• 한국미생물·생명공학회지
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• 제27권5호
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• pp.378-384
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• 1999

Protopectinase (PPases) are heterologous group of enzymes that degrade pectin from the insoluble protopection which is constituent of the middle lamella and primary cell wall of higher plants by restricted depolymerization. From the previous report[6], enzymatically separated plant cells, which are produced from plant tissues by PPases treatment, showed well-conserved cellular components with their rigid cell wall and this characteristic is applicable to preparation of novel food material. The purpose of this study is to investigate the effect of medium composition of PPase production from Bacillus subtilis EK11 which was selected as a PPase producer. Various carbon sources and concentrations on PPase production were studied and corn starch at 0.7% was the most effective for production of PPase. Among the nitrogen sources, yeast extract was the most effective for PPase production and the effect of (NH4)2SO4 was notable as inotganic nitrogen source. Inorganic compounds such as KH2PO4, K2HPO4, Na3-citrate.2H2O and MgSO4 were optimized for PPase production. PPase activity was inhibited by the adition of Ba2+ or Zn2+. The optimal medium for PPase production was devised: 0.7% corn starch, 0.3% yeast extract, 1.4% KH2PO4, 0.6% K2HPO4, 0.1% Na3-citrate.2H2O and 0.02% MgSO4. PPase production by using the optimum medium was carried out with shaking cultivation at 37$^{\circ}C$. The maximum PPase activity of 256unit/ml could be obtained after the cultivation for 48hrs. The activity was increased about 2.2timesthan the activity, 112 unit/ml, in basal medium.

• KSBB Journal
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• 제25권6호
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• pp.539-546
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• 2010

In this work, mass production of Bacillus licheniformis SCD121067 through medium optimization by statistical experimental method was studied. First, galactose, yeast extract and potassium phosphate dibasic were selected as carbon, nitrogen and phosphate sources for mass production of B. licheniformis SCD121067 by using one factor at a time method. Second, according to the result of Plackett-Burman experimental design, key factors was yeast extract and $K_2HPO$. Finally, the response surface methodology was performed to obtain the optimum concentrations of two selected variables. The optimized medium composition consisted of 20 g/L galactose, 36 g/L yeast extract, 0.41 g/L $K_2HPO4$, 0.25 g/L $Na_2CO_3$, 0.4g/L $MgSO_4$ and 0.01g/L $CaCl_2$. Dry cell weight (15.4 g/L) by optimum production medium were increased 10 times, as compared to that determined with basic production medium (1.5 g/L). Fermentation conditions were examined for the mass production of B. licheniformis. The effect of temperature, agitation speed, pH and aeration rate on the mass production of B. licheniformis were also studied in a batch fermenter which was carried out in a 2.5 L bioreactor with a working volume of 1.5 L containing optimized production medium. As a result, dry cell weight of batch culture was 30.7 g/L at $42^{\circ}C$, 300 rpm, pH 8.0 and 2 vvm.

• Journal of Microbiology and Biotechnology
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• 제16권12호
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• pp.1856-1861
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• 2006

A Bacillus sp. A-6 strain that produced xylanase was isolated from rice bran. The optimal temperature and pH for xylanase activity of the culture supernatant of Bacillus sp. A-6 were 40$^{\circ}C$ and pH 7, respectively. The optimal temperature and pH for xylanase production in the xylan medium were 30$^{\circ}C$ and pH 9, respectively. The optimal concentrations of oat spelt xylan and peptone for xylanase production were 0.5% and 1.5%, respectively. The best nitrogen sources for xylanase production was beef extract, but xylanase production was also supported comparably by tryptone and peptone. The bacterial growth in the optimal xylan medium reached stationary growth phase after 12 h of incubation. The xylanase production in the culture supernatant increased dramatically during the initial 12 h exponential growth phase and then remained constant at 23.8-24.5 unit/ml during the stationary growth phase. The pH of the culture medium decreased from 8.8 to 6.7 during the exponential growth phase and subsequently increased to 8.1 during the stationary growth phase. Rice bran, sorghum bran, and wheat bran as well as oat spelt xylan induced xylanase production. The xylanase production was repressed when glucose was added to the xylan-containing medium.

• Fisheries and Aquatic Sciences
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• 제1권1호
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• pp.19-23
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• 1998

Effects of pituitary and thyroid hormones on estradiol-induced vitellogenin (VTG) induction were electrophoretically examined in primary hepatocyte cultures of rainbow trout. Hepatocytes were precultured for 2 days and then estradiol-17 $\beta$ $(E_2,\;2 \times 10^{-6}M)$>, triiodothyronine $(T_3,\;10^{-8}-10^{-6}M)$, bovine growth hormone (bGH, 10-100 ng/ml), ovine prolactin (oPRL, 100-500 ng/ml), and pituitary extract (PE) of rainbow trout (0.75PE/dish) were added to the incubation medium. The hepatocytes were cultured for 7 more days. The addition of oPRL to the incubation medium was not effective in increasing VTG production at any concentrations. The addition of PE to the incubation medium with $E_2$ was not effective in increasing VTG production. The addition of bGH to the incubation medium with $E_2$ was not effective in increasing the rate of VTG production at concentrations of 10-50 ng/ml. However, a higher concentration of bGH, 100 ng/ml, increased VTG production. The various concentrations of $T_3$ were ineffective in stimulating VTG production. These results suggest that GH could be one of stimulus factors for VTG production in rainbow trout.

• 한국식품영양과학회지
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• 제23권5호
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• pp.845-848
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• 1994

The fermenting conditions for acetic acid production with Acetobacter sp. FM-10 which could grow in the medium containing 10% ehtanol were investigated. Initial concentration of acetic acid in broth medium affected greatly to the fermentation speed. For example , the acetic acid production increased proportionally by the increasing of initial concentration was higher that 1.0%. When the cultivation was started with broth medium containing 5% ethanol, the additional adding ethanol during the fermentation was not significantly increased the acidity of the medium. The acidity of the medium containing 10% ethanol was reached to 8.3% after shaking than static cultivation by about 10 days with 150 rpm shaking speed. Acetic acid production with shaking cultivation was faster the static cultivation by abot 10 days under the same condition except shaking. In acetic acid fermentation with the batch style fermentor , the optimum fermentation condition was 700 rpm of agitation speed and 5L/min air flow rate in 3L culture medium .

• 한국축산식품학회지
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• 제30권1호
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• pp.66-72
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• 2010

Pediococcus pentosaceus SA131 was isolated from jeotgal, is the bacteriocin producer against bovine mastitis pathogens, Streptococcus uberis E290, Enterococcus gallinarum E362, and Staphylococcus epidermidis ATCC 12228. The medium composition for pediocin SA131 production by P. pentosaceus SA131 was optimized using response surface methodology. Component of medium was studied as carbon source (glucose, fructose, lactose, glycerol, sucrose, maltose, and mannitol), nitrogen source (beef extract, yeast extract, peptone, malt extract, and tryptone), mineral and surfactant ($MgSO_4$, $KH_2PO_4$, $(NH_4)_2SO_4$, $MnSO_4$, NaCl, sodium acetate, and Tween 80). Through one factor-at-a-time experiment, glucose, fructose, yeast extract, malt extract, NaCl, $MgSO_4$, and Tween 80 were determined as the good ingredient. The effects of major factors for pediocin SA131 production were investigated by two-level fractional factorial designs (FFD). By a $2^4$ FFD, fructose, yeast extract, and $MnSO_4$ were found to be the important factors for the bacteriocin production. Subsequently, a $2^3$ central composite design (CCD) was adopted to derive a statistical model for optimizing the composition of the fermentation medium. The estimated optimum composition for the production of pediocin SA131 by P. pentosaceus SA131 was as follows; 0.13% fructose, 1% glucose, 1.8% yeast extract, 2.58% $MnSO_4$, 0.2% NaCl, and 0.2% Tween 80. The pediocin production under optimized medium was increased to 1,000 AU/mL, compared to the 400 AU/mL in MRS medium.

• KSBB Journal
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• 제11권3호
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• pp.288-294
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• 1996

CHO 세포를 0.5%, 1 %. 2%, 3%, 4% 및 5% 놓도의 FBSd를 함유한 MEMa 배지에 $1{\times}10^4cells/\textrm{cm}^2 와 2{\times}10^4cells/\textrm{cm}^2$의 초기 농도로 정치배양하여 세포 성장과 EPO 생산 특성을 조사하였다. 혈청 농도와 접종 농도를 증가시킴에 따라 세포 증식 속도와 최대 세포 농도가 증가하는 경향을 보였으며, 적절한 혈청 농도의 선택이 세포 성장의 최적화에 필 요하다고 할 수 있다. 세포 성장 도중에 무혈청배지로 교환한 결과 세포 성장과 EPO 생산이 증가되었다. 배지를 교환하지 않았을 경우 세포 성장이 최대 ($2.1{\times}10^5cells/\textrm{cm}^2$)에 도달된 후 급격히 세포농도가 감소하는 높은 사멸율을 보이고, EPO의 최대 농도 도 2,380units/mL에 불과하였으나, 무혈청배지로 교환한 배양에서는 세포 성장이 크게 증가하여 $6.2{\times}105cells/$\textrm{cm}^2$의 최대 세포농도와 7,470units/mL 의 EPO 농도를 얻었다. 따라서 CHO 세포 성장과 E EPO 생산과는 상호 연관이 있으며, 세포배양으로 EPO 생산을 극대화하기 위해서는 CHO 세포의 고 농도 배양이 필요하다고 할 수 있다.

• Journal of Plant Biotechnology
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• 제30권3호
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• pp.301-305
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• 2003

The effects of inorganic nitrogen sources such as KNO$_3$ and NH$_4$ NO$_3$ on cell growth and production of chlorogenic acid and eleutheroside E derivative were investigated in 5L bioreactor cultures of Eleutherococcus senticosus. The cell growth in the 1/2MS medium containing 15mMKNO$_{3}$. The fresh weight of cells harvested from bioreactor was affected by the concentration ratio of NO$_3$$^{[-10]}$ and NH$_4$$^{+}$ in culture medium. At the viewpoint of secondary metabolite production, the production of chlorogenic acid was affected by the concentration of NH$_4$$^{+}$ in the culture medium, but not by the total concentration of nitrogen sources in the culture medium. Futhermore, eleutheroside E derivative production was also affected by the concentration ratio of NO$_3$$^{[-10]}$ and NH$_4$$^{+}$ in the culture medium. Base on those results, it is suggested that cell growth and production of secondary metabolite(chlorogenic acid and eleutheroside E derivative) could be manipulated by controlling the total concentration of nitrogen sources and the concentration ratio of NO$_3$$^{[-10]}$ and NH$_4$$^{+}$ in the culture medium. medium.

• KSBB Journal
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• 제19권6호
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• pp.451-456
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• 2004

교반배양시 배지에 첨가되는 에탄올의 농도가 증가할수록 $Cel^-$ mutant의 발생율이 증가하므로 $1.5\%$ 에탄올이 첨가된 배지의 경우 500 rpm보다 높은 교반속도를 유지해야 효과적으로 $Cel^-$ mutant의 발생이 억제되고 BC 생산량을 증가시킬 수 있다. 교반 배양과 같은 강한 shear stress의 배양환경 하에서는 진탕배양의 경우와 달리 $1.0\%$ 에탄올을 분할공급하더라도 BC 생산의 효율성을 높일 수 없었다. Phosphate ion이 첨가된 배지보다 첨가되지 않은 배지에서 BC 생산량이 더 높았다. 배지조성 중 아세트산의 농도를 $1.0\%$로 증가시키면 균체의 건조중량은 변화가 없었으나 BC 생산량이 감소되었다. 배양액의 pH 제어는 BC의 생산에는 영향을 미치지 않았으나 균체의 성장과 WSPS의 생산을 향상시켰다.

• Biotechnology and Bioprocess Engineering:BBE
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• 제10권4호
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• pp.289-295
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• 2005

In this study, the cultural medium used for the efficient production of $\gamma$-PGA with a newly isolated Bacillus sp. RKY3 was optimized. It was necessary to supplement the culture medium with L-glutamic acid and an additional carbon source in order to induce the effective production of $\gamma$-PGA. The amount of $\gamma$-PGA increased with the addition of L-glutamic acid to the medium. The addition of 90 g/L L-glutamic acid to the medium resulted in the maximal yield of $\gamma$-PGA (83.2 g/L). The optimum nitrogen source was determined to be peptone, but corn steep liquor, a cheap nutrient, was also found to be effective for $\gamma$-PGA production. Both the $\gamma$-PGA production and cell growth increased rapidly with the addition of small amounts of $K_2HPO_4$ and $MgSO_4\cdot7H_{2}O$. Bacillus sp. RKY3 appears to require $Mg^{2+}$, rather than $Mn^{2+}$, for $\gamma$-PGA production, which is distinct from the production protocols associated with other, previously reported bacteria. Bacillus sp. RKY3 may also have contributed some minor $\gamma$-PGA depolymerase activity, resulting in the reduction of the molecular weight of the produced $\gamma$-PGA at the end of fermentation.