• Proceedings of the Korean Institute of Resources Recycling Conference
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• 2005.05a
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• pp.162-167
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• 2005

초산, 질산, 인산이 함유된 폐혼산으로부터 인산을 분리하여 재활용하기 위한 방법으로 용매추출법을 이용하였다. 폐혼산에서 초산과 질산을 선택적으로 분리하고, 추출 잔류액에서 인산을 회수하고자 하였다. 주요 실험 변수로는 추출제농도, 교반시간, 교반속도 등의 변화에 따른 초산, 질산, 인산의 추출거동을 조사하였다. 또한, McCabe-Thiele diagram으로부터 초산, 질산 성분의 추출 및 탈거에 필요한 이론적 단수를 조사하였다. 실험결과 인산염계 추출제를 사용할 경우 초산과 실산을 선택적으로 분리 추출이 가능하였으며, 추출제의 함량은 유기상의 50%가 적합하였다. 교반속도와 교반시간의 영향은 크게 없었으며, 상비(A/O)=1/3, 6단에서 초산과 질산을 완전히 추출 분리하여 인산을 추출잔류액에서 회수가 가능하였다.

• Food Industry
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• s.94
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• pp.37-40
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• 1988

1) 본 연구에서 시료로 선정한 충남 서산산 건강(dry ginger)은 수분이 $9.4\%$, 회분이 $8.7\%$ 그리고 alcohol에 의한 추출량이 약 $9\%$이다. 이는 선진국에 채택사용하고 있는 건강의 규격기준에 의하면 양호하다. 2) Non- flavor물질의 추출을 최소화하고 특히 증류과정에서 유효성분 손실을 최소화 할 수 있고, 엑기스내의 용매 잔류량이 인체에 유해하지 않고 추출효율을 높일 수 있는 용매는 ethyl alcohol이다. 3) 널리 사용하고 있는 관류추출(percolation)의 성능을 분석하고 이의 개선방안을제시하였다. - 추출효율을 높이기 위하여 건강(dry ginger)의 입자를 작게하면 압력강하가 증대되어순환되는 용액의 유속을 제어하기가 힘들다. - 입자가 작을 시에는 유체의 흐름이chan-nelling현상을 나타낸다. - 위와 같은 조건에서는 물질 전달속도가 느리므로 추출효율을 증대시킬 수가 없다. - 따라서 percolation추출에 사용되는 건강의 입자크기는 30mesh크기 이상이어야 운전조작이 용이하나 추출효율이 낮으므로, 추출시간 6시간에 회수된 생강엑기스양은 약 $2.5\%$이다. 4) percolation추출의 단점을 보완하기 위하여 기계적교반 추출을 선택하여 다음과 같은 개선점을 찾았다. - 교반형 추출에서는 고 - 액분리시 cake 저항에서 문제가 야기되지 않는 범위까지 건강의 입자를 작게할 수 있으므로 추출효율을 크게 향상시킬 수 있었다. 즉, 작게 분쇄된 건강(30mesh통과$90\%$)을 대상으로 추출시간 3시간에 $7\%$의 회수율로 증대시켰다. 최적 운전조건은 다음과 같다. 건강시료:1kg 시료크기:-30mesh$90\%$ 용매:ethyl alcohol 3$\iota$ 교반속도:900r.p.m 추출온도:상온($15\~25^{\circ}C$) 추출시간:3시간 일차 추출조건과 동일하게 하여 얻어진 엑기스의 수율이 $2\~2.5\%$이므로 총엑기스의 수율은 건강(dry ginger)무게기준으로 $8.5\~9.5\%$이었다. 5) 교반추출의 효율이 개선되었다 하더라도 추출물의 분리가 용이하여야만 공정의 이용이 가능하다. 그러므로 교반추출후 고 - 액분리를 위하여 정압여과 장치를 이용하여 여과시 cake의 평균 비저항을 얻었으며, 이의 값은 $4.31\times10^8cm\;/\;gr$으로서 여과에는 어려움이 없다는 것을 의미한다. 따라서 추출속도와 효율이 상대적으로 우수한 교반형 추출기의 가능성을 예시할 수 있음을 알 수 있었다. 6) 추출물을 농축과정에서 휘발성 oil의 손실을 최대로 줄이기 위해서는 단순증류를 하지 말고 분별증류를 수행하여야 하며, gingerol과 같은 중요성분의 열분해 반응을 억제하기 위해서는 열전달 효율을 증대시켜 증류조작을 원활히 수행하여야 하므로, still내의 농축물을 계속 교반시켜야 하며 감압상태에서 증류온도는 $40\~50^{\circ}C$로 유지시키는 것이 가장 바람직하다. 7) Ethyl alcohol로 추출된 엑기스내의 수분이나 회분함량은 외국산 제품에 비하여 약간 낮고, 반면에 조지방 및 조단백 성분의 함량은 약간 높게 나타나고 있어 대체적으로 본 연구에서 얻어진 엑기스내의 비풍미성분(non- fla-vour component) 함량은 외국산에 비하여 많은 차이가 없다. 8) 수입 외국산에 비하여 국산엑기스(본 연구에서 ethyl alcohol로 추출)내의 무기성분등의 함량은 비교적 낮은 편이다. 9) 건강에서부터 oleoresin을 얻어 paradol을 제거시킨 후 순수한 gingerol을 분리하여 IR과 NMR로 확인한 결과, 국산건강의 엑기스에는 주로 6-gingerol이고 약간의 10-gingerol이 함유된 것으로 나타났다. 10) 순수하게 분리된 gingerol을 열분석(TGA와 DTG)한 결과 약 $75^{\circ}C$에서 gingerol의 열분해 반응이 일어남을 알수 있었다. 11) 건강 분말시료와 엑기스내의 미생물 검사 결과 건강분말에서는 세균수가 많이 존재하는 것으로 나타났으나, 이는 ethyl alcohol로 추출하는 공정 중 대부분의 균들이 사멸된 것으로 나타났다. 12) 관능적 측면에선, 본 연구에서 제조한 엑기스와 수입엑기스를 비교한 결과 생강 특유의 맛은 비슷했으나, 수입엑기스에서는 쓴맛과 톱밥냄새를 느낀다는 결과를 나타내었으며 전체적인 종합적 풍미는 국산 건강엑기스가 좋은 것으로 나타났다.

• Journal of Korea Soil Environment Society
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• v.5 no.2
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• pp.45-53
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• 2000

Two extraction methods for total petroleum hydrocarbon (TPH) from contaminated soil were evaluated. The soil used for this study was sandy loam. Diesel oil was selected as representative petroleum hydrocarbons and was spiked at 100, 10,000, 50,000mg TPH/kg dry soil. Percentage recovery of TPH by shaking method was higher compared to Soxhlet extraction. At extraction time of 2 hours and sample to solvent ratio of 1 : 5, the highest percentage recovery was obtained. In this condition, percentage recovery of TPH in soil contaminated with 100mg/kg and 50,000mg/kg as TPH was 95.9% and 95.5%, respectively The volume of solvent lost by volatilization in shaking method was relatively small compared to Soxhlet extraction.

• Applied Chemistry for Engineering
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• v.5 no.2
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• pp.223-229
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• 1994

The effect of agitation speed on mass transfer coefficient in the extraction of citric acid from mixed aqueous solutions of citric and acetic acid with n-butylacetate solutions of di-isotridecylamine(DITDA) and 50% mixture of tri-n-octyl and try-n-hexyl phosphine oxide(MOHPO), were studied in batch extractor. Experimental results showed that the degree of extraction was higher with increasing agitation speed, and was best at 200rpm and 30 minutes in batch extractor. The higher degree of extraction was obtained in mixed solution of citric-acetic acid by using DITDA than MOHPO as an carrier. Mass transfer coefficient was proportional to the degree of extraction, and $K_r=1.254{\times}10^{-3}Re^{0.536}$ was found for she extraction of citric acid by DITDA.

• Resources Recycling
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• v.14 no.5 s.67
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• pp.18-23
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• 2005

Recovery of phosphoric acid from waste acid mixture of acetic, nitric and phosphoric acid has been attempted by using solvent extraction method. In this work, organic phosphate was used as an extraction agent. The effect of phosphate concentration, agitation speed and time on the solvent extraction of acetic and nitric acids has been investigated. The optimum concentration of phosphate for preferential extraction of acetic and nitric acids from waste acid was found to be about 50% irrespective of agitation speed and time. Purified phophoric acid was recovered from extraction residue at 1/3 of A/O ratio and 6th stage of extraction stage, which is well consistent with the value calculated by using McCabe-Thiele diagram.

• Korean Chemical Engineering Research
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• v.46 no.3
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• pp.555-560
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• 2008

Extraction was performed to prepare ash-free coal from low rank coal under the temperature of $200-430^{\circ}C$ and initial pressure of 0.1MPa. Three kinds of coal samples with different rank were used and N-methyl-2-pyrrolidinone(NMP, polar), 1-methyl naphthalene(I-MN, non-polar), Light Cycle Oil(LCO, non-polar) were used as solvents. Results showed that higher extraction yield could be obtained with NMP than with 1-MN and LCO, but the ash concentration shows minimun in the case of 1-MN. Three operation modes were compared, that is, idle, agitation and ultrasonic extraction mode. From the results, it was found that the extraction yield and ash concentration were 70.09% and 1.03% under the agitation mode, 80.7% and 0.76% under the ultrasonic operation mode respectively in the case of NMP used at the temperature of $350^{\circ}C$. Similar results were obtained with 1-MN. Effect of ultrasonic on the extraction was estimated as 15-20% increase in the yields and 26% reduction in the ash concentration.

• Journal of the Korean Society of Food Science and Nutrition
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• v.44 no.5
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• pp.695-701
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• 2015

This study was conducted to evaluate the effects of drying and extraction methods on antioxidant activity and total phenol content of Gnaphalium affine D. DON (GA). Hot-air, shade-drying, and freeze-drying were used for drying, after which magnetic stirring and ultrasonification were applied. Extracting solvents were water, 80% ethanol, and 80% methanol. Total phenol content was highest in 80% ethanol extract of freeze-dried and stirred GA. Total flavonoid content was highest in 80% methanol extract of freeze-dried and stirred GA. 2,2-Diphenyl-1-picrylhydrazyl (DPPH) radical scavenging activity was higher in 80% methanol and 80% ethanol extracts than in water extract. 2,2-Azino-bis(3-ethylbenzothiazoline-6-sulfonic acid) radical scavenging activity was highest in 80% ethanol extract of shade-dried and ultrasonicated GA. Reducing power was generally higher in 80% methanol extract than in 80% ethanol and water extracts of GA. Total phenol and total flavonoid contents were highly correlated with DPPH radical scavenging activity and reducing power, respectively. This result implies that the antioxidant activity of GA can be attributed to phenol compounds such as flavonoids. Conclusively, phenol compounds such as flavonoids are responsible for the antioxidant activity of GA, and there was no significant effect of drying and stirring conditions on antioxidant activity of 80% ethanol. Meanwhile, DPPH radical scavenging activity of water extract and reducing power of 80% methanol extract were higher in hot-air and shade-dried GAs than in freeze-dried GA.

• Journal of the Korea Organic Resources Recycling Association
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• v.32 no.2
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• pp.5-14
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• 2024

A study approached the development of a process for efficiently recycling discarded cigarette butts, reported as a major source of microplastic pollution in aquatic environments. Cigarette butts were sorted to extract filters, and cellulose acetate, the raw material of the filters, was extracted to a high degree of purity. The sorting of filters from cigarette butts was conducted through both wet and dry processes, each with optimized sorting conditions. Wet stirring sorting considered factors such as solid-liquid ratio, stirring speed, and stirring temperature. The highest efficiency of wet stirring sorting, at 46.21%, was observed with a solid-liquid ratio of 1:45, stirring speed of 200 rpm, and stirring temperature of 50℃. Dry wind power sorting took into account moisture content and residence time. The filter sorting efficiency reached its peak at 57.10% with a moisture content of 20% and a residence time of 5 minutes. There was no significant difference in the recovery rate of cellulose acetate between the two sorting processes. Dry wind power sorting was deemed a more advantageous process in terms of energy and environmental considerations within the scope of this study.

• KSBB Journal
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• v.19 no.6 s.89
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• pp.421-426
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• 2004

The extraction and separation of isoflavones from Korean soybean were peformed by various mechanical and chemical extraction methods. They included solvent extraction, stirring, supersonification and sub/supercritical water extraction. From the experimental results of the variation of solvent extraction by change in composition, the increase in extraction of a specific compound by stirring or supersonic energy, and the application of supercritical fluid with superior solvating power over solvents, the sonification was the most desirable extraction method in extracting aglycone isoflavones, daidzein and genistein from Korean soybean.

• Journal of Navigation and Port Research
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• v.28 no.5
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• pp.463-468
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• 2004

A lab-scale fundamental study to develop the solvent extraction process of ship wash wastewater containing TBT was carried out. For various solvents, including diesels for car and ship, bunker B, thinner, toluene, and ether, the extraction efficiencies of TBT from synthetic ship wash wastewater were compared The effect of extraction conditions, such as solvent amount, time and intensity of agitation, and pH, on the extraction efficiency of TBT was evaluated Diesel for ship showed better extraction efficiency of TBT than those of other tested solvents, and the proper amount of the extraction solvent for 1L of the wastewater was l0mL. When the agitation intensity was increased from 50rpm to 250rpm, the TBT remained in the wastewater after the extraction was decreased from around 120ppb to 2.8ppb. The remaining TBT in the wastewater was sharply decreased from 1hr of the extraction time, but was slightly increased again after 5hrs of the extraction time. The efficiency of TBT extraction was good in the weak acid range of pH, but was not significant as much as the others.