• Biotechnology and Bioprocess Engineering:BBE
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• 제9권4호
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• pp.245-251
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• 2004

The fungal species of Rhizopus oryzae 2062 has the capacity to carry out a single stage fermentation process for lactic acid production from potato starch wastewater. Starch hydrolysis, reducing sugar accumulation, biomass formation, and lactic acid production were affected with variations in pH, temperature, and starch source and concentration. A growth condition with starch concentration approximately 20 g/ L at pH 6.0 and 30$^{\circ}C$ was favourable for starch fermentation, resulting in a lactic acid yield of 78.3%∼85.5% associated with 1.5∼2.0 g/L fungal biomass produced in 36 h of fermentation.

• 한국의류학회지
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• 제22권7호
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• pp.843-850
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• 1998

The purpose of this study is the investigation of chemical properties of wool treated with oxidants and protease at low temperature. The chemical degradation of the fibers were investigated by measuring $\alpha$-amimo acid contents and FT-IR analysis. In addition, urea-hydrogensulfite solubility was measured to compare to the oxidation and protease treated wool. The results were as follows. 1) By the oxidation of wool, cystine is oxidised to cysteic acid by way of the intermediate oxides, cystine-S-monooxide and cystine-S-dioxide, in the case hydrolysis catalysed by the protease catalyse. Also, $\alpha$-amimo acid contents is increased, and urea-hydrogensulfite solubility was lower than that of untreated wool. This chemical degradation of wool was occurred due to oxidate hydrolysis in the order of permonosulfate>dichloroisocyanuric acid$\geq$chlorine. 2) The chemical degradation of wool was accelerated by the protease treatment of oxidized wool. Oxidation of wool is considered to make the fiber more susceptibled to enzymatic attact by opening disulphide bond within wool. Enzymatic attact was effectively directed to the wool oxidised by permonosulfate.

• Journal of the Korean Wood Science and Technology
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• 제42권2호
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• pp.183-192
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• 2014

For the structure determination of D-(+)-sucrose, which consists of ${\alpha}$-D-(+)-glucose and ${\beta}$-D-(+)-fructose, it was acetylated with acetic anhydride and triethyl amine, pyridine, zinc chloride, and sodium acetate as catalysts. The acetylated D-(+)-sucrose was acid-hydrolyzed using sulfuric acid and sodium chloride in methanolic solution. The structures of the reaction products were determined by $^1H$-NMR and $^{13}C$-NMR spectra. The yield of the acetylation indicated the high value in zinc chloride as 70% in zinc chloride catalyst. The acid-hydrolyzed product of the acetylated D-(+)-sucrose, 2,3,4,6,1',3',4',6'-octa-O-acetyl-D-(+)-sucrose, gave 2,3,4,6-tetra-O-acetyl-${\beta}$-D-(+)-glucose and it suggests that the acetylated D-(+)-sucrose was rearranged through the formation of oxonium ion by mutarotation in the 2,3,4,6-tetra-O-acetyl-${\alpha}$-D-(+)-glucose moiety and through the ring opening in the 1',3',4',6'-tetra-O-acetyl-${\beta}$-D-(+)-fructose moiety.

• Journal of Microbiology and Biotechnology
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• 제11권3호
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• pp.452-457
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• 2001

The glutaryl 7-aminocephalosporanic acid (glutaryl 7-ACA) acylase was purified from Pseudomonas diminuta KAC-1 cells isolated from soil, and characterized. The acylase was purified by procedures including ammonium sulfate fractionation and column chromatographies on DEAE-Sepharose, Phenyl-Sepharose, Q-Sepharose, and Superose 12H/R. The negative acylase was found to be composed of two subunits with molecular masses of approximately 55 kDa and 17 kDa, respectively. The isoelectric point of the enzyme was 4.0. The specific activities of the purified acylase were 8.0 and 7.0 U/mg on glutaryl 7-ACA and glutaryl 7-aminodesacetoxy cephalosporanic acid (glutaryl 7-ADCA), respectively, and $K_m$ values were 0.45 mM for glutaryl 7-ADCA and 0.67 mM for glutaryl 7-ADCA. The enzyme had a pH optimum at 8.0 and a tmperature optimum at $40^{\circ}C$. The acylase catalyzed the synthesis of glutaryl 7-ACA from glutaric acid and 7-ACA as well as the hydrolysis of glutaryl 7-ADCA, although the reaction rate of the synthesis was slower than that of the hydrolysis. In addition, it was found that the enzyme had a glutaryl transferase activity, thereby transferring the glutaryl group from one cephalosporin nucleus to another.

• Bulletin of the Korean Chemical Society
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• 제13권1호
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• pp.5-6
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• 1992

• Bulletin of the Korean Chemical Society
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• 제17권10호
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• pp.967-969
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• 1996

• 한국생물공학회:학술대회논문집
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• 한국생물공학회 2002년도 생물공학의 동향 (X)
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• pp.228-231
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• 2002

Itaconic acid has been produced during the cutivation of Aspergillus terreus DSMZ 5770 by using several starchs as carbon sources. The starchs were pretreated by partial hydrolysis with some acids at various pH conditions. The highest yield for the production of itaconic acid has been found when rice starch was pretreated by sulfonic acid at pH 2.5 and utilized for the cultivation. Using the results from shaker fermentation A. terreus has been cultivated in 2.5 L bioreactor for the production of itaconic acid and its on-line monitoring.

• KSBB Journal
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• 제22권4호
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• pp.201-206
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• 2007

농산 폐자원 및 견과류 껍질의 산 가수분해를 통하여 L-arabinose를 생산하기 위한 최적조건의 결정에 대한 연구를 수행하였다. 다양한 원료들을 분말로 제조하여 희석된 황산으로 가수분해 시킨 결과 corn fiber에서 arabinose가 가장 많이 생성되어, 이를 원료로 선정하였다. Corn fiber로부터 arabinose를 생성하기 위한 산 가수분해 반응의 최적조건은 0.4%의 황산으로 130$^{\circ}C$에서 60분간 처리하는 것이며, arabinose의 생성 수율은 기질의 농도가 낮을수록 증가하였으나 생성농도는 기질의 농도가 높을수록 증가하였다. 최종적으로 90 g/L의 corn fiber를 최적조건에서 산 가수분해 시킨 결과 20.1 g/L의 glucose, 10.1 g/L의 xylose, 7.8 g/L의 arabinose 및 1.8 g/L의 galactose가 생성되었다. 산 가수분해 용액을 암모니아수로 pH를 5.5로 조정하고 C. tropicalis를 접종하여 배양한 결과 7.6 g/L의 arabinose, 0.6 g/L의 xylose, 0.5 g/L의 xylitol 및 0.5 g/L의 galactose만이 존재하였다. 이는 효모의 배양에 의하여 당 혼합물로부터 L-arabinose의 비율을 증가시킬 수 있다는 것을 보여주었다. 막 여과에 의하여 고형물을 제거시킨 배양액에 activate carbon을 처리하여 organic contaminants와 색소를 제거하고 양이온과 음이온 교환 수지를 통과시켜 이온물질들을 제거시킨 후에 농축시켜 3.1 g의 L-arabinose의 분말을 얻었다.

• Korean Chemical Engineering Research
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• 제48권6호
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• pp.747-751
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• 2010

본 연구에서는 아임계 수 가수분해 공정을 이용하여 동결건조 된 미역(Undaria pinnatifida)으로부터 아미노산 생산 조건 및 생성된 물질의 특성에 대하여 고찰하였다. 가수분해 장치는 회분식으로 설계 되었으며, 반응기는 내경 4.6 cm, $200cm^3$ 부피 용량의 Hastelloy 276 강으로 제작된 것을 사용하였다. 반응기 내부에는 교반기가 부착되어 100 rpm으로 연속적으로 교반되도록 하였다. 시료는 동결건조 된 미역 파우더와 회수율 향상을 위해 부가된 1% acetic acid를 촉매로 한 반응용액을 1:100(w/v) 비율로 혼합시켜 반응을 진행시켰다. 반응물질의 혼합을 위해 100 rpm으로 일정하게 교반하였으며, 반응온도와 압력 변화에 따른 아미노산 생성 회수율을 고찰하였다. 실험조건은 온도 $180{\sim}374^{\circ}C$, 반응시간 1시간이었다. 총 아미노산 함량은 고온의 조건에 비해 저온에서 높은 함량을 나타내었으며 분자량이 작은 아미노산(glycine, alanine, serine 등)이 분자량이 큰 아미노산들보다 높은 함량을 나타내었다. 아미노산의 최대 회수율($290.84{\mu}g/mL$)은 $220^{\circ}C$, 촉매 첨가조건에서 분석되었다.

• 한국식품과학회지
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• 제28권3호
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• pp.521-527
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• 1996

세 품종의 강낭콩 전분에 대하여 분자구조적 측면에서 그 특성을 조사하였다. 전분의 아밀로오스 함량과 ${\beta}$-아밀라아제 분해한도는 Pink종이 다른 종에 비하여 다소 높았다. 그리고 아밀로펙틴의 사슬분포는 ${\overline{DP}$60 이상의 초장사슬, ${\overline{DP}}45{\sim}60$인 B 사슬, 그리고 ${\overline{DP}}10{\sim}20$인 A 사슬로 분포하였으며, 그 분포도는 품종별로 차이를 보였는데, Pink종은 B사슬, Red종은 초장사슬, 그리고 White종은 A 사슬이 다른 종에 비하여 더 많이 분포하였다. 전분의 딴 가수분해(2.2N HCI는 3 단계로 일어났으며, 각 품종간에는 가수분해 속도와 요오드 반응에서 다소 차이를 보였다. 전분은 산처리에 따라 아밀로오스와 무정형인 아밀로펙틴의 ${\alpha}$-1.6 결합이 점차 분해되어, 결국은 결정성을 가진 ${\overline{DP}}$ 20 정도의 사슬로 남았다. 이러한 결과로부터 강낭콩은 품종에 따라 전분의 분자구조가 다름을 알 수 있었다.