首页> 外文会议>International Pittsburgh Coal Conference >EXAMINATION OF THE PERFORMANCE OF A COAL BASED GAS TURBINE FUEL CELL HYBRID POWER GENERATION SYSTEM WITH PRE-COMBUSTION CARBON CAPTURE AND STAGED COMPRESSION AND EXPANSION
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EXAMINATION OF THE PERFORMANCE OF A COAL BASED GAS TURBINE FUEL CELL HYBRID POWER GENERATION SYSTEM WITH PRE-COMBUSTION CARBON CAPTURE AND STAGED COMPRESSION AND EXPANSION

机译:用预燃烧碳捕获和分阶段压缩和膨胀探测煤基燃气轮机燃料电池混合发电系统的性能

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In recent years there has been significant interest in different carbon capturing technologies that might be applied to fossil fuel power generation plants. These technologies are intended to reduce the amount of CO_2 that would normally be emitted into the atmosphere. In terms of system efficiency and operating costs carbon capture technology is expensive. The additional equipment that would be used to capture these emissions often requires an auxiliary heat source and they add to the complexity of the system. There has also been significant interest in coal based gas turbine solid oxide fuel cell hybrid power plants. A gas turbine fuel cell hybrid power plant can have a greater efficiency than a conventional gas turbine power plant because the heat that is normally unused in a standalone fuel cell is recovered in the hybrid system, and used to drive the turbine. It is thought that the increased system efficiency of the hybrid system might compensate for the increased expense of performing carbon capture. In order to provide some analytical insight on how to best use the heat that is generated from a solid oxide fuel cell (SOFC) in a coal fired power system, we examine several different configurations. In each system we assume that a 200 MW SOFC is driven by a coal derived syngas. Each system uses an isolated anode stream and assumes that carbon capture, has been performed upstream of the fuel cell thus providing a hydrogen rich syngas to the SOFC. This differs from hybrid systems which have been previously posed where an isolated anode stream was used as a means to isolate and capture CO_2 after the syngas has passed through the fuel cell and a post combustion process that is fed with pure oxygen producing an exhaust stream of water and CO_2. The configurations in this study are different in that the anode and cathode streams remain isolated so that the expansion leg of the heat engine cycle may be staged. By staging both the compression and expansion processes of the hybrid system we show that there is increased availability of useable heat over single staged systems. Maximizing this availability would give the hybrid system more energy to drive other auxiliary processes that are necessary for coal fired systems. These auxiliary operations could include fuel reforming or shift reactions, pre heating of coal for the gasification system, reheating the syngas after cooling for cleaning, or even heating steam in a bottoming cycle.
机译:近年来,一直在不同的碳捕获技术显著利益可能被应用到化石燃料的发电厂。这些技术旨在减少通常会被排放到大气中的CO_2量。在系统效率方面和运营成本的碳捕获技术是昂贵的。将被用来捕获这些排放的额外的设备通常需要辅助热源和它们增加了系统的复杂性。同时也出现了在煤基燃气涡轮固体氧化物燃料电池混合发电厂显著的兴趣。一种燃气涡轮机的燃料电池混合动力装置可以具有比传统的燃气涡轮机发电设备的更大的效率,因为这是在一个独立的燃料电池通常未使用的热量在混合动力系统被回收,并用于驱动所述涡轮机。据认为,混合动力系统的提高系统的效率可能会补偿进行碳捕获的增加费用。为了提供关于如何最好使用从在煤的固体氧化物燃料电池(SOFC)中产生的热发射功率系统中的一些分析洞察,我们研究几个不同的配置。在每个系统中,我们假设一个200 MW SOFC由煤衍生的合成气驱动。每个系统使用分离的阳极流,并且假定碳捕获,一直的从而所述燃料电池提供富含氢的合成气的SOFC进行上游。这不同于其中分离的阳极流被用作分离和捕获CO_2的装置中的合成气之后先前已经提出的混合系统已经通过被供给用纯氧产生的排气流的燃料电池和后燃过程通过水和CO_2。在这项研究中的所有配置,所述阳极和阴极流保持隔离,使得热力发动机循环的膨胀腿可以上演不同。通过分期两者混合动力系统的压缩和膨胀过程,我们表明,存在增加的可用热量的可用性在单个分级系统。这最大化可用性将使混合动力系统更多的能量来驱动燃煤系统所必需的其他辅助工序。这些辅助操作可以包括燃料重整或转换反应,用于气化系统煤的预加热,冷却的清洁,或者甚至在底循环加热蒸汽后重新加热合成气。

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