{"title":"固定化脂肪酶在改性疏水基质上催化合成生物表面活性剂果糖油酯","authors":"Chusnul Hidayat, Kholifaturrosyidah Fitria, Supriyanto, Pudji Hastuti","doi":"10.1016/j.aaspro.2016.02.150","DOIUrl":null,"url":null,"abstract":"<div><p>Enzymatic synthesis of fructose oleic ester (FOE) in stirred tank reactor using the immobilized lipase may cause a physical damage of support matrix, which causes a leaching of lipase from matrix. The objective of this research was to evaluate the best condition of FOE synthesis in fluidized bed reactor (FBR) using the immobilized lipase on modified hydrophobic matrix. Surface of Amberlite IRA 96 was modified with 2-phenylpropionaldehyde to obtain hydrophobic surface. <em>Candida rugosa</em> lipase was immobilized on the modified matrix. Subsequently, it was used for FOE synthesis in FBR system. Factors, such as reaction time, substrate flow rate, amount of water adsorbent, and substrate molar ratio were evaluated based on the conversion of oleic acid into FOE. Results from FTIR analysis showed that modified matrix had a peak at a specific wavelength ∼1674 cm<sup>-1</sup>. It indicated that a group of imine (-C=N-) occurred after surface modification. The highest adsorption of lipase was obtained after adsorption for 45<!--> <!-->min (13.28±0.57<!--> <!-->mg lipase/g matrix), which was equivalent to 52.95±1.67%. The lipase activity was 73.66±5.35 U/g matrix. The best FOE synthesis condition was obtained at flow rate of 0.4<!--> <!-->mL/min, molecular sieve of 12%, substrate molar ratio (fructose: oleic acid) 1:4 for 48<!--> <!-->h. FOE was confirmed by TLC and FT-IR analysis, which they had <em>Rf</em> 0.72 and specific wave number of ∼1712 cm<sup>-1</sup>, respectively. FOE had emulsion capacity, emulsion stability, droplet size, and HLB value of 92.83±0.46%; 85.65±0.92%; 7.86±0.93<!--> <!-->μm; 11-16, respectively. Emulsion type of FOE was oil in water emulsion.</p></div>","PeriodicalId":100063,"journal":{"name":"Agriculture and Agricultural Science Procedia","volume":"9 ","pages":"Pages 353-362"},"PeriodicalIF":0.0000,"publicationDate":"2016-01-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://sci-hub-pdf.com/10.1016/j.aaspro.2016.02.150","citationCount":"13","resultStr":"{\"title\":\"Enzymatic Synthesis of Bio-Surfactant Fructose Oleic Ester Using Immobilized Lipase on Modified Hydrophobic Matrix in Fluidized Bed Reactor\",\"authors\":\"Chusnul Hidayat, Kholifaturrosyidah Fitria, Supriyanto, Pudji Hastuti\",\"doi\":\"10.1016/j.aaspro.2016.02.150\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><p>Enzymatic synthesis of fructose oleic ester (FOE) in stirred tank reactor using the immobilized lipase may cause a physical damage of support matrix, which causes a leaching of lipase from matrix. The objective of this research was to evaluate the best condition of FOE synthesis in fluidized bed reactor (FBR) using the immobilized lipase on modified hydrophobic matrix. Surface of Amberlite IRA 96 was modified with 2-phenylpropionaldehyde to obtain hydrophobic surface. <em>Candida rugosa</em> lipase was immobilized on the modified matrix. Subsequently, it was used for FOE synthesis in FBR system. Factors, such as reaction time, substrate flow rate, amount of water adsorbent, and substrate molar ratio were evaluated based on the conversion of oleic acid into FOE. Results from FTIR analysis showed that modified matrix had a peak at a specific wavelength ∼1674 cm<sup>-1</sup>. It indicated that a group of imine (-C=N-) occurred after surface modification. The highest adsorption of lipase was obtained after adsorption for 45<!--> <!-->min (13.28±0.57<!--> <!-->mg lipase/g matrix), which was equivalent to 52.95±1.67%. The lipase activity was 73.66±5.35 U/g matrix. The best FOE synthesis condition was obtained at flow rate of 0.4<!--> <!-->mL/min, molecular sieve of 12%, substrate molar ratio (fructose: oleic acid) 1:4 for 48<!--> <!-->h. FOE was confirmed by TLC and FT-IR analysis, which they had <em>Rf</em> 0.72 and specific wave number of ∼1712 cm<sup>-1</sup>, respectively. FOE had emulsion capacity, emulsion stability, droplet size, and HLB value of 92.83±0.46%; 85.65±0.92%; 7.86±0.93<!--> <!-->μm; 11-16, respectively. Emulsion type of FOE was oil in water emulsion.</p></div>\",\"PeriodicalId\":100063,\"journal\":{\"name\":\"Agriculture and Agricultural Science Procedia\",\"volume\":\"9 \",\"pages\":\"Pages 353-362\"},\"PeriodicalIF\":0.0000,\"publicationDate\":\"2016-01-01\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"https://sci-hub-pdf.com/10.1016/j.aaspro.2016.02.150\",\"citationCount\":\"13\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Agriculture and Agricultural Science Procedia\",\"FirstCategoryId\":\"1085\",\"ListUrlMain\":\"https://www.sciencedirect.com/science/article/pii/S2210784316301504\",\"RegionNum\":0,\"RegionCategory\":null,\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"\",\"JCRName\":\"\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Agriculture and Agricultural Science Procedia","FirstCategoryId":"1085","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S2210784316301504","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
引用次数: 13
摘要
固定化脂肪酶在搅拌槽反应器中酶促合成果糖油酸酯(FOE)时,会对支撑基质造成物理损伤,导致脂肪酶从基质中浸出。研究了在改性疏水基质上固定化脂肪酶在流化床反应器(FBR)中合成FOE的最佳条件。用2-苯丙醛对Amberlite IRA 96进行表面改性,得到疏水表面。将念珠菌脂肪酶固定在改性基质上。随后,将其用于FBR系统中FOE的合成。考察了反应时间、底物流速、吸附剂用量、底物摩尔比等因素对油酸转化为FOE的影响。FTIR分析结果表明,改性后的基质在特定波长约1674 cm-1处有一个峰。结果表明,表面改性后产生了一组亚胺(- c =N-)。吸附45 min(13.28±0.57 mg脂肪酶/g基质)时,对脂肪酶的吸附率最高,相当于52.95±1.67%。脂肪酶活性为73.66±5.35 U/g基质。最佳合成条件为:流速0.4 mL/min,分子筛为12%,底物摩尔比(果糖:油酸)1:4,反应48 h。经TLC和FT-IR分析证实,其Rf值为0.72,比波数为~ 1712 cm-1。FOE的乳化容量、乳化稳定性、液滴大小、HLB值为92.83±0.46%;85.65±0.92%;7.86±0.93μm;分别为16。FOE的乳化液类型为油包水乳化液。
Enzymatic Synthesis of Bio-Surfactant Fructose Oleic Ester Using Immobilized Lipase on Modified Hydrophobic Matrix in Fluidized Bed Reactor
Enzymatic synthesis of fructose oleic ester (FOE) in stirred tank reactor using the immobilized lipase may cause a physical damage of support matrix, which causes a leaching of lipase from matrix. The objective of this research was to evaluate the best condition of FOE synthesis in fluidized bed reactor (FBR) using the immobilized lipase on modified hydrophobic matrix. Surface of Amberlite IRA 96 was modified with 2-phenylpropionaldehyde to obtain hydrophobic surface. Candida rugosa lipase was immobilized on the modified matrix. Subsequently, it was used for FOE synthesis in FBR system. Factors, such as reaction time, substrate flow rate, amount of water adsorbent, and substrate molar ratio were evaluated based on the conversion of oleic acid into FOE. Results from FTIR analysis showed that modified matrix had a peak at a specific wavelength ∼1674 cm-1. It indicated that a group of imine (-C=N-) occurred after surface modification. The highest adsorption of lipase was obtained after adsorption for 45 min (13.28±0.57 mg lipase/g matrix), which was equivalent to 52.95±1.67%. The lipase activity was 73.66±5.35 U/g matrix. The best FOE synthesis condition was obtained at flow rate of 0.4 mL/min, molecular sieve of 12%, substrate molar ratio (fructose: oleic acid) 1:4 for 48 h. FOE was confirmed by TLC and FT-IR analysis, which they had Rf 0.72 and specific wave number of ∼1712 cm-1, respectively. FOE had emulsion capacity, emulsion stability, droplet size, and HLB value of 92.83±0.46%; 85.65±0.92%; 7.86±0.93 μm; 11-16, respectively. Emulsion type of FOE was oil in water emulsion.