• 제목/요약/키워드: saccharification,

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대체연료(代替燃料) 생산(生産)을 위한 목질재료(木質材料)의 가수분해(加水分解)에 관한 연구(硏究)(II) - 탈(脫)리그닌처리가 폭쇄처리재(爆碎處理材)의 효소적(酵素的) 당화(糖化)에 미치는 영향(影響) - (Studies on the Enzymatic Hydrolysis of Lignocellulosic Materials for the Alternative Fuels (II) - The Effect of Delignification Treatment on the Enzymatic Hydrolysis of Steam - Exploded Woods -)

  • 조남석
    • Journal of the Korean Wood Science and Technology
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    • 제18권4호
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    • pp.18-25
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    • 1990
  • As polysaccharides in lignocellulosic materials are encrusted with aromatic lignin molecules and have high crystallinity, these require pretreatment to improve their digestability by cellulolytic enzymes. Though a number of pretreatment methods have been proposed, the steam explosion process is evaluated as a promising method. This study was performed to investigate the effect of delignification treatment by alkali, methanol and the others on the enzymatic hydrolysis. Delignification treatment resulted in great increase rate in enzymatic hydrolysis. Concerning to the effect of delignication reagents on the enzymatic hydrolysis, methanol treatment was more effective than alkali in the case of oak wood. In pine wood, the delignification did not showed any significant enhancement of hydrolysis rate. Complete delignification by Alkali-Oxygen. Alkali treatment showed high saccharification rate of 99.5%.

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알칼리 전처리가 굴참나무의 효소 당화에 미치는 영향 (Impact of Alkali Pretreatment to Enzymatic Hydrolysis of Cork Oak (Quercus Variabilis))

  • 윤수영;신수정
    • 펄프종이기술
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    • 제46권6호
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    • pp.1-7
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    • 2014
  • Dissolving part of xylan and lignin in lignocellulosic biomass by base can be used as pretreatment technique. Cork oak was pretreated with sodium hydroxide solution and the pretreatment effects were evaluated with two critical factors - NaOH concentration and pretreatment temperature. Some of xylan and lignin were removed by base pretreatment. At $90^{\circ}C$ and 13% NaOH pretreatment, 22.0% of lignin and 78.8% of xylan removed by base treatment. Enzymatic hydrolysis of cork oak which was pretreated at higher temperature or concentration was further improved. After pretreatment of cork oak with 13% NaOH at $90^{\circ}C$, the conversion rate of cellulose to fermentable sugars were reached up to 91.3%. At ethanol fermentation with enzymatic hydrolysate from different pretreatment conditions, all enzymatic saccharification liquids were well fermented by Saccharomyces cerevisiae.

생전분 직접 당화용 회전 원통형 Bioattritor의 조작조건과 동력소모량의 검토 (Evaluation of Operation Condition and Power Consumption of the Rotating Drum Type Bioattritor for Direct Saccharification of Raw Starch)

  • 박진서;이용현
    • 한국미생물·생명공학회지
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    • 제21권2호
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    • pp.157-162
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    • 1993
  • Raw starch can be effectively saccharified in an enzyme reaction system containing sttrition-milling media. In order to develop an effcient attrition-coupled bioreactor(bioattritor), a rotating drum type bioattitor was construced, and its optimal operation conditions and power consumptions were evaluated. The optimal conditions for 3l bioattritor were 4 baffled, baffle size of 1:0.05 (the ratio of drum diameter to baffle), drum rotation speed of 100 rpm, and 1.33g of 3 mm glass bead/g of raw corn starch.

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역원추형 발효조에서의 동시당화발효에 의한 전분으로 부터의 연속 에탄올 발효 (Continuous Ethanol Production from Starch by Simultaneous Saccharification and Fermentation in a Tapered Column Fermentor)

  • 김철호;유연우김철이상기
    • KSBB Journal
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    • 제5권4호
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    • pp.329-334
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    • 1990
  • In an attempt to develop a novel process for ethanol production from starch, a simultaneous saccharification and fermentation (SSF) process using Zymomonas mobilis and amyloglucosidase (AMG) was studied in continuous modes. Compared with a conventional cylindrical column type of fermentor, the tapered column type of fermentor was found to be superior in terms of reactor performance for ethanol fermentation. The tapered columm fermentor packed with coimmobilized Z. mobilis and AMG alleviated the problems which were associated with CO2 evolution and provided a significantly better flow pattern for both liquid and gas phases in the fermentor without channelling. However, the fluidized bed type of tapered column fermentor using flocculent strain of Z. mobiles and immobilized AMG showed lower productivity (5.2g/1/h) than that of packed bed type of tapered column fermentor(9.2g/l/h).

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동시당화 발효법에 의한 볏짚의 Acetone-Butanol 발효 (Acetone-Butanol Fermentation of Rice Straw by Simultaneous Saccharification and Fermentation)

  • 권기석;전영숙;김병홍
    • 미생물학회지
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    • 제26권3호
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    • pp.278-282
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    • 1988
  • 볏짚을 이용하여 acetone-butanol을 생산하기 위해 전처리한 볏짚을 C. acetobutylicum KCTC 1037(ATCC 4259)과 Trichoderma viride로부터 얻은 섬유소 분해효소를 이용하여 동시당화 발효법 (SSF)으로 발효하였다. Ball-mill로 처리한 볏짚을 SSF로 발효한 결과 acetate와 butyrate안을 생산하였으나, alkali로 전처리한 기질은 230 mM 이상의 solvent를 생산하였다. 이와 같은 발효의 차이는 볏짚에는 alkali 처리로 분해되는 물질이 있으며, 이 물질이 solvent 생산을 저해하기 때문인 것으로 판단된다. 이러한 solvent 생산 저해물질은 물이나 유기용매에 불용성으로 lignin 유도체 혹은 잔류농약으로 추측된다.

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Cassava 전분의 저온 증자에 의한 공업적 규모의 알코올 발효 (Large Scale Alcohol Fermentation with Cassava Slices at tow Temperature)

  • Ryu, Beung-Ho;Nam, Ki-Du
    • 한국미생물·생명공학회지
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    • 제15권2호
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    • pp.75-79
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    • 1987
  • 알코올 발효의 증자공정중에서 많은 에너지가 소요되므로 이를 줄이기 위한 방안으로서 저온증자법으로 Vietnam 산 cassava를 원료로 저온증자의 가능성을 고온증자와 비교 검토하였다. 알코올 발효에 당화 및 액화효소는 저온 및 고온증자에서 동일한 량을 사용하였으며 저온증자의 발효 mash중 소비된 glucose의 알코올 전환수율은 0.468g alcohol/gr. glucose로서 고온증자보다 좋은 결과를 보였다. 그러나 발효 불순물인 fusel oil은 고온증자의 0.48%보다 저온증자에서 0.64%로 다소 많았으나 증류과정에서 에너지소비 증가는 없었다.

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Complete Saccharification of Cellulose at High Temperature Using Endocellulase and ${\beta}$-Glucosidase from Pyrococcus sp.

  • Kim, Han-Woo;Ishikawa, Kazuhiko
    • Journal of Microbiology and Biotechnology
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    • 제20권5호
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    • pp.889-892
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    • 2010
  • We investigated a potential for glucose production from cellulose material using two kinds of hyperthermophilic enzymes, endocellulase (EG) and beta-glucosidase (BGL). Two BGLs, from hyperthermophile Pyrococcus furiosus and mesophile Aspergillus aculeatus, were compared with P. horikoshii endocellulase (EGPh) for complete hydrolysis of cellulose. The combination reactions by each BGL enzyme and EGPh could produce only glucose without the other oligosaccharides from phosphoric acid swollen Avicel (PSA). The combination of both the hyperthermophilic cellulases, BGLPf and EGPh, will be adaptable to a high efficiency system to produce glucose at high temperature.

섬유성 바이오매스를 이용한 Acetic Acid 생산 (Production of Acetic Acid from Cellulosic Biomass)

  • 우창호;박준호;윤현희
    • KSBB Journal
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    • 제15권5호
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    • pp.458-463
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    • 2000
  • Production of acetic acid from cellulosic biomass by Simultaneous Saccharification and Extractive Fermentation (SSEF) was investigated. The homoacetate organism used in this study was a strain of Clostridium thermoaceticum, ATCC # 49707. A batch operation of Simultaneous Saccharification and Fermentation(SSF) using ${\alpha}$-cellulose at pH 5.5 and 55$^{\circ}C$ yielded 40% conversion of cellulose to acetic acid, while a fed-batch SSF operation produced a maximum acetic acid concentration of 25 g/L, with 50% overall yield. In-situ extractive fermentation to reduce the end-product inhibition on both bacteria and enzyme was carried out. in a batch SSEF using 200 g/L IRA-400 resin, acetic acid concentration reached to 23.9 g/L and acetic acid yield and productivity were observed to be 48% and 0.20 g/L-hr, respectively.

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Simultaneous Saccharification of Inulin and Ethanol Fermentation by Recombinant Saccharomyces cerevisiae Secreting Inulinase

  • Kim, Youn-Hee;Nam, Soo-Wan;Chung, Bong-Hyun
    • Biotechnology and Bioprocess Engineering:BBE
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    • 제3권2호
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    • pp.55-60
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    • 1998
  • Various Saccharomyces cerevisiae strains were transformed with a 2 ${\mu}$-based multicopy expression plasmid, pYIGP, carrying Kluyveromyces marxianus inulinase gene under the control of GAPDH promoter. Among then two strains, SEY2102 and 2805, showed high levels of cell growth and inulinase expression, and were selected to study their fermentation properties on inulin. Jerusalem artichoke inulin was more effective for cell growth (10∼11 g-dry wt./L at 48 hr) and inulinase expression (1.0 units/mL with SEY2102/pYIGP and 2.5 units/mL with 2805/pYIGP) than other inulin sources such as dahlia and chicory. It was also found that maximal ethanol production of 9 g/L was obtained from Jerusalem artichoke inulin at the early stationary phase (around 30 hr), indicating that recombinant S. cerevisiae cells secreting exoinulinase could be used for the simultaneous saccharification of inulin and ethanol fermentation.

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Modeling and Simulation of Simultaneous Saccharification and Fermentation of Paper Mill Sludge to Lactic Acid

  • LIN, JIAN-QIANG;LEE, SANG-MOK;KOO, YOON-MO
    • Journal of Microbiology and Biotechnology
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    • 제15권1호
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    • pp.40-47
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    • 2005
  • Modeling and simulation for simultaneous saccharification and fermentation (SSF) process in bioconversion of paper mill sludge to lactic acid was carried out. The SSF process combined the enzymatic hydrolysis of paper mill sludge into glucose and the fermentation of glucose into lactic acid in one reactor. A mathematical modeling for cellulose hydrolysis was developed, based on the proposed mechanism of cellulase adsorption deactivation. Another model for simple lactic acid fermentation was also made. A whole mathematical model for SSF was developed by combining the above two models for cellulose hydrolysis and lactic acid fermentation. The characteristics of the SSF process were investigated using the mathematical model.