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Development of a hybrid catalytic combustor for a 1300℃ class gas turbine

机译:1300℃级燃气轮机混合催化燃烧室的研制

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摘要

The hybrid catalytic combustor concept proposed by the authors has an advantage concerned with catalyst durability, because the catalyst is maintained below 1000℃ even for application to 1300℃ class gas turbines. A full-scale hybrid catalytic combustor has been designed for a 200 MW (1300℃) class gas turbine. The catalyst bed was 450 mm in diameter and consisted of a Pd/ alumina washcoat on a cordierite monolith. In experiments, the combustor has demonstrated the capability of meeting the NO_x emission level of SCR (selected catalytic reduction) during atmospheric pressure testing. To predict the catalyst performance at an elevated pressure, the characteristics of the catalyst were studied using a small scale reactor test, and a material property test using a DTA/TGA-Q.MASS system. The catalyst showed a higher activity in the oxidized state (PdO) than in the metallic state (Pd). This activity difference was governed by the equilibrium of the oxygen release from PdO in bulk. It was considered that oxidation rate of the metallic Pd in bulk was not so high and this caused self-oscillation for the Pd catalyst around the temperature of the oxygen release equilibrium. Even below the temperature of the oxygen release equilibrium, both surface and bulk (lattice) oxygen of the PdO was consumed by the methane oxidation reaction, and resulted in a lack of surface oxygen on the catalyst. This caused a reversible decrease in the catalyst activity during combustion testing, and indicated that the oxygen dissociation step was a rate limiting step in the catalytic combustion.
机译:作者提出的混合催化燃烧器概念具有与催化剂耐用性有关的优点,因为即使将其应用于1300℃级的燃气轮机,催化剂也可保持在1000℃以下。已为200兆瓦(1300℃)级燃气轮机设计了全尺寸混合催化燃烧器。催化剂床的直径为450mm,由堇青石整料上的Pd /氧化铝修补基面涂层组成。在实验中,燃烧室已证明能够在大气压测试期间满足SCR的NO_x排放水平(选定的催化还原)。为了预测在高压下的催化剂性能,使用小规模反应器测试和DTA / TGA-Q.MASS系统的材料性能测试研究了催化剂的特性。催化剂在氧化态(PdO)的活性高于在金属态(Pd)的活性。此活性差异受散装PdO中的氧气释放平衡的支配。可以认为,金属Pd的整体氧化速率不是很高,这导致Pd催化剂在氧释放平衡温度附近发生自激振荡。即使低于氧气释放平衡的温度,PdO的表面和体(晶格)氧都被甲烷氧化反应消耗,导致催化剂上缺乏表面氧。这导致燃烧测试过程中催化剂活性的可逆降低,并且表明氧离解步骤是催化燃烧中的速率限制步骤。

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