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Development of fluidized bed combustion—An overview of trends, performance and cost

机译:流化床燃烧的发展-趋势,性能和成本概述

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The goal of this article is to chart and analyse the development and economical performance of fluidized bed combustion (FBC) and its derivates circulating fluidized bed (CFB) and bubbling fluidized bed (BFB). A descriptive overview is given of the technology and the market penetration is discussed. To make further analysis possible a database is constructed. This database comprises technological and economical data on 491 FBC projects. Analysis of these projects shows that the technology variants (CFB and BFB) diffused differently over time. Drivers, which influenced the market diffusion and technological development are market regulation, environmental legislation and RD&D programs. Important drivers for FBC technology are fuel availability, required applications in the market, innovation spill over and competing technologies. In this article technical characteristics are charted, which show improvements in fuel diversification, technical availability, efficiency and emissions. In terms of economical performance the results show a decline in specific investment cost. Finally, the effect of technological learning and experience on the economical performance of FBC technology is analysed using the experience curve method and theory on economies of scale. A problem with applying the experience curve method is that it is not used often for large power plants like FBC plants and with it lacking a methodological standard. A method is therefore suggested. The analyses yielded progress ratios (PR) from 0.42 to 0.93 for different groups of projects (new plant, repower, retrofit, add-on and conversion) and different parts of the capital breakdown (total project price, engineering, procurement and construction price and boiler price). This means that the specific investment prices (in $/kWe) decline with, respectively, 58% and 7% with every doubling of cumulative installed capacity (in MWe). The progress ratio found for new FBC plants lies between 0.90 and 0.93. These values correspond with the average PR of 0.90 found for power plants in the literature. Further results show that economies of scale have a significant influence on the investment price. Scale factors are found in the range of 0.62-0.81 for different groups of projects. According to these scale factors specific investment price decreases, respectively, between 25% and 12% with every doubling of plant capacity (in MWe).
机译:本文的目的是对流化床燃烧(FBC)及其衍生产品循环流化床(CFB)和鼓泡流化床(BFB)的发展和经济性能进行图表分析。对该技术进行了描述性概述,并讨论了市场渗透率。为了使进一步分析成为可能,构建了一个数据库。该数据库包含有关491个FBC项目的技术和经济数据。对这些项目的分析表明,随着时间的推移,技术变体(CFB和BFB)的传播方式有所不同。影响市场扩散和技术发展的驱动力是市场监管,环境立法和研发计划。 FBC技术的重要驱动因素是燃料的可用性,市场所需的应用,创新的溢出和竞争技术。本文列出了技术特征,显示了燃料多样化,技术可用性,效率和排放方面的改进。就经济表现而言,结果表明特定投资成本有所下降。最后,使用经验曲线法和规模经济理论,分析了技术学习和经验对FBC技术经济性能的影响。应用经验曲线法的一个问题是,它不经常用于大型电厂,如FBC电厂,并且缺乏方法论标准。因此建议一种方法。通过分析得出不同项目组(新工厂,改建,翻新,附加和转换)的进度比(PR)从0.42到0.93,以及资本细分的不同部分(项目总价格,工程,采购和建筑价格以及锅炉价格)。这意味着,随着累计装机容量(以MWe为单位)每增加一倍,特定投资价格(以$ / kWe为单位)分别下降58%和7%。发现新的FBC工厂的进度比在0.90和0.93之间。这些值对应于文献中发电厂的平均PR为0.90。进一步的结果表明,规模经济对投资价格有重大影响。对于不同的项目组,比例因子在0.62-0.81的范围内。根据这些规模因素,工厂产能每增加一倍(MWe),特定的投资价格就会分别下降25%至12%。

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