• Biotechnology and Bioprocess Engineering:BBE
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• 제8권3호
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• pp.205-209
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• 2003

Solubilization of domestic household waste through Steam explosion with Subsequent ethanol production by the microbial saccharifitation and fermentation of the exploded product was studied. The effects of steam explosion on the changes of the density, viscosity, pH, and amounts of extractive components in artificial household waste were determined. The composition of artificial waste used was similar to leftover waste discharged from a typical home in Japan. Consecutive microbial saccharification and fermentation, and simultaneous microbial saccharification and fermentation of the Steam-exploded product were attempted using Aspergillus awamori, Trichoderma viride, and Saccharomyces cerevisiae; the ethanol yields of each process were compared. The highest ethanol yield was obtained with simultaneous microbial saccharification and fermentation of exploded product at a steam pressure of 2 MPa and a steaming time of 3 min.

• Journal of Ginseng Research
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• 제31권4호
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• pp.191-195
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• 2007

Red ginseng sikhye is one of Korean unique beverages with the addition of effective ingredients of ginseng. Considering economical and mechanical efficiency and quality of sikhye, the optimum conditions for saccharification is to saccharify at 90 degree celsius for 3 hours in the composition of 4% of malt, 20% of steamed rice, and 6% of red ginseng power. The red ginseng sikhye has high soluble solid content over 33% compared with conventional commercial sikhye. On the other hand, ginseng sikhye, which shows low pH, has more or less higher acidity than conventional commercial one. Especially the turbidity of the red ginseng sikhye is much higher than that of commercial sikhye, due to as high amount of rice as 20% compared with 3% in the commercial one. The use of high quantity of rice affected the level of turbidity in red ginseng sikhye. In this study, we wanted to establish optimum conditions for saccharification in manufacturing red ginseng sikhye which contains effective herbal medicinal ingredients maintaining the original taste of traditional sikhye.

• 펄프종이기술
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• 제42권5호
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• pp.15-23
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• 2010

Bio-ethanol is the most potential next generation automotive fuel for reducing both consumption of crude oil and environmental pollution from renewable resources such as wood, forest residuals, agricultural leftovers and urban wastes. Lignocellulosic based materials can be broken down into individual sugars. Therefore, saccharification is one of the important steps for producing sugars, such as 6-C glucose, galactose, mannose and 5-C xylose, mannose and rhamnose. These sugars can be further broken down and fermented into ethanol. The main objective of this research is to study the feasibility and optimize saccharification and fermentation process for the conversion of lignocellulosic biomass to low cost bioethanol.

• 공업화학
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• 제26권4호
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• pp.511-514
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• 2015

차세대 바이오에탄올로 주목받고 있는 목질계 바이오매스를 이용한 셀룰로오스 에탄올 생산과정은 셀룰로오스를 단당류로 분해하는 전처리과정이 가장 중요한 역할을 한다. 본 연구에서는 산가수분해와 효소당화과정을 이용하여 볏짚, 톱밥, 복사지, 신문지 등과 같은 목질계 바이오매스로부터 셀룰로오스에탄올을 제조하였다. 전처리과정으로 10~30 wt% 황산을 이용한 산가수분해($100^{\circ}C$, 1 h), celluclast ($55^{\circ}C$, pH = 5.0), AMG ($60^{\circ}C$, pH = 4.5), spirizyme ($60^{\circ}C$, pH = 4.2)을 이용한 효소당화과정(30 min), 산가수분해 후 효소당화과정을 비교하였다. 전처리과정의 수율은 hybrid 과정 > 산가수분해 > 효소당화 순으로 셀룰로오스 에탄올로의 전환이 잘 이루어지는 것으로 나타났으며, 최적 발효시간은 2일이었다. 또한 20 wt% 황산을 이용한 산가수분해 후 celluclast를 이용하여 효소당화를 수행할 경우 톱밥 > 볏짚 > 복사지 > 신문지 순으로 셀룰로오스 에탄올 전환특성이 높게 나타났다.

• KSBB Journal
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• 제30권6호
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• pp.332-338
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• 2015

The objective of this study was designed to determine the possibility of bioethanol production from wasted medium density fiberboard (wMDF). We were investigated the enzymatic saccharification characteristics using the enzyme (Cellic CTec3) after pretreatment with sodium chlorite. According to the component analysis results, the lignin contents before and after the pretreatment of wMDF (milling using sieve size of $1,000{\mu}m$) was significantly reduced from 31.13% to 4.11%. Therefore, delignification ratio of pretreated wMDF was found to be up to about 87-89% depending on the sieve size. And we were tested to compare the saccharification ratio according to the sieve size of wMDF ($1,000{\mu}m$, $200{\mu}m$), but it was no significance depending on the sieve size. When enzyme dosage was 5% based on the substrate concentration, enzymatic saccharification ratio was obtained up to 70% by maintaining at $50^{\circ}C$ for 72 hours. We could made the substrate concentration of pretreated wMDF ($1,000{\mu}m$) up to 12% and then enzymatic saccharification ratio was 76.8%, also contents of glucose and xylose were analyzed to 77,750 and 14,637 mg/L, respectively.

• 한국식품조리과학회지
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• 제14권1호
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• pp.91-96
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• 1998

맥아제조(15$^{\circ}C$)시 amylase 활성이 가장 높은 1.5배~2.0배(1.20 cm-1.95 cm)의 잎눈 길이는 9일 째에 관찰되었고, 엿기름의 추출시간에 따른 총당과 환원당은 3시간 30분에 2.33%, 1.61%로 가장 높았고 4시간에는 다소 감소하였으며, 굴절당도계로 측정한 당도와 amy- lase 활성도 3시간 30분에 3.4 brix(%), 28,332 units로 같은 양상을 보였다. 당화과정 중 당화초기에서 8시간까지 변화를 보면 총당은 멥쌀의 경우 3.90%에서 9.27%로, 찹쌀의 경우 4.19%에서 11.91%로 증가하였고 환원당도 멥쌀의 경우 3.30%에서 7.61%로, 찹쌀의 경우 3.31%에서 9.11%로 각각 증가하였다 Brix도 멥쌀의 경우 3.6 brix(%)에서 10.8 brix(%)로, 찹쌀의 경우 3.6 brix(%)에서 12.8 brix(%)로 당화시간이 증가할수록 증가하였다. amylase 활성은 당화시간이 증가할수록 감소하는 경향을 보였고 pH는 서서히 감소하다가 4시간 이후에는 거의 변화가 없었다. 식혜밥알의 형태는 당화시간이 증가할수록 가수분해되어 전분립이 빠져 나와 구멍이 점점 크게 나타남을 볼 수 있었다.

• 한국식품과학회지
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• 제29권3호
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• pp.470-475
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• 1997

식혜 제조시 쌀 품종에 따른 당도의 변화를 조사하기 위하여 45종의 쌀 품종을 사용하였을 때 당화 10시간 후의 당도가 $9.0{\sim}11.1\;Brix$로 품종간에 차이를 나타내었다. 간척과 신금오, 서안, 계화 등을 이용시 당도가 높게 나타났으며, 상주, 남원, 영덕, 오봉 등은 당도가 상대적으로 낮았다. 간척과 상주품종을 비교하면 식혜제조시 당화 10시간에 약 19%의 당도 차이가 있었다. 쌀 품종 간척을 이용한 식혜의 HPLC분석에 의한 주요 당 조성은 fructose 3.6%, glucose 9.8%, maltose 78.3%, maltotriose 8.3%이었다. 육조 맥아와 이조 맥아를 이용한 당화력의 차이는 육조 맥아를 100 메쉬로 분쇄하여 사용시 이조 맥아보다 높았다. 육조 맥아의 당화 최적온도는 $60^{\circ}C$이었으며, 밥과 맥아 추출물의 비를 1:8로 하였을 때 맥아 첨가량 25% 추출물에서 당화력이 가장 높았다.

• Journal of Microbiology and Biotechnology
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• 제29권4호
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• pp.625-632
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• 2019

The unified saccharification and fermentation (USF) system was developed for direct production of ethanol from agarose. This system contains an enzymatic saccharification process that uses three types of agarases and a fermentation process by recombinant yeast. The $pGMF{\alpha}-HGN$ plasmid harboring AGAH71 and AGAG1 genes encoding ${\beta}-agarase$ and the NABH558 gene encoding neoagarobiose hydrolase was constructed and transformed into the Saccharomyces cerevisiae 2805 strain. Three secretory agarases were produced by introducing an S. cerevisiae signal sequence, and they efficiently degraded agarose to galactose, 3,6-anhydro-L-galactose (AHG), neoagarobiose, and neoagarohexose. To directly produce ethanol from agarose, the S. cerevisiae $2805/pGMF{\alpha}-HGN$ strain was cultivated into YP-containing agarose medium at $40^{\circ}C$ for 48 h (for saccharification) and then $30^{\circ}C$ for 72 h (for fermentation). During the united cultivation process for 120 h, a maximum of 1.97 g/l ethanol from 10 g/l agarose was produced. This is the first report on a single process containing enzymatic saccharification and fermentation for direct production of ethanol without chemical liquefaction (pretreatment) of agarose.

• Biotechnology and Bioprocess Engineering:BBE
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• 제10권1호
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• pp.52-59
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• 2005

The study was targeted to saccharify foodwastes with the cellulolytic and amylolytic enzymes obtained from culture supernatant of Trichoderma harzianum FJ1 and analyze the kinetics of the saccharification in order to enlarge the utilization in industrial application. T. harzianum FJ1 highly produced various cellulolytic (filter paperase 0.9, carboxymethyl cellulase 22.0, ${\beta}$-glucosidase 1.2, Avicelase 0.4, xylanase 30.8, as U/mL-supernatant) and amylolytic (${alpha}$-amylase 5.6, ${\beta}$-amylase 3.1, glucoamylase 2.6, as U/mL-supernatant) enzymes. The $23{\sim}98\;g/L$ of reducing sugars were obtained under various experimental conditions by changing FPase to between $0.2{\sim}0.6\;U/mL$ and foodwastes between $5{\sim}20\%$ (w/v), with fixed conditions at $50^{\circ}C$, pH 5.0, and 100 rpm for 24 h. As the enzymatic hydrolysis of foodwastes were performed in a heterogeneous solid-liquid reaction system, it was significantly influenced by enzyme and substrate concentrations used, where the pH and temperature were fixed at their experimental optima of 5.0 and $50^{\circ}C$, respectively. An empirical model was employed to simplify the kinetics of the saccharification reaction. The reducing sugars concentration (X, g/L) in the saccharification reaction was expressed by a power curve ($X=K{\cdot}t^n$) for the reaction time (t), where the coefficient, K and n. were related to functions of the enzymes concentrations (E) and foodwastes concentrations (S), as follow: $K=10.894{\cdot}Ln(E{\cdot}S^2)-56.768,\;n=0.0608{\cdot}(E/S)^{-0.2130}$. The kinetic developed to analyze the effective saccharification of foodwastes composed of complex organic compounds could adequately explain the cases under various saccharification conditions. The kinetics results would be available for reducing sugars production processes, with the reducing sugars obtained at a lower cost can be used as carbon and energy sources in various fermentation industries.

• 한국식품저장유통학회지
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• 제22권3호
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• pp.345-352
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• 2015

쌀과 히솝을 이용하여 히솝쌀음료를 가공하고자 제조특성을 조사하였다. 히솝쌀음료의 제조조건은 amylase 함량($X_1$, 1~5 mL), 당화시간($X_2$, 10~18 hr) 및 히솝 함량($X_3$, 1.0~3.0 g)으로 당화 후 당도, 황색도, 관능적 특성을 반응표면분석을 통하여 모니터링 하였다. 당화 중 당 함량이 가장 많이 생성되는 조건은 amylase 함량 4.96 mL, 당화시간 14.93 hr 및 히솝 함량 2 g에서 $9.62^{\circ}Brix$로 나타났다. 황색도인 Hunter's color b가 가장 높게 나타나는 조건은 amylase 함량 1.90 mL, 당화시간 16.64 hr 및 히솝 함량 2.51 g에서 $14.86^{\circ}Brix$로 나타났다. 색상에 대한 최대의 관능평점은 amylase 함량 4.60 mL, 당화시간 15.66 hr 및 히솝 함량 1.57 g에서 4.09로 나타났다. 향미에 대한 최대의 관능평점은 amylase 함량 3.46 mL, 당화시간 10.79 hr 및 히솝 함량 1.45 g에서 3.99로 나타났다. 맛에 대한 최대의 관능평점은 amylase 함량 3.67 mL, 당화시간 17.64 hr 및 히솝 함량 1.76 g에서 3.17로 나타났다. 소비자의 종합적인 선호도를 나타내는 전반적인 기호도는 amylase 함량 3.73 mL, 당화시간 13.66 hr 및 히솝 함량 1.85 g에서 3.61로 가장 높게 나타나 최적조건을 설정할 수 있었다.