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Catalytic Flash Pyrolysis of Biomass Using Different Types of Zeolite and Online Vapor Fractionation

机译:使用不同类型的沸石和在线蒸汽分馏进行生物质的催化快速热解

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摘要

Bio-oil produced from conventional flash pyrolysis has poor quality and requires expensive upgrading before it can be used as a transportation fuel. In this work, a high quality bio-oil has been produced using a novel approach where flash pyrolysis, catalysis and fractionation of pyrolysis vapors using two stage condensation are combined in a single process unit. A bench scale unit of 1 kg/h feedstock capacity is used for catalytic pyrolysis in an entrained down-flow reactor system equipped with two-staged condensation of the pyrolysis vapor. Zeolite-based catalysts are investigated to study the effect of varying acidities of faujasite Y zeolites, zeolite structures (ZSM5), different catalyst to biomass ratios and different catalytic pyrolysis temperatures. Low catalyst/biomass ratios did not show any significant improvements in the bio-oil quality, while high catalyst/biomass ratios showed an effective deoxygenation of the bio-oil. The application of zeolites decreased the organic liquid yield due to the increased production of non-condensables, primarily hydrocarbons. The catalytically produced bio-oil was less viscous and zeolites were effective at cracking heavy molecular weight compounds in the bio-oil. Acidic zeolites, H-Y and H-ZSM5, increased the desirable chemical compounds in the bio-oil such as phenols, furans and hydrocarbon, and reduced the undesired compounds such as acids. On the other hand reducing the acidity of zeolites reduced some of the undesired compounds in the bio-oil such as ketones and aldehydes. The performance of H-Y was superior to that of the rest of zeolites studied: bio-oil of high chemical and calorific value was produced with a high organic liquid yield and low oxygen content. H-ZSM5 was a close competitor to H-Y in performance but with a lower yield of bio-oil. Online fractionation of catalytic pyrolysis vapors was employed by controlling the condenser temperature and proved to be a successful process parameter to tailor the desired bio-oil properties. A high calorific value bio-oil having up to 90% organics was produced using two staged condensation of catalytic pyrolysis vapor. Zeolite-based acidic catalysts can be used for selective deoxygenation, and the catalytic bio-oil quality can be further improved with staged vapor condensation.
机译:由常规闪速热解产生的生物油质量差,需要昂贵的升级才能用作运输燃料。在这项工作中,使用一种新颖的方法生产了高质量的生物油,该方法将闪蒸热解,催化和使用两级冷凝的热解蒸气分馏合并在一个处理单元中。原料容量为1 kg / h的台式规模装置用于配备了热解蒸气两阶段冷凝的夹带下流反应器系统中的催化热解。研究了基于沸石的催化剂,以研究八角Y型沸石的不同酸度,沸石结构(ZSM5),不同的催化剂与生物质比以及不同的催化热解温度的影响。低催化剂/生物质比没有显示出生物油质量的任何显着改善,而高催化剂/生物质比显示出了生物油的有效脱氧。沸石的使用降低了有机液体的产率,这是由于增加了非冷凝物(主要是烃类)的产量。催化生产的生物油的粘度较低,沸石有效地裂解了生物油中的高分子量化合物。酸性沸石H-Y和H-ZSM5增加了生物油中所需的化合物,例如酚,呋喃和烃,并减少了不需要的化合物,例如酸。另一方面,降低沸石的酸性降低了生物油中一些不希望的化合物,例如酮和醛。 H-Y的性能优于所研究的其他沸石:产生了具有高化学和热值的生物油,具有高有机液体产率和低氧含量。 H-ZSM5在性能上与H-Y接近,但生物油的收率较低。通过控制冷凝器温度使用催化热解蒸气的在线分馏,并被证明是调整所需生物油特性的成功工艺参数。使用催化热解蒸气的两阶段冷凝,可以生产出有机物含量高达90%的高热值生物油。可以使用基于沸石的酸性催化剂进行选择性脱氧,并且通过分阶段的蒸汽冷凝可以进一步提高生物油的催化质量。

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