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Catalytic decomposition of ammonia in simulated coal-derived gas over supported nickel catalysts

机译:负载型镍催化剂上模拟煤衍生气中氨的催化分解

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As a hot gas clean-up technology for integrated coal gasification combined-cycle (IGCC) power plants, the catalytic decomposition of ammonia using simulated coal-derived gas was studied. Based on the selective catalytic oxidation of ammonia to nitrogen and water, the characteristics of five kinds of supported nickel catalysts were investigated. Ammonia decomposition experiments were carried out at 0.9 MPa, and the surface properties of the catalysts were investigated through surface area measurement, the temperature programmed desorption of ammonia (NH3-TPD), carbon analysis, XRD analysis, and transmission electron microscope (TEM) observation. The results showed that a nickel catalyst supported on ZSM-5 zeolite has the highest activity and selectivity for ammonia decomposition to nitrogen without carbon deposition from 250-400 °C among the tested catalysts.
机译:作为整体煤气化联合循环(IGCC)电厂的热气净化技术,研究了模拟煤衍生气对氨的催化分解。基于氨气选择性催化氧化为氮和水,研究了五种负载型镍催化剂的特性。在0.9 MPa下进行氨分解实验,并通过表面积测量,氨的程序升温脱附(NH3-TPD),碳分析,XRD分析和透射电子显微镜(TEM)观察催化剂的表面性质。 。结果表明,在250-400°C的测试催化剂中,负载在ZSM-5沸石上的镍催化剂具有最高的活性和氨分解成氮的选择性,而无碳沉积。

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