• Title/Summary/Keyword: Production and Purification

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Isolation of Microorganism Producing Chitinase for Chitooligosaccharides Production, Purification of Chitinase, and its Enzymatic Characteristics (Chitoologosaccharides 생산에 적합한 Chitinase를 분비하는 균주의 선별, Chitinase의 분리정제 및 반응특성)

  • 정의준;이용현
    • Microbiology and Biotechnology Letters
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    • v.23 no.2
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    • pp.187-196
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    • 1995
  • In order to produce fuctional chitooligosaccharides, a strain excreting mainly endo-type chitinase suitable for chitooligosaccharides production was newly screened and identified as Aspergillus fumigatus JC-19. The chitinase excretion was repressed in nutrient rich medium but stimulated by colloidal chitin indicating that the chitinase is inducible type enzyme. Maximum secretion of the enzyme was observed at pH 7.0 and 37$\circ$C . The growth and chitinase production patterns of Aspergillus fumigatus JC-19 showed that the cell growth reached maximum after 4-5 days with final chitinase concentration of 0.46 unit per ml. Excreted chitinase was purified by ammonium sulfate precipitation, colloidal chitin adsorption, anion exchange chromatography, and gel filtration, respectively, and measured M.W of 50 KDa. The enzyme reaction carried out both by crude and purified chitinase showed that the purified chitinase accumulated more chitooligosaccharides of 1-6 degree of polymerization than that of crude chitinase.

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Production and Purification of Soluble Recombinant Human Lymphotoxin in Escherichia coli

  • Choi, Yoon-Ho;Na, Doe-Sun;Pan, Jae-Gu;Park, Seung-Kiel;Yoo, Hyang-Sook;Kang, Kook-Hee;Sung, Moon-Hee
    • Journal of Microbiology and Biotechnology
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    • v.2 no.1
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    • pp.21-25
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    • 1992
  • Human lymphotoxin (LT) was produced in E. coli as a soluble protein. The level of recombinant human LT production was about 4% of the total souble proteins of E. coli extracts. Recominant human LT was purified to apparant homogeneity by a simple procedure utilizing FPLC on Mono Q and Mono S columns. The specific activity of the purified LT was $10\times10^7\;units/mg$.

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Production and Purification of Pepsin Inhibitor from Actinomycetes GF 155-2 (Actinomycetes GF 155-2에 의한 pepsin 저해물질의 생산 및 정제)

  • 박석규;성낙계;이상원
    • Microbiology and Biotechnology Letters
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    • v.17 no.2
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    • pp.121-125
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    • 1989
  • Actinomycetes GF 155-2, which produced an extracellular pepsin inhibitor, was isolated from soil samples. Optimal conditions of inhibitor production by flask-shacking culture were 2% glucose, 0.7% polypeptone, initial pH 1.0, culture time 60 hours and temperature 30%. Effect of in-organic salts was not observed. About 5mg of colorless crystalline inhibitor was obtained from 5L culture broth in jar tormentor by means of ammonium sulfate precipitation, methanol extraction, and column chromatographies on Amberlite IR-120, XAD-2 and silicagel 60.

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High-Level Production of Spider Silk Protein by Fed-Batch Cultivation of Recombinant Escherichia coli and Its Purification

  • Lee, Seok-Jae;Lee, Sang-Yeop
    • 한국생물공학회:학술대회논문집
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    • 2001.11a
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    • pp.719-722
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    • 2001
  • Silk proteins from Nephila clavipes are fibrous proteins containing repetitive sequences with both crystalline and amorphous domains. In order to obtain high-level production of silk protein, the synthetic genes had 16 contiguous units of the consensus repeat sequence of the silk protein were expressed in Escherichia coli BL21(DE3) under the strong inducible T7 promoter. For production of recombinant silk protein in large amounts, pH-stat fed-batch cultures were carried out. The recombinant silk protein was produced as soluble forms in E. coli, and the recombinant silk protein content was as high as 11% of the total protein. When cells were induced at $OD_{600}$ of 60, the amount of silk protein produced was 6.49 g/L. After simple purification steps, 9.2 mg of silk protein that was more than 80% pure was obtained from a 50 mL culture, and the recovery yield was 26.3%.

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Role of Atmospheric Purification by Trees in Urban Ecosystem -in the Case of Yongin- (도시생태계 수목의 대기정화 역할 -용인시를 사례료-)

  • 조현길;안태원
    • Journal of the Korean Institute of Landscape Architecture
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    • v.29 no.3
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    • pp.38-45
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    • 2001
  • This study quantified annual $CO_2$, SO$_2$ and NO$_2$ uptake and annual $O_2$ production by trees in Yongin´s urban ecosystem, and explored values of urban tree plantings in atmospheric purification. Woody plant cover was only 7.7% with planting density of 1. trees/100$m^2$, and the tree-age structure was largely characterized by a young, growing tree population. Annual per capita pollutant emissions from fossil fuel consumption were 7.3t/yr for $CO_2$, 7.6kg/yr for SO$_2$, and 26.6kg/yr for NO$_{x}$. Carbon dioxide storage per unit urban area by trees was 13.1t/ha and the economic value for $CO_2$ storage was ₩6.6millions/ha. Annual atmospheric purification was 2.0t/ha/yr for $CO_2$ uptake, 2.0kg/ha/yr for SO$_2$ uptake, 4.0kg/ha/yr for NO$_2$ uptake and 1.5t/ha/yr for $O_2$ production, and the annual economic value for the atmospheric purification was ₩1.5millions/ha/yr. Urbantrees stored an amount of $CO_2$ equivalent to about 3.1% of the total annual $CO_2$ emissions, and annually offset total $CO_2$ emissions by 0.5%. Annual SO$_2$ and NO$_2$ uptake by trees equaled 0.5% of total SO$_2$ emissions and 0.3% of total NO$_{x}$ emissions, respectively. Urban trees also played an important role through producing annually 9.2 of the $O_2$ requirement for Yongin´s total population, despite relatively poor tree plantings. Future active plantings and greenspace enlargement in the study city could enhance the role of atmospheric purification by urban trees. The results from this study are expected to be useful in emphasizing environment benefits of urban trees, and in urging the continuous necessity for tree planting and management budget.get.

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The Present and the Future of Biogas Purification and Upgrading Technologies (바이오가스 정제 및 고질화 기술 현황 및 전망)

  • Heo, Namhyo;Park, Jaekyu;Kim, Kidong;Oh, Youngsam;Cho, Byounghak
    • 한국신재생에너지학회:학술대회논문집
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    • 2011.05a
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    • pp.172-172
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    • 2011
  • Anaerobic digestion(AD) has successfully been used for many applications that have conclusively demonstrated its ability to recycle biogenic wastes. AD has been successfully applied in industrial waste water treatment, stabilsation of sewage sludge, landfill management and recycling of biowaste and agricultural wastes as manure, energy crops. During AD, i.e. organic materials are decomposed by anaerobic forming bacteria and fina1ly converted to excellent fertilizer and biogas which is primarily composed of methane(CH4) and carbon dioxide(CO2) with smaller amounts of hydrogen sulfide(H2S) and ammonia(NH3), trace gases such as hydrogen(H2), nitrogen(N2), carbon monoxide(CO), oxygen(O2) and contain dust particles and siloxanes. The production and utilisation of biogas has several environmental advantages such as i)a renewable energy source, ii)reduction the release of methane to the atomsphere, iii)use as a substitute for fossil fuels. In utilisation of biogas, most of biogas produced from small scale plant e.g. farm-scale AD plant are used to provide as energy source for cooking and lighting, in most of the industrialised countries for energy recovery, environmental and safety reasons are used in combined heat and power(CHP) engines or as a supplement to natural. In particular, biogas to use as vehicle fuel or for grid injection there different biogas treatment steps are necessary, it is important to have a high energy content in biogas with biogas purification and upgrading. The energy content of biogas is in direct proportion to the methane content and by removing trace gases and carbon dioxide in the purification and upgrading process the energy content of biogas in increased. The process of purification and upgrading biogas generates new possibilities for its use since it can then replace natural gas, which is used extensively in many countries, However, those technologies add to the costs of biogas production. It is important to have an optimized purification and upgrading process in terms of low energy consumption and high efficiency giving high methane content in the upgraded gas. A number of technologies for purification and upgrading of biogas have been developed to use as a vehicle fuel or grid injection during the passed twenty years, and several technologies exist today and they are continually being improved. The biomethane which is produced from the purification and the upgrading process of biogas has gained increased attention due to rising oil and natural gas prices and increasing targets for renewable fuel quotes in many countries. New plants are continually being built and the number of biomethane plants was around 100 in 2009.

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Microbiological Purification of L-Arabitol from Xylitol Mother Liquor

  • Jiang, Mingguo;Wang, Ben;Yang, Lifang;Lin, Shuangjun;Cheng, Hairong
    • Journal of Microbiology and Biotechnology
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    • v.21 no.1
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    • pp.43-49
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    • 2011
  • As a rare sugar alcohol, L-arabitol can be used in food and can prevent extra fat deposits in the intestinal tract. Commercially, L-arabitol is prepared from pure L-arabinose by hydrogenation, which needs a high temperature and high pressure, leading to a high production cost for Larabitol. Therefore, this study describes a novel L-arabitol production method based on biological purification from the xylitol mother liquor, a cheap and readily available raw material that contains a high concentration of Larabitol. First, a novel Bacillus megaterium strain was screened that can utilize xylitol, sorbitol, and mannitol, yet not L-arabitol. The isolated strain was inoculated into a medium containing the xylitol mother liquor under formulated culture conditions, where a high L-arabitol yield (95%) and high purity (80%) were obtained when the medium was supplemented with 50 g/l of xylitol mother liquor. Upon further purification of the fermentation broth by ion exchange and decolorization, L-arabitol was crystallized with a purity of 98.5%.

The production of Alkaline Protease by Aspergillus fumigatus and Purification of Enzyme (Aspergillus fumigatus에 의한 Alkaline Protease의 생산과 정제)

  • Cha, Woen-Suep;Cho, Young-Je;Choi, Cheong
    • Journal of the Korean Society of Food Science and Nutrition
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    • v.18 no.3
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    • pp.279-286
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    • 1989
  • The alkaline protease producing mold isolated from and identified as Aspergillus fumigatus. It was found that the production of alkaline protease reach to maximum was cultured for 3 days at $30^{\circ}C$. The enzyme was purified 86.13 fold and yield of the enzyme purification was 6.4%, The purification procedure include ammonium sulfate treatment, gelfiltration on Sephadex G-25, G-75, G-150 and DEAE-cellulose ion-exchange chromatography. When the purified enzyme was applied sodium dodecyl sulfate-polyacrylamide gel electrophoresis, the molecular weight was estimated about 63000. This enzyme composed 17 amino acids and main amino acids of this enzyme were glycine and glutamic acid.

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Plasmid-associated Bacteriocin Production by Leuconostoc sp. LAB145-3A Isolated from Kimchi

  • Choi, Yeon-Ok;Ahn, Cheol
    • Journal of Microbiology and Biotechnology
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    • v.7 no.6
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    • pp.409-416
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    • 1997
  • Leuconostoc sp. LAB145-3A isolated from kimchi produced a bacteriocin which was active against food pathogens, such as Listeria monocytogenes, Enterococcus faecalis, and E. faecium. Bacteriocin production occurred during the early exponential phase of growth and was stable upto the late stationary phase of growth. Optimum conditions for bacteriocin production were $37^{\circ}C$ with an initial pH of 7.0. The bacteriocin of LAB145-3A was sensitive to proteases, but stable for solvents, pH change and heat treatment. It was stable even at autoclaving temperature for 15 min. The bacteriocin exhibited a bactericidal mode of action against Lactobacillus curvatus LAB170-12. The bacteriocin produced by Leuconostoc sp. LAB145-3A was purified by CM-cellulose cation exchange column chromatography and Sephadex G-50 gel filtration. The purification resulted in an approximate 10,000-fold increase in the specific activity. Approximately 4% of the initial activity was recovered. Purified bacteriocin exhibited a single band on the SDS-PAGE with an apparent molecular weight of 4,400 daltons. This bacteriocin was named leucocin K. Leuconostoc sp. LAB145-3A had two residential plasmids with molecular sizes of 23 kb and 48 kb. A comparison of plasmid profiles between LAB145-3A and its mutants revealed that the 23 kb plasmid (pCA23) was responsible for bacteriocin production and immunity to the bacteriocin in Leuconostoc sp. LAB145-3A.

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