Modelling and experimental studies for the recovery of valuable chemical intermediates from mustard husk pyrolysis oil

IF 1.6 4区 工程技术 Q3 Chemical Engineering International Journal of Chemical Reactor Engineering Pub Date : 2023-06-20 DOI:10.1515/ijcre-2022-0236
Kanchan Drugkar, Anand Gupta Chakinala, Abhishek Sharma
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Abstract

Abstract This work presents a study on the separation of model compounds representative of mustard husk pyrolysis oil, through a combination of experimental and modelling approaches. Atmospheric and vacuum distillation were used to perform the separation, and the obtained results were validated by means of an Aspen simulation model. To simulate the pyrolysis oil, different fractions present in mustard husk pyrolysis oil were used. Atmospheric distillation was performed at temperatures ranging from 50 to 180 °C, while vacuum distillation was conducted at varying temperatures and pressures. The composition of the distillate and residue was analysed, and it was found that coking occurred due to polymerization reactions, even at moderate temperatures up to ∼100 °C during atmospheric distillation. Therefore, vacuum rotary evaporation was employed to carry out further studies at lower temperatures (50 °C) and pressures (50 mbar), resulting in a recovery percentage of 56 % for lighter fractions and 36 % for heavier fractions, with complete water (62 %) collected in the distillate phase. The simulated feed mixture, which consisted of Guaiacols, furfurals and furan methanols, was distributed equally in both the distillate and residue phases, and the experimental recoveries in distillate and residue phases were found to be similar with simulation values. Further studies are needed to comprehend the separation behaviour of real pyrolysis oil and to minimize polymerization reactions in the column.
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从芥菜壳热解油中回收有价化学中间体的模型和实验研究
摘要采用实验与模拟相结合的方法,对芥菜壳热解油中具有代表性的模型化合物的分离进行了研究。采用常压蒸馏和真空蒸馏进行分离,并利用Aspen模拟模型对分离结果进行了验证。采用芥菜壳热解油的不同馏分进行模拟。常压蒸馏在50 ~ 180 ℃的温度范围内进行,而真空蒸馏在不同的温度和压力下进行。对馏出物和残渣的组成进行了分析,发现即使在常压蒸馏过程中高达~ 100 °C的中等温度下,也会由于聚合反应而发生焦化。因此,采用真空旋转蒸发在较低温度(50 °C)和压力(50 mbar)下进行进一步的研究,结果表明,较轻馏分的回收率为56 %,较重馏分的回收率为36 %,馏分相收集了完整的水(62 %)。愈创木酚、糠醛和呋喃甲醇组成的模拟混合料在馏出相和残渣相分布均匀,馏出相和残渣相的实验回收率与模拟值相近。进一步的研究需要了解真实热解油的分离行为,并尽量减少塔内的聚合反应。
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来源期刊
CiteScore
2.80
自引率
12.50%
发文量
107
审稿时长
3 months
期刊介绍: The International Journal of Chemical Reactor Engineering covers the broad fields of theoretical and applied reactor engineering. The IJCRE covers topics drawn from the substantial areas of overlap between catalysis, reaction and reactor engineering. The journal is presently edited by Hugo de Lasa and Charles Xu, counting with an impressive list of Editorial Board leading specialists in chemical reactor engineering. Authors include notable international professors and R&D industry leaders.
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