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Development Status of a Coal Powered Oxy-fired Pressurized Fluidized Bed Combustor with CO_2 Capture and Purification

机译:具有CO_2捕获和纯化的煤动力氧的加工流化床燃烧器的开发现状

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Oxy-fired Pressurized Fluidized Bed Combustor (Oxy-PFBC) technology is under development as a method to enable the use of coal for electricity generation while capturing the CO_2 and other emissions at a cost that is significantly less than the current commercially deployed post-combustion capture technologies. This paper discusses the features of the Oxy-PFBC, commissioning test results for the 1 MW_(th) pilot scale system, techno-economic analysis results, and development and commercialization plans. The plant was successfully commissioned in April, 2017, demonstrating coal ignition and burning, and is now ready for performance testing. The Oxy-PFBC is a 1 MW_(th) pilot scale system installed at the Natural Resources Canada facilities in Ottawa, and includes a CO_2 Purification Unit (CPU) from Linde. The combustor utilizes elevated pressure and a heat exchanger in the fluidized bed to reduce the combustor size and cost, while oxy-combustion enables lower cost CO_2 separation by producing an exhaust stream that is primarily CO_2 and water vapor. The CPU operates at elevated pressure and utilizes a direct contact cooler for HCl and water vapor removal, followed by a Linde LiCONOX unit to remove SO_x and NO_x, and a De-Oxo Reactor to remove excess oxygen. The carbon capture penalty (increase in cost of electricity) for current CO_2 capture technology is approximately 70%. Current predictions indicate the Oxy-PFBC can reduce the carbon capture penalty by more than half, to 30%, and capture up to 98% of CO_2 emissions. These results assume no economic benefit of the captured CO_2. The system could achieve no net increase in electricity cost through the sale of CO_2 at $30/ton. The current development plans include completion of the initial phase of pilot scale testing by mid-2017, followed by technology upgrades to the pilot plant and testing of these upgrades by the end of 2017. Preliminary planning for a 30 MW_(th) large pilot plant is underway with potential program start in 2018 and operation by 2021.
机译:富氧燃烧加压流化床燃烧(氧PFBC)技术正在开发的,使发电煤炭的使用方法,同时捕捉CO_2和其他排放量是显著小于当前商业部署燃烧后成本捕获技术。本文讨论了富氧PFBC的功能,调试为1个MW_(TH)试系统,技术经济分析结果,开发和商业化计划的测试结果。该工厂成功投产,2017年4月,表明煤炭点火和燃烧,并正准备进行性能测试。氧 - PFBC是安装在渥太华的加拿大自然资源设施1个MW_(TH)试规模系统,并且包括从一个林德CO_2纯化单元(CPU)。燃烧器利用了升高的压力和在流化床中的热交换器,以减少燃烧器的尺寸和成本,同时氧燃烧使成本更低CO_2分离通过产生的废气流也就是主要CO_2和水蒸汽。所述CPU在升高的压力下操作,并且利用直接接触冷却器为HCl和水蒸汽去除,接着是林德LiCONOX单元以除去SO_x和NO_x的,和去羰化反应器以除去过量的氧。碳捕获罚款(增加电力成本)当前CO_2捕捉技术大约是70%。当前预测表明氧 - PFBC可以通过进一步降低碳捕集惩罚超过一半,至30%,并捕获到CO_2排放的98%。这些结果假定捕获CO_2的没有经济效益。该系统可以实现在30 $ /吨通过出售CO_2没有净增加电力成本。目前的发展计划包括由中期2017年试点规模测试的初始阶段完成,其次是技术升级该中试装置,并通过2017年的初步规划结束的30 MW_(次)大型中试装置,这些升级测试正在进行与2018年潜在的程序启动和运作到2021年。

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