• 자원리싸이클링
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• 제26권2호
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• pp.3-10
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• 2017

희토류 원소는 첨단 산업용 소재의 구성 성분으로 고순도가 요구된다. 국내산 monazite광과 Ni-MH전지는 경희토류를 함유한 자원이다. 이러한 자원을 염산으로 침출한 용액에서 경희토류성분을 용매추출로 분리하는 공정에 대해 고찰하였다. 양이온 추출제와 3차 아민의 혼합추출제로 경희토류를 추출시 상승효과가 있으며 pH 감소가 둔화된다. 혼합추출제 사용시 수상의 pH가 금속의 추출 및 상승효과에 미치는 영향을 분석하였다. 향후 양이온과 아민의 혼합추출제에 의한 경희토류 분리공정을 개발하기 위해서는 mixer-settler의 조업 자료 확보가 필요하다.

• 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.

• 신재생에너지
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• 제19권4호
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• pp.27-34
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• 2023

In this study, microalgal oil was extracted from Nannochloropsis oceanica cultured in an open raceway pond and converted into biodiesel using a solid acid catalyst. Microalgal oil was extracted from two types of microalgae with and without nitrogen starvation using the KOH-solvent extraction method and the fatty acid content and oil extraction yield from each microalgae were compared. The fatty acid content of N. oceanica was 184.8 mg/g cell under basic conditions, and the oil content increased to 340.1 mg/g under nitrogen starvation conditions. Oil extraction yields were 90.8 and 95.4% in the first extraction, and increased to 97.5 and 98.8% after the second extraction. Microalgal oil extracted by KOH-solvent extraction was yellow in color and had reduced viscosity due to chlorophyll removal. In biodiesel conversion using the catalyst SO₄^2-/HZSM-5, solvent-extracted oil showed a FAME content of 4.8%, while KOH-solvent-extracted oil showed a FAME content of 90.4%. Solid acid catalyst application has been made easier by removal of chlorophyll from microalgal oil. The FAME content increased to 96.6% upon distillation, and the oxidation stability increased to 11.07 h with addition of rapeseed biodiesel and 1,000 ppm butylated hydroxyanisole.

• 대한약침학회지
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• 제21권2호
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• pp.48-60
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• 2018

Objective: The aim of this study is to optimize the extraction of beneficial substance from Cudrania tricuspidata leaves grown at Jirisan Mountain in South Korea by three different solvents depending on extraction time and at different temperature. Methods: The total phenolic contents were determined by the method reported by $S{\acute{a}}nchez$-Moreno et al. The total flavonoid contents were analyzed by Slinkard and Singleton. The DPPH radical scavenging activity was determined according to the method reported by Blois Results: The extraction yield for each solvent is 9.05-14.1%, 2.17-5.67%, and 2.3-3.9% for D.W., ethanol, and hexane, respectively. The overall results were maximized for the extract obtained with D.W. for 5 min at $100^{\circ}C$. The average phenol contents were 77.11, 45.64, and 0.343 mg/g at $100^{\circ}C$ in water, $78^{\circ}C$ in ethanol, and $68^{\circ}C$ in hexane, respectively. The flavonoid contents were the highest in the materials extracted with D.W., and were increased with increasing temperature, regardless of the extraction solvents, whether water (green), polar organic ethanol, or nonpolar organic hexane. In the ethanol extract, the flavonoid contents are increased gradually from 5.66 mg/g to 7.73 mg/g. The total flavonoid contents were proportional to the concentrations of the water extracts, ranging from 4.14 mg/g to 48.89 mg/g. The antioxidative activities of the water-extracted compounds are generally increased with increasing temperature from 42.5% to 85.5%. Those of the hexane extracts are increased slowly from 3.79% to 8.8%, while those of ethanol extracts are increased from 29.8% to 47.4%. Conclusion: The extraction yields were dependent upon solvents for extraction as well as extraction time and the temperature. The optimal extraction time was 5 min and the extraction yields were increased with increasing temperature excepted hexane. Of the three tested extraction solvents, the greenest solvent of water shows excellent results, suggesting that water is among the most effective solvents for natural sample extractions for general medicinal, pharmaceutical, and food applications.

• 한국지하수토양환경학회지:지하수토양환경
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• 제17권1호
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• pp.42-46
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• 2012

The ISO document of ISO/TC/190/SC3/WG11/N11 is a working draft of international standard (WD) dealing with analytical method for the determination of explosives and related compounds using high performance liquid chromatography. The scope of this WD covers the storage of samples, preparing test portion, extraction and instrumentation. The main purpose of this study was to improve the extraction conditions which were already adopted in the WD. For this purpose, mechanical shaking method could be corresponded up to 18 hours of ultrasonic bath extraction in the WD was tested. Methanol was also tested with the intention of being added as an extracting solvent other than acetonitrile in the WD. According to the results, 16 hours of mechanical shaking method showed statistically the same effectiveness as that of 18 hours of ultrasonic bath extraction. In case of extracting solvent, methanol also showed statistically the same extraction capability as acetonitrile for DNB, TNT, 2-A-DNT and 2,4-DNT. However, the recovery rate of TNB with methanol extraction was 40% higher than that of acetonitrile extraction. Through adding mechanical shaking method into committee draft (cf. the next stage draft of the WD during the process for making international standard), ISO standard of analyzing explosives and related compounds in soil would become more useful in dealing with huge number of field samples in the laboratory. In other aspect, adopting methanol as an alternative extracting solvent would be very effective in the terms of exchangeability with GC-ECD/MS method which is being developed by German experts.

• Korean Chemical Engineering Research
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• 제60권4호
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• pp.499-505
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• 2022

본 연구에서는 크라프트 리그닌(Kraft Lignin)을 사용해 바닐린을 생산하는 공정의 개념 설계를 진행하였다. 기존 크라프트 리그닌은 대부분 저품질의 보일러 연료로 사용되거나 폐수로 버려지고 오직 2% 이하의 리그닌만 고품질의 제품으로 정제된다. 버려지는 크라프트 리그닌을 활용하기 위해 새로운 공정을 제안하였다. 기존 바닐린 생산 개념 공정은 NaOH를 사용한 알칼리 산화, 여과, 크로마토그래피, 결정화 단계로 진행됐다. 이중 상용화가 어려운 크로마토그래피를 용매 추출 공정으로 변경하였다. 제안된 용매 추출 공정의 바닐린 회수율 92.9%, 순도 99.5%이며, 이는 기존 크로마토그래피 공정과 유사한 수준이다. 크로마토그래피와 비슷한 결과를 보이는 용매 추출 공정이 기존 크로마토그래피 공정을 대체할 수 있는 이유를 분석하였다.

• 한국식품영양학회지
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• 제29권2호
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• pp.228-236
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• 2016

본 연구에서는 치아씨의 항산화 활성을 증가시키기 위하여 추출용매 종류와 용매농도, 추출시간과 추출온도를 달리하여 총 폴리페놀 함량과 DPPH 라디칼 소거능을 측정한 후 반응표면분석을 이용하여 최적조건을 수립하였다. 치아씨 추출조건은 에탄올과 메탄올용매 모두에서 추출용매 60%, 추출시간 130분과 추출온도 $20^{\circ}C$에서 총 폴리페놀 871.00mg%($R^2=0.9507$), 557.70mg%($R^2=0.9784$)로 가장 함량이 많았고, DPPH 라디칼 소거능은 72.14%($R^2=0.9675$), 52.79%($R^2=0.9524$)의 항산화력을 보였다. 용매종류에서는 에탄올 추출용매가 메탄올 추출용매보다 같은 조건에서는 월등히 높은 항산화력을 보여 에탄올이 치아씨 추출용매로 더 우수한 용매로 선정되었다. 또한 반응표면분석 결과, 용매추출 조건에서는 에탄올 용매에서는 용매추출 시간이나 온도보다는 용매농도에 가장 큰 영향을 받았고, 메탄올 추출조건에서는 용매추출 시간에서 가장 큰 영향력을 주었다. 반응표면분석 후 용매 농도, 시간과 온도의 최적 추출조건의 범위는 에탄올 추출조건은 에탄올농도 63%, 추출시간 100분과 추출온도 $18^{\circ}C$가 최적조건이고, 메탄올 추출조건에서는 추출농도 65%, 추출시간 120분과 추출온도 $16^{\circ}C$를 보였다.

• 한국생물공학회:학술대회논문집
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• 한국생물공학회 2002년도 생물공학의 동향 (X)
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• pp.112-115
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• 2002

본 연구에서는 균주의 배양과 동시에 생산물을 회수할 수 있는 동시추출공정을 건조질량의 $15{\sim}75$ %의 탄화수소를 생산한다고 알려진 B. braunii 배양에 적용하고자 한다. 일반적인 tow-phase 동시 추출공정의 적용시 B. braunii의 경우 생산된 탄화수소가 균주 외벽의 matrix에 강하게 부착되어 있기 때문에, two phase 추출공정 적용시 bubble solumn내에서 단지 폭기에 의한 교반만으로는 충분한 탄화수소의 회수율을 얻을 수가 없었다. 본 연구에서는 배양액과 유기용매층의 접촉기회를 증대시킨 two-stage 동시추출 공정을 개발하여 기존의 two-stage 동시추출 공정보다 2배 이상 높은 57 %의 탄화수소 회수율을 얻을 수가 있었고, 이를 회분배양후 후속분리공정으로 이용할 경우 6시간 추출후 62 %의 회수율을 얻을 수가있었다.

• 한국작물학회:학술대회논문집
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• 한국작물학회 2017년도 9th Asian Crop Science Association conference
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• pp.255-255
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• 2017

Sesame has been consumed for centuries as flavoring ingredient in eastern Asian countries, especially Korea. Sesame seeds have been used as health food for traditional medicine to prevent disease in Asian countries for several thousand years. Sesame seed has higher oil content (around 50%) than most of the known oilseeds. Sesame oil is rich in monounsaturated and polyunsaturated fatty acids. Extraction of sesame has developed significantly over the years. The mechanical method was an early means of separation which was physical pressure to squeeze the oil out. Nowadays, solvent extraction becomes the commonly used commercial technique to recover oil from oilseeds. In this study, we investigated extraction efficiency and quality of oil affected by cultivars and extraction methods of sesame seed. Different variables were investigated; roasting temperature ($170{\sim}220^{\circ}C$), extraction methods (solvent and physical pressure), forced ventilation system and cultivars. The Contents of B(a)P in sesame oil after roasting at $170{\sim}220^{\circ}C$ were 0.30~2.53 ppm. When we introduced forced ventilation system during roasting, B(a)P Contents were decreased up to 36%. The Oil extraction efficiency on sesame seed was statistically depending on the cultivars and extraction methods. The oil extraction yields of solvent and physical pressure extraction were 56.3% and 44.6%, respectively. Many of sesame cultivars and genetic resources are linolenic acid content of less than 0.5%. The results supported that we have developed a safe and high quality sesame oil processing methods for small and medium-sized companies.

• Journal of Applied Biological Chemistry
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• 제55권3호
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• pp.149-156
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• 2012

The effects of solvent type and concentration, solid/liquid ratio, extraction time and repeated extraction on recovery of keratinase from solid-state fermentation (SSF) of chicken feather by a local Streptomyces sp. NRC 13S were investigated in order to establish the experimental conditions for keratinase yield. Among solvents tested, 0.5% (v/v) glycerol was the best. Box-Behnken design was used to investigate the effect of relevant variables on keratinase recovery. The factors investigated were solid/liquid ratio (1:1.66-1:6.66 g/mL), glycerol concentration (0.5-5% v/v) and repeated extraction (1-5 cycle). The results showed that the maximum recovery of keratinase (6933.3 U/gfs) was obtained using 0.5 (v/v) glycerol as extracting solvent, in a solid/liquid ratio of 1:5 and three extraction cycles.