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One Step Transesterification Process of Sludge Palm Oil (SPO) by Using Deep Eutectic Solvent (DES) in Biodiesel Production

机译:利用深共晶溶剂(DES)在生物柴油生产中使用深层共晶溶剂(DES)进行污泥棕榈油(SPO)的一步替代方法

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Biodiesel production by using sludge palm oil (SPO) as raw material is generally synthesized in two step reactions, namely esterification and transesterification, because the free fatty acid (FFA) content of SPO is relatively high. However, the presence of choline chloride (ChCl), glycerol based deep eutectic solvent (DES), in transesterification may produce biodiesel from SPO in just one step. In this study, DES was produced by the mixture of ChCl and glycerol at molar ratio of 1:2 at a temperature of 80°C and stirring speed of 400 rpm for 1 hour. DES was characterized by its density and viscosity. The transesterification process was performed at reaction temperature of 70 °C, ethanol to oil molar with ratio of 9:1, sodium hydroxide as catalyst concentration of 1 % wt, DES as cosolvent with concentration of 0 to 5 % wt, stirring speed of 400 rpm, and one hour reaction time. The obtained biodiesel was then assessed with density, viscosity, and ester content as the parameters. FFA content of SPO as the raw material was 7.5290 %. In this case, DES as cosolvent in one step transesterification process of low feedstock could reduce the side reaction (saponification), decrease the time reaction, decrease the surface tension between ethanol and oil, and increase the mass transfer that simultaneously simplified the purification process and obtained the highest yield. The esters properties met the international standards of ASTM D 6751, with the highest yield obtained was 83.19% with 99.55% of ester content and the ratio of ethanol:oil of 9:1, concentration of DES of 4%, catalyst amount of 1%, temperature of reaction at 70°C and stirring speed of 400 rpm.
机译:生物柴油生产通过使用为原料在两个步骤的反应,即酯化和酯交换一般合成污泥棕榈油(SPO),因为SPO的游离脂肪酸(FFA)的含量相对较高。但是,胆碱盐酸盐(CHCL)的存在下,甘油基于深共晶溶剂(DES),在酯基转移反应可以在一个步骤就SPO生产生物柴油。在80℃的温度下2和搅拌400转的速度进行1小时:在这项研究中,DES用三氯甲烷的混合物和甘油以1:1的摩尔比制备。 DES的特点是它的密度和粘度。酯基转移法在70℃的反应温度,乙醇为9比进行油摩尔:1,氢氧化钠为1%重量的催化剂浓度,DES作为共溶剂,以0至5重量%浓度,在搅拌的400速度转,一小时的反应时间。将所获得的生物柴油,然后用密度,粘度,和作为参数酯含量评估。 SPO的游离脂肪酸含量的原料为7.5290%。在此情况下,DES作为在低的原料可以减少副反应(皂化)中的一个步骤的酯交换过程的助溶剂,减少时间反应,降低乙醇和油之间的表面张力,提高质量传递,其同时简化纯化过程和获得的最高产率。酯特性与酯含量99.55%和乙醇的比满足ASTM d 6751的国际标准,以获得最高的产率是83.19%:油的9:1,浓度DES的4%,催化剂用量的1% ,在70℃下反应的温度和400rpm的搅拌速度。

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