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Pd/SAPO-5的制备及其在合成甲基正戊基酮中的应用

Preparation of Pd/SAPO-5 Bifunctional Catalysts for One-step Synthesis of Methyl Amyl Ketone
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摘要 以三乙胺为模板剂,采用水热法制备了Pd/SAPO-5双功能催化剂,并用H2-TPR,XRD,SEM,XRF,^(29)Si MASNMR等手段对催化剂进行了表征。结果表明:钯的加入并不能改变分子筛的晶体结构;而不同的硅铝比(SiO2与Al2O3的物质的量比,下同)会导致SAPO-5分子筛晶体结构以及形貌上的差异。将所制备的催化剂用于丙酮和丁醛气相一步法合成甲基正戊基酮(MAK)的反应中,考察了硅铝比、反应温度和金属负载量对催化活性的影响,在SAPO-5分子筛结构完整的前提下,Pd/SAPO-5催化活性随硅铝比的上升而增加。在硅铝比为1.5、反应温度180℃、w(Pd)=0.25%时,MAK的收率最高,可达57.86%,并可运行500 h以上而不明显失活。 A series of Pd/SAPO-5 bifunctional catalysts were prepared through hydrothermal method by using triethylamine as template and were characterized by H2-TPR, XRD, SEM, XRF and ^(29) Si MAS NMR. The results revealed that the doping of Pd didn't change the molecular sieve crystalline structure of SAPO-5, while the alteration of molar ratio of Si O2 to Al2 O3 could induce the changes in crystalline structure and morphology of SAPO-5. Subsequently, the Pd/SAPO-5 bifunctional catalysts were applied for one-step synthesis of methyl amyl ketone(MAK) from acetone and butyraldehyde. The influences of SiO2/Al2 O3 molar ratio, reaction temperature and amount of palladium loading on the catalytic activity of catalyst were investigated. When the SAPO-5 crystalline structure kept intact, the activity of Pd/SAPO-5 increased with increasing the SiO2/Al2 O3 molar ratio. When the SiO2/Al2 O3 molar ratio was 1.5, the reaction temperature was 180 ℃, and the amount of Pd loading was 0.25%, the catalytic activity reached the best. The highest yield of MAK was 57.86%. Moreover, the catalytic activity was rather stable under 500 h time-on-stream test.
作者 王强 王乃威 付睿峰 王忍青 江志东 WANG Qiang;WANG Nai-wei;FU Rui-feng;WANG Ren-qing;JIANG Zhi-dong(Shanghai Key Laboratory of Electric Insulation and Thermal Aging,School of Chemistry and Chemical Engineering,Shanghai Jiao Tong University,Shanghai 200240,China)
出处 《精细化工》 EI CAS CSCD 北大核心 2018年第10期1667-1672,共6页 Fine Chemicals
关键词 Pd/SAPO-5 双功能催化剂 硅铝比 一步合成 甲基正戊基酮 催化技术 Pd/SAPO-5 bifunctional catalyst SiO2/Al2O3 molar ratio one-step synthesis methyl-amyl-ketone catalysis technology
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