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    有机朗肯循环耦合二氧化碳捕集系统效果分析

    Effect analysis of carbon dioxide capture system with integrated organic Rankine cycle

    • 摘要: 摘要:通过化学吸收法捕集二氧化碳能够有效降低燃煤电厂的CO2排放量,但碳捕集系统在CO2解吸过程中需消耗大量蒸汽,这导致电厂发电效率降低。为了减少碳捕集对电厂发电效率的影响,提出一种集成有机朗肯循环的碳捕集系统。在Aspen plus中建立每年百万吨CO2捕集工艺系统,利用有机朗肯循环回收解吸塔排气和再沸器凝结水余热。选取RC318、R152a、R600a、R600、R245fa共5种有机工质,对有机朗肯循环系统的净发电功率与吸热量、热效率与?效率以及集成系统的冷却水循环量进行模拟分析。结果表明,集成系统中有机工质的蒸发压力和流量均与净发电功率成正比,但二者存在相互制约的关系;5种工质中,R152a的效果最佳。其在蒸发压力为3MPa,流量为188kg/s时净发电功率可达7.3899MW,带来的冷却水循环量增幅仅为3.36%,其能够将发电厂损失降低18.66%。 关键词:CO2捕集;过程系统;模拟;有机朗肯循环;

       

      Abstract: Carbon dioxide capture by chemical absorption can effectively reduce the CO2 emissions of coal-fired power plants, but the carbon capture system consumes a lot of steam in the process of CO2 desorption, which reduces the power generation efficiency of the power plant. In order to reduce the impact of carbon capture on power generation efficiency, a carbon capture system with organic Rankine cycle is proposed. A carbon capture process system capturing 1 million tons of CO2 per year was established in Aspen plus, and organic Rankine cycle was used to recover the residual heat of desorption tower exhaust and reboiler condensate. Five organic working materials, RC318, R152a, R600a, R600 and R245fa, were selected to analyze the net power generation and heat absorption, thermal efficiency and exergy efficiency of the organic Rankine cycling system, and the cooling water circulation volume of the integrated system. The results show that the evaporation pressure and flow rate of organic working medium in the integrated system are proportional to the net generating power, but there is a phenomenon where these two factors limit each other. When the evaporation pressure is 3MPa and the flow rate is 188kg/s, the working medium R152a is the maximum net power, up to 7.3899MW, and the increase of cooling water circulation is the smallest, only 3.36%, which can reduce the loss of the power plant by 18.66%.

       

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