• 대한전자공학회:학술대회논문집
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• 대한전자공학회 2001년도 하계종합학술대회 논문집(2)
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• pp.33-36
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• 2001

In this paper, we have studied the characteristics of wet etching using citric acid based wet etchant. We have used the citric acid / hydrogen peroxide solution, citric acid / hydrogen peroxide / D.I. water solution. From our experimental result, a volumetric 1：3 ratio of citric acid and hydrogen peroxide and 1 ： 3 ： 1 ratio of citric acid, hydrogen peroxide, and D.I. water is shown to be a better wet etchant of PHEMT's system.

• 한국지하수토양환경학회:학술대회논문집
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• 한국지하수토양환경학회 2000년도 창립총회 및 춘계학술발표회
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• pp.133-136
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• 2000

Soil decontamination process was conducted to study adsorption and modeling characteristic of Sr$^{2+}$ ion using citric acid and water system with TRIGA soil. When the concentration of citric acid was increased, the BTC of Sr$^{2+}$ ion was to be closed to the BTC of $^3$$H_2O$ at experiments of soil adsorption. Beside, when the concentration of citric acid was under 0.01M Sr$^{2+}$ ion, BTLs was asymmetry. It was characteristic of nonequilibrium adsorption. R and $K_{p}$ , were decreased to be increased the concentration of citric acid. Asymmetry modeling was nearly the same to be compare with symmetry modeling in decontamination process, when the concentration of citric acid was decreased. Result of experiment was agree with asymmetry and symmetry model, when the concentration of citric acid was increased.eased.

• Membrane and Water Treatment
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• 제7권2호
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• pp.143-154
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• 2016

Acetic acid can be removed from wastewater by esterification in a membrane reactor. Pervaporation membrane reactor (PVMR) is an alternative process to conventional separation processes. It is an environmentally friendly process. The main advantages of the PVMR are simultaneous water removal and production of an ester economically. In this study, the synthetic wastewater has been used. Esterification reaction of acetic acid with isopropanol has been studied in the presence of tungstosilicic acid hydrate as a catalyst in a batch reactor and in a PVMR. The effects of important operating parameters such as reaction temperature, initial molar ratio of isopropanol to acetic acid and catalyst concentration has been examined. Removal of acetic acid (conversion of acetic acid) was obtained as 85% using a PVMR by removal of water from the reaction mixture.

• 문화기술의 융합
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• 제10권2호
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• pp.73-80
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• 2024

우리는 섬오갈피의 70% 에탄올과 열수추출물의 지표성분인 Acanthoic acid과 Kaurenoic acid 함량을 확인하기 위해 시료 내 각 화합물의 정량분석을 HPLC-UVD로 실시하였다. 또한, LC-MS 분석을 통해 시료 내 각 화합물의 성분을 확인하였다. 그 결과, 70% 에탄올 추출물의 Acanthoc acid와 Kaurenoic acid의 함량은 각각 28.84±0.21 mg/g(2.88%), 26.38±1.63 mg/g(2.64%)로 나타났다. 그러나 열수추출물에서는 두 가지 화합물의 Acanthoc acid와 Kaurenoic acid의 함량이 관찰되지 않았다. 결론적으로 섬오갈피 추출물로부터 Acanthoc acid과 그 대사산물을 추출하기 위한 최적의 추출용매로서 70% 에탄올이 열수용매보다 우수함을 알 수 있었다. 또한 DPPH 라디컬 소거능, total polyphenols, flavonoids 함량이 삼채+섬오갈피 복합추출물의 70% 에탄올 복합 추출물이 열수용매보다 더 우수한 효과를 보였다. 삼채와 섬오갈피 등 에탄올복합추출물(SEC) 처리에 의해 유의적 또는 부분적으로 항염증을 감소되었다.

• 수산해양교육연구
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• 제18권3호
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• pp.293-301
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• 2006

연속식 스테인레스 단자 방식의 전해수의 기기특성과 오징어를 담수빙과 산성전해수빙, 염기성전해수빙 저장 중 선도보존 효과 및 표피색변화에 대하여 검토하여, 향후 연안 어류의 전기분해수 빙장 적용기초 자료로 이용하고자 연구한 결과를 요약하면 다음과 같다. 1. 본 연구에서는 TMD에서 개발된 기기에 단자를 구리에서 스테인레스로 교체한 TMD II기기의 성능을 평가하였다.실험결과 전체적으로 동일한 전류를 걸었을때, 산성전해수의 경우 낮은 pH를 유지했으며, 유량을 늘릴수록 산성도가 떨어지는 것을 알 수 있었다.본 장치는 단자부분 재질의 감도를 보다 높이고 전해 촉매제를 사용할수 있다면, 충분히 더 낮은 혹은 더 높은 pH를 확보할 수 있으며 또한 알카리 영역의 경우도 그럴 수 있으리라 예측된다. 2. 먹는물 수질기준에 따른 유속별 생산 전해수의 수질분석 및 미생물검사결과 세균학적인 검사의 경우 모든 검사과정에서 먹는물 기준 이하치를 나타내고 있으나 산성전해수의 경우 미생물학적인 검사에서 음성의 결과를 나타냈으나, 알카리수의 경우 중온성 세균수에 있어서는 먹는물의 수준은 될 수 없음을 알 수 있다. 3. 전해수빙과 담수빙 저장중 오징어의 일반성분과 VBN관찰 결과 수분 함량은 77.65%였으며 단백질 함량은 18.32%, 지질의 함량은 2.41%, 회분 함량은 1.62%로 나타났다. 오징어 빙장 직전 11.2mg/100g이었으며, 저장 초기에 모든 산성 전해수 빙장구에서 VBN 증가가 억제되었다.담수빙 법에서의 VBN 증가가 전해수빙중 산성수빙보다 훨씬 빠르게 진행되었으며 염기성수빙 보다는 느리게 진행되었다. 4. 저장중 오징어의 외관 및 색도 변화를 색차계로 저장시간별로 측정한 결과, 명도(L)는 저장시간별로 감소하는 경향이었으며, 적색도, 황색도는 저장방법에 따른 차이는 있었지만 저장기간에 따라서 증가하는 경향을 보였다. 즉, 저장시간별로 적색에서 녹색으로 청색에서 황색으로 색깔의 변화가 진행됨을 알 수 있었다. 백색도의 경우도 명도와 비슷한 경향 이었다.

• 한국응용과학기술학회지
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• 제5권2호
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• pp.9-15
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• 1988

In order to investigate the amino acid and fatty acid content in Thuja biotae water extract treated with alkaline, it was performed. There are 16 kinds of different amino acid and 20 kinds of different fatty acid in Thuja biotae water extract. An aspartic acid was contained 52％ and proline was contained 10％, particulary, r-aminobutyric acid was analysed. Essential fatty acids; linoleic acid, linolenic acid and arachidonic acid were cotained a lot amount. There are 11 different unknown materials which were identified by GC-MS spectrum, such as N-[($4{\alpha},5{\alpha}$)-cholestan-4-yl]-acetamide; 22,26-Epithio-furost-5-en-3-ol; 2-Methyl-6-(4-methyl-3-cyclohexen-1-yl)-4-heptanone; 3,12,14-Tris(acetyloxy)-pregnane-15,20-dione;22-Methyl-26-thio-furost-5-en-3-ol; 7-Ethenyl-1,2,3,4,4a,4b,5,6,7,9,10,10a-dodecahydro-1,4a,7-trimethyl-1-phenanthrene carboxyaldehyde; Methoxyiminopro-panedioic acid; 13-Methyl-13-${\beta}$-Methyl-13-vinyl-dodecaarp-7-en-3-3-ol; 22-Methyl-26-thio-furost-6-methyl-3-ol; $5{\alpha}-Androstane-2$,11-dione; 9-Methyl-heptadecanoic acid.

• 한국물환경학회지
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• 제21권6호
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• pp.569-574
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• 2005

In this study, alginic acid that had an high affinity for a heavy metal and was noted for biological adsorbent was modified by an oxidizer, $KMnO_4$. Chemical modification changed hydroxyl of the alginic acid into carboxyl and compare with alginic acid, modified alginic acid exhibited a characteristics that carboxyl groups are comparatively high. For the use of them as an adsorbent, beads were prepared by dropping alginic acid and modified alginic acid solution in dilute 2 wt% $CaCl_2$ solution for non water soluble. The amount of removed $Cu^{2+}$ and $Pb^{2+}$ by modified alginic acid beads showed 84.7 mg and 90.9 mg per gram of beads, respectively. And it showed the amount of adsorbed heavy metal ions 10~20% higher than that of alginic acid beads in range of pH 4~7. In particular, modified alginic acid have a good adsorption capacity for $Cu^{2+}$ and $Pb^{2+}$ by Freundlich adsorption isotherm. According to this study, it is verified that alginic acid that is a nature high molecular substance improved capacity for actual application by increased heavy metal adsorption capacity by chemical modification.

• Membrane and Water Treatment
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• 제13권4호
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• pp.201-208
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• 2022

Emulsion Liquid Membrane (ELM) is a prominent technique for the separation of heavy metal ions from wastewater due to the fast extraction and is a single-stage operation of stripping-extraction. The selection of the components (Surfactant and Carrier) of ELM is a very significant step for its preparation. In the ELM technique, the primary water- in-oil (W/O) emulsion is emulsified in water to produce water-in-oil-in-water (W/O/W) emulsion. The water in oil emulsion was prepared by mixing the membrane phase and internal phase. To prepare the membrane phase, the extractant D2EHPA (di-2-ethylhexylphosphoric acid) was used as a mobile carrier, Span-80 as a surfactant, and Paraffin as a diluent. Moreover, the internal (receiving) phase was prepared by dissolving sulphuric acid in water. Di-(2- ethylhexyl) phosphoric acid such as surfactant concentration, carrier concentration, sulphuric acid concentration in the receiving (internal) phase, agitation time (emulsion phase and feed phase), the volume ratio of the membrane phase to the receiving phase, the volume ratio of the external feed phase to the primary water-in-oil emulsion and pH of feed were studied on the percentage extraction of metal ions at 20℃. The results show that it is possible to remove 78% for As(V), 98% for Cd(II), and 99% for Pb(II). Emulsion Liquid Membrane (ELM) is a well-known technique for separating heavy metal ions from wastewater due to the fast extraction and is a single-stage operation of stripping-extraction. The selection of ELM components (Surfactant and Carrier) is a very significant step in its preparation. In the ELM technique, the primary water-in-oil (W/O) emulsion is emulsified to produce water-in-oil-in-water (W/O/W) emulsion. The water in the oil emulsion was prepared by mixing the membrane and internal phases. The extractant D2EHPA (di-2-ethylhexylphosphoric acid) was used as a mobile carrier, Span-80 as a surfactant, and Paraffin as a diluent. Moreover, the internal (receiving) phase was prepared by dissolving sulphuric acid in water. Di-(2-ethylhexyl) phosphoric acid such as surfactant concentration, carrier concentration, sulphuric acid concentration in the receiving (internal) phase, agitation time (emulsion phase and feed phase), the volume ratio of the membrane phase to the receiving phase, the volume ratio of the external feed phase to the primary water-in-oil emulsion and pH of feed were studied on the percentage extraction of metal ions at 20℃. The results show that it is possible to remove 78% for As(V), 98% for Cd(II), and 99% for Pb(II).

• 한국의류학회지
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• 제19권3호
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• pp.425-425
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• 1995

The interaction and detergency between liquid oily soil and surfactant solution were studied by the mechanism of formation of liquid crestal(LC). Samples used were triolein as a triglyceride, oleic acid as a free fatty acid and sodium dodgily sulfate (SDS) as a surfactant. The results were as follows: In the phase diagram of SDS/oil/Water system, the area of liquid crystalline phase region were in the order of SDS/trillion/water< SDS/oleic acid/water< SDS/mixture of trillion and oleic acid/water. In the system of oleic acid alone or mixture of trillion and oleic acid contacted with SDS solution, the LC phase was formed right after or after some time with SDS concentration. But in a case of trillion alone, the LC phase was not formed although the concentration of the SDS solution was relatively high. The detergency of model oily soils were seldom changed with temperature, and the detergency of oleic acid was very high compared to that of the trillion. The detergency of mixed soil was improved with the increase of the ratio of oleic acid in the mixture.

• 한국의류학회지
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• 제19권3호
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• pp.426-433
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• 1995

The interaction and detergency between liquid oily soil and surfactant solution were studied by the mechanism of formation of liquid crestal(LC). Samples used were triolein as a triglyceride, oleic acid as a free fatty acid and sodium dodgily sulfate (SDS) as a surfactant. The results were as follows: In the phase diagram of SDS/oil/Water system, the area of liquid crystalline phase region were in the order of SDS/trillion/water< SDS/oleic acid/water< SDS/mixture of trillion and oleic acid/water. In the system of oleic acid alone or mixture of trillion and oleic acid contacted with SDS solution, the LC phase was formed right after or after some time with SDS concentration. But in a case of trillion alone, the LC phase was not formed although the concentration of the SDS solution was relatively high. The detergency of model oily soils were seldom changed with temperature, and the detergency of oleic acid was very high compared to that of the trillion. The detergency of mixed soil was improved with the increase of the ratio of oleic acid in the mixture.