Arias Borja, Alvarez Criado Yolanda, Méndez Alberto, Marqués Paula, Finca I, Abanades J Carlos
CSIC-INCAR, Francisco Pintado Fe, 26, Oviedo 33011, Spain.
HUNOSA, Avenida de Galicia 44, 33055 Oviedo, Spain.
Energy Fuels. 2024 Jul 24;38(15):14757-14764. doi: 10.1021/acs.energyfuels.4c02472. eCollection 2024 Aug 1.
Postcombustion CO capture by calcium looping using circulating fluidized bed technology, CFB-CaL, is evolving to tackle industrial sectors that are difficult to decarbonize. In addition to the known advantages of CFB-CaL (i.e., retrofittability and competitive energy efficiencies and cost), the fuel flexibility by using renewable biomass in the oxy-fired CFB calciner and the possibility to reach extremely high CO capture efficiencies in the carbonator are demonstrated in this paper. Results from the latest experimental campaigns in the TRL7 CFB-CaL pilot of the La Pereda are reported, treating over 2000 N m/h of flue gases in the carbonator with a firing capacity of biomass pellets up to 2 MW in the oxy-fired calciner. A new strategy to reach high CO capture efficiencies (above 99% in some cases) in the carbonator has been tested. This involves decoupling the carbonator in two temperature zones by cooling the solids-lean top region to below 550 °C and ensuring that a sufficient flow of active CaO reaches such a region.
采用循环流化床技术(CFB-CaL)通过钙循环进行燃烧后二氧化碳捕集,正在不断发展以应对难以脱碳的工业领域。除了CFB-CaL已知的优势(即可改造性、具有竞争力的能源效率和成本)外,本文还展示了在富氧燃烧循环流化床煅烧炉中使用可再生生物质的燃料灵活性以及在碳酸化器中实现极高二氧化碳捕集效率的可能性。报告了在拉佩雷达的技术就绪水平7(TRL7)CFB-CaL中试装置上最新实验活动的结果,碳酸化器中处理超过2000 N m/h的烟气,富氧燃烧煅烧炉中生物质颗粒的燃烧能力高达2兆瓦。已经测试了一种在碳酸化器中实现高二氧化碳捕集效率(在某些情况下高于99%)的新策略。这包括通过将贫固体顶部区域冷却至550°C以下,使碳酸化器在两个温度区解耦,并确保有足够的活性CaO流到达该区域。