按来源划分的电力成本
投资回收期
发电站
电
发电
天然气
联合循环
废物管理
碳捕获和储存(时间表)
环境科学
工厂效率
化学链燃烧
工艺工程
经济分析
整体气化联合循环
燃烧
工程类
功率(物理)
生产(经济)
化学
机械工程
经济
燃气轮机
电气工程
气候变化
宏观经济学
物理
有机化学
生物
量子力学
农业经济学
生态学
流化床
作者
Oghare Victor Ogidiama,Mohammad R.M. Abu‐Zahra,Tariq Shamim
出处
期刊:Journal of Energy Resources Technology-transactions of The Asme
[ASME International]
日期:2018-06-12
卷期号:140 (11)
被引量:18
摘要
High energy penalty and cost are major obstacles in the widespread use of CO2 capture techniques for reducing CO2 emissions. Chemical looping combustion (CLC) is an innovative means of achieving CO2 capture with less cost and low energy penalty. This paper conducts a detailed techno-economic analysis of a natural gas-fired CLC-based power plant. The power plant capacity is 1000 MWth gross power on a lower heating value basis. The analysis was done using Aspen Plus. The cost analysis was done by considering the plant location to be in the United Arab Emirates. The plant performance was analyzed by using the cost of equipment, cost of electricity, payback period, and the cost of capture. The performance of the CLC system was also compared with a conventional natural gas combined cycle plant of the same capacity integrated with post combustion CO2 capture technology. The analysis shows that the CLC system had a plant efficiency of 55.6%, electricity cost of 5.5 cents/kWh, payback time of 3.77 years, and the CO2 capture cost of $27.5/ton. In comparison, a similar natural gas combined cycle (NGCC) power plant with CO2 capture had an efficiency of 50.6%, cost of electricity of 6.1 cents/kWh, payback period of 4.57 years, and the capture cost of $42.9/ton. This analysis shows the economic advantage of the CLC integrated power plants.
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