• 한국생물공학회:학술대회논문집
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• 2000.11a
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• pp.237-240
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• 2000

Organic acids which were produced from biomass wastes streams by cell-recycle fermentation using Propionibacterium acidipropionici ATCC 4965 were extracted by Membrane Contactor using TOA/MIBK system. Maximum productivity was 3.32g organic acid/L/hr at the dilution rate of 0.2/hr in the results of continuous fermentation. The diluted organic acids in the fermenter were selectively separated by Membrane Contactor extraction using 30%(w/w) trioctylamine(TOA) dissolved in methylisobutylketone(MIBK). The flow rate of aqueous phase is 200ml/min and that of extraction phase is 100ml/min. The degree of Acetic acid and Propionic acid extraction from fermentation broth was reached 56.25%, 72.41% respectively.

• Microbiology and Biotechnology Letters
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• v.20 no.5
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• pp.583-587
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• 1992

This study was conducted in order to optimize the media composition and cultural conditions for kasugamycin production by Streptomyces kasugaensis. The optimum culture conditions are pH 6.6 (before sterilization) and $28^{\circ}C$ for the production of kasugamycin. The kasugamycin concentration was not increased when silicone oil as antifoam agent was added. The addition of water during the cultivation in the various media showed a positive effect for the production of kasugamycin.

• The Korean Journal of Mycology
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• v.22 no.4
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• pp.286-297
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• 1994

The optimum nutritional and cultural conditions of polygalacturonase by Ganoderma lucidum in liquid culture were studied. The optimal temperature, pH, and the duration of culture for production of the enzyme was $30^{\circ}C$, 5.5 and 14 days, respectively. The maximal production of the enzyme was obtained in a synthetic medium containing 10 g of pectin, 10 g of soluble starch, 1 g of yeast extract, 2 g of peptone, 1 g of phenylalanine, 2 g of $KH_2PO_4$, 0.2 g of $MgSO_4{\cdot}7H_2O$, 0.05 g of $CaCI_2$ and 100 g of $thiamin{\cdot}HCI$ in 1000 ml of distilled water.

• Korean Management Science Review
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• v.6 no.2
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• pp.89-96
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• 1989

본 논문에서는 제품의 유효기간이 짧고, 그 수요분포가 정규분포 함수로 주어지는 다품목 생산롯트의 크기를 결정하는 문제가 다루어진다. 총 생산량의 제약하에 2기간 동안의 생산재고 비용을 최소화하는 조건으로부터 적정 기초 재고수준과 롯트 크기를 구하는 효율적 해법이 제시된다. 특수 형태의 하나로 단일품목의 경우에 대한 최적 조건식도 아울러 주어진다.

• Proceedings of the Korean Society of Precision Engineering Conference
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• 1993.04b
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• pp.61-65
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• 1993

절삭작업에 있어서 생산기술자가 제품을 경제적으로 생산하기 위해서는 기계의 사양이나 요구되는 제품의 정밀도 등 을 고려하여 목적에 맞는 절삭조건을 선택하여야 한다. 특히 임금이 과거에비해 크게 오르고 기계의 가격이 자동화로 인하여 고가가 됨에 따라서 기계의 효율적 운용이 점점 더 중요하게 되었다. 따라서 목적에 맞는 절삭조건의 선정은 기업의 경쟁력 향상에 있어서 중요한 문제로 부상되고 있다. 본 논문에서는 정면밀링작업시, 인서트 초기위치오차( Runout)를 고려한 표면조도와 절삭력 시뮬레이션 프로그램을 이용하여 구한 허용동력을 제한조건으로 고려하여 보다 실제에 가까운 상황에서 최소비용과 최대 생산율을 얻도록 프로그램을 개발하였다.

• Journal of agriculture & life science
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• v.50 no.5
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• pp.81-93
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• 2016

Rehmannia glutinosa(Gaertn.) DC. is a herbaceous perennial plant and belonging to the Scrophulariaceae and used as roots for medicinal part and purpose. R. glutinosa is and usually used for fresh rehmannia root or prepared rehmannia root. However, it is very difficult to propagate using the seeds because of lack germination so it is propagated using the vegetative method as the rootstock. Currently, propagation and harvesting using the rootstock of R. glutinosa has difficulties about production of the high quality and quantity in R. glutinosa because of root rot disease. To optimize in vitro cultures and to improve the rootstock and seedling of R. glutinosa after morphological and genetical determination, 5 plant culture media (MS, DJ, LS, QL, and WPM) were used in this study then WPM was selected for better growth, for multiplication condition(WPM + IAA 1.0 mg/L + IBA 0.5 mg/L), and for root enlargement condition(WPM + NAA 0.1 mg/L) of R. glutinosa. Based on these results, in vitro seedlings of R. glutinosa were transferred to soil for acclimation with environment adaptation and shown the positive effects about root enlargement and root formation. Therefore, it can be used for high quality of R. glutinosa production and production of the rootstock based on propagation using in vitro seedlings of R. glutinosa.

• KSBB Journal
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• v.17 no.1
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• pp.14-19
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• 2002

The objective of this study is to investigate optimum condition for lignin peroxidase production by white rot fungi Phanerochaete chysosporium IFO 31249 immobilized in a rotating bioreactor. The maximum lignin peroxidase activity of batch culture in rotating bioreactor was 300 U/L. The optimum rotating speed and packing ratio of support for lignin peroxidase production in a rotating bioreactor were 1 rpm and 20%, respectively. The optimum concentration of $MnSO_4$$\cdot$$H_2O$ for manganese-dependent peroxidase production in a rotating bioreactor was 50 ppm. The sufficient supply of oxygen was the most important factor to achieve maximum lignin peroxidase production. It was possible to produce lignin peroxidase (LiP) and manganese-dependent peroxidase (MnP) for at least 3 times successive repeated-batch cultures, respectively.

• KSBB Journal
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• v.10 no.2
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• pp.176-182
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• 1995

The environmental and physiological factors affecting the production of exopolysaccharide (Methylan) and Poly-${\beta}$-hydroxybutyrate(PHB) by Methylobacterium organophilum were investigated. The maximum PHB content was obtained at $38^{\circ}C$ whereas maximum polysaccharide concentration was $3.54g/\ell$ at $30^{\circ}C$. Optimum pH was pH 7-8 for PHB production and pH 6-7 for polysaccharide production, respectively. Under the condition of $Mo^{2+}, Mg^{2+} or Mn^{2+}$ limitation with nitrogenlimitation, the PHB accumulation was increased, whereas the polysaccharide production was decreased as compared with that of solenitrogenlimitation. Under the condition of sole K+ limitation, cell growth was significantly inhibited and no polysaccharide was produced. However, the PHB content was as high as 60% of dry cell weight. Effect of C/N ratios (methanol/ammonium) in the feeding solution was examined for the simultaneous production of polysaccharide and PHB. The higher ratio of C/N showed the lower cell growth, higher content of PHB in cells, and higher yield of polysaccharide.

• Journal of the Korean Institute of Gas
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• v.22 no.3
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• pp.65-73
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• 2018

Coalbed methane has a nonlinear desorption curve depending on the pressure, so an appropriate production system should be constructed considering this phenomenon. The capacity and specification of the coalbed methane gas production facility are determined by the gas flow rate and pressure in the coalbed, which is the external boundary condition of the system. Thus, it is essential to analyze these characteristics in gas production. The gas inflow equation was calculated using the reservoir flow model and utilized as the boundary condition of the whole production facility in this study. Also, to understand the effect of pressure drop on the gas flow in the production facility, the nodal analysis was performed using the flow analysis simulator of production equipment, and we determined the proper specifications and operating conditions of the production facility. This study presents a design criteria as to production and gathering system capable of effectively transporting coalbed methane.

• Applied Chemistry for Engineering
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• v.23 no.6
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• pp.594-598
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• 2012

In the present study, biogas was produced from the anaerobic digestion of marine macroalgae (Laminaria japonica) biomass. The optimal anaerobic condition for producing the sludge was the freeze treatment at $-70^{\circ}C$ for 20 min. Total amounts of hydrogen and methane gas produced were 667.28 mL/L and 3420.24 mL/L, respectively, which were 2.7 and 3.4 times greater than that in the control group. Freeze treatment of sludge produced the maximum biogas under an initial optimum pH of 7.0 and the maximum biomass at an initial optimum pH of 8.0. We confirmed that biogas production was greatly reduced under acidic conditions compared to that under alkaline conditions. Sludge was freeze treated, and the biomass and sludge production was optimal the total amounts of hydrogen and methane gas produced were 643.73 mL/L and 4291.6 mL/L, respectively, which were 2.6 and 4.3 times greater than in the control group. Also the results showed that under optimal conditions in a 5-L bioreactor, a maximum of 1605.03 mL/L of hydrogen and 4593.71 mL/L of methane gas could be produced by the substrate contained in the marine macroalgae biomass.