• Microbiology and Biotechnology Letters
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• v.22 no.6
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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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• 2000.04a
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• pp.45-50
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• 2000

For the maximum production of pullulan from glucose as a carbon source, the effects of glucose concentration, pH and dissolved oxygen concentration on the cell growth and mass production of high-molecular weight pullulan by A. pullulans ATCC 42023 were evaluated. A. pullulans showed optimum pullulan productivity when glucose concentration was 0.3M (54g/L). And inhibitory effects on the cell growth and the pullulan production were observed at the glucose concentration higher than 0.3M (54g/L). The influence of pH control and dissolved oxygen on the pullulan production and growth of A. pullulans was studied. In shake-flasks, maximum pullulan production was obtained with $11.98g/{\ell}$ when initial pH was 6.5. In the batch fermentation, the maximum pullulan production of $13.31g/{\ell}$ was obtained with constant pH 4.5. And it was found that pullulan yield and synthesis rate increased with oxygen availability. For the production of commercially useful pullulan with high-molecular weight, a mixed carbon source, which was a mixture of glucose and glucosamine, was used for the pullulan fermentation with A. pullulans. On the basis of 5% mixed carbon source, culture with 3% glucosamine with 2% glucose was optimum condition for the production of high (M.W.> 1,000,000) and medium (M.W.> 200,000) molecular weight pullulan with considerable yields of cell mass and product. And the influence of pH control on the molecular weight of pullulan was studied in batch fermentation. It was found that the productivity of high-molecular weight pullulan with pH control at 6.5 was higher than that with no pH control.

• 한국생물공학회:학술대회논문집
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• 2000.11a
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• pp.325-328
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• 2000

The effects of DO and pH on the mass production of pullulan with high-molecular weight from A. pullulans ATCC 42023 were evaluated. The maximum pullulan production yield (51%) was obtained at pH non control (initial pH 6.5) and DO control (above 50%) condition. The pullulan degrading enzyme was activated when the pH of broth reached lower than 5.0 and portion of low molecular weight pullulan was increased. The formation of a black pigment was observed at the initial stationary phase, 40hr of fermentation. Therefore, the fermentation should be carried out in pH non control and DO control condition and harvested before reaching stationary phase around 40h for the production of high molecular weight pullulan.

• Journal of Microbiology and Biotechnology
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• v.12 no.1
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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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• 2000.04a
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• pp.283-286
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• 2000

The effects of dissolved oxygen and pH on the cell growth and mass production of high-molecular weight pullulan by A. pullulans ATCC 42023 were evaluated. For the production of commercially useful pullulan with high-molecular weight, the influence of pH control on the pullulan production and growth of A. pullulans was studied in batch fermentation. It was found that the productivity of high-molecular weight pullulan with pH control at 6.5 was higher than that with no pH control. The influence of dissolved oxygen on the pullulan production and growth was studied. It was found that pullulan yield and synthesis rate increased with oxygen availability.

• KSBB Journal
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• v.5 no.2
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• pp.101-106
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• 1990

The aspects of pullulan production by Aureobasidium pullulans were investigated under various initial pH, carbon source and nitrogen source conditions. The resulting pullulan fermentation broths were analyzed by using GC, LC and GPC techniques. The maximum pullulan production was obtained in the culture medium containing 5% sucrose at pH 6, 28$^{\circ}C$ after 7 days of cultivation. Under the pH 3, pullulan was almost not produced although the total cell mass of A. pullulans was increased, and the case on using (NH4)SO4 as a nitrogen source, which usually cause the fermentation medium under pH 3, also gave the similar phenomena. Sucrose was believed to converted to trisaccharide and glucose extracellulary and polymerization of glucose was proceeded intracellulary.

• Korean Journal of Food Science and Technology
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• v.38 no.6
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• pp.838-842
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• 2006

Gum was added to Jeungpyun (steamed Korean rice cake) to extend the shelf life and prevent retrogradation. The hardness of Jeungpyun was analyzed and the type of retrogradation was calculated by the Avrami equation. Guar gum, xanthan gum and pullulan were added to the steamed Korean rice cake at contents of 0.05%, 0.1% and 0.5% (w/w). The moisture contents of the steamed Korean rice cake stored at $4^{\circ}C$ remained unchanged over the three days. When the concentration of added gums was less than 0.1 %, the hardness was lower than that of the non-added gum. At a gum concentration of 0.5%, the hardness of Jeungpyun with added guar gum and xanthan gum was higher than that of pullulan and non-added Jeungpyun. The types of retrogradation varied according to the amount and the kind of the added gums. The type of retrogradation of pullulan-added rice cake was similar to that of xanthan-added rice cake. The Avrami exponent of pullulan-added and xanthan-added Jeungpyun was 1.4${\sim}$1.49 and 1.25${\sim}$1.43, respectively. As the concentrations of pullulan were increased from 0.05% to 0.5%, the time constant (1/k) increased from 5.37 to 15.65. Pullulan and xanthan gum were confirmed to be more effective than guar gum for preventing the retrogradation of the steamed Korean rice cake known as Jeungpyun.

• 한국생물공학회:학술대회논문집
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• 2003.04a
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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.

• 한국생물공학회:학술대회논문집
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• 2000.04a
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• pp.287-290
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• 2000

The pullulan production and morphological change of Aureobasidium pullulans ATCC 42023 were investigated in shake-flasks and in 2.5L batch fermentor. In shake-flasks, maximum pullulan production was obtained with $11.98g/{\ell}$ when initial pH was 6.5. The batch fermentation was performed in the medium with pH control ranged pH 2.5-7.5. The maximum pullulan production of $13.31g/{\ell}$ was obtained with pH 4.5. However, the cell growth was the highest at pH 6.5.

• KSBB Journal
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• v.11 no.4
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• pp.497-503
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• 1996

In this study, the effects of nitrogen sources and pH on pullulan production were investigated. As a result, the best nitrogen source in pullulan production by Aureobasidium pullulans was shown to be peptone and its product yield was 62%. Optimum concentration of carbon/nitrogen source ratio was 50/0.15 and the production of pullulan was inhibited at ratios higher than 50/0.15. Aureobasidium pullulans had produced 29.1, 27.4 and 26.5 g/L pullulan, respectively in media I, II, and III containing mixed nitrogen sources. This result showed that pullulan could be produced efficiently from mixed nitrogen source. It was found that pullulan yield with pH control was higher than that with no pH control. In fedbatch fermentation, pullulan yield obtained with a feeding rate of 0.05 N-g/L for nitrogen source was higher than that without nitrogen source feeding.