• Bulletin of the Korean Chemical Society
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• 제20권6호
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• pp.689-695
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• 1999

Supercritical fluid extraction (SFE), ultrasonic extraction (USE), and accelerated solvent extraction (ASE) were compared with the well known Soxhlet extraction for the extraction of polychlorinated biphenyls (PCBs) and polychlorinated dibenzo-p-dioxins(PCDDs) from the XAD-2 resin which was used to adsorb PCDDs in the atmosphere. XAD-2 resin spiked with five PCDDs was chosen as a sample. The optimum conditions for the extraction of PCDDs by SFE were turned out to be the use of CO2 modified with 10% toluene at 100 ℃ and 350 atm, with 5 min static extraction followed by 20 min dynamic extraction. SFE gave a good extraction rate with good reproducibility for PCDDs ranging from 68 to 98%. The ultrasonic extraction of PCDDs from XAD-2 was investigated and compared with other extractions. A probe type method was compared with a bath type. Two extraction solvents, toluene and acetone were compared with their mixture. The use of their mixture in probe type, with 9 minutes of extraction time, was found to be the optimum condition. The average recovery of the five PCDDs for USE was 82-93%. Accelerated solvent extraction (ASE) with a liquid solvent, a new technique for sample preparation, was performed under elevated temperatures and pressures. The effect of tem-perature on the efficiency of ASE was investigated. The extraction time for a 10 g sample was less than 15 min, when the organic solvent was n-hexaneacetone mixture (1 : 1, v/v). Using ASE, the average recoveries of five PCDDs ranged from 90 to 103%. SFE, USE, and ASE were faster and less laborious than Soxhlet extraction. The former three methods required less solvent than Soxhlet extraction. SFE required no concentration of the solvent extracts. SFE and ASE failed to perform simultaneous parallel extractions because of instrumental limitations.

• 한국응용과학기술학회지
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• 제38권1호
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• pp.292-299
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• 2021

본 연구에서는 해삼속의 폴리페놀과 플라보노이드의 생리활성물질을 추출하기 위한 용매분획의 수율을 확인하고자 연구를 시도하였다. 이미 보고된 사례에서 50%에탄올 추출 용매분획은 해삼 항산화 물질의 높은 수율 결과로 확인되었다. 해삼의 항산화물질 추출량을 결정짓는 것은 추출에 적용된 추출 용매분획의 결과로 확인되었다. 또한 '추출용매에 따라 해삼생리활성 항산화물질 추출함량이 크게 차이가 있다.'는 선행연구를 통해 용매분획추출에 관한 필요성의 결과를 얻었다. 50%에탄올 추출 용매분획의 해삼추출물에 포함된 페놀물질의 높은 항산화성분 추출 결과가 증명되었다. 추출용매분획 연구사례에서 수율이 가장 저조한 아세트산에틸 용매분획은 다른 용매분획에 비해 높은 페놀함량을 수확하여 항산화효과가 확인되었다. 이에, 추출 용매분획물의 적용에 따른 수율변화를 통해 항산화추출물의 높은 수율에 미치는 영향을 확인 하였다. 따라서 본 연구를 통해 50%에탄올 용매의 최적화된 해삼생리활성물질 추출 용매분획으로 검증되었다.

• 식품보건융합연구
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• 제5권5호
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• pp.11-25
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• 2019

Extraction of oil from Moringa oleifera seed using Response Surface Methodology (RSM) was investigated. Effects of three factors namely: sample mass, particle size and extraction time on the response, Moringa oleifera a volume extracted, were determined. The Box-Behnken design of RSM was employed which resulted in 15 experimental runs. Extraction was carried out in a 250 ml Soxhlet extractor with Hexane and Ethanol as solvent. The Moringa oleifera seed powder was packed inside a muslin cloth placed in a thimble of the Soxhlet extractor. The extraction was carried out at 60℃ using thermostatic heating mantle. The solvent in the extracted oil was evaporated and the resulting oil further dried to constant weight in the oven. This study demonstrates that Moringa oleifera oil can be extracted from its seed using ethanol and acetone as extraction solvent. The optimum process variables for both solvent (ethanol and acetone) was determined at sample weight of 40 g, particle size of 325 ㎛ and extraction time of 8 hours. It can be deduced that using acetone as solvent produces a higher yield of oil at the same optimum variable conditions compared to when ethanol was used.

• Natural Product Sciences
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• 제25권2호
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• pp.150-156
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• 2019

Conventional extraction of oil and azadirachtin, a botanical insecticide, from Azadirachta indica involves defatting the seeds and leaves using hexane followed by azadirachtin extraction with a polar solvent. In order to simplify the process while maintaining the yield we explored a binary extraction approach using Soxhlet extraction device and hexane and ethanol as non-polar and polar solvents at various ratios and extraction times. The highest oil and azadirachtin yields were obtained at 6 h extraction time using a 50:50 solvent mixture for both neem leaves (44.7 wt%, $720mg_{Aza}/kg_{leaves}$) and seeds (53.5 wt%, $1045mg_{Aza}/kg_{leaves}$), respectively.

• Food Science and Biotechnology
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• 제14권6호
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• pp.836-840
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• 2005

Extraction characteristics of Bonus species of Brassica oleracea var. capita and functional properties of corresponding extract were monitored by response surface methodology (RSM). Maximum extraction yield of 44.07% was obtained at ratio of solvent to sample of 27.94 mL/g, ethanol concentration of 24.35%, and extraction temperature of $55.21^{\circ}C$. At ratio of solvent to sample, ethanol concentration, and extraction temperature of 21.11 mL/g, 58.53%, and $68.83^{\circ}C$, respectively, maximum electron-donating ability was 48.44%. Maximum inhibitory effect on tyrosinase was 68.94% at ratio of solvent to sample, ethanol concentration, and extraction temperature of 24.08 mL/g, 10.49%, and $78.71^{\circ}C$, respectively. Superoxide dismutase (SOD) showed maximum pseudo-activity of 24.78% at ratio of solvent to sample of 22.66 mL/g, ethanol concentration of 45.69%, and extraction temperature of $93.81^{\circ}C$. Based on superimposition of four-dimensional RSM with respect to extraction yield, electron-donating ability, and pseudo-activity of SOD, optimum ranges of extraction conditions were ratio of solvent to sample of 20-30 mL/g, ethanol concentration of 35-65%, and extraction temperature of $50-80^{\circ}C$.

• 한국태양에너지학회 논문집
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• 제31권6호
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• pp.66-71
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• 2011

Various single solvents were tested to find the effective solvent for the extraction of algae oil from wet-form Chlorella minutissima. In the case of single solvents, their extractabilities for algae oil were increased with their polarity because the water in wet algae cell is to form a solvent shell around the lipids. Based on these results, the wet-form algae samples were treated with a polar alcohol solvent and then a nonpolar solvent was added in algae residue. In the algae oil extraction by ethanol/n-hexane, total lipid contents were 40-50% and composition of triglyceride in extracted oil was 46.50%. Considering solvent toxicity of conventional solvent mixture such as chloroform and methanol for algae oil extraction, the ethanol/n-hexane system was identified as the effective one for the oil extraction from wet-form Chlorella minutissima.

• KSBB Journal
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• 제15권4호
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• pp.346-351
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• 2000

식물세포 배양액으로부터 회수한 식불세포 내 수분 함 량에 따른 추출효율은 건조 정도 보다는 건조방법 에 상당 히 영향을 받음을 알 수 있었으며 건조하여 추출할 경우 사용되는 추출용매를 절약할 수 있었다. 여러가지 유기용 매를 이용하여 paclitaxe1의 추출 경향을 조사한 결과 메탄올의 경우 가장 적 은 양으로 가장 높은 paclitaxe1 회 수율을 얻어 가장 효과적임을 알 수 있었다. 추출방법의 경우 counter-current 형태를 사용할 경우 batch형태에 비하여 용 매 사용량을 줄일 수 있으며 paclitaxe1 회수율은 거의 차이가 없음을 알 수 있었다. Batch 형태를 이용한 메탄올 추출시 식불세포의 경우 4회 (회수율>99%), 식불세포조각의 경우 1회 (회수융>96%)의 추출로 대부분의 paclitaxe1 회수가 가능 하였다. 또한 메탄올 추출시 90% 이상의 머탄올 농도이변 충분하며 (회수율>98%), 추출시biomass와 메탄올 의 흔합비 (Kg biomass: L MeOH)는 1: 1, 추출시간은 1회 5분 이상이면 적당 하였다. 메탄올 추출불에 포함된 극성불 순물들은 다음 공정 인 액/액 (methylene chloride/ MeOH)추 출로 제거하여 정제공정에 사용되어 진다.

• 폴리머
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• 제25권5호
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• pp.665-670
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• 2001

에탄올에 의한 폴리에틸렌글리콜(PEG)위 용매추출법이 Sr-페라이트/PEG/carnaubawax/HDPE로 구성된 분말사출성형체에서 연구되었다. 에탄올에 의한 PEG의 추출율은 용매의 온도에 민감하게 비례하나, PEG의 첨가량, PEG의 분자량, 그리고 시편의 두께에는 반비례한다. 에탄올에 의한 PEG의 효과적인 용매추출은 7$0^{\circ}C$의 용매온도, 30%의 PEG 첨가량, 400g/mo1의 PEG 분자량에서 가능하였다. 용매추출의 초기단계에서 에탄올에 의한 PEG의 추출율은 추출시간의 제곱근과 정비례관계를 갖지 않으므로 Fickian 거동을 나타내지 않는다. 그러나 180분 이상의 용매추출시간에서 PEG의 추출율은 Fickian 거동을 따른다. 에탄올에 의한 PEG의 추출속도는 상용화가 가능한 수준인 약 $1.0{ imes}10^{-6}g/cm^2sec$를 나타낸다.

• Journal of Microbiology and Biotechnology
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• 제14권5호
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• pp.932-937
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• 2004

In situ extraction by organic solvent was studied in order to improve the recovery yield of hydrocarbon from the culture of Botryococcus braunii, a green colonial microalga. When the solvent mixture of octanol as an extractive solvent and n-octane as a biocompatible solvent was added to a two-phase column, the algal growth was seriously inhibited, even at a low concentration of polar octanol. Therefore, a two-stage cell-recycle extraction process was proposed to improve the contact area between the organic phase and the aqueous phase. The hydrocarbon recovery with in situ cell-recycle extraction showed a three-fold increase (57% of cell) in yield over that with two-phase extraction. In addition, over 60% of the hydrocarbon could be recovered without serious cell damage by downstream separation when this process was applied to the culture broth after batch fermentation.

• Bulletin of the Korean Chemical Society
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• 제19권12호
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• pp.1351-1355
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• 1998

A simple apparatus for adding a modifying solvent to supercritical CO2 extractant was described. Small, fixed volumes (typically 100 μL) of liquid modifying solvents were delivered during the extraction process by use of an in-line high pressure loop injector and an air pump. Without disconnecting the extraction cell from the supercritical fluid extraction system, the modifying solvent was repeatedly delivered. The solvent modification device was optimized during the extraction of carbaryl and bis(acetylacetonato) copper(Ⅱ). Extraction recoveries from spiked filter paper and soil samples ranged between 22% and 109%, depending on the analyte and matrix components. The addition of polar modifying solvents were necessary to improve the extractability of the nonpolar CO2.