用于煤炭就地气化化学循环燃烧的自热双循环流化床反应器的自洽设计方法

Xi Chen, Haibo Zhao
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摘要

本文建立了以煤为燃料的原地气化化学循环燃烧(iG-CLC)工艺的自热双循环流化床反应器(DCFBR)的设计方法。该方法以自洽现象学模型为基础,全面阐明了反应器内的质量和能量守恒、燃料和氧载体(OC)反应过程以及流化特性等因素。它特别适用于快速筛选众多潜在的设计方案,获得详细的设计参数,并研究它们之间的相互关系。利用这种方法,研究了 5 MWth iG-CLC DCFBR 中双床互动迁移反应现象的调节模式。首先,分析了主要设计参数对 OC 循环速率和床层存量的影响。随后,研究了循环速率对两床间交互传热和传质的影响,为自热 CLC 过程的控制划定了一个合理的范围(循环速率为 50-90 kg/m2s,温差为 30-90 °C,OC 转化率为 0.2-0.35 和氧燃料比为 3-6)。随后,本文研究了主要设计参数对气体/固体燃料转换、运行成本和运行效益等性能指标的影响。研究发现,只要碳剥离器的分离效率保持在 70%-95% 以上,它就能显著提高设备的碳捕获效率。敏感性分析用于研究性能指标对输入参数变化的响应模式。最后,在这些分析的基础上,确定了 5 MWth 反应器的设计方案,并详细研究了设计条件下反应器的压力平衡状态,以及反应器入口和出口的平衡物质流和能量流。
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A self-consistent design method of the autothermal dual circulating fluidized bed reactor for in-situ gasification chemical looping combustion of coal
This paper establishes a design method for the autothermal dual circulating fluidized bed reactor (DCFBR) of the coal-fueled in-situ gasification chemical looping combustion (iG-CLC) process. This method, grounded in a self-consistent phenomenological model, comprehensively elucidates the factors of mass and energy conservation, fuel and oxygen carrier (OC) reaction processes, and fluidization characteristics within the reactor. It is particularly suitable for the rapid screening of numerous potential designs, obtaining detailed design parameters, and studying their interrelationships. Utilizing this method, the regulation patterns of dual-bed interactive transport-reaction phenomena within a 5 MWth iG-CLC DCFBR are studied. Firstly, the effects of key design parameters on the OC circulation rate and bed inventory are analyzed. Following this, the impacts of circulation rate on the interactive heat and mass transfer between two beds are examined, delineating a reasonable range for the control of autothermal CLC process (circulation rate of 50–90 kg/m2s, temperature difference of 30–90 °C, OC conversion of 0.2–0.35, and oxygen-fuel ratio of 3–6). Subsequently, this paper investigates the influences of main design parameters on the performance metrics, such as gas/solid fuel conversion, operational costs, and operational benefits. It is found that the carbon stripper significantly enhances the carbon capture efficiency of the device, provided that its separation efficiency is maintained above 70–95 %. Sensitivity analysis is employed to study the response patterns of performance metrics to changes in input parameters. Ultimately, based on these analyses, a design scheme for the 5 MWth reactor is determined, with a detailed examination of the pressure balance state of the reactor under the design conditions, and the balanced material and energy flows at the reactor inlets and outlets.
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