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Production of isoamyl acetate with candida antarctica lipase b (calb) as enzyme in a solvent-free system using miniaturised intensified reactor

Production of isoamyl acetate with candida antarctica lipase b (calb) as enzyme in a solvent-free system using miniaturised intensified reactor / Sathiswaran Sangaran
Isoamil acetat adalah salah satu ester yang mempunyai kewangian sama dengan buah pisang. Isoamil acetat selalunya digunakan sebagai perasa tambahan khasnya dalam industry pemakanan. Pada zaman dahulu, kajian tentang isoamil acetat telah dilakukan secara tradisional, iaitu menggunakan kaedah pengestrakan ester diikuti dengan penghasilan isoamil acetat dengan proses tindak balas kimia. . Kini, proses esterifikasi telah berkembang maju kearah penghasilan isoamyl acetat dengan menggunakan pemangkin. Hal ini kerana, pelanggan lebih suka akan isoamyl acetat yang dihasilkan dengan proses semula jadi berbanding dengan proses tindak balas kimia. Selain itu, process intensifikasi juga sedang menjadi popular dalam kalangan penyelidik. Hal ini kerana proses intensifikasi boleh dilakukan dalm reactor miniatur yang mempunyai kelebihan untuk menghasilkan isoamil acetat yang berkualiti dalam masa yang singkat berbanding reactor kontemporari. Oleh itu, eksperimen ini telah dikhususkan untuk megkaji penghasilan isoamyl acetat dengan menggunakan pemangkin Candida antarctica Lipase B (CALB) dalam reactor miniatur. Faktor factor yang memberi impak kepada penghasilan isoamil acetat telah dikaji seperti suhu tindak balas, nisbah asid-alkohol dan penggunaan pemangkin dalam proses esterifikasi. Faktor-faktor tersebut dikaji menggunakan kaedah penkajian satu–faktor-pada-suatu-masa (OFAT). Tambahan pula, process pengoptimuman pun telah dilakukan menggunakan Kaedah Sambutan Permukaan (KSP). Keputusan menunjukkan bahawa Kaedah OFAT lagi tepat daripada kaedah KSP. _______________________________________________________________________________________________________ Isoamyl acetate is a type of ester that has similar fragrance to banana. It is widely being used as banana flavouring in food industries. Initially, isoamyl acetate was extracted using tradition method from plants and fruits, and then followed by chemical synthesis. Over the time, the esterification process is conducted using enzyme because consumers highly prefer naturally synthesized ester compared to chemically synthesized ester. On the other hand, lately process intensification is gaining momentum among the researchers. This is because the maximum conversion and yield can be achieved in shorter time in miniaturised intensified reactors compared to the large conventional reactors. Thus this study is conducted to investigate the performance of isoamyl acetate production using enzyme Candida antarctica Lipase B (CALB) in miniaturised intensified reactors. The effect of operating parameters such as reaction temperatures, acid-alcohol ratio and presence of enzyme on the final concentration and conversion of isoamyl acetate produced was studied using One-Factor-At-A-Time (OFAT) method and also Response Surface Methodology (RSM) to optimise the results. The results of OFAT show that it is more reliable than RSM method because the regression coefficient value is very closer to unity which is more than 0.91. The optimum operating condition obtained through OFAT is 50⁰C for temperature and 0.6 for acid-alcohol ratio. The optimum temperature with enzyme is 40⁰C.
Primary Item Type:
Final Year Project
Identifiers:
Accession Number : 875007565
Language:
English
Subject Keywords:
Isoamyl acetate; fragrance; banana
First presented to the public:
6/1/2018
Original Publication Date:
7/18/2018
Previously Published By:
Universiti Sains Malaysia
Place Of Publication:
School of Chemical Engineering
Citation:
Extents:
Number of Pages - 102
License Grantor / Date Granted:
  / ( View License )
Date Deposited
2018-07-31 15:38:34.087
Date Last Updated
2019-01-07 11:24:32.9118
Submitter:
Mohd Jasnizam Mohd Salleh

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Production of isoamyl acetate with candida antarctica lipase b (calb) as enzyme in a solvent-free system using miniaturised intensified reactor1 2018-07-31 15:38:34.087