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Catalytic upgrading of sugarcane bagasse pyrolysis vapours over rare earth metal (Ce) loaded HZSM-5: Effect of catalyst to biomass ratio on the organic compounds in pyrolysis oil

机译:负载稀土金属(Ce)的HZSM-5上甘蔗渣热解蒸气的催化提纯:催化剂/生物质比对热解油中有机化合物的影响

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The main objective of the current work is to investigate the influence of catalyst to biomass ratio (by weight%) on the catalytic upgrading of sugarcane bagasse derived pyrolysis vapours over cerium (Ce) loaded Hydrogen exchanged Zeolite Socony Mobil-5 (HZSM-5) catalyst via in-situ fixed bed reactor. The temperature of pyrolysis was kept at 500 degrees C for all investigated samples. The HZSM-5 catalyst was used as a support with 1 wt% of Ce as promoter loaded via incipient wetness impregnation method. The biomass sample was fixed at 2 g, while the catalyst mass loading was loaded according to the catalyst to biomass ratio which are 0.5:1.0, 1.0:1.0, 1.5:1.0, and 2.0:1.0. For comparison, the non-catalytic and biomass catalytic over HZSM-5 catalyst was also pyrolyzed at the same operating conditions. The results show that the yields of pyrolysis oil and coke were significantly influenced by the use of Ce/HZSM-5 catalyst at various catalyst to biomass ratio than the catalytic pyrolysis over HZSM-5, in which generate higher pyrolysis oil yield (58.0-68.0 wt%) and lower coke yield (2.9-4.1%). The increasing loading of mass in Ce/HZSM-5 catalyst has additional effect with respect to C-6-C-8 hydrocarbon contents in pyrolysis oil than the catalytic samples over the HZSM-5 catalyst. Among the tested catalyst to biomass ratio, the catalyst to biomass ratio of 1.5:1 has demonstrated to be the potential candidates in the catalytic upgrading of sugarcane bagasse derived oxygenated pyrolysis vapours into higher content of C-6-C-8 hydrocarbons (2.45%) in pyrolysis oil with lower coke yield (3.2%) over Ce/HZSM-5 catalyst. The bi-functional Ce/HZSM-5 catalyst was more effective in suppressing the coke formation in comparison to HZSM-5 catalyst at all investigated catalyst to biomass ratios and this was attributed to the synergistic effect of Ce on HZSM-5 support.
机译:当前工作的主要目的是研究催化剂/生物质比(按重量%)对负载铈(Ce)的甘蔗渣提取热解蒸气的催化提质的影响氢交换沸石Socony Mobil-5(HZSM-5)催化剂通过原位固定床反应器。所有研究样品的热解温度均保持在500摄氏度。使用HZSM-5催化剂作为载体,通过初湿含浸法负载了1重量%的Ce作为助催化剂。将生物质样品固定为2 g,同时根据催化剂与生物质的比例0.5:1.0、1.0:1.0、1.5:1.0和2.0:1.0加载催化剂质量负载。为了比较,在相同的操作条件下,HZSM-5催化剂的非催化和生物质催化也被热解。结果表明,在不同的催化剂/生物质比下,使用Ce / HZSM-5催化剂对热解油和焦炭的收率的影响明显大于在HZSM-5上进行催化热解的结果,其中热解油的收率更高(58.0-68.0 wt%)和较低的焦炭收率(2.9-4.1%)。与在HZSM-5催化剂上的催化样品相比,Ce / HZSM-5催化剂中不断增加的质量负载对热解油中C-6-C-8烃含量具有额外的影响。在测试的催化剂与生物质比率中,催化剂与生物质比率为1.5:1已证明是甘蔗渣衍生的含氧热解蒸气催化转化为更高含量的C-6-C-8烃(2.45%)的潜在候选物。 )在热解油中的焦炭收率比Ce / HZSM-5催化剂低(3.2%)。在所有研究的催化剂与生物质比下,双功能Ce / HZSM-5催化剂与HZSM-5催化剂相比,在抑制焦炭形成方面更有效,这归因于Ce对HZSM-5载体的协同作用。

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