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A comparative thermodynamic, economic and risk analysis concerning implementation of oxy-combustion power plants integrated with cryogenic and hybrid air separation units

机译:关于与低温和混合空气分离装置集成的氧气燃烧电厂实施的热力学,经济和风险比较分析

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This paper presents a comparison of two types of oxy-combustion power plant that differ from each other in terms of the method of oxygen separation. For the purpose of the analysis, detailed thermodynamic models of oxy-fuel power plants with gross power of approximately 460 MW were built. In the first variant (Case 1), the plant is integrated with a cryogenic air separation unit (ASU). In the second variant (Case 2), the plant is integrated with a hybrid membrane-cryogenic installation. The models were built and optimized using the GateCycle, Aspen Plus and Aspen Custom Modeller software packages and with the use of our own computational codes. The results of the thermodynamic evaluation of the systems, which primarily uses indicators such as the auxiliary power and efficiencies of the whole system and of the individual components that constitute the unit, are presented. Better plant performance is observed for Case 2, which has a net efficiency of electricity generation that is 1.1 percentage points greater than that of Case 1. For the selected structure of the system, an economic analysis of the solutions was made. This analysis accounts for different scenarios of the functioning of the Emission Trading Scheme and includes detailed estimates of the investment costs in both cases. As an indicator of profitability, the break-even price of electricity was used primarily. The results of the analysis for the assumptions made are presented in this paper. A system with a hybrid air separation unit has slightly better economic performance. The break-even price of electricity in this case is approximately 3.4 €/MW h less than for the system with a cryogenic unit. The main risk factors concerning implementation of such technologies were identified. The analysis of risk connected with the selection of these technologies was performed with the use of two methods - sensitivity analysis and a Monte Carlo method. The values of the probability were calculated, and the main results are presented and discussed in the paper.
机译:本文对两种类型的氧气燃烧发电厂进行了比较,它们在氧气分离方法方面互不相同。为了进行分析,建立了总功率约为460 MW的富氧电厂的详细热力学模型。在第一种方案(案例1)中,工厂与低温空气分离装置(ASU)集成在一起。在第二种方案(案例2)中,该工厂与混合膜低温装置集成在一起。使用GateCycle,Aspen Plus和Aspen Custom Modeller软件包并使用我们自己的计算代码来构建和优化模型。给出了系统热力学评估的结果,该结果主要使用诸如辅助功率和整个系统以及构成该单元的各个组件的效率之类的指标。对于案例2,观察到更好的工厂性能,其发电的净效率比案例1高1.1个百分点。对于系统的选定结构,对解决方案进行了经济分析。该分析说明了排放交易计划运作的不同情况,并包括了两种情况下投资成本的详细估算。作为获利能力的指标,主要使用电力的收支平衡价格。提出的假设的分析结果在本文中给出。带有混合空气分离单元的系统具有更好的经济性能。在这种情况下,电力的收支平衡价格比带有低温装置的系统低约3.4欧元/兆瓦时。确定了与实施此类技术有关的主要风险因素。与这些技术的选择有关的风险分析是使用两种方法进行的:敏感性分析和蒙特卡洛方法。计算概率值,并在本文中介绍和讨论主要结果。

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