{"title":"四氢呋喃对改性粘土催化棕榈油酯交换制生物柴油的影响","authors":"Ilham Salim, Alex A. Lepa","doi":"10.20902/ijctr.2019.130116","DOIUrl":null,"url":null,"abstract":"Transesterification of palm oil into biodiesel has been done using modified clay catalyst.The modified clay catalyst was synthesized by destructing the clay with 8M HCl solution, then fusion by NaOH pellet (NaOH/clayratio = 0.8), followed by treating with AlCl3.6H2O, CTAB and distilled water.Then the mixture was regulated to pH of 11.5. Next, the mixture was then poured into a reactor for hydrothermal process at 140 o C for 48 h. The results of the dealumination of clay was characterized byX-ray Fluorescence and the synthesized zeolite was characterized using surface area analyzer and X-Ray Diffraction. The transesterification of palm oil (PO) process was carried out in the variation of temperatures of 55 and 65 o C.Ratio of catalyst :PO : methanol was 1.0 : 20.0 : 13.3and reaction time was 6h. The liquid product was analyzed using Gas Chromatography Mass Spectrometer. The resulted showed that the dealumination of clay had Si content of 34.77 % and Al of 5.67 %. The modified clay (MC) had surface area of 5.5685 m 2 /g, pore volume of 0.0126 cm 3 /g, and pore diameter of 8.871 nm. The results of measurements with XRD produced a different form of chromatogram and type of mineral. The main mineral was gismondine.In this research, the transesterification reaction of PO at a temperature of 55 °Cusing MC catalyst without THF resulted methyl esters (biodiesel)of 41.5 wt%. Furthermore, after adding THFwith ratio of methanol : THF of 1 : 1 and the same treatment, the resulting methyl ester (biodiesel) was the same phase (a one-phase) and methyl esters (biodiesel) product was more than 100 wt%..","PeriodicalId":13853,"journal":{"name":"International Journal of ChemTech Research","volume":"16 1","pages":"132-141"},"PeriodicalIF":0.0000,"publicationDate":"2020-01-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"The Effect of Tetrahydrofuran on Transesterification of Palm\\nOil Using Modified Clay Catalystinto Biodiesel\",\"authors\":\"Ilham Salim, Alex A. 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The resulted showed that the dealumination of clay had Si content of 34.77 % and Al of 5.67 %. The modified clay (MC) had surface area of 5.5685 m 2 /g, pore volume of 0.0126 cm 3 /g, and pore diameter of 8.871 nm. The results of measurements with XRD produced a different form of chromatogram and type of mineral. The main mineral was gismondine.In this research, the transesterification reaction of PO at a temperature of 55 °Cusing MC catalyst without THF resulted methyl esters (biodiesel)of 41.5 wt%. Furthermore, after adding THFwith ratio of methanol : THF of 1 : 1 and the same treatment, the resulting methyl ester (biodiesel) was the same phase (a one-phase) and methyl esters (biodiesel) product was more than 100 wt%..\",\"PeriodicalId\":13853,\"journal\":{\"name\":\"International Journal of ChemTech Research\",\"volume\":\"16 1\",\"pages\":\"132-141\"},\"PeriodicalIF\":0.0000,\"publicationDate\":\"2020-01-01\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"International Journal of ChemTech Research\",\"FirstCategoryId\":\"1085\",\"ListUrlMain\":\"https://doi.org/10.20902/ijctr.2019.130116\",\"RegionNum\":0,\"RegionCategory\":null,\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"\",\"JCRName\":\"\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"International Journal of ChemTech Research","FirstCategoryId":"1085","ListUrlMain":"https://doi.org/10.20902/ijctr.2019.130116","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
引用次数: 0
摘要
用改性粘土催化剂进行了棕榈油酯交换制生物柴油的研究。采用8M HCl溶液破坏粘土,再用NaOH球团(NaOH/粘土比= 0.8)熔融,再用AlCl3.6H2O、CTAB和蒸馏水处理,合成改性粘土催化剂。然后将混合物调节到pH为11.5。然后,将混合物倒入反应器中,在140℃下进行水热处理48 h。用x射线荧光对粘土脱铝的结果进行了表征,并用x射线衍射和表面积分析仪对合成的沸石进行了表征。在55℃和65℃的温度下进行棕榈油酯交换反应,催化剂:PO:甲醇的比例为1.0:20.0:13.3,反应时间为6h。液相产物采用气相色谱质谱分析。结果表明,脱铝后的粘土硅含量为34.77%,铝含量为5.67%。改性粘土(MC)的比表面积为5.5685 m2 /g,孔隙体积为0.0126 cm 3 /g,孔径为8.871 nm。XRD测量结果产生了不同形式的色谱图和矿物类型。主要矿物为吉斯蒙丁。在本研究中,在没有THF的情况下,在温度为55°的MC催化剂下,PO的酯交换反应得到了41.5%的甲酯(生物柴油)。此外,以甲醇:四氢呋喃1:1的比例加入四氢呋喃,经过同样的处理,得到的甲酯(生物柴油)是同相的(一相),甲酯(生物柴油)的产物质量大于100%。
The Effect of Tetrahydrofuran on Transesterification of Palm
Oil Using Modified Clay Catalystinto Biodiesel
Transesterification of palm oil into biodiesel has been done using modified clay catalyst.The modified clay catalyst was synthesized by destructing the clay with 8M HCl solution, then fusion by NaOH pellet (NaOH/clayratio = 0.8), followed by treating with AlCl3.6H2O, CTAB and distilled water.Then the mixture was regulated to pH of 11.5. Next, the mixture was then poured into a reactor for hydrothermal process at 140 o C for 48 h. The results of the dealumination of clay was characterized byX-ray Fluorescence and the synthesized zeolite was characterized using surface area analyzer and X-Ray Diffraction. The transesterification of palm oil (PO) process was carried out in the variation of temperatures of 55 and 65 o C.Ratio of catalyst :PO : methanol was 1.0 : 20.0 : 13.3and reaction time was 6h. The liquid product was analyzed using Gas Chromatography Mass Spectrometer. The resulted showed that the dealumination of clay had Si content of 34.77 % and Al of 5.67 %. The modified clay (MC) had surface area of 5.5685 m 2 /g, pore volume of 0.0126 cm 3 /g, and pore diameter of 8.871 nm. The results of measurements with XRD produced a different form of chromatogram and type of mineral. The main mineral was gismondine.In this research, the transesterification reaction of PO at a temperature of 55 °Cusing MC catalyst without THF resulted methyl esters (biodiesel)of 41.5 wt%. Furthermore, after adding THFwith ratio of methanol : THF of 1 : 1 and the same treatment, the resulting methyl ester (biodiesel) was the same phase (a one-phase) and methyl esters (biodiesel) product was more than 100 wt%..