and after regeneration,but the slightly alkaline environment during regeneration results in a 19.5% decrease in the relative abundance of Methanobrevibacter and a 18.7% increase in the relative abundance of unclassified f Methanobacteriaceae,respectively.In conclusion,the above experimental results indicate the feasibility of biomethana-tion combined with carbon capture.

integrated carbon capture and conversion(iCCC)absorbentCO2-rich solutionbio-regenerationbiomethanation

赵敏楠、张佳音、张新妙、徐恒、栾金义、陆丁香、赵鹏宇、陈湘泽、武振康

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中国矿业大学(北京) 化学与环境工程学院,北京 100089

中石化(北京)化工研究院有限公司,北京 100013

碳捕集转化一体化 吸收剂 CO2富液 生物再生 生物甲烷化

国家自然科学基金青年科学基金资助项目

51908547

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(1)
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