首页> 外文期刊>Journal of Analytical & Applied Pyrolysis >Thermal and catalytic micropyrolysis for conversion of cottonseed oil dregs to produce biokerosene
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Thermal and catalytic micropyrolysis for conversion of cottonseed oil dregs to produce biokerosene

机译:热和催化微热解法转化棉籽渣以生产生物煤油

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A sample of cottonseed oil dregs was obtained by the alkali pretreatment of the oil to remove free fatty acids and other impurities before an industrial biodiesel production process. The alkali dregs was characterized and submitted to non-catalytic, catalytic, and reactive hydrogen atmosphere micropyrolysis experiments to assess the capacities for type SPK-HEFA biokerosene production. Non-catalytic and catalytic micropyrolyses were performed at 500 and 550 degrees C. In the catalytic experiments, catalysts based on Mo or W oxides supported on Zr or Ti oxides were tested for the first time for this purpose. The moisture content of the cottonseed oil dregs was 23.4% (wt%) and the other major components were triacylglycerols + free fatty acids (65.0%) and inorganic material (9.8%). The products of the micropyrolysis experiments were characterized by GC-MS and quantified by GC-FID. The presence of moisture in the initial feedstock provided better results in the thermal conversion to liquid biofuel (16%), compared to dry biomass (6%), considering the n-alkanes and n-alkenes produced in the range C-9-C-16. The mass conversion performed in the presence of catalysts at 550 degrees C resulted in an average yield of around 32%, compared to a value of 19% for a non-catalytic process under a nitrogen atmosphere, with the same values for the yields under a reactive hydrogen atmosphere. The reactive atmosphere and the catalysts did not have any substantial influence on the ratio between n-alkanes and n-alkenes.
机译:在工业生物柴油生产过程之前,通过对该油进行碱预处理以除去游离脂肪酸和其他杂质,获得了棉籽油渣的样品。对碱渣进行了表征,并进行了非催化,催化和反应性氢气氛微热解实验,以评估SPK-HEFA型生物油的生产能力。非催化和催化微热解在500和550摄氏度下进行。在催化实验中,为此目的首次测试了基于负载在Zr或Ti氧化物上的Mo或W氧化物的催化剂。棉籽油渣的水分含量为23.4%(wt%),其他主要成分为三酰基甘油+游离脂肪酸(65.0%)和无机物质(9.8%)。微裂解实验的产物用GC-MS表征,并用GC-FID定量。考虑到在C-9-C范围内生产的正构烷烃和正构烯烃,初始原料中水分的存在与干生物质(6%)相比,能更好地热转化为液态生物燃料(16%)。 -16。在催化剂存在下于550摄氏度下进行的质量转化产生的平均收率约为32%,而在氮气氛下,非催化过程的平均收率为19%,而在氮气氛下,收率相同。反应性氢气氛。反应性气氛和催化剂对正构烷烃和正构烯烃之间的比例没有实质性影响。

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