Jawad Abbas, Ahmed Sura
Midland Refineries Company MRC/AL Daura Refinery Company/Training and Development Division/Baghdad Iraq
Midland Refineries Company MRC/AL Daura Refinery Company/Maintenance Board/Baghdad Iraq
RSC Adv. 2023 Apr 6;13(16):11081-11095. doi: 10.1039/d2ra08235g. eCollection 2023 Apr 3.
A systematic study of the comparative performances of 4% Ga-, 4% Zr-, and 1% Cr-impregnated H-ZSM-5 catalysts for oxidative dehydrogenation of propane in the presence and absence of CO is presented. It was found that methane, ethene, propene, butene, pentene, and BTX are the major products from all of these catalysts at various reaction temperatures (400-550 °C), WHSV, 4 kg s mol and feed gas, CH/N = 2.5/97.5 and CH/CO/N = 2.5/5/92.5; flow rate, 75 mL min under atmospheric pressure for 10 h. The combination of material characterization and catalytic testing revealed that Ga-, Zr-, and Cr-doped H-ZSM-5 are excellent catalysts for this process, helping to achieve around 61% CO conversion. The co-doped Ga/H-ZSM-5 catalysts significantly enhanced the activity (65% propane and 61% CO conversion at 550 °C) among all the tested catalysts, with approximately 100% total selectivity 62% towards BTX and 26% towards propene, but with lower selectivity for methane, ethene, and pentene (, light hydrocarbons). TPR profiles indicated that the redox cycle between Cr(iii)O and Cr(vi)O played an important role in the dehydrogenation of CH over Cr/Zr-Ga/H-ZSM-5. CO could oxidize a part of the Cr(iii) species to Cr(vi) species under the reaction conditions used.
本文介绍了对4%Ga浸渍、4%Zr浸渍和1%Cr浸渍的H-ZSM-5催化剂在有无CO存在下丙烷氧化脱氢的比较性能进行的系统研究。发现在各种反应温度(400 - 550°C)、WHSV为4 kg s mol、进料气CH/N = 2.5/97.5以及CH/CO/N = 2.5/5/92.5;流速为75 mL min、大气压下反应10 h的条件下,甲烷、乙烯、丙烯、丁烯、戊烯和BTX是所有这些催化剂的主要产物。材料表征和催化测试相结合表明,Ga、Zr和Cr掺杂的H-ZSM-5是该过程的优良催化剂,有助于实现约61%的CO转化率。在所有测试催化剂中,共掺杂的Ga/H-ZSM-5催化剂显著提高了活性(550°C时丙烷转化率为65%,CO转化率为61%),对BTX的总选择性约为100%,对丙烯的选择性为62%,对甲烷、乙烯和戊烯(轻烃)的选择性较低。TPR曲线表明,Cr(iii)O和Cr(vi)O之间的氧化还原循环在Cr/Zr-Ga/H-ZSM-5上CH的脱氢过程中起重要作用。在所使用的反应条件下,CO可将部分Cr(iii)物种氧化为Cr(vi)物种。