• 농업과학연구
• /
• 제22권1호
• /
• pp.54-61
• /
• 1995

영지 extract가 유당발효성 효모인 Kluyveromyces fragilis KCCM 35458의 발효에 미치는 영향을 조사하기 위하여 탈지유 배양액에 영지 1호의 extract를 0%, 0.1%, 0.5% 및 1.0%의 농도별로 첨가하고 $30^{\circ}C$에서 72시간을 정치배양하면서 조사한 결과는 다음과 같다. 1. 영지 extract를 1.0% 첨가한 시험구(試驗區)는 대조구(對照區)에 비하여 시간이 경과함에 따라 pH에서 빠른 감소를 보였으며 적정산도에서는 빠른 증가를 보였다. 2. $CO_2$ 발생량(發生量)은 영지 extract를 첨가한 전(全) 시험구(試驗區)에서 높았으며 1.0% 첨가구의 효과가 월등하였다. 3. Alcohol 생성량(生成量)은 72시간 배양함에 따라 영지 extract 첨가구(添加區)에서 높게 나타났으며 1.0% 첨가구(添加區)에서 가장 높은 alcohol 생산성을 보였고 발효시간을 단축시켰다. 4. 효모수는 영지 extract 0.5%, 1.0%첨가구에서 대조구에 비하여 현저한 증식효과를 나타내었다. 5. 탈지유 배양액에 있어서의 Kluyveromyces fragilis의 유당발효 상태는 배양시간 경과에 따라 영지 extract 첨가구가 대조구에 비하여 발효가 촉진되었으며 1.0% 영지 extract 첨가구에서 효과적이었다.

• 한국미생물·생명공학회지
• /
• 제6권4호
• /
• pp.167-171
• /
• 1978

전보에 개발된 배지에 국산 포도당을 이용한 발효결과, 구연산 생성은 37∼43g/ι이었다. 제품X의 경우는 제품Y에 비해 구연산 생성이 우수하여 43g/ι가 생성되었다. 국산 포도당을 Ambelite-IR -120으로 처리하고, peptone도 potassium ferrocyan-ide로 처리하여 금속이온을 제거한 뒤에, 10mg/ι의 철 이온을 첨가하였을 때 구연산 생성은 53gm/ι에 달하였다. 또한 원래 Sakaguchi 배지에 비해 3배나 많이 구연산이 생성되었다. 분리 동정된 Asp. niger를 다른 문헌과 비교하였을 때 큰 손색이 없었으며, 앞으로의 생리연구 및 mutation 연구가 필요하겠다.

• 한국미생물·생명공학회지
• /
• 제28권6호
• /
• pp.341-348
• /
• 2000

Selection of high producer strain, optimization of production medium and cultivation in bioreactor system were carried out in order to produce an antifungal substance, PAFS in large amounts which sources and 41 kinds of nitrogen sources, a synthetic medium consisting of fructose(70 g/1) and ammonium sulfate (10g/l) and a complex medium including galactose(30g/l), fructose(20g/l) and cottonseed flour(35g/l) were determined as opti-mized media for PAFS production. In bioreactor studies examining physiological characteristics of the pro- ducer microorganism with the complex medium, typical pattern of diauxic growth was observed as demonstrated by the result that fructose was not used before almost exhaustion on readily utilizable carbon source, galactose. When galactose was supplemented additionally during the fermentation period. PAFS pro-ductivity did no increases any more, indicating that large portion of the added galactose was used for cell growth instead of biosynthesis of the secondary metabolite. It was deduced that PAFS production could be enhananced by employing fed-batch operation in order to overcome the apparent phenomenon of catabolite repression and /or inhibition.

• 한국미생물·생명공학회지
• /
• 제27권4호
• /
• pp.327-332
• /
• 1999

A highly productive fed-batch fermentation process was developed for the production of L-ornithine by using a new stabilized strain, Breviabcterium ketoglutamicum BK52. Fed-batch cultures with a continuous feeding of the complex medium were conducted on various operating conditions. The optimal concentration of phosphate in the complex medium was 2.1g/L. The optimal feeding rate of L-arginine was 0.028g/L/hr. The optimal feeding point of the complex medium was determined to be at 40 OD of the cell mass. The final L-ornithine concentrations within 64hrs of cultivation in 5 and 50 liter fermenters were 73g/L and 71g/L, respectively. The maximum overall L-ornithine productivity was 1.14g/L/hr which was about 2 times higher than that of the conventional fed-batch culture with intermittent feeding. The overall productivity of the fermentation system is remarkably improved by employing the optimized conditions, and it offers a significant potential for industrial application.

• Journal of Microbiology and Biotechnology
• /
• 제22권11호
• /
• pp.1518-1522
• /
• 2012

Leuconostoc mesenteroides is a heterofermentative Grampositive bacterium that plays key roles in fermentation of foods such as kimchi, sauerkraut, and milk, leading to the production of various organic acids and aromatic compounds. To study the microbiological and genomic characteristics of L. mesenteroides, we have developed a new chemically defined minimal medium by using the single omission technique. During the exponential cell growth, this species required glutamine, methionine, valine, and nicotinic acid as essential nutrients and 8 amino acids (arginine, cysteine, histidine, leucine, phenylalanine, proline, threonine, and tryptophan), 5 vitamins (ascorbic acid, folic acid, inosine, calcium panthothenate, and thiamine), and others (manganese, magnesium, adenine, uracil, and Tween 80) as supplemental nutrients. This medium is useful to study the metabolic characteristics of L. mesenteroides and to explain its role in food fermentation.

• Journal of Microbiology and Biotechnology
• /
• 제24권1호
• /
• pp.52-58
• /
• 2014

Structurally, herboxidiene contains the tetrahydropyran acetic acid moiety and a side chain including a conjugated diene, and has been isolated from Streptomyces chromofuscus ATCC 49982. Its production was significantly elevated nearly 13.5-fold (0.74 g/l) in a medium supplemented with glycerol (medium No. 6A6), and was more efficacious (1.08 g/l; 19.8-fold) in fed-batch fermentation at 36 h in medium No. 6A6, from Streptomyces chromofuscus. For further enhancement, regulatory genes metK1-sp and afsR-sp from Streptomyces peucetius were overexpressed using an expression vector, pIBR25, and similarly ACCase from Streptomyces coelicolor and two genes, metK1-sp and afsR-sp, were also overexpressed using an integration vector, pSET152, under the control of the strong $ermE^*$ promoter in Streptomyces chromofuscus. Only the recombinant strains S. chromofuscus SIBR, S. chromofuscus GIBR, and S. chromofuscus AFS produced more herboxidiene than the parental strain in optimized medium No. 6A6 with an increment of 1.32-fold (0.976 g/l), 3.85-fold (2.849 g/l), and 1.7-fold(1.258 g/l) respectively.

• 한국미생물·생명공학회지
• /
• 제41권1호
• /
• pp.52-59
• /
• 2013

The nutritional requirements for the maximum production of lipopeptides by Bacillus subtilis N7 (B. subtilis N7) were investigated and optimized using response surface methodology (RSM) under shake flask fermentation. A one-factor-at-a-time experimental setup was used to screen carbon and nitrogen sources. A Plackett-Burman design (PBD) was employed to screen the most critical variables for lipopeptides production amongst ten nutritional elements. The central composite experimental design (CCD) was finally adopted to elucidate the composition of the fermentation medium. Statistical analyses (analysis of variance, ANOVA) of the results showed that KCl, $MnSO_4$ and $FeSO_4{\cdot}6H_2O$ were important components and that their interactions were strong. Lipopeptide production was predicted to reach 709.87 mg/L after a 60 h incubation using an optimum fermentation medium composed of glucose 7.5 g/L, peanut oil 1.25 g/L, $MgSO_4$ 0.37 g/L, $KH_2PO_4$ 0.75 g/L, monosodium glutamate 6.75 g/L, yeast extract and $NH_4Cl$ (5:3 w/w) 10 g/L, KCl 0.16 g/L, $FeSO_4{\cdot}6H_2O$ 0.24 mg/L, $MnSO_4$ 0.76 mg/L, and an initial pH of 7.0. Lipopeptide production ($706.57{\pm}3.70$ mg/L) in the optimized medium confirmed the validity of the predicted model.

• 한국미생물·생명공학회지
• /
• 제47권2호
• /
• pp.220-233
• /
• 2019

Bacterial lysates have become a common ingredient for natural health care. Lactic acid bacteria (LAB) could serve as potential candidates for lysate production: the lactic acids produced by LAB have been utilized for their moisturizing, antimicrobial, and rejuvenating effects, while other substances provide topical benefits and health effects for the skin. Our study aimed to obtain lysate from a LAB S. macedonicus MBF 10-2 through an optimized fermentation using the Response Surface Methodology. Strain MBF10-2 was cultivated in a 2L fermenter tank in de Man Rogosa and Sharpe (MRS) medium and in plant-based peptone modified MRS, i.e. Soy-peptone and Vegitone. The duration and the medium composition (dextrose and soy peptone or proteose peptone) were adjusted to obtain an optimum production of cell lysate. Central Composite Design was employed for Design Expert 7.0.0 by adjusting 3 factors: dextrose (1%, 1.5%, 2%, 2.5%, 3%), soy or proteose peptone (0.5%, 0.75%, 1%, 1.25% and 1.5%), and duration of fermentation (8, 10, 12 14, and 16 h for MRS-Soy peptone and 15, 17, 19, 21, and 23 h for MRS Vegitone). Bacteriocin-Like Inhibitor Substance activity of lysate and pH were used as indicators. The optimum condition for lysate production using MRS Soy Peptone and Vegitone are as follows: dextrose concentration 2.5%, plant-based peptone 1.25%, while optimum fermentation duration were 11.18 h (MRS Soy Peptone) and 17 h (MRS Vegitone) with a starter concentration of 10% at $OD_{600nm}$ $0.2{\pm}0.05$. However, the standard MRS medium produced better quality lysate compared to MRS plant-based peptones.

• 생명과학회지
• /
• 제26권5호
• /
• pp.571-583
• /
• 2016

바이오제닉 아민은 주로 발효식품에 존재하는 미생물에 의해 발생하며, 종종 사람의 체내에서 심각한 독성을 나타내기도 한다. 따라서 바이오제닉 아민 비생성 균주의 선별을 위하여 순창군에서 제조된 전통 장류 200여 종으로부터 620종의 다양한 미생물을 분리하였고, 이중에서 다양한 생리활성 분석 및 바이오제닉 아민 생성여부를 조사하여 최종적으로 바이오제닉 아민 비생성 균주로써 Bacillus subtilis SCJ1을 선별하였다. 최종 선별한 SCJ1의 생화학적 특성과 16S rRNA 염기서열 분석을 통하여 Bacillus subtilis SCJ1로 명명하였다. Bacillus subtilis SCJ1의 산업적 적용이 가능한 최적배지 조성을 확립하기 위해 먼저 SCJ1균체 성장을 조사하였으며, 이를 기반으로 통계학적 방법인 반응표면 분석법을 사용하여 최적화를 수행하였다. 실험계획법은 배지 조성 성분의 선별을 위해 Plackett-Burman design을 사용하여 모델을 설정하였다. 실험 모델을 통하여 선별된 배지 성분으로는 molasses, yeast extract, peptone으로 예측되었으며, 배지조성에 대한 최적 농도를 설정하기 위해 중심합성계획법을 사용하여 최적화를 수행하였다. 최종적으로 예측된 배지 성분의 농도는 molasses 27.5 g/l, yeast extract 7.5 g/l, peptone 17.5 g/l로 예측되었고, 이때의 최대 균체량은 2.03704 g/l로 예측되어 모델의 검증실험을 통한 예측 모델과 실제 결과가 동일함을 확인하였다. 또한, 기본 배지와 균체량을 비교하였을 때 1.32 g/l에서 1.9722 g/l로 약 49.4% 증가하였고, 효소활성과 항균활성 또한 증가함을 확인하였다.

• Biotechnology and Bioprocess Engineering:BBE
• /
• 제8권5호
• /
• pp.269-278
• /
• 2003

Gibberellic acid (GA$_3$) is a commercially important plant growth hormone, which is gaining much more attention all over the world due to its effective use in agriculture and brewing industry. Industrially it is produced by submerged fermentation technique using Ascomycetous fungus Gibberella fujikuroi. Solid state and immobilized cell fermentation techniques had also been developed as an alternative to obtain higher yield of GA$_3$. This review summarizes the problems of GA$_3$ fermentation such as production of co-secondary metabolites along with GA$_3$, substrate inhibition and degradation of GA$_3$ to biologically inert compound gibberellenic acid, which limits the yield of GA$_3$ in the fermentation medium. These problems can be overcome by various bioprocessing strategies e.g. two - stage and fed batch cultivation processes. Further research on bioreactor operation strategies such as continuous and / or extractive fermentation with or without cell recycle / retention system need to be investigated for improvement in yield and productivity. Down stream processing for GA$_3$ isolation is also a challenge and procedures available for the same have been critically evaluated.