Dal Pozzo Daniel Marcos, Azevedo Dos Santos José Airton, Júnior Edward Seabra, Santos Reginaldo Ferreira, Feiden Armin, Melegari de Souza Samuel Nelson, Burgardt Ismael
Federal Technological University of Parana (UTFPR) Avenida Brasil 4232 85884-000 Medianeira Brazil
Engineering of Energy in Agriculture, State University of West Parana, Rua Universitária 2069 85819-110 Cascavel Brazil.
RSC Adv. 2019 Feb 8;9(9):4900-4907. doi: 10.1039/c8ra10248a. eCollection 2019 Feb 5.
The catalytic activity of the protonated form of H-Y(80) zeolite (Faujasite with high Si/Al ratio) was evaluated as an acid catalyst in the esterification step pre-treatment of FFA by means of the esterification reaction of oleic acid with methanol in soybean oil. The zeolite structure was characterized by XRD and FTIR. Textural characterization was carried out by N physisorption. The thermal stability was evaluated by TG-DTA and the acidity measured by NH-TPD and Pyridine-FTIR. The limitations of the use of this zeolite in a pre-treatment for biodiesel production was investigated through oleic acid esterification in soybean oil, as a model reaction, performed with different temperatures, catalyst amounts and molar ratios. The results showed that the amount of remaining FFA decreased to values well below the initial amount. Under the optimal reactional conditions, conversions to methyl esters above 95% were achieved. Results support that such reactions can be performed under H-Y(80) zeolite catalysis and can be applied in a pre-treatment esterification of feedstocks with high contents of FFA. Catalyst reuse is feasible due to its easy separation from reaction products allowing new reaction cycles, as well as the application of the H-Y(80) zeolite in biodiesel production.
通过油酸与甲醇在大豆油中的酯化反应,评估了质子化形式的H-Y(80)沸石(高硅铝比的八面沸石)作为酸催化剂在游离脂肪酸(FFA)酯化步骤预处理中的催化活性。通过XRD和FTIR对沸石结构进行了表征。通过N物理吸附进行了织构表征。通过TG-DTA评估了热稳定性,并通过NH-TPD和吡啶-FTIR测量了酸度。通过在大豆油中进行油酸酯化反应(作为模型反应),在不同温度、催化剂量和摩尔比下进行,研究了这种沸石在生物柴油生产预处理中使用的局限性。结果表明,剩余FFA的量降至远低于初始量的值。在最佳反应条件下,甲酯转化率达到95%以上。结果支持这样的反应可以在H-Y(80)沸石催化下进行,并可应用于高FFA含量原料的预处理酯化。由于其易于与反应产物分离,从而允许进行新的反应循环,以及H-Y(80)沸石在生物柴油生产中的应用,催化剂的重复使用是可行的。