• 한국생물공학회:학술대회논문집
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• 한국생물공학회 2000년도 춘계학술발표대회
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• pp.45-50
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• 2000

A. pullulan ATCC 42023를 사용하여 고분자량의 pullulan을 대량생산하기 위한 연구로써, 탄소원의 농도, 용존산소량과 pH가 균체 성장 및 pullulan 생산에 미치는 영향에 대하여 연구하였다. Glucose의 당 농도에 따른 실험결과에서 glucose 농도가 0.3M (54g/1)일 때 최대의 pullulan 생산률을 나타내었고, 0.3M (54g/1)이상에서는 productivity가 급격하게 감소하는 기질 저해현상을 나타내었다. 삼각플라스크를 이용한 초기 pH의 영향에 대한 실험결과, 초기 pH 6.5는 $11.98g/{\ell}$의 pullulan을 생산하였고, pH 4.5로 일정하게 조절한 결과, pullulan 생산은 $13.31g/{\ell}$의 최대값을 나타내었다. 그러나 균체성장은 pH 6.5에서 가장 높았다. 그리고 용존산소량의 증가로 pullulan productivity를 증가시킬 수 있었다. 또한 산업적으로 유용한 고분자량의 pullulan을 생산하기 위한 탄소원으로 아미노당인 glucosamine을 사용하여 pullulan의 생성 및 분자구조 변형에 대하여 실험하였다. 탄소원 농도 50g/1 기준에서, glucose와 glucosamine을 40 : 60의 비율로 혼합하여 공급 하였을 때 분자량 20만 이상의 mediun size 및 200만 이상의 high molecular weight의 productivity가 가장 높았으며, A. pullulans의 specific growth rate도 가장 높았다.

• 한국미생물·생명공학회지
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• 제22권6호
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• pp.565-570
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• 1994

The pullulan production and morphological change of Aureobasidium pullulans ATCC 9348 were investigated both in batch fermentation and in continuous fermentation. The best carbon source for pullulan production was sucrose among seven different carbon sources. The pullulan production of A. pullulans was increased with increasing the carbon to nitrogen ratio of the medium using sucrose as a carbon source. In batch fermentation, production of pullullan occurred following exhaustion of the nitrogen source from the medium. The continuous fermentation showed that the pullulan production was closely parallelled with cell growth and was most effective at a dilution rate of 0.06~0.07 hr$^{-1}$-. The ratio of yeast-like cells(blastospores) of A. pullulans increased with the increase of growth rate, and reached 100% over the growth rate of 0.07 hr$^{-1}$. The growth rate, within a certain range, affected not only on the cell morphology, but on the specific pullulan productivity of A. pullulans.

• 한국생물공학회:학술대회논문집
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• 한국생물공학회 2000년도 춘계학술발표대회
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• pp.283-286
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• 2000

A. pullulans ATCC 42023를 사용하여 고분자량의 pullulan을 대량생산하기 위한 연구로써, 용존산소량과 pH가 균체 성장 및 pullulan 생산에 미치는 영향에 대하여 연구하였다. pullulan의 분해 효소에 대한 저항성을 가지고 산업적으로 유용한 고분자량의 pullulan을 생산하기 위해서 pH를 6.5로 조절할 경우, 분자량 20만 이상의 high molecular weight의 productivity가 가장 높았으며 용존산소량의 증가로 pullulan productivity를 증가시킬 수 있었다.

• KSBB Journal
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• 제9권2호
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• pp.91-97
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• 1994

Aureobasidium pullulans에 의한 whey배지에서 플루란의 생산에 대한 연구가 수행되었다. Whey배지에서 풀루란의 발효생산에 대한 실험결과, 최종균체농도는 sucrose 기본배지에서와 동일하였으나 풀루란의 생산은 5g/$\ell$로 저조하였다. Whey배지에서 풀루란 생산을 향산시키이 위하여 lactose와 galactose 기본배지에서 적응배양을 시도하였다. 적응배양을 시도하지 않은 경우, lactose를 탄소원으로 한 배지에서 3.4g/$\ell$, galactose를 탄소원으로 한 배지에서 2.5g/$\ell$의 풀루란 생산을 보였으나 적응배양방법을 이용하여 lactose로부터 10~12g/$\ell$, galacrose 기본배지에서 lactose에 적응배양된 균은 13.5g/l의 풀루란을 생산하였고 galactose에 적응배양된 균은 18.6g/l를 생산하였다. Whey배지에 적응배양된 균을 접종한 결과 초기 pH3.0일때 풀루란 생산이 최대값을 보였다.

• 미생물학회지
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• 제25권4호
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• pp.360-366
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• 1987

For the production of pullulan from the high concentration of sugar, the utilization of sugars by a pullulan-producing fungus, Aureobasidium pullulans was examined. A. pullulans showed the different utilization patterns for sugars such as sucrose, maltose, and maltotriose. Especially for maltotriose, the hydrolysis of sugar was accompanied by a transferase activity. Glucose and maltose showed the inhibitory effect on the cell growth and the pullulan production at the sugar concentration higher than 0.28M, but sucrose showed the inhibitory effect at the sugar concentration higher than 0.14M. Among the sugars examined, sucrose gave the best result for the pullulan production. 27.5g/l of pullulan was obtained from 5% sucrose.

• Journal of Microbiology and Biotechnology
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• 제14권2호
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• pp.237-242
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• 2004

Cell growth and the production of pullulan by Aureobasidium pullulan HP-2001, the UV-induced mutant of A pullulans ATCC 42023, increased with increased concentration of glucose up to 15.0% (w/v). Maximal production of pullulan in the flask scale was 27.65 g/l, when concentrations of glucose and yeast extract were 15.0 and 0.25% (w/v), respectively. Maximal conversion rate of pullulan from glucose as the carbon source was 0.37, when those of glucose and yeast extract were 5.0 and 0.15% (w/v), respectively. On the basis of total amount of pullulan, the conversion rate of pullulan from glucose, and utilization rate of glucose to cell mass and pullulan by A. pullulans HP-2001, the optimal concentrations of glucose and yeast extract for the mass production of pullulan were determined to be 10.0 and 0.25% (w/v), respectively, at which concentrations the production of pullulan and its conversion rate were 27.14 g/l and 0.27, respectively. Maximal production of pullulan with optimized concentrations of carbon and nitrogen sources by A. pullulans HP-200l in a 7-1 bioreactor was 32.12 g/l for 72 h culture, and that in a 100-1 bioreactor with the inner pressure of $0.4 kgf/cm^2$ was 36.87 g/l. Increased inner pressure of a 100-1 bioreactor resulted in a higher concentration of dissolved oxygen in the medium, which might enhance the production of pullulan by A. pullulans HP-2001.

• 한국생물공학회:학술대회논문집
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• 한국생물공학회 2000년도 추계학술발표대회 및 bio-venture fair
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• pp.380-383
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• 2000

불완전 곰팡이의 일종인 Aureobasidium pullulans ATCC 42023 균주를 이용한 pullulan의 최적조건 및 pH 조절에 따른 pullulan의 생성 그리고 균체형태와 고분자 pullulan 생산에 미치는 영향을 조사 하였다. 삼각플라스크 내에서 최대의 pullulan 생산은 초기 pH 6.5일때 11.98 g/l의 pullulan을 생산하였고, 회분식 발효에서는 산소 공급속도 0.5 vvm일때 15.16 g/l의 최대의 pullulan생산량을 나타내었다. pH조절에 따른 실험에서는 pH 4.5일때 13.31 g/l의 pullulan 생산량을 보였고, 이때 균체의 형태는 효모형과 균사형태의 성장을 하였다. 그러나 분자량 생성면에서는 pH 6.5일때 100만 이상의 고분자가 가장 많이 생산되었다.

• Journal of Microbiology and Biotechnology
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• 제12권1호
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• pp.1-7
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• 2002

The effects of DO and pH on the mass production of pullulan with high molecular weight and the morphology of A. pullulans ATCC 42023 were evaluated. A. pullulans showed a maximum production of pullulan (11.98 g/l) when the initial pH of the culture broth was 6.5 in a shake-flask culture. In a batch culture, the mixture of a yeast-like and mycelial cell forms was found at a pH of 4.5, and the maximum production of pullulan (13.31 g/l) was obtained. However, a high proportion of high molecular weight pullulan (M.W.>2,000,000) was produced at a pH of 6.5, with a yeast-like morphology. The maximum pullulan production yield ($51\%$) was obtained at a pH noncontrol (initial pH 6.5) and DO control (above $50\%$) condition. Pullulan degrading enzyme was activated when the pH of the broth was lower than 5.0 and the portion of low molecular weight pullulan was increased. The formation of a black pigment was observed at an initial stationary phase, at 40 h of fermentation. Therefore, the fermentation should be carried out in a pH noncontrol (initial pH of 6.5) and DO control (above $50\%$) condition, and should be harvested before reaching the stationary phase (around 40 h) for the production of high molecular weight pullulan.

• 한국생물공학회:학술대회논문집
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• 한국생물공학회 2003년도 생물공학의 동향(XII)
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• pp.204-207
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• 2003

Pullulan as useful biopolymer has been focused on its industrial production. The objectives of this thesis were to enhance the production of pullulan for the industrial production and to characterize pullulan physical properties. In order to find the economical optimum of the fermentation conditions and promote pullulan productivity, effect such as the carbon source, pH have been estimated and measured molecular weight of produced pullulan.

• Journal of Microbiology and Biotechnology
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• 제3권4호
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• pp.298-302
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• 1993

Pullulan was produced from starch hydrolysate with Aureobasidium pullulans SH8646. We could measure the correct amount of pullulan produced without the interference of starch from the culture supernatant by using a bacterial $\alpha$-amylase treatment and ethanol: acetone (1:1) precipitation. When 5% acid-hydrolyzed starch was used as a carbon source, the dry cell weights obtained were similar irrespective of DE values of starch hydrolysates. The dry cell weights of those on the starch hydrolysate media prepared with 0.1 N HC1 treatment, were slightly higher (9.5~10.5 g/l) than those on the starch hydrolysate media prepared with 1.0 N HCl (8.5~9.5 g/l). And among the starch hydrolysates showing DE values lower than 50, maximum pullulan production of 15 g/l was obtained at DE 30~40 starch hydrolysate but those showing DE values higher than 50, the pullulan production was increased with the increase of the DE value of starch hydrolysates. From the media containing 5%, 10%, and 15% starch hydrolysate (DE 25, 45, and 75), about 20~34% pullulan yield was obtained and the maximum pullulan yield of 34% (17g/l) was obtained from 5% DE 75 starch hydrolysate. The pullulan yields from starch hydrolysate media were much lower than those from glucose, maltose, maltotriose, and sucrose media.