• 산업기술연구
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• 제27권B호
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• pp.161-167
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• 2007

The objetives of this study are to set up optimum extraction temperature, time and organic solvent for propolis extraction, to investigate chemical properties, and to develop health foods from propolis preparation. In this study, ethanol and ultrasonic extracts method performed to optimum extraction temperature was at 60, $20^{\circ}C$, optimum extraction time was at 12, 4 hours and optimum extraction amount of solvent was at 20, 15 times of propolis weight. When various ethanol solutions were used, whereas flavonoid content was highest in 70, 80% aqueous ethanol, respectively. So the ultrasonic extracts method used gave better results than the ethanol extracts method in this work. Extraction of propolis with etanol and ultrasonic extracts method was performed by using the water and various concentrations of aqueous ethanol as solvent. Sensitivity of propolis samples to Staphylococcus aureus was investigated and the results were shown. Samples of water extract did not inhibit microbial growth, where as 50% aqueous ethanol extract the largest inhibitory zone for Staphylococcus aureus, then decreased inhibition with increasing ethanol concentrations.

• 한국환경과학회지
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• 제9권2호
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• pp.159-164
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• 2000

For the purpose of development of a liquid membrane permeator which separates metal ions from aqueous solutions continuously and effectively, a continuous membrane permeator with the membrane solution trapped between extraction and stripping phases by two micro-porous hydrophilic films was manufactured. Experimental researches on the separation of zinc ion from aqueous solutions were performed in the liquid membrane permeator with 30 vol % D2EHPA solution in kerosine as liquid membrane. As results, the liquid membrane permeator separates zinc ion from aqueous solutions continuously and effectively in the wide range of operating conditions. A simple mass transfer rate model using equilibrium constant of the extraction reaction for the system used were proposed, and the model was compared with experimental results of separation of zinc ion in the permeator. And the effects of operating factors, such as space time, pH of extraction solution, extraction temperature, on the separation rate of zinc ion in the permeator were experimentally examined.

• Nuclear Engineering and Technology
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• 제32권6호
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• pp.531-536
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• 2000

The extraction of precious metals from aqueous solutions is performed by using a photoredox reaction with a Q-switched Nd:YAG laser. The metallic silver was efficiently precipitated and extracted from the silver nitrate solution by laser photolysis. An optimum reaction condition for silver extraction was determined by adjusting various experimental factors such as type of reducing agent, type of acids and reaction time. The composition of the reaction product was analyzed and it was identified as metallic silver, not other molecular types. The photoreaction of chromium(III) chloride in an acidic aqueous solution was also investigated. The 355 nm laser light was better suited for the reaction of silver nitrate as well as chromium(III) chloride in an acidic solution compared to the 532 nm light.

• Preventive Nutrition and Food Science
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• 제21권4호
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• pp.355-360
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• 2016

The influence of extraction temperature, powder concentration, and extraction time on the antioxidant properties of aqueous ginger extract was investigated. The possibility of estimating the antioxidant properties of the extract from its absorbance and colour properties was also investigated. Results indicated that powder concentration was the most significant factor to consider in optimizing antioxidant extraction. However, temperature and time still influenced the 2,2'-azinobis-(3-ethylbenzothiazoline-6-sulfonic acid) (ABTS) radical scavenging activity while extraction temperature influenced the 2,2-diphenyl-1-picrylhydrazyl (DPPH) radical scavenging activity of the extract. Using the total phenol content, total flavonoid content, ABTS radical scavenging activity, and DPPH radical scavenging activity of the extract, the multiresponse optimization condition for extraction of antioxidant based on the experimental range studied is $96^{\circ}C$, 2.10 g/100 mL, and 90 min. The absorbance of the ginger extract at 610 nm could be exploited for rapid estimation of its total flavonoid and polyphenol with a $R^2$ of 0.713 and 0.753, respectively.

• 한국재료학회지
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• 제34권5호
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• pp.247-253
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• 2024

The separation of zirconium and hafnium using tributyl phosphate (TBP)-Dodecane extractants in nitric acid medium was performed. Zirconium oxychloride, used as extraction feed, was obtained from the synthesis of Kalimantan zircon sand concentrate smelted using NaOH. The extraction process was carried out by dissolving chloride-based metals in nitric acid media in the presence of sodium nitrate using TBP-Dodecane as an extractant. Some of the extraction parameters carried out in this study include variations in organic phase and aqueous phase (O/A), variations in contact time, and variations in nitric acid concentration. Extraction was carried out using a mechanical shaker according to the parameter conditions. X-ray fluorescence (XRF) was used for elemental (Zr and Hf) composition analysis of the aqueous solution. The results showed that zirconium was separated from hafnium at optimum conditions with an organic/aqueous ratio of 1:5, contact time of 75 min, and an HNO₃ concentration of 7 M. The resulting separation factor of zirconium and hafnium using TBP-Dodecane was 14.4887.

• 자원리싸이클링
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• 제9권3호
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• pp.29-36
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• 2000

아연제련잔사로부터 고순도 갈륨을 회수하기 위하여 알칼리 갈륨의 용매추출실험을 수행하였다 실험결과 Isopropyl Ether에 의한 갈륨의 추출시 수용액의 염산농도가 증가할수록 갈륨의 추출이 증가하여 약 7.4M/L의 염산농도에서 증가할수록 추출이 증가하여 갈륨과 분리하기가 매우 어렵다. 그러나 D2EHPA에 의해 추출할 경우 철은 염산농도 2M/L 까지는 100% 추출되고 있으나, 갈륨은 염산농도 2M/L에서는 거의 추출이 이루어지지 않아 수용액의 염산농도를 조절함으로써 갈륨과 철을 용이하게 분리. 회수할 수 있다. 아연제련잔사로부터 알칼리침출, 중화침전, Isopropyl Ether과 D2EHPA를 사용한 용매추출공정을 거쳐 갈륨을회수한 결과, 순도 99wt%, 이상의 $Ga_2O_3{\cdot}H_2O$를 얻을 수 있었다.

• 한국축산식품학회지
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• 제24권1호
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• pp.80-85
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• 2004

본 연구에서는 역미셀을 이용한 단백질 추출공정에서 적극적으로 활용되지 못했던 양이온 계면활성제에 의한 단백질 추출 가능성을 제시하였으며 초유로부터 IgG의 분리를 위한 반응조건을 조사하였다. IgG의 분리에 적합한 조건은 반응 수용액상의 경우 pH 8, 50 mM KCl었으며 유기용매상의 계면활성제(CDAB) 농도는 100 mM로 나타났다. 위의 조건에서는 초기시료에 존재하는 IgG의 90%이상이 회수되었으며 회수된 단백질의 93%가 IgG로 나타났다. 또한 본 연구는 기존의 역미셀을 이용한 일반적인 단백질 추출공정인 정추출 및 역추출 공정을 이용하지 않고 정추출 공정만을 이용함으로써 추출과정을 단순화하였다.

• Nuclear Engineering and Technology
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• 제51권3호
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• pp.761-768
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• 2019

Understanding the phenomena of formation of single drops is necessary to understand the hydrodynamics in solvent extraction equipment which are used for separation of nuclear materials. In this work, the phenomena of aqueous phase and organic phase drop formation at submerged nozzles are compared by conducting experiments with 30%TBP (v/v) in dodecane as the organic phase and nitric acid as the aqueous phase. Two different nozzles and three different nitric acid concentrations are used. For each nozzle and nitric acid concentration, velocity of the dispersed phase is varied. Drops of aqueous phase formed at downward oriented nozzles submerged in organic phase are observed to be smaller than the drops of organic phase formed at upward oriented nozzles submerged in aqueous phase. Correlations to estimate drop diameter are proposed.

• Fibers and Polymers
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• 제5권1호
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• pp.68-74
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• 2004

This work presents a series of experimental tests on new practical approaches in membrane design to improve extraction capacity and rate. We chose an extraction system involving Aliquat 336 as the extractant and Cd(II) as the metal ion to be extracted to demonstrate these new approaches. The core element in the new membrane assembly was the extractant loaded sintered glass filter. This membrane assembly provided a large interface area between the extractant and the aqueous solution containing metal ions. By recycling the aqueous solution through the membrane assembly, the extraction rate was significantly improved. The membrane assembly also offered good extraction capacity.

• 청정기술
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• 제13권4호
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• pp.274-280
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• 2007

본 연구에서는 염화 제2철 수용액의 재생 공정에 주로 쓰이고 있는 철환원법을 대체하기 위한 방법으로, 액-액 용매 추출법을 사용하여 수용액 내에 잔존해 있는 중금속인 Fe와 Ni을 분리 회수하는 공정을 개발하였다. Lab 실험을 통해 우선 염화 제2철 수용액으로부터 선택적으로 염화 제2철만을 추출할 수 있는 용매조건을 개발하였고, 그 결과를 사용하여 액-액 추출공정의 상업화 추진을 위한 pilot 공정 및 장치를 개발하였다. 또한 pilot test를 통하여 추출단과 역추출단의 단수를 결정할 수 있었고, 양산 공정에 적용할 수 있는 공정 데이터를 확보하였다.