• Title/Summary/Keyword: hydrolysis condition

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Effect of Carbon Source on the Hydrolytic Ability of the Enzyme from Fomitopsis pinicola for Lignocellulosic Biomass

  • Kim, Hyun-Jung;Kim, Yoon-Hee;Shin, Keum;Kim, Tae-Jong;Kim, Yeong-Suk
    • Journal of the Korean Wood Science and Technology
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    • v.38 no.5
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    • pp.429-438
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    • 2010
  • In this study, effect of carbon source on the hydrolytic ability of the enzyme from Fomitopsis pinicola, a brown rot fungi, for lignocellulosic biomass were examined on two lignocellulosic biomasses (rice straw and wood) without any pretreatment. Cellulase activities of crude enzyme from F. pinicola, which was cultured on softwood mixture as a carbon source, were 19.10 U/$m{\ell}$ for endo-${\beta}$-1,4-gulcanase (EG), 36.1 U/$m{\ell}$ for ${\beta}$-glucosidase (BGL), 7.27 U/$m{\ell}$ for cellobiohydrolase (CBH), and 7.12 U/$m{\ell}$ for ${\beta}$-1,4 xylosidase (BXL). Softwood mixture as a carbon source in F. pinicola comparatively enhanced cellulase activities than rice straw. The optimal pH and temperature of the cellulase was identified to pH 5 and $50^{\circ}C$for the hydrolysis of rice straw. Under these condition rice straw was hydrolyzed to glucose by the cellulase up to $32.0{\pm}3.1%$ based on the glucan amount of the rice straw for 72 h, while the hydrolytic capability of commercial enzyme (Celluclast 1.5${\ell}$) from rice straw to glucose was estimated to $53.7{\pm}4.7%$ at the same experimental condition. In case of addition of Tween 20 (0.1% w/w, substrate) to the cellulase the hydrolysis of rice straw to glucose was enhanced to $38.1{\pm}2.0%$.

Hydrolysis of DFP Using Cu(II)-Lactic Acid and Cu(II)-LMWS-Chitosan Chelates (Cu(II)-Lactic Acid와 Cu(II)-LMWS-Chitosan 착물의 DFP 가수분해반응 연구)

  • Kye, Young-Sik;Jeong, Keunhong;Kim, Dongwook
    • Applied Chemistry for Engineering
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    • v.31 no.5
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    • pp.475-480
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    • 2020
  • Chelates synthesized with Cu(II) ion and lactic acid or chitosan were applied to the hydrolysis of organophosphate simulant, DFP (diisopropyl fluorophosphate). Under the homogeneous reaction condition, Cu(II)-lactic acid chelate hydrolyzed DFP with the half life time of 37.1 min. Cu(II)-LMWS chitosan chelate was synthesized with 1 kDa molecular weight of chitosan, which showed low solubility, and then crystallized. The half life time for hydrolyzing DFP using Cu(II)-LMWS chitosan was 32.9 h indicating that the reaction rate is enhanced as much as 16 times more than that of using 18 kDa chitosan-Cu(II) complex. Under the homogeneous reaction condition, the half life time of Cu(II)-LMWS chitosan was 8.75 h. Therefore, we found out that the solubility of Cu(II)-LMWS chitosan makes the difference in the reaction rate as much as 4 times.

Kinetic Modeling of Simultaneous Saccharification and Fermentation for Ethanol Production Using Steam-Exploded Wood with Glucose- and Cellobiose-Fermenting Yease, Brettanomyces custersii

  • Moon, Hyun-Soo;Kim, Jun-Seok;Oh, Kyeong-Keun;Kim, Seung-Wook;Hong, Suk-In
    • Journal of Microbiology and Biotechnology
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    • v.11 no.4
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    • pp.598-606
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    • 2001
  • A mathematical model is proposed that can depict the kinetics of simultaneous saccharification and fermentation (SSF) using steam-exploded wood(SEW) with a glucose- and cellobiose-fermenting yeast strain. Brettanomyces custersii. An expression to describe the reduction of the relative digestibility during the hydrolysis of the SEW is introduced in the hydrolysis model. The fermentation model also takes two new factors into account, that is, the effects of the inhibitory compounds present in the SEW hydrolysates on the microorganism and the fermenting ability of Brettanomyces custersii, which can use both glucose and cellobiose as carbon sources. The model equations were used to simulate the hydrolysis of the SEW, the fermentation of the SEW hydrolysates, and a batch SSF, and the results were compared with the experimental data. The model was found to be capable of representing ethanol production over a range of substrate concentrations. Accordingly, the limiting factors in ethanol production by SSF under the high concentration of the SEW were identified as the effect of inhibitory compounds present in the SEW, the enzyme deactivation, and a limitation in the digestibility based on the physical condition of the substrate.

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Surface-Modified Porous Polymeric Membrane Using Vesicles

  • Im, Ji-Youn;Lee, Sang-Hee;Ko, Suck-Beom;Lee, Kuk-Haeng;Lee, Youn-Sik
    • Bulletin of the Korean Chemical Society
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    • v.23 no.11
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    • pp.1616-1622
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    • 2002
  • If the surfaces of vesicles are chemically modified so that they can be dispersed in organic solvents, the application of vesicular colloids may be expanded. A polymerizable surfactant (BDAC) and nonpolymerizable bipolar surfactant (BPAS) were synthesized in multi-steps. Large vesicles composed of BDAC and BPAS with embedded a cross-linking agent (divinylbenzene) underwent a radical polymerization. BPAS was extracted out using methanol (skeletonization). The headgroup of BDAC was cleaved off via hydrolysis in an acidic condition to yield vesicles where surfaces were covered with -COOH groups. There was no significant change in the overall shape. The skeletonized vesicles appear to have many holes with diameters up to about 25 nm. The holes retained even after hydrolysis. The hydrolyzed vesicles were not dispersed in water and most organic solvents such as tetrahydrofuran and chloroform, but dispersed in methanol.

가금부산물인 닭 용골연골로부터 chondroitin sulfate를 포함하는 뮤코다당단백질의 추출에 관한 연구

  • 신승철;김동욱;김관응;안승민;유선종;김성권;안병기;강창원
    • Proceedings of the Korea Society of Poultry Science Conference
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    • 2004.11a
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    • pp.26-27
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    • 2004
  • This study was conducted to evaluate the value of chicken keel cartilage as a source of mucopoly-saccharide-protein containing chondroitin sulfate (CS) and to find the optimum extraction conditions. The hot water extraction and alcalase hydrolysis methods were performed for extraction mucopolysaccharide in lyophilized chicken keel cartilage. The most efficient condition was hydrolysis with 2 % alcalase in 10 volumes of distilled water for 120 min. The yield of hydrolysate and CS content were 75.87 % and 25.61 %, respectively. For further separation of CS from hydrolysate by alcalase, ethanol precipitation was performed. The yield of ethanol precipitate and its CS content were 21.41 % and 46.31 %, respectively.

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A Study on the Alkali Hydrolysis of PET fabric with Ultrasonic Application(I) - Decomposition Rate Constant and Activation Energy - (초음파를 적용한 PET 직물의 알칼리 가수분해에 관한 연구(I) - 분해속도상수와 활성화 에너지-)

  • 서말용;조호현;김삼수;전재우;이승구
    • Textile Coloration and Finishing
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    • v.14 no.4
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    • pp.214-222
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    • 2002
  • In order to give a silk-like touch to PET fabrics, the PET fabrics were treated with NaOH alkaline solution in various conditions. In alkaline treatment, the liquor flow type pilot weight reduction apparatus with magnetostrictive ultrasonic transducer was used for the study. The weight loss of PET fabrics hydrolyzed in 4% and 6% NaOH solution, at $95^\circ{C}$ and $99^\circ{C}$ for 60min. with ultrasonic application showed 3.7~4.6% higher than that of treated fabric without ultrasonic application. From the difference of specific weight loss, the treatment condition of the maximum of hydrolyzation effect appeared at $95^\circ{C}$ in $4^\circ{C}$ and at $90^\circ{C}$ in 6% NaOH solution, respectively. During the alkali hydrolysis of PET fabrics, the decomposition rate constant(k) increased exponentially with the treatment temperature and were not related with ultrasonic cavitation. The activation energy$(E_a)$ in decomposition of PET fabrics were 21.06kcal/mol with ultrasonic application and 21.10kcal/mol without ultrasonic application. The ultrasonic application gave a little higher value of the activation entropy$(\Delta{S}^\neq)$ and a little lower value of Gibbs free energy$(\Delta{S}^\neq)$ compared with not used ultrasonic apparatus.

Morphology Changes of Hydroxyapatite in Different Hydrolysis Conditions (가수분해 조건에 따른 수산화인회석의 형상변화)

  • Choi, Kyoung-Rim;Lee, Dong-Kyu
    • Journal of the Korean Applied Science and Technology
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    • v.35 no.2
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    • pp.350-356
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    • 2018
  • Hydroxyapatite has been used for biomaterials since it has high biocompatibility. In this study, c-plane oriented hydroxyapatite was synthesized by hydrolysis of dicalcium phosphate intermediate by controlling temperature, concentration and pH. In basic condition, rod-like hydroxyapatite crystals were aggregated to form irregular particles in low concentration and plate-like particles exposed c-plane of hydroxyapatite crystal were obtained in high concentration, causing difference of 3 mV in zeta potential. Physicochemical properties of product were characterized by XRD, SEM, FT-IR, zeta potential measurement.

Wet Air Oxidation Pretreatment of Mixed Lignocellulosic Biomass to Enhance Enzymatic Convertibility

  • Sharma, A.;Ghosh, A.;Pandey, R.A.;Mudliar, S.N.
    • Korean Chemical Engineering Research
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    • v.53 no.2
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    • pp.216-223
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    • 2015
  • The present work explores the potential of wet air oxidation (WAO) for pretreatment of mixed lignocellulosic biomass to enhance enzymatic convertibility. Rice husk and wheat straw mixture (1:1 mass ratio) was used as a model mixed lignocellulosic biomass. Post-WAO treatment, cellulose recovery in the solid fraction was in the range of 86% to 99%, accompanied by a significant increase in enzymatic hydrolysis of cellulose present in the solid fraction. The highest enzymatic conversion efficiency, 63% (by weight), was achieved for the mixed biomass pretreated at $195^{\circ}C$, 5 bar, 10 minutes compared to only 19% in the untreated biomass. The pretreatment under the aforesaid condition also facilitated 52% lignin removal and 67% hemicellulose solubilization. A statistical design of experiments on WAO process conditions was conducted to understand the effect of process parameters on pretreatment, and the predicted responses were found to be in close agreement with the experimental data. Enzymatic hydrolysis experiments with WAO liquid fraction as diluent showed favorable results with sugar enhancement up to $10.4gL^{-1}$.

Preparation of Ferroelectric PZT Thin Film by Sol-Gel Processing; (II) Effect of Catalysts on Densification and Crystallization (솔-젤법에 의한 강유전성 PZT 박막의 제조;(II) 치밀화 및 결정화에 미치는 촉매의 영향)

  • 김병호;박성호;김병호
    • Journal of the Korean Ceramic Society
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    • v.32 no.7
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    • pp.783-792
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    • 1995
  • Sol-Gel derived ferroelectric PZT thin films were fabricated on ITO/Glass and Si/SiO2 substrates. In order to investigate the effect of catalysts on the densification and crystallization of PZT thin films, a nitric acid or ammonium hydroxide was added to the PZT stock solution at the state of partial hydrolysis reaction. The measured pH for a stable PZT sol was 5.2~9.3. In case of an acid-catalyzed PZT sol, a highly condensed particulate PZT sol was formed by accelerating the hydrolysis reaction. But weakly branched polymeric PZT sol was formed with a base-catalyzed condition. The difference in densification behavior was not found in the pH range of added catalyst, but the refractive index of PZT thin film was increased rapidly as the annealing temperature increased. The PZT thin film annealed at 54$0^{\circ}C$ for 10 min was fully densified and its refractive index was above 2.4. When the annealing temperature increased, the transition from the pyrochlore phase to perovskite appeared at 54$0^{\circ}C$. The base-catalyzed PZT thin film suppressed to form the pyrochlore phase and proceeded effectively to convert the perovskite phase. This was due to the formation of polymeric molecular structure by controlling the hydrolysis and condensation reaction through the additiion of the ammonium hydroxide.

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Optimal Conditions for the Enzymatic Hydrolysis of Isolated Sesame Meal Protein (효소에 의한 참깨박 단백질의 최적 가수분해 조건)

  • Lee, S.H.;Cho, Y.J.;Kim, S.;Ahn, B.J.;Choi, C.
    • Applied Biological Chemistry
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    • v.38 no.3
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    • pp.248-253
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    • 1995
  • Optimum conditions for the enzymatic hydrolysis of isolated sesame meal protein were investigated. Optimum conditions by papain were $60^{\circ}C$, pH 6.0, 3% enzyme concentration to substrate and 1.5% substrate concentration, respectively. The optimum operating conditions using pepsin were $55^{\circ}C$, pH 9.0, 3% enzyme concentration to substrate and 1% substrate concentration. The optimum operating conditions using trypsin were $60^{\circ}C$, pH 9.0, 1% enzyme concentration to substrate and 1% substrate concentration.

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