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The concept of reactive surface area applied to uncatalyzed and catalyzed carbon (char) gasification in carbon dioxide and oxygen.

机译:反应表面积的概念适用于二氧化碳和氧气中未催化和催化的碳(炭)气化。

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The main objective of this investigation was to explain and/or predict the reactivity variations with conversion (or reactivity profiles) of carbons (chars) gasified in carbon dioxide and oxygen. The virtues of, and/or problems with, utilizing the concepts of total and active surface area to explain the reactivity profiles were evaluated and discussed. An alternative approach, involving the concept of reactive surface area (RSA), was introduced and results based on the direct measurement of RSA were presented. Here, reactive surface area is defined as the concentration of carbon atoms on which the carbon-oxygen C(O) surface intermediate forms and subsequently decomposes to give gaseous products. The transient kinetics (TK) approach gave a direct measurement of RSA for chars gasified in CO{dollar}sb2{dollar} and O{dollar}sb2{dollar}, i.e., gasification rates normalized with respect to RSA were essentially constant over the entire conversion range. A temperature-programmed desorption technique was also used to determine the amount of reactive surface intermediate formed on these chars during gasification in CO{dollar}sb2{dollar} and O{dollar}sb2{dollar}; the results were in good agreement with those obtained by TK. The application of these two independent, but complementary, techniques provided the heretofore elusive quantitative understanding of char reactivity variations with conversion in CO{dollar}sb2{dollar} and O{dollar}sb2{dollar}. A comparison of turnover frequencies for different chars gasified in 1 atm CO{dollar}sb2{dollar} suggested that char gasification may be a structure sensitive reaction.; The concept of RSA was also used to achieve a better quantitative understanding of catalyzed char reactivity variations with conversion in CO{dollar}sb2{dollar}. For a calcium-exchanged lignite char gasified in 1 atm CO{dollar}sb2{dollar}, a poor correlation was found between RSA and reactivity, suggesting that in addition to the direct decomposition of the reactive C(O) intermediate, other processes, e.g., oxygen spillover, contributed to the transient evolution of CO. An extensive study of Saran char loaded with calcium, potassium or nickel by impregnation to incipient wetness (IW) or ion exchange (IE) was undertaken. An excellent correlation was found between reactivity and RSA variations with conversion for both IW and IE K-catalyzed chars, suggesting that TK indeed titrates the reactive K-O-C complexes formed during gasification in CO{dollar}sb2{dollar}.
机译:这项研究的主要目的是解释和/或预测反应性随二氧化碳和氧气中气化的碳(炭)的转化率(或反应性分布)而变化。评估和讨论了利用总表面积和活性表面积来解释反应性特征的优点和/或问题。引入了涉及反应性表面积(RSA)概念的替代方法,并提出了基于RSA直接测量的结果。在此,反应表面积定义为碳氧C(O)表面中间体形成并随后分解以生成气态产物的碳原子浓度。瞬态动力学(TK)方法直接测量了CO {dollar} sb2 {dollar}和O {dollar} sb2 {dollar}中气化的焦炭的RSA,即,相对于RSA标准化的气化速率在整个过程中基本上是恒定的转换范围。还使用了程序升温脱附技术来确定在CO {dollar} sb2 {dollar}和O {dollar} sb2 {dollar}气化过程中在这些炭上形成的反应性表面中间体的数量。结果与TK获得的结果非常吻合。这两种独立但互补的技术的应用提供了迄今为止对于焦炭反应性变化与CO {dollar} sb2 {dollar}和O {dollar} sb2 {dollar}中转化的难以理解的定量理解。对在1个大气压CO {dollar} sb2 {dollar}中气化的不同炭的转换频率进行比较,表明炭气化可能是结构敏感的反应。 RSA的概念还用于更好地定量理解CO {dollar} sb2 {dollar}中转化时催化的炭反应性变化。对于在1个大气压CO {dols} sb2 {dollar}中气化的钙交换褐煤炭,发现RSA与反应性之间的相关性较弱,这表明除了活性C(O)中间体的直接分解外,其他过程还包括例如,氧气的溢出,导致了CO的瞬时释放。通过对初湿(IW)或离子交换(IE)的浸渍,对撒兰炭中的钙,钾或镍进行了广泛的研究。发现IW和IE K催化的焦炭的反应性和RSA变异与转化率之间有极好的相关性,这表明TK确实滴定了在CO {dollar} sb2 {dollar}的气化过程中形成的反应性K-O-C络合物。

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