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The Effect of KI and KIO_3 Impregnation on Prepared Hydroxyapatite Catalyst on Biodiesel Production

机译:Ki和Kio_3浸渍对生物柴油生产制备的羟基磷灰石催化剂的影响

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Substitution of homogeneous catalyst to heterogeneous catalyst is one of the alternative ways to simplify the separation process. In this research, hydroxyapatite (HAP) that was used as a catalyst on biodiesel production was prepared from natural phosphate rock. Effect of various impregnation on the catalyst was studied in characterized and performance test. The catalytic performance test was done using simultaneous esterification and transesterification reaction under operating condition of 60oC for 6 hours using waste cooking oil as the raw material. FTIR analysis showed that HAP catalyst had been successfully synthesized with the existence of functional group PO_(43-) (phosphate) and CO_(3-) (carbonate). The surface area of the catalyst by 13.513 m2/gr and specific pore volume by 0,0083 cc/gr at a concentration of 5%w/w KI while at 5% w/w KIO_3 the surface area of the catalyst by 10.651 m2/gr and specific pore volume by 0.0065 cc/gr. The result of XRD analysis gives the value obtained at 2θ = 46,75° for KI and 2θ = 34,53° for KI03, which indicates that those components was successfully impregnated on HAP catalyst. The best value for each yield dan FAME obtained on 91,78% and 59,1% at a concentration of catalyst impregnation 5% w/w KI
机译:将均相催化剂取代为异质催化剂是简化分离过程的替代方式之一。在本研究中,用作生物柴油生产催化剂的羟基磷灰石(HAP)由天然磷酸盐岩制备。研究了各种浸渍对催化剂的影响,进行了表征和性能试验。使用废料烹饪油作为原料,使用60℃的同时酯化和酯交换反应在6小时内进行催化性能试验。 FTIR分析表明,HAP催化剂已成功合成,存在官能团PO_(43-)(磷酸盐)和CO_(3-)(碳酸盐)。催化剂的表面积为13.513m2 / gr和特定的孔体积,浓度为5%w / w ki的浓度为5%w / w ki,而催化剂的表面积为10.651m2 / GR和特定的孔体积0.0065 CC / GR。 XRD分析的结果使得在ki和2θ= 46,75°处获得的值为Ki03,表明这些组分在Hap催化剂上成功浸渍。在催化剂浸渍的浓度为91,78%和59,1%的催化剂浸渍5%w / wki

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