Transformation of LPG into Aromatic Hydrocarbons and Hydrogen over Zeolite Catalysts

IF 9.3 2区 化学 Q1 CHEMISTRY, PHYSICAL
G. Giannetto, R. Monque, R. Galiasso
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引用次数: 161

Abstract

Abstract A way to increase the value of LPG cut from petroleum feedstocks is its direct transformation to H2 and aromatic products; these aromatic products, BTX—essentially benzene (B), toluene (T), and C, -aromatics (X)—can be used as raw material for the petrochemical industry or as a blending mixture to enhance the octane number of gasoline. However, these transformations require high temperatures. Thermodynamic data show that the conversion of paraffins into aromatics is favored by increasing the length of the chain, and that aromatics are favored in relation to olefins (Table 1) [1,2]. Whereas aromatization of propane and higher paraffins can be carried out at temperatures lower than 500°C, transformation of ethane, and especially that of methane, requires much higher temperatures. This is experimentally supported by the transformation of various hydrocarbons, at constant temperature and space velocity. For instance, over H-[All-ZSM-5, butane and isobutane react four times faster than propane and 100...
沸石催化剂上液化石油气转化为芳烃和氢的研究
从石油原料中提取的液化石油气直接转化为H2和芳烃产品是提高其生产价值的一种途径;这些芳香族产品,btx -本质上是苯(B),甲苯(T)和C -芳香族(X) -可以用作石油化工的原料或作为调合混合物来提高汽油的辛烷值。然而,这些转变需要高温。热力学数据表明,增加链的长度有利于烷烃转化为芳烃,而芳烃相对于烯烃更有利(表1)[1,2]。丙烷和高级烷烃的芳构化可以在低于500℃的温度下进行,而乙烷的转化,尤其是甲烷的转化,则需要更高的温度。这在实验上得到了各种碳氢化合物在恒定温度和空间速度下的转化的支持。例如,在H-[All-ZSM-5]上,丁烷和异丁烷的反应速度比丙烷快4倍,比丙烷快100倍。
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来源期刊
CiteScore
22.30
自引率
2.80%
发文量
29
期刊介绍: Catalysis Reviews is dedicated to fostering interdisciplinary perspectives in catalytic science and engineering, catering to a global audience of industrial and academic researchers. This journal serves as a bridge between the realms of heterogeneous, homogeneous, and bio-catalysis, providing a crucial and critical evaluation of the current state of catalytic science and engineering. Published topics encompass advances in technology and theory, engineering and chemical aspects of catalytic reactions, reactor design, computer models, analytical tools, and statistical evaluations.
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