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In situ analysis of zirconia based catalysts during n-butane isomerization.

机译:正丁烷异构化过程中基于氧化锆的催化剂的原位分析。

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The objective of this project was to further our understanding of the phenomena occurring on the surface of sulfated zirconia (SZ) and tungstated zirconia (WZ), thus allowing us to clarify the nature of the active sites involved in acid catalyzed reactions. n-Butane isomerization was used as a probe reaction to clarify the complexity of those sites.; In the first part of the thesis, butene, an intermediate in the reaction, was added during reaction at 150°C and at 250°C to better understand the reaction pathway. Added olefin contributed to catalyst deactivation without eliminating the reaction induction period, both at 150°C and 250°C. However, at 150°C, it increased the activity of SZ before 30 min time-on-stream (TOS). Isotopic transient kinetic-analysis at 5 min TOS showed that added olefin increased the concentration of surface intermediates, N iso-C4, both at 150°C and 250°C. However, it decreased the activity of the sites at 250°C. Butene added for 2 min at the beginning of reaction increased the activity of the catalyst during 250 min TOS. The added 1-butene contributed to the formation of isobutane for multiple times before its elimination, suggesting that it may have been involved in the formation of additional active sites.; In the second part of the thesis, the nature of the active acid sites was investigated. Pretreatment of SZ at 500°C improved the activity of SZ due to an increase in the concentration of surface intermediates, Niso-C4. CO (known to adsorb on Lewis acid sites) suppressed isobutane formation.; Butene, added along with CO, for 2 min, had a promoting impact on the activity of SZ once CO and butene feed were terminated. The results support the hypothesis that the “active centers” for reaction are probably Brønsted acid sites neighboring Lewis acid sites.; The final part of the thesis focused on n-butane isomerization on WZ in the temperature range 280°C–360°C. Butene addition increased dramatically the activity of WZ and shortened its reaction induction period. H2 pretreatment decreased the concentration of active sites thus, the activity of WZ. Our results indicate that formation of butene is a limiting step in the reaction on WZ.
机译:该项目的目的是进一步了解硫酸化氧化锆(SZ)和钨酸化氧化锆(WZ)表面上发生的现象,从而使我们能够阐明参与酸催化反应的活性位点的性质。正丁烷异构化被用作探针反应以阐明那些位点的复杂性。在论文的第一部分中,在反应过程中于150°C和250°C添加了丁烯(一种反应中间体),以更好地理解反应途径。在150℃和250℃下,添加的烯烃有助于催化剂失活而不消除反应诱导期。但是,在150°C下,它在30分钟的运行时间(TOS)之前增加了SZ的活性。 TOS 5分钟的同位素瞬态动力学分析表明,在150°C和250°C的温度下,添加的烯烃均会增加表面中间体 N iso-C4 的浓度。但是,它降低了250°C下位点的活性。在反应开始时添加2分钟的丁烯在250分钟的TOS期间增加了催化剂的活性。所添加的1-丁烯在异丁烷被消除之前多次促成异丁烷的形成,表明它可能已经参与了其他活性位点的形成。在论文的第二部分,研究了活性酸位的性质。由于表面中间体 N iso-C4 浓度的增加,在500°C预处理SZ可以提高SZ的活性。 CO(已知吸附在路易斯酸位上)可抑制异丁烷的形成。一旦终止CO和丁烯进料,将丁烯与CO一起添加2分钟,对SZ的活性有促进作用。该结果支持以下假设:反应的“活性中心”可能是邻近路易斯酸位的布朗斯台德酸位。论文的最后部分集中在WZ在280°C–360°C的温度范围内进行正丁烷异构化。丁烯的添加显着提高了WZ的活性并缩短了其反应诱导期。 H 2 预处理降低了活性位点的浓度,从而降低了WZ的活性。我们的结果表明,丁烯的形成是WZ反应中的限制步骤。

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