• KSBB Journal
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• v.8 no.4
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• pp.313-319
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• 1993

Methyl fructoside was synthesized from sucrose and methanol using an immobilized invertase. The enzyme was covalently bound by glutaraldehyde on porous silica coated with polyethyleneimine to give loading capacity of 120mg of invertase per one gram of dry porous silica and effective activity of 100U per one milligram of bound invertase. Polyethyleneimine coating imparted a hydrophillic character, good activity retention and high loading capacity to the surface of porous silica as well as hydrophillic microenviroment in the vicinity of bound invertase. The immobilized enzyme was formed into an alginate-enclosed silica bead to have enough activity for methyl fructoside synthesis from aqueous methanol-sucrose solution. Using the alginate-enclosed biocatalyst the yield of methyl fructoside was obtained as high as 55.9% from aqueous 30% (v/v) methanol and 0.291mo1/l sucrose with 2U/ml activity at $25^{\circ}C$, pH 4.8.

• 한국신재생에너지학회:학술대회논문집
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• 2005.11a
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• pp.688-688
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• 2005

• Journal of Life Science
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• v.21 no.1
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• pp.127-133
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• 2011

${\beta}$-Galactosidase was immobilized on chitosan bead by covalent bonding using glutaraldehyde. The characteristics of the immobilized enzyme were investigated. Maximum immobilization yield of 75% was obtained on chitosan bead. Optimum pH and temperature for the immobilized enzyme was 7.0 and $50^{\circ}C$, respectively. The immobilized enzyme showed a broader range of pH and temperature compared to a free one. A mathematical model for the operation of the immobilized enzyme in a packed-bed reactor was established and solved numerically. Under different inlet lactose concentrations and feed flow rate conditions, lactose conversion was measured in a packed-bed reactor. The experimental results of continuous operation in a packed-bed reactor were compared to theoretic results using Michaelis-Menten kinetics with competitive product inhibition and external mass transfer resistance. The model predicted the experimental data with errors less than 5%. Process optimization of continuous operation in a packed-bed reactor was also conducted. In a recirculation packed-bed operation, conversion of lactose was 97% in 3 hours. In a continuous packed-bed operation, the effect of flow rate and initial lactose concentration was investigated. Increasing flow rates and initial lactose concentration decreased the conversion of substrate.

• KSBB Journal
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• v.8 no.4
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• pp.307-312
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• 1993

A fructosyltransferase from Aureobasidium pullulans was immobilized onto a polystyrene-type anionic ion-exchange resin and the production of fructo-oligosaccharides was Investigated by the immobilized enzyme. The optimum pH and the temperature of immobilized enzyme were found to be pH 5.0, $55^{\circ}C$ respectively. The thermal stability of the enzyme was greatly enhanced after immobilization. The reaction profiles of the immobilized enzyme was almost identical to those of the free cells and the soluble enzyme. The immobilized enzymes were stable up to 20 cycles without loss of initial activity in a repeated-batch operation $50^{\circ}C$.

• Applied Chemistry for Engineering
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• v.25 no.6
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• pp.619-623
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• 2014

The acid hydrolysis and enzymatic saccharification were carried out for the production of cellulosic ethanol. The possibility of bio-energy production from tangerine peel and apple and watermelon rind was evaluated by determining the optimum production condition. The optimum conditions for the production of cellulosic ethanol from fruit peel were as follows: the sulfuric acid concentration and reaction time of acid hydrolysis for the ethanol production from an apple rind were 20 wt% and 90 min, respectively. The concentration of sulfuric acid for tangerine peel and a watermelon rind at the hydrolysis time of 60 min were 15 wt% and 10 wt%, respectively. A viscozyme was proven as the best conversion for the ethanol production when using enzymatic saccharification from fruit peels. The optimum enzymatic saccharification time for tangerine peel and apple and watermelon rind were 60, 180, and 120 min, respectively.

• The Microorganisms and Industry
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• v.13 no.3
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• pp.28-29
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• 1987

산업화 정책에 힘입어 각 분야의 산업이 크게 발전하였으며 피혁공업도 비약적으로 성장하여 1987년 현재 가죽처리 능력(소가죽 기준)이 1000-1200만매 수준에ㅔ 이르게 되었고, 공장규모도 커져 1000매/일~4000매/일의 처리능력을 갖춘 공장이 20가사 이상이 되며 새로운 공업단지내에 집단화 되어 존재하는데 반원공단에 집단피혁가공단지가 대표적이다. 피혁공업은 가공수출로 외화획득에 크게 기여하고 있는데 주요 원자재의 해외의존도가 높을 뿐만 아니라 피혁공정에 사용되는 자재의 수입의존도도 크며 이중 효소제제는 거의 수입에 의존하고 있어 이효소제제의 국산화가 시급한 실정이다.

• Microbiology and Biotechnology Letters
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• v.20 no.4
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• pp.437-444
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• 1992

An innovative process for high fructose corn syrup (HFCS) production coupled with direct saccharification of raw corn starch in the agitated bead enzyme reactor (bioattitor) was investigated. The required high concentration/purity of glucose solution suitable for isomerization was produced directly in a bioattritor. without condensation of hydrolyzate, 398 g glucose/$\ell$ and 98% glucose content from 400 g/$\ell$ (w/v) of raw corn starch after 24 hours. The unsaccharified residual starch could be separated easily upon centrifugation, and resaccharified. The obtained solution also possessed other desirable requirements as substrate for isomerization, such as. low concentrations of denatured protein and calcium ions, thereby, simplified the purification step. The obtained glucose solution was isomerized in an enzyme reactor paked with immobilized glucose isomerase to evaluate the suitability as a substrate. The proposed new HFCS process seems to have many advantages over the conventional process via liquefaction-saccharification steps. The follow-up investigations of the proposed process need to be conducted to evaluate the feasibility of industrial application.

• Proceedings of the Korean Environmental Sciences Society Conference
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• 2016.10a
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• pp.132-132
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• 2016

• Journal of Korean Society of Environmental Engineers
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• v.39 no.11
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• pp.607-612
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• 2017

The effect of carbonic anhydrase on $CO_2$ absorption rates and the heat of reaction were evaluated in various amine solutions for post combustion $CO_2$ capture process. The $CO_2$ absorption rate was analyzed in 30 wt% MEA, AMP, DMEA, MDEA aqueous solutions with and without carbonic anhydrase (250 mg/L) from bovine erythrocyte. $CO_2$ absorption rates were increased in all solutions with carbonic anhydrase. The effect of carbonic anhydrase on absorption rates was more in tertiary amine (DMEA and MDEA) solutions than in primary amine (MEA) and hindered amine (AMP) solutions. The heat of reaction of MEA, DMEA, MDEA aqueous solutions with and without carbonic anhydrase were measured using reaction calorimeter. Carbonic anhydrase decreased the heat of absorption in all solutions. The results suggested that tertiary amines that have the excellent desorption ability were suitable for applying carbonic anhydrase to the post combustion $CO_2$ capture process and the effect of carbonic anhydrase was best in MDEA solution.

• Korean Journal of Fisheries and Aquatic Sciences
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• v.32 no.1
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• pp.83-87
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• 1999

Immobilization of amyloglucosidase (AMG) with chitosan microbead and its possible applications were evaluated. The diameter of chitosan inicrobead was about 1.2 mm and the optimum enzyme concentration for immobilization was 6 mg/ml. The relative activity of the immobilized enzyme was $97.8\%$ at pH 4.2 and $55^{\circ}C$ and the optimum condition for the immobilized enwme was the same to that of free enzyme. In case of temperature above $30^{\circ}C$, the activity of the immobilized enzyme was a little higher than that of free enzyme. The enzyme activities of both free and immobilized were stable for 6 months when stored at $35^{\circ}C$. The optimum temperatures of both enzymes for saccharification of the dextrinized starch were $55^{\circ}C$ while the relative activity of the immobilized enzlme was $62.6\%$.