• 제목/요약/키워드: hydrolysis yield

검색결과 419건 처리시간 0.021초

Effects of Ar-Plasma Treatment in Alkali-Decomposition of Poly(ethylene terephthalate)

  • Seo, Eun-Deock
    • Macromolecular Research
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    • 제11권5호
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    • pp.387-392
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    • 2003
  • The ablation effects of Ar-plasma treatment and alkali-decomposition behavior in NaOH solution of polyethylene terephthalate (PET) film were investigated. The modifications were evaluated by analysis of atomic force microscopy topographical changes, and by the measurement of decomposition yield in conjunction with heats of formation and electron densities of acyl carbon calculated by Parameterization Method 3 method. It has shown that the alkali-decomposition is hampered by plasma treatment and its decomposition yield is closely related with plasma treatment conditions such as exposure time to plasma. Plasma-treated PET films exhibited lower decomposition yield, compared to that of virgin PET. Increasing plasma exposure time contributes positively to decrease the decomposition yield. It has also shown that the topography of PET surface was affected by the base-promoted hydrolysis as well as Ar-plasma treatments. These behaviors are attributed to the decreased nucleophilicity of acyl carbon damaged by the ablation of Ar-plasma.

Synthesis of 3-Amino-1,4-dihydropyridine Derivative via an Intramolecular Rearrangement of 1,4-Dihydropyridine-3-hydroxamate

  • Suh, Jung-Jin;Hong, You-Hwa;Bae, Myn
    • Archives of Pharmacal Research
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    • 제14권4호
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    • pp.319-324
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    • 1991
  • 2,6-Dimethyl-4-(3'-nitrophenyl)-3-methoxylaminocarbonyl-1,4-dihydropyridine-5-carboxylic acid methylester, 3b reacted with 2-cyanoethanol or benzylalcohol to give the corresponding cyanoethylurethane compound 6c in 40.6% yield and benzylurethane compound 6d in 32% yield. The cyanoethylurethane 6c was hydrolized in ethanolic NaOH to give 2,6-dimethyl-4-(3'-nitrophenyl)-1,4-dihydropyridine-3-amino-5-carboxylic acid 5-methyl ester. HCl 8 in 64.8% yield. Another acid hydrolysis of benzylurethane 6d gave 2,6-dimethyl-4-(3'-nitrophenyl)-1,4-dihydropyridine-3-amino-5-carboxylic acid 5-methylester. HBr 11 in 54.7% yield.

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회분식 반응 증류에 의한 lactic acid의 분리 특성 (Separation Characteristics of Lactic Acid by Batch Reactive Distillation)

  • 최종일;홍원희
    • KSBB Journal
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    • 제14권2호
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    • pp.220-224
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    • 1999
  • 본 논문에서 회분식 반응 증류에 의한 lactic acid의 분리 특성을 연구하였다. 휘발성이 있는 lactate ester의 생성을 위한 lactic acid와 alcholo과의 반응에서, 반응에 의해 생성된 lactate ester의 휘발성이 높을 수록 증류탑으로 들어가는 lactate ester양은 증가하여 재비기에서 얻어진 lactic acid의 회수율은 증가 하였다. 부분응축기의 온도가 감소할수록 재비기로 모이는 lactate ester양은 증가하였고 재비기 내의 수화 반응에 의해 얻어지는 lactic acid의 양은 증가하였다 Lactic acid의 정제를 위한 lactate ester와 물과의 수화 반응은, 비록 증류탑 내에서 lactate ester와 물이 반응을 할 수 있으나, 증류탑 내에서의 체류시간이 짧기 때문에 대부분 재비기에서 이루어진다.

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에탄올 발효 배지로서 홍삼박의 활용 (Potential of Red Ginseng Marc for Ethanol Production as a Fermentation Medium)

  • 김동청;인만진
    • Journal of Applied Biological Chemistry
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    • 제56권4호
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    • pp.245-247
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    • 2013
  • 홍삼박을 에탄올 발효의 원료로 활용하기 위하여 홍삼박을 탄수화물 분해효소와 단백질분해효소로 처리한 결과 환원당의 함량이 7.2 g/L에서 101.1 g/L로 증가하였다. 홍삼박 효소분해물에 영양성분을 추가하지 않고 시판 효모를 접종하여 $25^{\circ}C$에서 7일간 발효한 결과 에탄올은 29.3 g/L까지 생성되었으며 총당대비수율은 0.274 g/g로 계산되었다. 이는 대조군보다 에탄올 생산량은 1,000% 이상, 수율은 50% 이상 향상된 결과이다.

Optimization of Bio-based Succinic Acid Production from Hardwood Using the Two Stage pretreatments

  • Jung, Ji Young;Jo, Jong Soo;Kim, Young Wun;Yoon, Byeng Tae;Kim, Choon Gil;Yang, Jae Kyung
    • Journal of the Korean Wood Science and Technology
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    • 제41권2호
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    • pp.111-122
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    • 2013
  • The steam explosion-chemical pretreatment is a more effective wood pretreatment technique than the conventional physical pretreatment by accelerating reactions during the pretreatment process. In this paper, two-stage pretreatment processes of hardwood were investigated for its enzymatic hydrolysis and the succinic acid yield from the pretreated solid. The first stage pretreatment was performed under conditions of low severity to optimize the amount of solid recovery. In the second stage pretreatment washed solid material from the first stage pretreatment step was impregnated again with chemical (alkaline or chlorine-based chemicals) to remove a portion of the lignin, and to make the cellulose more accessible to enzymatic attack. The effects of pretreatment were assessed by enzymatic hydrolysis and fermentation, after the two stage pretreatments. Maximum succinic acid yield (16.1 g $L^{-1}$ and 77.5%) was obtained when the two stage pretreatments were performed at steam explosion -3% KOH.

Production of 4-Ethyl Malate through Position-Specific Hydrolysis of Photobacterium lipolyticum M37 Lipase

  • Lim, Chae Ryeong;Lee, Ha young;Uhm, Ki-Nam;Kim, Hyung Kwoun
    • Journal of Microbiology and Biotechnology
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    • 제32권5호
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    • pp.672-679
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    • 2022
  • Microbial lipases are used widely in the synthesis of various compounds due to their substrate specificity and position specificity. 4-Ethyl malate (4-EM) made from diethyl malate (DEM) is an important starting material used to make argon fluoride (ArF) photoresist. We tested several microbial lipases and found that Photobacterium lipolyticum M37 lipase position-specifically hydrolyzed DEM to produce 4-EM. We purified the reaction product through silica gel chromatography and confirmed that it was 4-EM through nuclear magnetic resonance analysis. To mass-produce 4-EM, DEM hydrolysis reaction was performed using an enzyme reactor system that could automatically control the temperature and pH. Effects of temperature and pH on the reaction process were investigated. As a result, 50℃ and pH 4.0 were confirmed as optimal reaction conditions, meaning that M37 was specifically an acid lipase. When the substrate concentration was increased to 6% corresponding to 0.32 M, the reaction yield reached almost 100%. When the substrate concentration was further increased to 12%, the reaction yield was 81%. This enzyme reactor system and position-specific M37 lipase can be used to mass-produce 4-EM, which is required to synthesize ArF photoresist.

사무용 폐지에서 유래된 글루코오스를 이용한 레불린산 생산 (Production of Levulinic Acid Using Glucose Derived from Office Waste Paper)

  • 반세은;박윤;이성초;임예은;이재원
    • 신재생에너지
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    • 제17권2호
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    • pp.32-39
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    • 2021
  • The optimal conditions for producing levulinic acid from office waste paper were investigated. Glucose was produced by enzymatic hydrolysis and its yield maximized by varying the soaking time of the substrate and amounts of enzyme and substrate. The optimal conditions to produce levulinic acid using the hydrolysate were determined by response surface methodology, with reaction temperature and catalyst (sulfuric acid) concentration as independent variables. The production model was assessed with an ANOVA regression analysis, and the results indicate its suitability for levulinic acid production (p, F, and lack-of-fit values were 0.003, 20.1, and 0.058, respectively). The optimal conditions were a reaction time of 56.27 min and catalyst concentration of 5.9% with a predicted yield of 2.588 g/L. We verified the findings under the same conditions and obtained 2.323 g/L of levulinic acid.

압출조리에 의한 밀가루 전분질의 분자구조 변화와 알콜발효 효율에 관한 연구 (Effect of Extrusion-Cooking on the Molecular Structure and Alcohol Yield of Wheat Starch)

  • 이철호;김기명;김지용;임재각
    • 한국식품과학회지
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    • 제23권6호
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    • pp.683-688
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    • 1991
  • 단일축 압출조리기를 이용하여 밀가루를 조리한 후 탁주발효용 기질로 사용하여 알코올 수율을 조사하였다. 또한 스팀가열과 비교하여 압출조리에 의한 밀가루 전분질의 분자구조 변화와 효소 민감성에 대하여 gel permeation chromatography(GPC)와 고유점도 측정으로 평가하였다. 밀가루의 GPC patternd은 스팀 가열이나 방출조리에 의하여 크게 변화되지 않았다. 그러나 ${\alpha}-amylase$를 30분간 처리할 경우 압출성형된 밀가루의 맥아당 생산량이 크게 증가하며 GPC pattern도 크게 변하여 저분자 전분질의 함량이 증가하며 고유점도는 감소하였다. 압출성형된 밀가루로 탁주발효를 한 결과 스팀증자된 밀가루로 탁주발효를 한 경우보다 실험실 규모 실험에서는 26%의 알콜생산 증대가 기록되었으며 공장규모 발효에서는 10% 이상의 알콜생산 증대를 얻을 수 있었다.

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Enzymatic Hydrolysis of Crystalline Chitin in an Agitated Bead Reaction System and Its Reaction Characteristics

  • Lee, Yong-Hyun;Bae, Young-Ki;Jeong, Eui-Jun
    • Journal of Microbiology and Biotechnology
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    • 제6권6호
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    • pp.432-438
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    • 1996
  • Native crystalline chitin was hydrolyzed in an agitated bead reaction system using crude chitinase excreted from Aspergillus fumigatus JC-19. The reaction was enhanced significantly, and the concentration and yield of reducing sugar after 48 hours were measured to be 35.42 g/I (w/v) and 0.64, respectively, around 1.86 times higher than those of the conventional system that was carried out without glass beads. The effect of reaction conditions, such as the amounts of chitin, chitinase and glass beads, and the size of glass bead, were examined. Ball milled chitin was also hydrolyzed in the agitated bead reaction system, the conversion yield and reaction rate of ball milled chitin for 24 hours increased up to 0.87 and 48.02 g/I, respectively. Chitinase showed relatively high stability in the agitated bead reaction system, particularly in the presence of enzyme stabilizer, $Ca^{++}$, which played a critical role in preventing the deactivation of chitinase by the physical impact of glass beads. The variations of the structural features of chitin during the reaction were followed by SEM and X-ray diffraction, and the enhanced hydrolysis reaction was caused by both the fragmentation of chitin particles and the destruction of the crystalline structure owing to the synergic effects of the attrition of glass beads and the hydrolytic action of chitinase.

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만니톨의 효소 가수분해 반응 조건 최적화 (Optimization for Enzymatic Hydrolysis of Mannitol)

  • 박은영;김용진;정승미;이동훈
    • KSBB Journal
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    • 제28권2호
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    • pp.65-73
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    • 2013
  • This study aimed to investigate the enzymatic hydrolysis of mannitol using Viscozyme$^{(R)}$ L, Celluclast$^{(R)}$ 1.5 L, Saczyme$^{(R)}$, Novozym$^{(R)}$, Fungamyl$^{(R)}$ 800 L, Driselase$^{(R)}$ Basidiomycetes sp., and Alginate Lyase, and to optimize of reaction conditions for production of reducing sugar. Response surface methodology (RSM) based on central composite rotatable design was used to study effects of the independent variables such as enzyme (1-9% v/w), reaction time (10-30 h), pH (3.0-7.0) and reaction temperature ($30-70^{\circ}C$) on production of reducing sugar from mannitol. The coefficient of determination ($R^2$) of $Y_1$ (yield of reducing sugar by Viscozyme$^{(R)}$ L) and $Y_3$ (yield of reducing sugar by Saczyme$^{(R)}$) for the dependent variable regression equation was analyzed as 0.985 and 0.814. And the p-value of $Y_1$ and $Y_3$ showing 0.000 and 0.001 within 1% (p < 0.01), respectively, was very significant. The optimum conditions for production of reducing sugar with Viscozyme$^{(R)}$ L were 9.0 % (v/w) amount of enzyme, 30.0 hours of reaction time, pH 4.5 and $30.0^{\circ}C$ of reaction temperature, and those with Saczyme$^{(R)}$ were 9.0% (v/w) of amount of enzyme dosage, 30.0 h of reaction time, pH 7.0 and $30.0^{\circ}C$ of reaction temperature, consequently, the predicted reducing sugar yields were 22.5 and 27.9 mg/g-mannitol, respectively.