石灰厂二氧化碳的高效捕集:利用间接加热碳酸盐循环技术对综合概念进行技术经济评估

Martin Greco-Coppi , Peter Seufert , Carina Hofmann , Angela Rolfe , Ye Huang , Sina Rezvani , Jochen Ströhle , Bernd Epple
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引用次数: 0

摘要

由于二氧化碳排放的数量和性质,寻求石灰和水泥行业脱碳具有挑战性。除非采用碳捕集技术,否则煅烧过程中的排放是不可避免的。然而,大多数现有的碳捕集技术成本高且能效低。间接加热碳酸盐循环(IHCaL)工艺是一种从石灰和水泥生产中捕获二氧化碳的有前途的技术,其特点是经济性和能源利用率低。以前的工作已经强调了 IHCaL 的潜力,但对该工艺的优化还没有进行足够详细的讨论,对其技术经济影响也还没有充分了解。在这项工作中,模拟了使用 IHCaL 技术从石灰厂捕集二氧化碳的十种方案。因此,计算了不同的工艺配置、热回收策略和燃料选择。利用 Aspen Plus® 软件对捕集设施进行了计算,并利用 EBSILON®Professional 对蒸汽循环进行了模拟。结果表明,燃烧器燃料的选择不仅会影响二氧化碳平衡和能源性能,而且也是一个重要的成本驱动因素--使用中热值固体回收燃料(SRF)的计算案例具有相当大的经济优势。分析表明了如何优化热回收策略,以实现量身定制的结果,如减少燃料需求或提高发电量。与相同应用的其他技术相比,使用 SRF 的一次能源消耗量(-0.3 至 +2.5 MJLHV/tCO2,av)和避免二氧化碳排放的成本(-11 至 +25 欧元/tCO2,av)都相当低。敏感性研究表明,影响经济性的主要参数是贴现率和项目寿命。与参考电厂相比,捕集电厂对参数变化的敏感性更高,而使用 SRF 的电厂则比以褐煤为燃料的电厂更为敏感。这项工作的结论为实验研究开辟了一条新途径,以验证关键假设,并在 2030 年前实现 IHCaL 技术的工业化应用。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

Efficient CO2 capture from lime plants: Techno-economic assessment of integrated concepts using indirectly heated carbonate looping technology

Efficient CO2 capture from lime plants: Techno-economic assessment of integrated concepts using indirectly heated carbonate looping technology

The quest to decarbonize the lime and cement industry is challenging because of the amount and the nature of the CO2 emissions. The process emissions from calcination are unavoidable unless carbon capture is deployed. Nevertheless, the majority of the available carbon capture technologies are expensive and energy inefficient. The indirectly heated carbonate looping (IHCaL) process is a promising technology to capture CO2 from the lime and cement production, featuring low penalties in terms of economics and energy utilization. Previous works have highlighted the potential of the IHCaL, but the optimization of the process has not been discussed in enough detail and techno-economic implications are not yet fully understood. Within this work, ten scenarios using IHCaL technology to capture CO2 from a lime plant were simulated. Hereby, different process configurations, heat recovery strategies and fueling options were computed. The calculations for the capture facilities were performed with Aspen Plus® software and EBSILON®Professional was used to simulate the steam cycles. A techno-economic assessment was included as well, aided by the ECLIPSE software.

The results demonstrate that the selection of the fuel for the combustor not only affects the CO2 balance and energy performance but is also an important cost driver —there were considerable economic advantages for the computed cases with middle-caloric solid recovered fuel (SRF). The analysis shows how the heat recovery strategy can be optimized to achieve tailored outcomes, such as reduced fuel requirement or increased power production. The specific primary energy consumption (from −0.3 to +2.5 MJLHV/tCO2,av) and cost for CO2 avoided (from −11 to +25 €/tCO2,av) using SRF are considerably low, compared with other technologies for the same application. The sensitivity study revealed that the main parameters that impact the economics are the discount rate and the project life. The capture plants are more sensitive to parameter changes than the reference plant, and the plants using SRF are more sensitive than the lignite-fueled plants. The conclusions from this work open a new pathway of experimental research to validate key assumptions and enable the industrial deployment of IHCaL technology before 2030.

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