• Asian-Australasian Journal of Animal Sciences
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• 제14권6호
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• pp.844-849
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• 2001

This study was carried out to determine the optimum conditions for cholesterol removal from homogenized milk by treatment with saponin using a response surface methodology (RSM). The effects of temperature, reaction time, and amounts of celite or saponin added on cholesterol removal from milk were investigated. The level of cholesterol removal from milk increased with saponin concentration and varied from 57.4 to 73.3%. The optimum reaction time, amount of celite addition determined by a partial differentiation of the model equation, and amount of saponin addition were 30min, 0.95% and 1.5%, respectively. Under these conditions, the predicted cholesterol removal by RSM was estimated to be 73.4%. The experimental removal value was 73.7%. Thus, there was no appreciable difference between the experimental value and the predicted value based on RSM.

• 대한치과교정학회지
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• 제32권5호
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• pp.301-312
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• 2002

상악골 전방견인 장치를 이용한 골격성 III급 부정교합 환자의 악정형적 치료에서 치료시기는 치료효과에 지대한 영향을 미칠 수 있으며 이상적인 치료시기는 연구자에 따라 다소의 차이는 있으나 다른 형태의 부정교합보다는 다소 이른 사춘기 이전의 어린 나이라는 것이 선학들의 공통된 의견이었다 하지만 통계적 자료들을 바탕으로 한 최근의 논문들은 과거 선학들의 의견을 뒷받침 해주는 논문과 그렇지 않은 논문들로 나뉘고 있어 이상적 치료시기에 대한 정립된 의견이 없는 실정이다. 이에 본 연구에서는 119명의 환자들의 수완부골 방사선 사진을 평가하여 골성숙도에 따라 사춘기전군과 사춘기군으로 분류하고 치료전후 측모두부방사선 사진을 분석하여 상악골 전방견인에 대한 치료효과를 비교하였다. 평균 치료기간은 사춘기전군은 6.5개월, 사춘기군은 6.1개월이었으며 치료전후의 측모두부방사선 사진을 분석한 결과 다음과 같은 결론을 얻었다. 1. 상악골의 전방이동양은 사춘기전군과 사춘기군간에 차이가 없었다. 2. 상악골의 하방이동양은 사춘기전군과 사춘기군간에 차이가 없었다. 3. 하악골의 하방이동양과 후하방회전양은 사춘기전군과 사춘기군간에 차이가 없었다. 4. 치성이동양은 사춘기전군과 사춘기군간에 차이가 없었다. 이상의 결과로 사춘기전 뿐 아니라 사춘기에서도 상악골 전방견인에 의해 상악골 성장촉진과 함께 성공적인 악정형 치료가 가능함을 알 수 있었다.

• 한국의류학회지
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• 제33권7호
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• pp.1121-1127
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• 2009

This study presents an eco-friendly and one-step finishing method for modifying fiber property that reduces fiber damage in wool/polyester blend fabrics. Lipase from aspergillus oryzae is used in this experiment. The enzymatic treatment condition is optimized by measuring the relative activity of lipase depending on pH level, temperature, concentration of lipase, and treatment time. The concentration of $CaCl_2$as an activator is determined by the characteristics including whiteness, water contact angle (WCA), and dyeing property. The modified properties of lipase treated fabrics are tested for pill resistance and surface morphology. The results are described as follows: the optimum condions for lipase treatment constitute a pH level of 8.0, treatment temperature of 40$^{\circ}$$_C$, concentration of lipase at 100% (o.w.f), and a treatment time of 90 minutes. $CaCl_2$helps in raising lipase activation, and the optimum concentration is 50mM. The whiteness, wet ability, and pill resistance of lipase treated fabrics improves as compared to the control. The dyeing property of lipase treated fabrics improved by 53.5% after using the one-bath dyeing method. This means that lipase treatment can save time and cost during the dyeing process since lipase treatment modifies wool and polyester fibers. The surface of lipase treated wool fibers do not exhibit any change, however voids and cracks manifest on the surface of lipase treated polyester fibers.

• 상하수도학회지
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• 제23권2호
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• pp.207-214
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• 2009

This study examines the optimum filtration conditions in pretreatment of seawater desalination by reverse osmosis. For this purpose, Masan bay seawater is treated through a gravity filter column while $FeCl_3$ is added as coagulant. The conditions of coagulantd osage, media depth, filtration rate, and backwash time are evaluated. The study results show that the filtrate quality improved with increasing coagulant dosage, but head loss rapidly increased. After 4mg/L, the unit filter run volume reduced to less than $200m^3/m^2$. Considering the head loss development, 4mg/L is determined as the optimum dosage. The better filtrate qualities are obtained with depth of 100cm than that of 80cm. The two stage filtration, which outperformed the single stage filtration, is suggested for treatment of Masan bay. The filtration rate of 5m/h is decided as the optimum condition considering the head loss development. At 10m/h, the filtrate quality deteriorated even though the extent was minimal, and head loss increased rapidly. The backwash time of 10 min is decided appropriate.

• 한국의류학회지
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• 제32권7호
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• pp.1075-1081
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• 2008

Eco-friendly processing using enzymes has been focused in textile industry in order to reduce environmental pollutions. This paper was suggested to hydrolyze non-cellulose, such as fats and waxes in cotton fabrics by lipase treatment. Enzymatic treatment conditions were controlled according to pH, temperature, enzyme concentration, and treatment time. The physical properties of the lipase-treated cotton fabrics were evaluated by measuring weight loss, moisture regain and dyeing properties. The surface morphology of lipase-treated cotton fabrics were observed by SEM. As a result, the optimum conditions for the lipase treatment were at pH 4.2, temperature 50$^{\circ}C$, concentration 50%, and treatment time 90 minutes. Calcium chloride and Triton X-100 were effective auxiliaries in lipase treatment.

• 상하수도학회지
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• 제21권3호
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• pp.359-366
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• 2007

Slow sand filtrations have been widely used for water treatment in small communities, however their capacity is often limited by high turbidity in the raw water. For this reason, several pre-treatment facilities were required for a slow sand filter. Turbidity removal from the highly turbid raw water was investigated in roughing filters as a pre-treatment process. The roughing filters followed by rapid mixing tank were operated in the form of a contact filtration. In several jar tests, the predetermined optimum aluminium sulfate (alum) doses for turbid water of 30 and 120NTU were 30 and 50mg/L, respectively. At the optimum alum dose, physically optimum parameters including G value of $220sec^{-1}$ and rapid mixing time of 3 minutes were applied to the contact filtration system. Without addition of alum, the filtrate turbidity from the roughing filters, packed respectively with different media such as sand, porous diatomite ball and gravel, was in the range of 5~30NTU at filtration velocities of 30 and 50m/day. However, the application of a contact filtration to roughing filters showed stably lower filtrate turbidity below 1.0NTU at filtration velocity of 30 m/day. Although the filtration velocity increased to 50m/day, filtrate turbidity was still below 1.0NTU in both single and double layer roughing filters. At influent turbidity of 120NTU, the filtrate turbidity was over 5 NTU in the triple layer roughing filter, which shortened the filter run time. The flocs larger than $10{\mu}m$, formed in the rapid mixing tank, were almost captured through the roughing filter bed, while the almost flocs smaller than $10{\mu}m$ remained in filtrate.

• Journal of Ginseng Research
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• 제39권4호
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• pp.304-313
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• 2015

Background: Ginsenoside Rg3 is a promising anticancer agent. It is usually produced by heat treatment of ginseng, in which ginsenoside Rb1 is the major ginsenoside. A kinetic study was conducted to optimize ginsenoside Rg3 production by the heat treatment of ginsenoside Rb1. Methods: Ginsenoside Rb1 was heated using an isothermal machine at $80^{\circ}C$ and $100^{\circ}C$ and analyzed using HPLC. The kinetic parameters were calculated from the experimental results. The activation energy was estimated and used to simulate the process. The optimized parameters of ginsenoside Rg3 production are suggested based on the simulation. Results: The rate constants were $0.013h^{-1}$ and $0.073h^{-1}$ for the degradation of ginsenosides Rb1 and Rg3 at $80^{\circ}C$, respectively. The corresponding rate constants at $100^{\circ}C$ were $0.045h^{-1}$ and $0.155h^{-1}$. The estimated activation energies of degradation of ginsenosides Rb1 and Rg3 were 69.2 kJ/mol and 40.9 kJ/mol, respectively. The rate constants at different temperatures were evaluated using the estimated activation energies, and the kinetic profiles of ginsenosides Rb1 and Rg3 at each temperature were simulated based on the proposed kinetic model of consecutive reaction. The optimum strategies for producing ginsenoside Rg3 from ginsenoside Rb1 are suggested based on the simulation. With increased temperature, a high concentration of ginsenoside Rg3 is formed rapidly. However, the concentration decreases quickly after the reaching the maximal concentration value. Conclusion: The optimum temperature for producing ginsenoside Rg3 should be the highest temperature technically feasible below $180^{\circ}C$, in consideration of the cooling time. The optimum reaction time for heat treatment is 30 min.

• 한국잠사곤충학회지
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• 제42권1호
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• pp.48-57
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• 2000

This study was undertaken to figure out the effects of hydrolysis conditions on the solubility of insoluble sericin, molecular weight distribution and thermal characteristics of hydrolysates in enzymatic hydrolysis by Alcalase 2.5L. It was indicated that the optimum treatment temperature and pH for the insoluble sericin were 50$\^{C}$ and 11, respectively. When the insoluble sericin was hydrolyzed with a various treatment conditions, the solubility of all hydrolysates were represented above 85% at given conditions. As the enzyme concentration increased, the solubility increased roughly, but the solubility increasement ratio was less above 2% enzyme concentration. As the treatment time increased, the solubility was also increased. It was showed in the molecular weight distribution of hydrolysates treated various enzyme concentrations and treatment times that when enzyme concentrations were 0.5, 2, 3%, the peaks of the distribution curve were shifted to left side which meant low molecular weight and was distributed much quantity with shifted to be left side, but treatment time was 6 hr. the peak was shifted to right side. When enzyme concentration was 5% and treatment time was below 2 hr., the peaks were shifted to right side, but treatment time was above 4hr. the peak was shifted to left side. The number-average molecular weights were distributed from 300 to 800 and those were decreased when treatment time was up to 4 hr., but increased a little when treatment time was 6hr. It was showed in the DSC curves of hydrolysates treated with treatment time of 0.5, 1, 2, 4, 6 hr. fixed 1% o.w.s enzyme concentration and control that the endothermic peak was observed near at 200$\^{C}$. The denaturation peak of the hydrolysates depending on treatment times had a tendency to shift to higher temperature. But, when the treatment time was 6 hr., the peak was shifted to lower temperature comparing another hydrolysates.

• 한국자원리싸이클링학회:학술대회논문집
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• 한국자원리싸이클링학회 2003년도 추계정기총회 및 국제심포지엄
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• pp.122-128
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• 2003

To develop a Mg-Zeolite for simultaneous recovery of the N and the P from sewage water, the natural zeolite was treated with 20% $MgCl_2$ solution by changing the pH the temperature and the treating time of the solution. And the contents of Ca Fe Na K Mg of Mg-Zeolite were analyzed by ICP. The optimum treatment condition for Mg-Zeolite was induced to pH 7.0 $50^{\circ}C$ in 20% $MgCl_2$ solution and for 80min treatment. And the Na and the K ions in natural zeolite are significant factors for Mg exchange in the zeolite.

• 대한환경공학회지
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• 제22권6호
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• pp.1011-1019
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• 2000

본 연구는 유입수의 농도, 수리학적 체류시간 및 F/M비와 슬러지 첨전성과의 상관관계를 새롭게 명확히 밝혀 기존에 제시된 각 처리법 즉 장기포기법, 재래식 활성슬러지법, 고율 활성슬러지법 및 수정포기법의 설계조건이 도출된 원인을 밝히고 동시에 이들 기 제시된 설계조건에 관계없이 설계가 가능함을 확인하기 위한 연구이다. 본 실험은 특히 체류시간과 미생물의 침강성을 중심으로 고찰되었는데, 이는 슬러지의 침강성이 기존 각 처리법의 운전조건을 결정하는 주인자$^{1)}$이기 때문이다. 따라서 각각의 처리법에 대해 제시된 설계범위를 벗어날 경우 슬러지는 팽화하는 것으로 알려져 있으며, 설계의 기초를 제공한 Lesperance$^{1)}$의 실험결과에서도 침강성이 확보되지 않는 부하범위가 발생하는 것으로 나타냈다. 위와 같이 일정 조건에서 슬러지가 팽화하는 원인은 Lesperance가 이전 다년간의 실패와 시도로 밝혀진 연속운전이 가능한 것으로 밝혀진 몇몇의 운전조건을 실험조건으로 채용함에 따라 각각의 체류시간에 해당하는 최적의 부하가 적용되지 않았기 때문이다. 하지만 본 실험결과 부하를 적절히 유지할 경우, F/M비 $6.3kg-BOD/kg-MLSS{\cdot}day$ 이하, HRT 0.67hr 이하의 조건에서 슬러지의 침강성이 SVI치 120 이하로 확보될 수 있음을 확인하였다. 따라서 본 연구에서는 체류시간과 그에 해당하는 최적 부하를 제시하였으며, 체류시간이 미생물의 침강성에 결정적 영향인자임을 밝히고, 아울러 본 실험결과를 근거로 이제까지 알려진 처리법에서는 적용된 바 없는 1시간 이하의 체류시간에서 고율 활성슬러지법의 적용 부하치를 수 배 능가하는 새로운 운전법 (UHR : Ultra high rate)도 가능함을 제시하였다.