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Mild upgrading of biomass pyrolysis vapors via ex-situ catalytic pyrolysis over an iron-montmorillonite catalyst

机译:通过在铁蒙脱石催化剂上通过前型催化热解的生物质热解蒸汽的轻度升级

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Pyrolysis vapor upgrading can improve the stability of pyrolysis liquids to facilitate storage, transport, and drop in use as fuels and chemical feedstocks in existing refining infrastructure. This study investigates a low cost iron based catalyst for mild in-situ upgrading of fast pyrolysis vapors to increase the stability of pyrolysis liquid. Irondoped montmorillonite K10 catalysts were characterized by ICP-OES, BET porosimetry, XRD, XPS, and NH3-TPD. The effect of three upgrading process parameters are evaluated by Box-Behnken experimental design using a fixed catalyst bed. Predictive model equations are developed based on response surface methodology to describe the effect of iron loading, catalyst to biomass ratio, and catalyst bed temperature on yields of pyrolysis liquids, non-condensable gas, and coke on the catalyst. Compared to non-catalytic pyrolysis, pyrolysis vapor upgrading over iron catalyst reduce pyrolysis liquid yields and increase gas yields as pyrolysis vapors are catalytically cracked into lighter molecules. Liquid yield decreases with C:B ratio while gas yields increase. By increasing Fe loading from 0% to 10%, catalyst coking decreases from 11.7% to 3.5% yield. Iron loading of 10% is the least susceptible to coking, but results in greater amounts of polyaromatics in the pyrolysis liquid product. According to GCMS analysis of the pyrolysis liquids, upgraded pyrolysis liquids have lower concentrations of unstable carboxylic acids and aldehydes. In addition, formation of phenols shift towards a greater fraction of alkyl phenols and lower fraction of methoxy phenols leading to a more stable liquid product as a result of upgrading. Overall, iron-doped montmorillonite catalyst is demonstrated to be a viable, low cost catalyst for mild upgrading of fast pyrolysis vapors.
机译:热解蒸气升级可以提高热解液的稳定性,以促进在现有炼油基础设施中用作燃料和化学原料的储存,运输和下降。本研究调查了一种低成本的铁基催化剂,用于轻度原位升级的快速热解蒸汽以增加热解液的稳定性。通过ICP-OES,BET POROSIMETRY,XRD,XPS和NH3-TPD表征ICONDOPED MONTMORILLONITE K10催化剂。使用固定催化剂床的Box-Behnken实验设计评估三个升级过程参数的效果。基于响应表面方法开发预测模型方程,以描述铁载荷,催化剂对生物质比的影响和催化剂床温度对热解液,不可冷凝气体和焦炭上的催化剂的焦炭。与非催化热解相比,通过铁催化剂升级的热解蒸气降低热解液产率并增加气体产量,因为热解蒸气被催化裂化成较浅的分子。液体产率随C:B比率降低,而气体产量增加。通过将0%升高至10%的加载量增加,催化剂焦化从11.7%降至3.5%收率。 10%的铁载荷是最不易焦化的,但导致热解液产物中的多芳烃。根据热解液的GCMS分析,升级的热解液具有较低浓度的不稳定羧酸和醛。此外,形成酚展朝向更大的烷基酚和较低的甲氧基酚的少量部分,导致升级的液体产品更稳定。总的来说,将铁掺杂的蒙脱石催化剂被证明是一种可行的低成本催化剂,用于轻度热解蒸汽升级。

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