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首页> 外文期刊>Mitigation and Adaptation Strategies for Global Change >Increasing the efficiency of chemical looping combustion of biomass by a dual-stage fuel reactor design to reduce carbon capture costs
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Increasing the efficiency of chemical looping combustion of biomass by a dual-stage fuel reactor design to reduce carbon capture costs

机译:通过双级燃料反应器设计提高生物质化学环燃烧的效率,以减少碳捕获成本

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This paper analyzes the capabilities of a pilot-scale chemical looping combustion plant firing wood biomass in two stages to efficiently achieve negative carbon dioxide emissions. The utilized in situ gasification-chemical looping combustion (iG-CLC) process isolates the oxygen supply via air from the fuel conversion itself with the help of two separate fluidized bed reactors and an oxygen carrier to supply the necessary oxygen for the combustion. As a result, a relatively pure stream of carbon dioxide and steam is generated. Thus, the process makes capturing carbon emissions more feasible since it eliminates the need for the cost- and energy-intensive separation of the produced gases. A major issue when using biomass in a chemical looping plant is the high amount of the volatiles exiting unconverted. This problem was mitigated by using a two-stage fuel reactor system. Two bubbling fluidized beds were arranged one upon the other. The lower stage, where the fuel is introduced, is used to release the volatiles and partly convert them. The remaining volatiles rise up into the second stage and are further converted to a high degree. A series of experiments were carried out with a 25-kW(th)pilot plant located at the Hamburg University of Technology. Gas concentrations were continuously measured after both stages of the fuel reactor to see the gradual conversion of the fuel gases. Additionally, carbon slip at the exhaust was measured to show the effectiveness. The experiments with the reactor concept showed promising results since already at a reactor temperature of 850 degrees C, the total oxygen demand needed to oxidize the combustible component in the exhaust gas was well below 2%. The carbon dioxide (CO2) capture efficiency when using German hardwood slightly decreased to 93-96% compared to 97% for German lignite. In the future, the reactor design must prove that it scales and that the efficiency can be further increased. Nevertheless, firing biomass with a two-stage iG-CLC process might allow a cost-efficient negative carbon dioxide emission while generating heat with relatively high efficiency. Therefore, it might be a sustainable alternative to generate heat in the future.
机译:本文分析了两种阶段试验规模化学循环燃烧厂烧制木材生物质的能力,以有效地达到负二氧化碳排放。利用原位气化 - 化学循环燃烧(IG-CLC)工艺通过两个单独的流化床反应器和氧载体的帮助,通过空气从燃料转换本身和氧载体中的氧气供应将氧气供给。结果,产生相对纯度的二氧化碳和蒸汽流。因此,该过程使捕获碳排放更加可行,因为它消除了所生产的气体的成本和能量密集分离的需要。在化学循环厂使用生物质时的主要问题是退出未转化的高量挥发物。使用两级燃料电抗器系统减轻了这个问题。将两个鼓泡流化床放在另一个上。介绍燃料的下级用于释放挥发物并部分转换它们。剩余的挥发物上升到第二阶段,并进一步转化为高度。通过位于汉堡理工大学的25千瓦(TH)先导工厂进行了一系列实验。在燃料反应器的两个阶段连续测量气体浓度,以看到燃料气体的逐渐转换。另外,测量排气时的碳滑动以显示有效性。与反应器概念的实验显示出有希望的结果,因为已经在850℃的反应器温度下,氧化废气中可燃组分所需的总需氧量远低于2%。二氧化碳(CO2)捕获效率时,使用德国硬木略微下降至93-96%,而德国褐煤为97%。将来,反应器设计必须证明它缩放,并且可以进一步提高效率。然而,具有两级IG-CLC工艺的烧制生物质可能允许成本有效的负二氧化碳排放,同时产生具有相对高效率的热量。因此,它可能是在未来产生热量的可持续替代品。

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