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Fatty Acid Methyl Ester (FAME) Production From Waste Cooking Oil

机译:废物烹饪油的脂肪酸甲酯(名称)生产

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Biodiesel is clear liquid with a light to dark yellow color. Biodiesel is one of the alternative fuels that are attractive because of its favorable characteristics such as being non-toxic, biodegradable, renewable, carbon neutral and low emission. Fatty acid methyl ester (FAME) is a type of biodiesel. In this study, it was produced by using transesterification of waste cooking oil (WCO) which was reacted with methanol and heterogeneous catalyst. The two heterogeneous catalysts that were used in this study were sodium (Na) metal hydroxide supported on oil palm frond (OPF) and Na metal supported on oil palm kernel shell (OPKS). The support metal used was sodium hydroxide solution (NaOH). OPF and OPKS were used as they are the major residues obtained from the oil palm plantation that covers approximately 14.72% of Malaysian's total landmass. The parameters that in this study were the reaction temperatures of the transesterification process from 30°C to 60°C and the catalyst loading from 0.5wt% to 3wt%. The reaction time and ratio methanol to oil were kept constant which were 4 hours and 1:10 respectively. This experiment was conducted in order to investigate the effect of two different heterogeneous catalysts on both temperature and catalyst loading on the yield production of FAME. The results were obtained by using GCMS analysis. From the experiment that was conducted, the results of FAME production by using two different catalysts indicate that the higher the reaction temperature is, the higher the production of FAME which is at 60°C. It also shows that the percentage yield of FAME increases with the increase of catalyst loading until it reaches the best value which is at lwt%.
机译:生物柴油是透明液体,浅色黄色。生物柴油是替代燃料之一,由于其具有无毒,可生物降解,可再生,碳中性和低排放等良好特性,因此具有吸引力。脂肪酸甲酯(名称)是一种生物柴油。在该研究中,通过使用与甲醇和非均相催化剂反应的废物烹饪油(WCO)的酯交换来制备。本研究中使用的两个异质催化剂是在油棕榈叶片(OPF)和Na金属上负载的钠(Na)金属氢氧化物,并在油棕榈籽壳(Opps)上负载。使用的支撑金属是氢氧化钠溶液(NaOH)。 OPF和OPKS被用作,原样是从油棕种植园获得的主要残留物,占马来西亚总土地的约14.72%。本研究中的参数是酯交换方法的反应温度从30℃至60℃,催化剂负载量为0.5wt%至3wt%。将反应时间和比例与油的甲醇保持恒定,分别为4小时和1:10。进行该实验,以探讨两种不同的异质催化剂对催化剂载荷对成本产生的催化剂负荷的影响。通过使用GCMS分析获得结果。从进行的实验中,使用两种不同催化剂的MAME生产结果表明反应温度越高,在60℃下的增物越高。它还表明,随着催化剂负载的增加,百分比的百分比增加,直至其达到LWT%的最佳值。

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