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Performance of Catalytic Cracking of Biomass Tar and Catalyst Preparation

机译:生物质焦油和催化剂制备催化裂化的性能

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The purification of biomass - derived syngas via tar and methane abatement by catalytic cracking over Ni catalysts using naphthalene as model compounds was investigated. The performance of catalyst activity, ageing and regeneration was valued by means of conversion ratio calculating and gas products composition analysis. The catalysts were prepared by using metallic nickel as active phase grafted on dolomite. The results show: the ratio of single conversion on naphthalene is 95% at space time 0.81h~(-1) and 700°C; with saturated air as regeneration gas, the regeneration time is within 0.5h on the condition of program heating; In order to keep the stability at high reaction temperature (700°C), catalysts should be calcined at 900°C for 4h; compared with heat cracking, the catalytic cracking is propitious to deep cracking of naphthalene.
机译:研究了通过催化裂解在使用萘作为模型化合物的Ni催化剂上通过催化破裂的焦油和甲烷的纯化生物质衍生的合成气。催化剂活性,老化和再生的性能通过转化率计算和天然气产品组成分析来估值。通过使用金属镍作为在白云石上接枝的活性相制备催化剂。结果表明:空间时间为0.81H〜(-1)和700°C时,萘对萘对萘的比例为95%;随着饱和空气作为再生气体,再生时间在程序加热条件下0.5小时内;为了保持高反应温度(700℃)的稳定性,催化剂应在900℃下煅烧4小时;与热裂化相比,催化裂化有利于萘的深裂化。

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