Browsing by Author "Abdul Rahman R.N.Z.R."
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Publication Biocatalytic production of lactose ester catalysed by mica-based immobilised lipase(2012) ;Zaidan U.H. ;Abdul Rahman M.B. ;Othman S.S. ;Basri M. ;Abdulmalek E. ;Abdul Rahman R.N.Z.R. ;Salleh A.B. ;Faculty of Science and Technology ;Universiti Putra Malaysia (UPM) ;Malaysia Genome InstituteUniversiti Sains Islam Malaysia (USIM)Enzyme immobilisation technology is an effective means to improve sugar ester production through the employment of biocatalysts. In the present study, immobilisation of Candida rugosa (CRL) lipase onto amino-activated mica is performed via covalent bonding (namely Amino-CRL) and the cross-linking of lipases into nano-reactors through physical adsorption (namely NER-CRL). Free and immobilised lipases were tested for their esterification activities. Specific activities for Amino-CRL and NER-CRL increased by 2.4 and 2.6-fold, respectively, upon immobilisation. Extending this work, immobilised lipases have novel capabilities in the synthesis of sugar esters. The optimised conditions for sugar fatty acid ester syntheses are 48 h at 2:1 of molar ratio of lactose sugar to capric acid at 55 �C. Furthermore, a high operational stability with half-lives of over 13 and 10 runs was achieved for NER-CRL and Amino-CRL, respectively, indicating the efficiency of the immobilisation process. � 2011 Elsevier Ltd. All rights reserved. - Some of the metrics are blocked by yourconsent settings
Publication Kinetics of enzymatic synthesis of liquid wax ester from oleic acid and oleyl alcohol(Japan Oil Chemists Society, 2010) ;Radzi S.M. ;Mohamad R. ;Basri M. ;Salleh A.B. ;Ariff A. ;Rahman M.B.A. ;Abdul Rahman R.N.Z.R. ;Faculty of Science and Technology ;Universiti Putra Malaysia (UPM)Universiti Sains Islam Malaysia (USIM)The kinetics of wax ester synthesis from oleic acid and oleyl alcohol using immobilized lipase from Candida antartica as catalyst was studied with different types of impeller (Rushton turbine and AL-hydrofoil) to create different mixing conditions in 2l stirred tank reactor. The effects of catalyst concentration, reaction temperature, and impeller tip speed on the synthesis were also evaluated. Rushton turbine impeller exhibited highest conversion rate at lower impeller tip speed as compared to AL-hydrofoil impeller. A second-order reversible kinetic model from single progress curve for the prediction of fractional conversion at given reaction time was proposed and the corresponding kinetic parameter values were calculated by non-linear regression method. The results from the simulation using the proposed model showed satisfactory agreement with the experimental data. Activation energy shows a value of 21.77 Kcal/mol. The thermodynamic parameters of the process, enthalpy and entropy, were 21.15 Kcal/mol and 52.07 cal/mol.K, respectively. � 2010 by Japan Oil Chemists' Society.