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Biodiesel production from waste cooking oil over sulfonated catalysts

机译:用磺化催化剂从废食用油中生产生物柴油

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Biodiesel production from waste cooking oil with methanol was carried out in the presence of poly(vinyl alcohol) with sulfonic acid groups (PVA-SO3H) and polystyrene with sulfonic acid groups (PS-SO3H), at 60 degrees C. The PVA-SO3H catalyst showed higher catalytic activity than the PS-SO3H one. In order to optimize the reaction conditions, different parameters were studied. An increase of waste cooking oil conversion into fatty acid methyl esters with the amount of PVA-SO3H was observed. When the transesterification and esterification of WCO was carried out with ethanol over PVA-SO3H, at 60 degrees C, a decrease of biodiesel production was also observed. The WCO conversion into fatty acid ethyl ester increased when the temperature was increased from 60 to 80 degrees C. When different amounts of free fatty acids were added to the reaction mixture, a slight increase on the conversion was observed. The PVA-SO3H catalyst was reused and recycled with negligible loss in the activity.
机译:在60°C下,在具有磺酸基团的聚乙烯醇(PVA-SO3H)和具有磺酸基团的聚苯乙烯(PS-SO3H)的存在下,用甲醇制成的食用废油生产生物柴油。PVA-SO3H催化剂表现出比PS-SO3H更高的催化活性。为了优化反应条件,研究了不同的参数。观察到随着PVA-SO3H量的增加,废食用油转化为脂肪酸甲酯的比例增加。当在60℃下用乙醇在PVA-SO 3 H上用乙醇进行WCO的酯交换和酯化时,还观察到生物柴油产量的减少。当温度从60℃升高至80℃时,WCO向脂肪酸乙酯的转化率增加。当向反应混合物中添加不同量的游离脂肪酸时,观察到转化率略有提高。 PVA-SO3H催化剂可重复使用和再循环,而活性损失可忽略不计。

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