• Journal of the Korean Society of Food Science and Nutrition
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• v.15 no.4
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• pp.40-46
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• 1986

The beta-galactosidase of Aspergillus niger CAD 1 described in previous report was immobilized to cellulose triacetate. The optimal conditions for immobilization of the enzyme were obtained when 13%(v/v) of the soluble enzyme (349 unit/ml) was entrapped in fiber prepared from 10%(w/v) cellulose triacetate in methylene chloride. The optimal temperature and pH for the activity of the immobilized enzyme were $45^{\circ}C$ and 4.5, respectively, which stowed the same values as those of the soluble enzyme. It was found that Km of the immobilized enzyme for lacotse exhibited high value compared with that of the soluble enzyme. The immobilized enzyme showed good storage stability, reusability, and also hydrolysis of lactose when introduced into skim milk and acidic whey.

• Journal of the Korea Organic Resources Recycling Association
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• v.20 no.2
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• pp.36-43
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• 2012

Objective of this study was to investigate the effects of pre-treatment of rice straw by sizes(3cm, milled), temperatures($35^{\circ}C\;and\;55^{\circ}C$), with/without NaOH treatment, and RPM on the characteristics of volatile fatty acids production. The concentration of total volatile fatty acids (TVFAs) was increased with the hydrolyzed time. Concentration of VFAs in milled rice straw was higher than that in 3 cm cut. With the alkali treatment, the concentration of TVFAs were sharply increased, which showed 3 times higher than non-treatment. Concentration of VFAs was high at 150 rpm at $35^{\circ}C$, and at 80rpm and 200 rpm at $55^{\circ}C$. Among them acetic acid was dominant, which showed the similar increase with TVFAs. It was also observed that in the case of fibrous material, the contents of cellulose and hemi-cellulose were reduced a little, but no change in lignin.

• Clean Technology
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• v.17 no.2
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• pp.156-165
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• 2011

The process for bioethanol production from lignocellulosic biomass was studied through process simulation using PRO/II. Process integration was conducted with concentrated acid pretreatment, hydrolysis process, SMB (simulated moving bed chromatography) process and pervaporation process. Energy consumption could be minimized by the heat recovery process. In addition, material and energy balance were calculated based on the results from the simulation and literature data. A net production yield of 4.07 kg-biomass and energy consumption value of 3,572 kcal per 1 kg ethanol were calculated, which is indicating that 26% yield increase and 30% energy saving compared to the bioethanol production process with dilute-acid hydrolysis (SRI report). In order to make it possible, sugar conversion yield of cellulose and hemi-cellulose is to be reached up to 90% and fermentation of xylose needs to be developed. In order to reduce the energy consumption up to 30%, the concentration of acid solution after being separated by 5MB should exceed 20%. If acid/sugar separation by SMB process is to be practical, the bioethanol process designed in this study can be commercially feasible.

• Applied Biological Chemistry
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• v.7
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• pp.1-13
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• 1966

1) Three ${\beta}-1$, 4-mannanases were isolated from germinated guar bean through extraction, ammonium sulfate fractionation, column chromatography on cellulose derivatives and gel filltration on Sephadex G-100. They were designated as ${\beta}-1$, 4-mannanase A,B and C, respectively, in the order of isolation. 2) These enzymes were different in several aspects such as pH optimum, effect of metal ions, adsorbability on cellulose derivatives, molecular weight, Michaelis constant toward reduced ivory nut mannan A, mode of action and extent of hydrolysis of the mannan. 3) ${\beta}-1$, 4-Mannanases A and C were proposed to be two different endo-enzymes of random-splitting type producing a series of oligosaccharides from ${\beta}-1$, 4-mannans. ${\beta}-1$, 4-Mannanase B was suggested to be possibly an exe-type enzyme catalyzing a stepwise splitting from the non-reducing end of ${\beta}-1$, 4-mannans to produce mannose. 4) Guaran was subjected to hydrolysis by the purified enzymes and the consequence was discussed in connection with structural requirements of the enzymes toward substituted ${\beta}-1$, 4-mannans and their role in germinating guar seeds.

• Microbiology and Biotechnology Letters
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• v.31 no.3
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• pp.224-229
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• 2003

A keratinolytic protease was purified from the culture medium of Pseudomonas sp. KP-364 by use of an assay of the hydrolysis of feather keratin. Membrane ultrafiltration and DEAE-cellulose ion-exchange resin and Sephadex G-150 gel chromatographies were used to purify the enzyme. The specific activity of the purified keratinolytic protease relative to that in the original medium was approximately 72-fold high. Sodium dodecyl sulfate-polyacrylamide gel electrophoresis and Sephadex G-150 chromatography indicated that the purified keratinolytic protease is monomeric and has a molecular weight of 36 kDa. The optimal pH and temperature of the keratinolytic protease activity were 6.6 and 37 C, respectively, and the keratinolytic protease was relatively stable at pH value from 3.0 to 10.0 at 37 C for 1hour. The keratinolytic protease was inhibited by EDTA and EGTA, indicating that the keratinolytic protease was a kind of metalloprotease that require Li+ for cofactor.

• Microbiology and Biotechnology Letters
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• v.30 no.3
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• pp.247-252
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• 2002

A bacterium producing the extracellular mannanase was isolated from Korean formented food and has been identified as a member of the genus Bacillus from the result of the phylogenic analysis based on partial 165 rRNA sequences. The isolate, named Bacillus sp. WL-3, was shown to be similar to B. subtilis strain on the basis of its biochemical properties. The mannanase of culture supematant was the most active at $55^{\circ}C$ and pH 6.0. The additional carbohydrates including u-cellulose, avicel, oat spelt xylan, guar gum and locust bean gum (LBG) increased the mannanase productivity. Especially, the maximum mannanase productivity was reached 65.5 U/ml in LB medium supplemented with 0.5% (w/v) LBG, which was 131-folds more than that in LB medium. It was sug-gested that the increase of mannanase production was owing to induction of mannanase biosynthesis by LBG hydrolysates transported following initial hydrolysis by extracellular mannanase during the cell growth. The molec-ular weight of WL-3 mannanase was estimated to approximately 38.0 kDa by zymogram on SDS-PAGE.

• Biomedical Science Letters
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• v.6 no.4
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• pp.261-268
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• 2000

Fibrinolytic enzyme (FE-2) was purified from the fruiting bodies of Tricholoma saponaceum using DEAE-Cellulose chromatography and Mono-S column chromatography, The enzyme has a molecular weight of 18.23 kDa and include Zn$^{2+}$ ion as found by ICP/MS. The N-terminal amino acid sequence of the enzyme was A-L-Y-V-G-X-S-P-X-Q-Q-S-L-L-V It has a pH optimum at pH 7.5, suggested that FE-2 was a neutral pretense. The activity of FE-2 was highly inhibited by EDTA and 1,10-phenanthroline, indicating that the enzyme is a metalloprotease. The activity of FE-2 was increased by $Mg^{2+}$, Zn$^{2+}$, Fe$^{2+}$, and Co$^{2+}$, but the enzyme activity was totally inhibited by Hg$^{2+}$. No inhibition was found with PMSF, E-64, pepstatin and 2-mercaptoethanol. The enzyme hydrolyzed both $A\alpha$ and B$\beta$ chains of human fibrinogen. The $\gamma$ chain was resistant to hydrolysis by FE-2.

• Journal of Life Science
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• v.12 no.2
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• pp.151-157
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• 2002

A trypsin inhibitor was isolated and purified from Azismatis Rhizoma which has been used as a galenic for diuretic and antiphlogistic. Purification was carried out by 0-80% saturated ammonium sulfate salting out, DEAE- cellulose ion exchange chromatogrphy, Sephadex G-150 gel filtration. The molecular weight of Alismatis Rhizoma trypsin inhibitor(ARTI) was estimated to be about 23,000 Da by gel filtration and SDS-PAGE, it must be monomer. ARTI was stable at 0~6$0^{\circ}C$, but at higher temperature its activity was decreased about 35%. When benzoyl-dl-arginine p-nitroanilide was used as a substrate of trypsin, half-maximal inhibition of ARTI was observed at 0.071 $\mu$M. ARTI inhibited the hydrolysis of trypsin non-competitively and Km value was 0.81 $\mu$M.

• Journal of Microbiology and Biotechnology
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• v.27 no.2
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• pp.271-276
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• 2017

A highly thermostable ${\beta}-(1-4)-glucanase$ (NA23_08975) gene (fig) from Fervidobacterium islandicum AW-1, a native-feather degrading thermophilic eubacterium, was cloned and expressed in Escherichia coli. The recombinant FiG (rFiG) protein showed strong activity toward ${\beta}-{\small{D}}-glucan$ from barley (367.0 IU/mg), galactomannan (174.0 IU/mg), and 4-nitrophenyl-cellobioside (66.1 IU/mg), but relatively weak activity was observed with hydroxyethyl cellulose (5.3 IU/mg), carboxymethyl cellulose (2.4 IU/mg), and xylan from oat spelt (1.4 IU/mg). rFiG exhibited optimal activity at $90^{\circ}C$ and pH 5.0. In addition, this enzyme was extremely thermostable, showing a half-life of 113 h at $85^{\circ}C$. These results indicate that rFiG could be used for hydrolysis of cellulosic and hemicellulosic biomass substrates for biofuel production.

• Journal of Forest and Environmental Science
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• v.27 no.3
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• pp.143-149
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• 2011

The possibility of employing biomass of Salix viminalis cv. Q683 as a resource of bio-energy was evaluated. The chemical analysis of S. viminalis cv. Q683 leaf biomass showed components such as, extractives (2.57%), lignin (39.06%), hemicellulose (21.61%), and cellulose (37.83%), whereas, its stem was composed of extractives (1.67%), lignin (23.54%), hemicellulose (33.64%), and cellulose (42.03%). The biomass of S. viminalis cv. Q683 was saccharified using two enzymes celluclast and viscozyme. The saccharification of S. viminalis cv. Q683 biomass was influenced by enzymes and their strengths. The optimal enzyme combination was found to be celluclast (59 FPU/g substrate) and viscozyme (24 FBG/g substrate). On saccharification the glucose from leaf and stem biomass was 7.5g/L and 11.7g/L, respectively after 72 hr of enzyme treatment. The biomass and enzyme-treated biomass served as the feedstock for ethanol production by fermentation. The ethanol production from stem and leaf biomass was 5.8 g/L and 2.2 g/L respectively, while the fermentation of the enzymatic hydrolysates yielded 5 g/L to 8 g/L bioethanol in 72 hours.