• Proceedings of the Korean Society for Bio-Environment Control Conference
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• 1998.10a
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• pp.129-133
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• 1998

감자 무병종서의 대량급속 증식을 위해 기내소괴경 생산방법을 이용하는 연구가 많이 이루어져 왔다. 기내소괴경 형성에 관한 연구는 Grego(1956)에 의하여 최초로 가능성이 제시된 이후 많은 연구자들이 이에 대하여 보고하였으나 (Han, 1987; Hussey 등, 1984; Garcia 와 Gomez, 1973; Wiersema 등, 1987), 소괴경의 크기가 작아 파종후 입모율이 떨어지고, 생육초기 포장관리가 까다로운 점등의 문제점으로 실용화가 정착되지 못하고 있다. (중략)

• Journal of the Korea Organic Resources Recycling Association
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• v.11 no.1
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• pp.127-128
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• 2003

본 연구는 퇴비화 과정 중 난용성 인산의 가용화와 무기태 인산의 변화를 알아보기 위하여 수행하였다. 비료와 퇴비중의 인산형태는 다른 성분들보다 토양에 흡착 또는 고정되거나 불용화 되는 양이 많아 작물의 흡수량이 적다. 시비된 인산의 흡수율은 낮고, 그 대부분은 난용화되기 때문에 토양에 축적되거나 세탈과 용탈에 의해 수질을 오염화시키는 주원인이 되고 있다. 퇴비화 과정중의 인산형태별 함량변화를 분석조사하여 작물에 시비되는 인산비료와 퇴비의 시용량을 적절하게 조절하여 인산의 과잉 시비량을 저감시키기 위한 연구이다. 돈분을 원료로 한 퇴비화 과정에서 단계별로 퇴비시료를 채취하여 총인산(T-P), 유효인산(Avail. -P)과 무기태인산분획별(Ca-P, Al-P, Fe-P)로 분석한 결과는 다음과 같다. 퇴적더미의 초기부피는 570L였으며, 약 2개월간의 퇴비화를 통해서 시료채취와 미생물등의 분해작용으로 최종부피는 430L정도로 감소하였다. 이는 초기의 부피보다 25% 감소하였다. 퇴적더미의 분해로 인한 용적밀도의 변화를 고려하면, 총인산 함량은 초기 약 17,500mg/kg에서 최종시료는 22,500mg/kg로 증가되었다. 또한 퇴비화가 진행됨에 따라 인산의 가용태가 증가하는 결과를 보였으며, 초기의 유효인산이 4,500mg/kg에서 최종시료에서는 8,900mg/kg으로 증가되었다. 그리고 무기태 인산분획별 인산의 형태별 변화를 조사한 결과, 퇴비화 과정 중 Ca-P의 경우 pH와의 중요한 상관관계를 갖고 있었다. 유기물분해를 통해 유리된 인산과 Ca은 난용태로 전환되는데, 초기의 약 10일 동안 Ca-P의 감소원인은 pH의 감소로 인한 Ca이 유리되는 정도가 낮기 때문인 것으로 해석된다. 초기 Ca-P형태의 인산함량은 11,900mg/kg으로 Fe-P와 Al-P보다 많았다. 또한 퇴비화가 안정화되어 부숙된 최종시료의 무기태 인산분획물 중 Ca-P는 18,000mg/kg로 증가하였으며, Ca-P>Al-P>Fe-P의 순 이었다. 그러나 Al-P와 Fe-P 형태의 무기태인산은 초기의 함량비율보다 다소 감소한 결과를 보였다. 결론적으로, 퇴비화과정 중 단계별 인산함량의 형태전환을 분석한 결과 총인산의 함량은 퇴비화가 안정화될수록 부피감소로 인한 인산함량이 증가하는 경향을 보였지만, 유기물질의 분해로 인한 원료내 인산의 형태가 불용태와 난용태에서 가용태 인산으로 전환되는 것을 도출하였다. 또한 무기태 인산분획물에서는 Ca-P 인산형태가 퇴비화가 진행될수록 증가한다는 결과를 얻었으며, Fe-P와 Al-P는 분해된 유기물의 킬레이트작용으로 감소되었다고 판단되며, 그 존재형태가 경쟁적임을 알 수 있었다. 따라서 화학비료와 퇴비의 시용이 병행될 경우에는 퇴비의 가용태 인산함량뿐만 아니라 무기태 인산의 함량을 분석한 후 인산질비료의 시비량을 조절해야할 것으로 판단된다.

• Journal of the Institute of Electronics and Information Engineers
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• v.52 no.3
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• pp.199-205
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• 2015

This study is about ionic water generator filter Recently, a lot of people feel deep interest in health and drinking water. And there are various types of water. Ionic water generator is a system with special function, and can be classified as a medical device and should be manufactured after approval from the Food and Drug Administration. Basically ionized water is different from the packaged and stored water. When the tap water or ground water passes through the various filters of ionic water generator, it turns to the purified water of pH7 ~ 7.5 and we can electrolyze that water into anion and cation by diaphragm. And in negative electrode side, we can get alkaline water with calcium ($Ca^+$), potassium ($K^+$), magnesium ($Mg^+$), sodium ($Na^+$) for body. In general, we can change pH value from 5 to 9 of ionizer by controlling the level of electrolysis voltage in the ionizer. In general, 1stage (pH8), 2stage (pH8.5), 3stage (pH9), 4stage (pH9.5) are used as the alkaline ionized water, -1Stage (pH6.0), -2 stage (pH5.0) are used as the acidic water. But in early stage, the water that passed through filter was weakly alkaline water and that was problem. Therefore, when filter condition is stable, the pH and ORP value of water is different with the early one. the initial setting pH value of the ionizer was confirmed that changes significantly. In order to resolve this problem we need to wash filter for some period time and neutralize by acidification treatment of the filter.

• Microbiology and Biotechnology Letters
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• v.20 no.2
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• pp.203-206
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• 1992

Conditions of fermentation for the production of demethyltetracycline were examined using the mutant, which was obtained through the cell fusion of demeclocycline producing strains, The optimum temperature and the initial pH of broth for demethyltetracycline fermentation were $25^{\circ}C$ and 6.7, respectively. Unlike any other cases, the control of pH with alkali solution during the fermentation process affected the productivity. As a general rule, the larger the inoculum size the higher the early consumption of sugar and the viscosity of broth, which means that fermentation proceeds more rapidly as the inoculum size is increased. The highest productivity was shown when the inoculum size was 5% (v/v), and the phase of seed also influenced the fermentation. Among the parameters of pre-culture thus examined, pH was the most important factor.

• Journal of Korean Society of Environmental Engineers
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• v.22 no.11
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• pp.1985-1994
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• 2000

This research was designed to investigate the effect of initial adsorbed amount of phenol, temperature, and pH on the desorption reaction of phenol from spent activated carbon loaded with phenol. Methanol, acetone, and N,N-dimethylformamide( DMF) were used as test organic solvents. The initial adsorbed quantities of phenol investigated here were 166.1mg/g, 180.7mg/g, and 197.9mg/g. The effect of temperature was evaluated from 15 to $55^{\circ}C$ with an interval of $10^{\circ}C$, while that of pH was investigated under acidic. neutral. and alkaline conditions. The extent of phenol desorption was proportional to the strength of dipole moment such as methanol < acetone < DMF. Over 90% desorption of phenol was achieved by acetone and DMF. The quantity of des orbed phenol by the organic solvents decreases with increasing the initial adsorbed amount of phenol. DMF is affected least by the initially adsorbed amount of phenol. An increase in reaction temperature leads to higher desorption of phenol. Desorption reaction by methanol is most sensitive to the temperature. As the pH of solvents increases. the desorption rate is also increasing. At pH=12. the desorption rate of phenol by methanol increases sharply by 10%. Although methanol demonstrated the weakest desorption power. the desorption capacity of methanol would approach that of acetone and DMF by adjusting temperature and pH. Methanol may emerge as a promising solvent for removing phenol from activated carbon because of acceptable regeneration efficiency as well as relatively cheap price.

• Journal of the Korea Organic Resources Recycling Association
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• v.5 no.2
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• pp.17-28
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• 1997

To study the possibility of agricultural utilization of industrial wastewater sludge, the changes of the substances, such as temperature, pH, inorganic and organic matter, the form of nitrogen, fatty acid and the population number of microorganisms during composting periods were investigated. Temperature and $CO_2$ generation were the highest in the second day of composting peroids, and then were gradually fallen. And they were similar to room temperature after the sixth day of composting periods. C/N ratio was a little increased as time went by. pH value was not changed in early composting periods and then pH had been gradually decreased since it was rapidly increased. It was in the range of 8.7~8.8 in late composting periods. The contents of $P_2O_5$, $K_2O$, CaO, MgO and Fe were a little increased and that of ${SO_4}^{2-}$ was increased with 62~67% in late in comparing with early composting periods. The contents of ether extracted materials, water soluble polysaccharides, hemicellulose and cellulose were decreased but that of resins and lignin were not changed during composting periods. The contents of total and organic nitrogen were decreased but that of inorganic nitrogen was increased during composting periods. The population number of microorganism during composting periods was too much changed according to the kinds of bulking agents and microorganisms, and the composting periods.

• KSBB Journal
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• v.10 no.3
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• pp.304-316
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• 1995

For fuel alcohol production, enzymatic liquefaction and saccharification of tapioca starch by ${\alpha}$-amylase and glucoamylase were studied. The thermophilic ${\alpha}$-amylase Termamyl produced from Bacillus licheniformis gave a better liquefaction than the relalively low temperature enzyme BAN from B. subtilis. Oplimal temperature and pH with Termamyl were $90∼95^{\circ}C$ and 5.8, respectively. Minimal amount of Termamyl 240uc for a satisfactory liquefaction for a two-hour reaction was about 0.0125% (v/w) with respect to the mass of tapioca used. For saccharification experiments two enzymes, Novo AMG and Do-I1 enzymes were compared. The enzymatic activity of each enzyme was a little different depending on the substrate used and the latter was found to have a significant amount of ${\alpha}$-amylase activity. With Novo AMG optimal temperature was about $58^{\circ}C$ The pH optimum was 4.3 with maltose, however, with tapioca, no difference was observed between pH 4.3 and 5.7 which is a natural, unadjusted pH of liquefied tapioca. For 85% of completion of saccharification, it was necessary to use 0.0625% (v/w) of Novo AMG 400L for tapioca and to run the reaction for more than 10 hr, Packed volume of solid particles in tapioca slurry remained at around 30% during liquefaction and saccharification. This indicates that the removal of the solid particle before fermentation is not economically feasible at all, even though the solid particles make it very difficult to operate the bioreactor in a continuous mode with cell-recycle.

• Microbiology and Biotechnology Letters
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• v.30 no.1
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• pp.26-32
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• 2002

For commercial production of Korean fermented anchovy sauce through rapid fermentation, a bacterial strain which showed the high protease activity was isolated from a commercially fermented anchovy sauce. The isolate was Bacillus amyloliquefaciens, and named as B. amyloliquefaciens HTP-8. The incubation temperature, initial pH, and cultivation time for optimal production of protease by B. amyloliquefaciens HTP-8 were $30^{\circ}C$, 7.0, and 3 days, respectively. In jar fermenter, B. amyloliquefaciens HTP-8 showed higher protease activity when grown at pH 7.0. The protease was partially purified by 80% ammonium sulfate precipitation and CM-Sephadex C-50 ion exchange chromatography. The partially purified enzyme had specific activity of 103.3 units/mg, yield of 0.4%, and purification fold of 43.0. The optimal pH and temperature for the protease activity were 10.0 and $50^{\circ}C$, respectively. The protease was relatively stable at the pH range of 7.0~12.0 and at the temperatures below 4$0^{\circ}C$. The activity of the enzyme was inhibited by $Ag^{＋}$ /, $Ba^{2＋}$ and selectively inhibited by PMSF, suggesting that it is a serine protease.

• Proceedings of the Korean Society of Soil and Groundwater Environment Conference
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• 2001.04a
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• pp.34-37
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• 2001

폐수처리분야에 널리 사용되어 온 펜톤산화반응을 응용한 Fe$^{\circ}$/$H_2O$$_2$시스템을 이용하여 고농도 유류오염 미세호양(100$\mu\textrm{m}$이하)의 화학적 산화처리 실험을 수행하였다. 반응은 100$m\ell$, 삼각프라스크에 오염토양(5g)과 반응시약을 주입한 후 자석교반기를 이용하여 회분 식으로 진행하였으며 일정 시간(0, 1, 2, 4, 8, 24hr)별로 TPH를 측정하였다. 그리고 각 조건별 시간에 따른 반응특성을 살펴보았다. 일반적으로 알려진 펜톤산화반응의 수요 반응조건인 초기 pH /$H_2O$$_2$ 및 Fe$^{\circ}$의 주입농도, 그리고 초기 디젤오염농도의 조건을 변화하며 각 조건별 처리효과를 알아보았다. 본 연구결과에서 최적 pH조건은 3인 것으로 나타났으며, 분말철(Fe$^{\circ}$)과 $H_2O$$_2$의 주입농도를 증가함에 따라 오염토양의 TPH 제거효율도 비례적으로 향상되었다. 초기오염농도에 따른 최종 처리효율은 큰 차이가 없었으나. 고농도 오염일수록 제거된 디젤의 총량은 크게 나타나. 본 논문에서 제시한 방법이 고농도 오염토양일수록 더 큰 효과를 얻을 수 있음을 보여주었다. 대부분의 반응이 반응개시 후 약 8시간 이내에 이루어졌는데, 반응에 수반되는 pH 상승과 그에 따른 반응성의 저감효과를 일정 pH 조절에 의해 감소시킴으로써 반응성의 향상을 좀 더 높일 수 있을 것으로 판단된다. 결론적으로, Fe$^{\circ}$/$H_2O$$_2$시스템을 이용한 화학적 산화처리방법은 경제성과 처리성능에서 고농도 유류오염 미세토양의 효율적인 처리방안으로서 향후 적용 가능성이 높을 것으로 기대된다.

• 한국생물공학회:학술대회논문집
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• 2002.04a
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• pp.201-204
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• 2002

The gellan was extracellular polysaccharide produced by Pseudomonas elodea A TCC 31461 at aerobic condition. Gellan provides various functionalities such as gelling, suspending, stabilizing, emulsifying and binding properties in aqueous systems. In this study, the effect of pH on the cell growth and the gellan production were evaluated in shake- flasks and in 5 ${\ell}$ batch fermentor. In the shake-flasks culture, maximum gellan production was obtained with 1.66g/ ${\ell}$ when initial pH was 7.0. The batch fermentation was performed in the medium pH control ranged pH 5.5-8.5. The maximum gellan production of 1.97g/l was obtained with constant pH 6.0.