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Dynamic analysis of the absorption/desorption loop of a carbon capture plant using an object-oriented approach

机译:使用面向对象的方法动态分析碳捕集装置的吸收/解吸回路

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Post-combustion capture of CO2 is regarded as a possible technology in order to reduce CO2 emission to the atmosphere. This paper provides a dynamic analysis of the absorption/desorption loop of a carbon capture plant with the help of a simulation model, built using the object-oriented Modelica Library Thermal Separation. The solvent used is an amino-acid salt. The dynamic behaviour is investigated for a reduction in regeneration heat flow rate but constant flue gas flow rate. Hereby four different control strategies are compared, one keeping the lean solvent loading constant, one keeping the solvent flow rate constant, one where flue gas bypasses the capture plant and a last one where an additional solvent tank is introduced. The simulation shows i.e. that for a constant lean solvent loading the response of the absorbed CO2 flow rate is much faster than for a constant solvent flow rate. Also the effect on the dynamic behaviour is investigated, comparing the whole cycle model to a standalone desorber model and to a stand-alone absorber model respectively. It was found that the dynamic responses on a short time scale are very similiar, but different on a long time scale.
机译:燃烧后捕获二氧化碳被认为是减少二氧化碳向大气排放的一种可行技术。本文借助使用面向对象的Modelica库热分离建立的仿真模型,对碳捕集装置的吸收/解吸回路进行了动态分析。使用的溶剂是氨基酸盐。研究了动态行为,以减少再生热流量,但烟道气流量恒定。因此,对四种不同的控制策略进行了比较,一种保持贫溶剂负载恒定,一种保持溶剂流速恒定,一种在烟气绕过捕集装置的情况下进行,另一种在引入额外的溶剂箱的情况下进行。该模拟表明,即,对于恒定的稀溶剂负载,吸收的CO 2流量的响应比恒定的溶剂流量快得多。还研究了对动力学行为的影响,将整个循环模型分别与独立的解吸器模型和独立的吸收器模型进行了比较。发现在短时间尺度上的动态响应非常相似,但是在长时间尺度上是不同的。

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