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Capturing CO2 from ambient air using a polyethyleneimine–silica adsorbent in fluidized beds

机译:在流化床中使用聚乙烯亚胺-二氧化硅吸附剂从环境空气中捕获二氧化碳

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摘要

Carbon Capture and Storage (CCS) uses a combination of technologies to capture, transport and store carbon dioxide (CO2) emissions from large point sources such as coal or natural gas-fired power plants. Capturing CO2 from ambient air has been considered as a carbon-negative technology to mitigate anthropogenic CO2 emissions in the air. The performance of a mesoporous silica-supported polyethyleneimine (PEI)–silica adsorbent for CO2 capture from ambient air has been evaluated in a laboratory-scale Bubbling Fluidized Bed (BFB) reactor. The air capture tests lasted for between 4 and 14 days using 1 kg of the PEI–silica adsorbent in the BFB reactor. Despite the low CO2 concentration in ambient air, nearly 100% CO2 capture efficiency has been achieved with a relatively short gas–solid contact time of 7.5 s. The equilibrium CO2 adsorption capacity for air capture was found to be as high as 7.3 wt%, which is amongst the highest values reported to date. A conceptual design is completed to evaluate the technological and economic feasibility of using PEI–silica adsorbent to capture CO2 from ambient air at a large scale of capturing 1 Mt-CO2 per year. The proposed novel “PEI-CFB air capture system” mainly comprises a Circulating Fluidized Bed (CFB) adsorber and a BFB desorber with a CO2 capture capacity of 40 t-CO2/day. Large pressure drop is required to drive the air through the CFB adsorber and also to suspend and circulate the solid adsorbents within the loop, resulting in higher electricity demand than other reported air capture systems. However, the Temperature Swing Adsorption (TSA) technology adopted for the regeneration strategy in the separate BFB desorber has resulted in much smaller thermal energy requirement. The total energy required is 6.6 GJ/t-CO2 which is comparable to other reference air capture systems. By projecting a future scenario where decarbonization of large point energy sources has been largely implemented by integration of CCS technologies, the operating cost under this scenario is estimated to be $108/t-CO2 captured and $152/t-CO2 avoided with an avoided fraction of 0.71. Further research on the proposed 40 t-CO2/day ‘PEI-CFB Air Capture System’ is still needed which should include the evaluation of the capital costs and the experimental investigation of air capture using a laboratory-scale CFB system with the PEI–silica adsorbent.
机译:碳捕集与封存(CCS)结合使用多种技术来捕获,运输和存储来自大型点源(如煤炭或天然气发电厂)的二氧化碳(CO2)排放。从环境空气中捕获二氧化碳一直被认为是减少空气中人为二氧化碳排放的碳负技术。已经在实验室规模的鼓泡流化床(BFB)反应器中评估了介孔二氧化硅负载的聚乙烯亚胺(PEI)-二氧化硅吸附剂从周围空气中捕获二氧化碳的性能。在BFB反应器中使用1 kg PEI-二氧化硅吸附剂进行的空气捕获测试持续4到14天。尽管环境空气中的CO2浓度较低,但相对较短的7.5 s的气固接触时间仍可实现近100%的CO2捕集效率。发现用于空气捕获的平衡CO 2吸附能力高达7.3 wt%,是迄今为止报道的最高值之​​一。完成了一个概念设计,以评估使用PEI-二氧化硅吸附剂从环境空气中捕集CO2的技术和经济可行性,每年可大量捕集1 Mt-CO2。拟议的新型“ PEI-CFB空气捕集系统”主要包括循环流化床(CFB)吸附器和BFB解吸器,其CO2捕集能力为40 t-CO2 / day。需要很大的压降才能驱动空气通过CFB吸附器,并使悬浮的固体吸附剂在回路中循环并使之循环,与其他报道的空气捕获系统相比,电力需求更高。但是,在单独的BFB解吸器中,作为再生策略采用的变温吸附(TSA)技术导致所需的热能要小得多。所需的总能量为6.6 GJ / t-CO2,与其他参考空气捕获系统相当。通过预测未来的情景,其中通过整合CCS技术在很大程度上实现了大型点能源的脱碳,在此情景下的运营成本估计为108美元/吨二氧化碳捕获量,避免152美元/吨二氧化碳,避免了0.71。仍需要对拟议的40吨二氧化碳/日的“ PEI-CFB空气捕集系统”进行进一步研究,其中应包括资本成本评估以及使用实验室规模的CFB系统和PEI-二氧化硅进行空气捕集的实验研究。吸附剂。

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