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Development of a Carbon Stripper Particle Separation System for Chemical Looping Applications

机译:用于化学循环应用的碳汽提塔颗粒分离系统的开发

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The development of chemical looping combustion technology for electrical power generation is of great interest due to its ability to generate highly concentrated CO_2 exhaust gas streams that more easily facilitate carbon capture and sequestration efforts. A significant amount of research has been devoted towards the study of chemical looping of coal due to the abundance and relatively cheap cost of coal as a fuel source. In its most simplistic form, chemical looping involves the cycling of a metal oxide (hence forth referred to as an oxygen carrier) between to fluidized bed reactors. In one reactor, the oxygen carrier is mixed with the fuel coal under conditions that lead to the reduction of the oxygen carrier. The oxygen released by the carrier then reacts with the coal. This is commonly known as the fuel reactor. Upon exiting the fuel reactor, the oxygen carrier is then separated from any remaining unburnt carbon and introduced into the second reactor, known as the air reactor. In this reactor, the carrier compound is oxidized, thus regaining the oxygen lost in the fuel reactor. This cycle of passing the oxygen carrier between the two reactors is repeated, thus the reason behind the name "chemical looping". In this process, it is critical that only the reduced oxygen carrying metal oxide is passed into the air reactor. If any unburnt carbon (aka coal) is introduced into the air reactor, combustion is likely to occur. Among other adverse consequences, this results in the inability to efficiently capture the CO_2 produced. Because of this, it is absolutely critical that an efficient means of separating the oxygen carrier compound from coal char, or unburnt carbon be developed. In fact, a recent report from the U.S. Department of Energy on chemical looping combustion determined that the lack of an effective means of separating char from the oxygen carrier would prevent implementation of this technology. To address this issue, researchers at National Energy Technology Laboratory (NETL) have proposed a novel carbon stripper unit for use with chemical looping combustion systems. The proposed unit is a conical spouted bed that combines an annular opening between the top of the cone-shaped spout inlet and the inner wall of the bed (See figure 1), and the use of a sweep gas to restrict the flow of particles through this opening. A mixture of granular oxygen carrier and coal particles are introduced into the bed above the spout cone via a feed screw. The spouting gas is injected from the bottom of the spout cone, forming a vertical jet along the longitudinal axis of the bed riser and inducing an eddy-like recirculating motion within the bed of oxygen carrier and coal particles (see figure 2).
机译:化学循环燃烧技术在发电方面的发展备受关注,因为它具有产生高浓度CO_2废气流的能力,可以更轻松地促进碳捕获和封存工作。由于煤作为燃料源的丰富和相对便宜的成本,大量的研究致力于煤的化学循环研究。在最简单的形式中,化学循环包括金属氧化物(以下称为氧气载体)在流化床反应器之间循环。在一个反应​​器中,在导致氧载体还原的条件下,将氧载体与燃料煤混合。载体释放的氧气然后与煤反应。这通常称为燃料反应堆。在离开燃料反应器后,然后将氧气载体与任何剩余的未燃烧碳分离并引入第二反应器,称为空气反应器。在该反应堆中,载体化合物被氧化,从而重新获得了在燃料反应堆中损失的氧气。重复进行使氧载体在两个反应器之间通过的循环,因此是“化学循环”这一名称背后的原因。在这个过程中,至关重要的是只有还原的携带氧的金属氧化物进入空气反应器。如果将任何未燃烧的碳(又名煤)引入空气反应堆,则很可能发生燃烧。除其他不利后果外,这导致无法有效捕获所产生的CO_2。因此,开发一种有效的方法将氧载体化合物与煤焦或未燃烧的碳分离是至关重要的。实际上,美国能源部最近关于化学循环燃烧的报告确定,缺乏将焦炭与氧气载体分离的有效手段将阻止该技术的实施。为了解决这个问题,美国国家能源技术实验室(NETL)的研究人员提出了一种用于化学循环燃烧系统的新型碳汽提塔装置。拟议中的装置是一个锥形喷头床,它在锥形喷头入口的顶部和床的内壁之间具有一个环形开口(见图1),并使用吹扫气体来限制通过的气流。这个开口。粒状氧气载体和煤颗粒的混合物通过进料螺杆引入到喷口锥上方的床中。喷出的气体从喷出锥的底部注入,沿床立管的纵向轴线形成垂直射流,并在床中引起氧气载体和煤颗粒的涡流状循环运动(见图2)。

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