2000
DOI: 10.1016/s0141-0229(99)00149-0
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Optimization of isoamyl acetate production by using immobilized lipase from Mucor miehei by response surface methodology

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Cited by 103 publications
(53 citation statements)
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“…Various enzyme sources either in the form of free lipases [19,20] or immobilized lipases [9,21] have been used for production of flavor acetates in organic solvents. The effect The esterification reaction was carried out using alcohol/acid molar ratio of 1.6 with 100 g/l of mycelium bound lipase.…”
Section: Discussionmentioning
confidence: 99%
“…Various enzyme sources either in the form of free lipases [19,20] or immobilized lipases [9,21] have been used for production of flavor acetates in organic solvents. The effect The esterification reaction was carried out using alcohol/acid molar ratio of 1.6 with 100 g/l of mycelium bound lipase.…”
Section: Discussionmentioning
confidence: 99%
“…The positive effect of enzyme concentration on the synthesis of butyric ester is in agreement with the reports of other authors dealing with the production of favour esters (ethyl hexanoate, isoamyl isovalerate, isoamyl acetate) using microbial lipases. 24,27,28 At a temperature of 30 ºC, the highest ester concentrations were found with a butyric acid concentration ranging from 0.3 to 0.7 mol L -1 and an enzyme concentration between 0.015 and 0.025 g mL -1 , respectively. At a temperature of 50 ºC, the highest values for ester concentration were found in the range from 0.5 to 0.9 mol L -1 with an enzyme concentration from 0.015 to 0.025 g mL -1 .…”
Section: Model Fitting 2 3 Central Composite Rotatable Design (Ccrd)mentioning
confidence: 99%
“…The initial water content (0.1-0.9% w/v), reaction temperature (25-65ºC), enzyme loading (16-60 mg g -1 ), acid/alcohol molar ratio (1:2-5:2) and time of addition of molecular sieves (0-20 hrs) were the variables investigated. These variables were chosen based on the results obtained in a preliminary study and are the most commonly used for modeling esterification reactions (Krishna et al 2000;Chiang et al 2003;Knežević-Jugović et al 2008).The ester yield in mol% (Y%) was taken as the response variable.…”
Section: Esterification Reaction In a Batch Reactor Systemmentioning
confidence: 99%
“…Besides, the same flavor and fragrance esters prepared by enzymatic synthesis may be labeled as "natural" (Gillies et al 1987). Consequently, lipases have been extensively employed for direct esterification and transesterification reactions in both non-aqueous and solvent-free systems to produce esters of shortchain aliphatic carboxylic acids and alcohols such as isoamyl acetate, and butyl acetate (Krishna et al 2000;Ozyilmaz and Gezer, 2010); ethyl butyrate, butyl butyrate and butyl isobutyrate (Yadav and Lathi, 2003;Santos and Castro, 2006;Pires-Cabral et al 2007), ethyl valerate (Ozyilmaz and Gezer, 2010). However, the synthesis of esters of medium-chain fatty acids and monohydric alcohols including amyl caprylate here investigated, has received lesser attention in the literature (Vaidya et al 2008).…”
Section: Introductionmentioning
confidence: 99%