Faculty of Chemical Engineering, Amirkabir University of Technology, Tehran Polytechnic, P.O. Box 15875-4413, Hafez Ave., Tehran, Iran.
Department of Petroleum and Chemical Engineering, Science and Research Branch, Islamic Azad University, Tehran, Iran.
Comb Chem High Throughput Screen. 2021;24(4):534-545. doi: 10.2174/1386207323666200428093154.
The research focuses on recent progress in the production of light olefins. Hence, as the common catalyst of the reaction (SAPO-34) deactivates quickly because of coke formation, we reorganized the mechanism combining SAPO-34 with a natural zeolite in order to delay the deactivation time.
The synthesis of nanocomposite catalyst was conducted hydrothermally using experimental design. Firstly, Clinoptilolite was modified using nitric acid in order to achieve nano-scaled material. Then, the initial gel of the SAPO-34 was prepared using DEA, aluminum isopropoxide, phosphoric acid and TEOS as the organic template, sources of Aluminum, Phosphor, and Silicate, respectively. Finally, the modified zeolite was combined with SAPO-34's gel.
20 different catalysts due to D-Optimal design were synthesized and the nanocomposite with 50 weight percent of SAPO-34, 4 hours Crystallization and early Clinoptilolite precipitation showed the highest relative crystallinity, partly high BET surface area and hierarchical structure.
Different analyses illustrated the existence of both components. The most important property alteration of nanocomposite was the increment of pore mean diameters and reduction in pore volumes in comparison with free SAPO-34. Due to the low price of Clinoptilolite, the new catalyst renders the process as economical. Using this composite, according to the formation of multi-sized pores located hierarchically on the surface of the catalyst and increased surface area, significant amounts of Ethylene and Propylene, in comparison with free SAPO-34, were produced, as well as the deactivation time was improved.
本研究专注于轻烯烃生产的最新进展。因此,由于反应的常用催化剂(SAPO-34)由于积碳而迅速失活,我们重新组织了该机制,将 SAPO-34 与天然沸石结合在一起,以延迟失活时间。
纳米复合催化剂的合成是通过实验设计水热法进行的。首先,用硝酸对斜发沸石进行改性,以获得纳米级材料。然后,使用 DEA、异丙醇铝、磷酸和 TEOS 作为有机模板、铝源、磷源和硅源,制备 SAPO-34 的初始凝胶。最后,将改性沸石与 SAPO-34 的凝胶结合。
由于 D-最优设计,共合成了 20 种不同的催化剂,纳米复合材料中 SAPO-34 的含量为 50wt%,结晶时间为 4 小时,早期斜发沸石沉淀显示出最高的相对结晶度,部分具有较高的 BET 表面积和分级结构。
不同的分析表明两种成分的存在。与自由 SAPO-34 相比,纳米复合材料最重要的性质变化是孔平均直径的增加和孔体积的减少。由于斜发沸石价格低廉,新型催化剂使该工艺具有经济性。使用这种复合材料,由于催化剂表面上形成了具有多尺寸孔的分级结构和增加的表面积,与自由 SAPO-34 相比,可以产生大量的乙烯和丙烯,并且失活时间得到了改善。