微波催化裂化液体直链烷烃选择性生成直链烯烃

V. A. Bolotov, S. Tikhov, K. Valeev, V. T. Shamirzaev, V. Parmon
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引用次数: 0

摘要

具有四个或四个以上碳原子的线性偶碳数α -烯烃(LAO)是化学工业中需求量很大的重要化合物,是多种高附加值化学品的前体[1]。LAO被用作生产聚乙烯、生产醇(主要用于洗涤剂和增塑剂)和合成聚α烯烃(用于合成润滑剂)的共聚单体。α -烯烃(C4, C6, C8和C10)主要用于生产聚氯乙烯增塑剂,高密度和线性低密度聚乙烯,以增强抗应力-开裂性。C10-C14 α -烯烃可用来合成直线型烷基苯磺酸盐(合成洗涤剂)。生产-烯烃的常规方法是乙烯的低聚反应。该工艺可生产高质量的α -烯烃,但成本很高。如果不发生低聚反应,蜡质石蜡可通过热裂解产生LAO,但产物不纯,内部含有大量烯烃、二烯烃和石蜡杂质。该工艺在相对较低的裂解温度下在气相中进行,需要快速淬火以防止异构化或环化等副反应。在我们之前的工作[2]中,我们证明了在选择性MW加热催化剂下,正构烷烃的催化裂化可以大大提高对α -烯烃的选择性。本文介绍了正构烷烃微波裂解的一般规律。研究了多孔陶瓷基Al2O3/Al复合材料(陶瓷金属)和具有高介电损耗的各种碳材料(CM)作为催化剂的载体。用n-C16H34和n-C28H58进行了MW裂解。研究了金属陶瓷的粒径和表面形貌对产物结构和基团组成的影响。结果表明,在旧支架选择性MW加热下,LAO (C2-C23)和正构烷烃(C2-C26)是主要裂解产物。产物的定量分析表明,在MW催化裂化过程中液相过程对α -烯烃的选择性高于对流热裂化过程。CM表面的二氧化硅改性抑制了火花放电(通常在CM的MW加热时观察到);因此,CM表面C-C键的热裂解对自由基的形成贡献最大,而不是在等离子体放电中。结果表明,金属陶瓷在E场节点的MW加热下对α -烯烃的选择性可达85%以上,在H场节点的选择性明显降低。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
SELECTIVE FORMATION OF LINEAR ALPHA-OLEFINS VIA MICROWAVE CATALYTIC CRACKING OF LIQUID STRAIGHT-CHAIN ALKANES
Linear even-carbon-number alpha-olefins (LAO) with four or more carbon atoms are important compounds of high demand in chemical industry as precursors of a wide range of value-added chemicals [1]. LAO are used as co-monomers for polyethylene production, for the production of alcohols (mainly in detergents and plasticizers) and for synthesis of polyalphaolefins (used in synthetic lubricants). Alpha-olefins (C4, C6, C8 and C10) are mainly used to produce poly(vinyl chloride) plasticizers, high-density and linear low-density polyethylene to impart the stress-crack resistance. C10–C14 alpha-olefins can be used to synthesize linear alkylbenzene sulfonates (synthetic detergents). A conventional route to produce alpha-olefins is oligomerization of ethylene. The process provides production of high quality alpha-olefins but is very costly. If not oligomerization, LAO can be produced by thermal cracking of waxy paraffins but the product is not pure and contains numerous internal olefins, dienes and paraffin impurities. The process is conducted in the vapor phase at relatively low cracking temperatures and needs rapid quenching to prevent side reactions such as isomerization or cyclization. In our previous work [2], we showed that the selectivity to alpha-olefins can be increased considerably via catalytic cracking of n-alkanes under selective MW heating of catalysts. In the present work, the general regularities of MW cracking of n-alkanes are presented. Porous ceramic matrix Al2O3/Al composites (ceramometals) and various carbon materials (CM) having high dielectric losses were studied as supports of the catalysts. MW cracking was conducted with n-C16H34 and n-C28H58. The influence particle size and surface morphology of ceramometals and CM on the structural and group composition of the products was studied. It was established that LAO (C2-C23) and n-alkanes (C2-C26) were the main cracking products under selective MW heating of the used supports. The quantitative analysis of the products demonstrated that the liquid-phase process is more selective to alpha-olefins at the MW catalytic cracking than at the convectional thermal cracking. Silica modification of the surface of CM was shown to suppress spark discharge (usually observed at MW heating of CM); hence, the thermal cleavage of C-C bonds on the CM surface but not in the plasma discharge contributes the most to the formation of radicals. It was shown that the selectivity to liquid alpha-olefin could be more than 85 % under MW heating of cermets in region of the E - field node and decrease considerably in the region of H - field node.
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