• Journal of the Korean Wood Science and Technology
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• 제43권1호
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• pp.76-85
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• 2015

본 연구에서는 2단계 산 처리 방법을 이용하여 목질계 바이오매스로부터 푸르푸랄(furfural) 생산 조건을 탐색하고 생성된 푸르푸랄은 XAD-4 resin을 이용하여 회수하였다. 1차 산 처리 촉매로는 옥살산(oxalic acid)과 황산(sulfuric acid)을 사용하였다. 1차 산 처리로부터 얻어진 액상가수분해산물에 포함된 자일로스 농도는 옥살산과 황산 촉매에서 각각 $18.86g/{\ell}$, $19.35g/{\ell}$로 유사한 값을 나타냈다. 반면 올리고머 함량은 황산 촉매에서 높은 값을 나타냈다. 옥살산 전처리와 2차 황산 처리(황산 $0.1m{\ell}$, 90분)의 연속과정에서 최대 55.10%의 푸르푸랄 생산 수율을 나타냈다. 2차 산처리 과정에서 반응시간이 증가할수록 푸르푸랄 생산 수율은 증가하였다. 생성된 푸르푸랄은 XAD-4 resin을 이용하여 대부분 회수하였다.

• Journal of Ginseng Research
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• 제34권2호
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• pp.93-97
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• 2010

To enhance the functionalities of ginseng, an acid impregnation pre-treatment was applied during red ginseng processing. Acetic, ascorbic, citric, malic, lactic, and oxalic acid were used for the acid impregnation treatment, and total and crude saponin concentrations and ginsenoside patterns were evaluated. Total and crude saponin contents of red ginseng pre-treated by acetic, ascorbic, and citric acid were similar to those of red ginseng without pre-treatment, whereas lactic, malic, and oxalic acid pre-treatment caused a reduction of total and crude saponin in red ginseng. From the high performance liquid chromatography analysis of ginsenosides, increased $Rg_3$ density was shown in red ginseng pre-treated by acetic, ascorbic, and citric acid impregnation. In the case of lactic, malic, and oxalic acid pre-treatment, increased $Rg_1$ density was observed in red ginseng. Increased $Rg_1$ and $Rg_3$ contents due to acid impregnation during red ginseng processing may contribute to improving bioactive functionalities of red ginseng.

• 한국표면공학회지
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• 제17권3호
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• pp.78-86
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• 1984

Hard anodic oxide film was investigated formed on pure aluminium with various temperature (30$^{\circ}-60^{\circ}C$), current densities (1.5-3.0A/$dm^2$) and concentrations(3-15g/l) of oxalic acid in 0.5M malic acid bath. The resulting characteristic of the anodic oxide film obtained were summarized as follows in the view point of physical and mechanical properties in relation with the above process variables. 1. The film thickness increased with oxalic acid concentration and bath temperature, while the reversed phenomena were obtained at a high concentration of oxalic acid and high temperature due to the severe dissolution of the anodic oxide film. 2. The hardness and the abrasion resistance were improved by lowering the addition of oxalic acid and the bath temperature. This feature was directly dependent on the porosity formed on the anodic oxide film. 3. The maximum hardness of anodic oxide film showed Hv 579 in the temperature of 30$^{\circ}C$ with the current density, 2.5A/$dm^2$ in the 0.5M malic acid bath mixed with 5g/l oxalic acid.

• 농업과학연구
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• 제36권2호
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• pp.225-232
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• 2009

The ratio of saccharification and formation of furans during the acid hydrolysis of agar with oxalic acid and sulfuric acid were examined base on the contents of the agar and acids. The ratio of saccharification in oxalic acid appeared to be 51~59% somewhat higher than 49~61% of sulfuric acid. Formation of the furans during the acid hydrolysis increased proportional to the contents of agar and acid. The relative formation ratio was high 10~47% for furfural (FUR) and 15~29% for hydroxy-methyl furfural (HMF) in 0.5~1.25% sulfuric acid rather than those of oxalic acid. When comparing the removal efficiency of the furans using an alkali treatment, steam stripping and hydrophobic resins, FUR was eliminated 60% by the alkali treatment, 62~90% by steam stripping and 71~75% by Amberlite XAD4 and 7HP, while HMF was removed to low levels of 10.5%, 4~17% and 13~25%, respectively. The loss of reducing sugar was also observed in process of the removal of furans, and the loss rate was the level of 2~4% in alkali treatment, 11~16% in steam stripping and 7~9% in Amberlite resins.

• 펄프종이기술
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• 제33권1호
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• pp.73-79
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• 2001

Stricter environmental demands have increased the need to replace conventional C/D bleaching sequence by chlorine-free sequence. Permanganate is well known as a powerful oxidant and have been used industrially in variable fields. However, it has considered to be difficult to use permanganate as a bleaching reagent because of its strong oxidative effect decreasing the viscosity of pulps extremely. We have tried to use permanganate as a bleaching reagent for KP under the mild condition and it was clear that pernanganate oxidized lignin remained in pulps selectively and increased pulp brightness decreasing K number of pulps with small degradation of cellulose. We have employed the neutral condition in the permanganate bleaching process in this study. In this case, permanganate was converted to manganese dioxide after bleaching reaction. The manganese dioxide is remained in the treated pulp fibers because of its insolublity in water. So it was required to reduction the manganese oxide to manganese ion by using reductants with acid. In this paper, we proposed to use oxalic acid as a reducing reagent converting manganese oxide to manganese ion after bleaching reaction. Oxalic acid plays the role as a reductant and a acid, so post-treatment after bleaching became to be easy by using oxalic acid. On the study using lignin model compounds, it was clear that permaganate react with phenols firstly, after that oxalic acid reduce the manganese oxide to manganese ion in the mixture of permanganate, phenols and oxalic acid. Several lignin model compounds ($\textit{p}$-hydroxybenzaldehyde, vanillin, syringaldehyde, veratraldehyde) are selected to elucidate the effect of substituents on reaction rate and its mechanism with permanganate including oxalic acid in this study. Except for veratraldehyde, the rate of oxidative degradation of phenolic compounds by permanganate with oxalic acid are higher than neutral condition. Especially, the degradation rate of $\textit{p}$-hydroxybenzaldehyde are strongly dependent on pH of reaction mixture. On the other hand, the degradation rate of veratraldehyde are decreased with decreasing pH and main degradation product is veratric acid. This result indicate that pH of bleaching liquor should be kept over 2 to degrade of non-phenolic lignin in the pulps effectively in permanganate bleaching.

• 한국표면공학회지
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• 제55권1호
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• pp.24-31
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• 2022

This study investigated the effect of pre-treatment on the PEO film formation of AZ91 Mg alloy. The pre-treatment was conducted for 10 min at room temperature in 0.5 M oxalic acid (C₂H₂O₄) solution containing various ammonium fluoride (NH₄F) concentrations. The pre-treated AZ91 Mg specimens were anodized at 100 mA/cm² of 300 Hz AC for 2 min in 0.1 M NaOH + 0.4 M Na₂SiO₃ solution. When AZ91 Mg alloy was pretreated in 0.5 M oxalic acid with NH₄F concentration less than 0.3 M, continuous dissolution of the AZ91 Mg alloy occurred together with the formation of black smuts and arc initiation time for PEO film formation was very late. It was noticed that corrosion rate of the AZ91 Mg alloy became faster if small amount of NH₄F concentration, 0.1 M, is added. The fast corrosion is attributable to fast formation of porous fluoride together with porous oxides in the reaction products. On the other hand, when AZ91 Mg alloy was pretreated in 0.5 M oxalic acid with sufficient NH₄F more than 0.3 M, a thin and dense protective film was formed on the AZ91 Mg alloy surface which resulted in faster initiation of arcs and formation of PEO film.

• Food Science and Biotechnology
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• 제17권3호
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• pp.534-539
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• 2008

This study investigated the effects of pretreatment and storage conditions on the properties of stored chestnuts. Effects on chestnuts of refrigerated storage (RNT) and frozen storage (FNT) with no pretreatment, frozen storage after oxalic acid treatment without blanching (FON) and with blanching (FOB) were examined. Water binding capacity, swelling power, solubility, and viscosity of the starch produced from RNT, FNT, and FON were similar to those of the starch produced from control (CON). FOB showed significant differences in these properties from CON. Textural properties of starch gels prepared from stored chestnuts except FOB also were very similar to those of CON starch gels. The sensory characteristics of steamed FON and FNT were similar to those of steamed CON except in brown color and hardness. Steamed FNT tended to have higher brown color and lower hardness than steamed FON. Steamed RNT showed significant differences in all the sensory properties except in hardness and cooked chestnut flavor. Steamed FOB was significantly higher than steamed CON in water release and off-flavor. Among the storage conditions examined, frozen storage with oxalic acid treatment is recommended for the long-term storage of chestnuts.

• 청정기술
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• 제29권1호
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• pp.46-52
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• 2023

옥살산(oxalic acid)은 기존에 질산을 사용한 carbohydrates의 산화 공정에 의해 얻어질 수 있으며 여러 분야에서 사용되고 있다. 하지만 이 반응은 다양한 질소 산화물을 형성하고 많은 증간 생산물의 분리를 필요로 하기에 복잡하고 환경에 유해하다. 한편, 이산화탄소로부터 전기화학적 방법에 의해 옥살산을 높은 효율로 얻을 수 있는 방법이 제안되었다. 아연 전극 산화에 의해 생성된 Zn²⁺이온과 CO₂ 환원에 의한 oxalate이온의 반응으로 zinc oxalate(ZnC₂O₄)가 얻어진다. 이후 산처리에 의해 옥살산이 생성될 수 있으나 강산과 열을 필요로 한다. 본 연구에서는 CO₂의 전기화학적 전환으로 형성된 ZnC₂O₄을 강산을 사용하지 않고, 간단하고 분리가 쉬운 방법을 적용하여 옥살산으로 전환하고자 한다. 또한, 고부가 물질인 글리콜산으로 더 전환시킴으로써 이산화탄소에서 고부가 물질로의 전환 가치를 높이고자 하였다. ZnC₂O₄를 상온, 상압에서 화학적 방법 및 여과 과정을 통해 효과적으로 Zn(OH)₂ 입자와 oxalate 용액으로 분리하였으며 얻어진 Zn(OH)₂와 oxalate는 전기화학적 방법을 사용하여 각각 Zn, 글리콜산으로 전환되었다.

• 한국식품조리과학회지
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• 제4권1호
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• pp.27-32
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• 1988

탈검제로 인산 및 초산, 구연산, 수산, 질산, 붕산 등 6종을 평지씨 기름과 대두유에 적용시킨 결과 수산을 사용하여 인산과 거의 동일한 탈검 효과를 얻을 수 있었다. 즉, 평지씨 기름에서 85% 인산 처리군과 5.10% 수산 처리군의 탄산유내의 잔류 비누물질과 인함량, 탈색유에서의 색상, 탈취유의 과산화물값, trans 지방산 함량 등은 유사한 결과를 나타내었다. 대두유에서도 동일한 결과를 얻었으므로 탈검제로서 인산 대신 수산을 사용할 수 있음을 확인하였다. 한편 85% 인산처리군과 10% 수산처리군으로부터 얻어진 폐수를 분석한 결과 특히 BOD, COD 등에서 현격한 차이를 보였으며 침전분리 및 화학처리한 결과 인산 처리군은 수산 처리군에 비하여 처리시약 요구량 및 처리시간이 각각 3배, 1.7배로 차이가 극심하였다. 따라서 이들 식물성 기름에서 인산대신 수산을 사용하여 동일한 탈검효과를 얻을 수 있었을 뿐만 아니라 폐수 처리도 개선할 수 있었다.

• 자원환경지질
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• 제40권2호
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• pp.141-151
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• 2007

충북 영동지역에서 산출되는 일라이트를 대상으로 철 성분을 제거하는 실험을 수행하였다. 이는 일라이트 광석에 들어있는 철 성분을 제거하여 백색도를 향상시킴으로써 광석의 활용 가능성을 높여 주는데 있다. 철 성분의 제거 효율성을 평가하기 위해 무기산(황산, 염산), 유기산(L-아스코르브산, 옥살산), 혼합산(무기산+유기산)을 사용하였다. 실험결과 0.15 M L-아스코르브산을 0.5 N 황산에 첨가한 혼합산과의 탈철 반응을 수행한 경우, 60분 반응 시 1.5 wt%의 산화철 성분을 제거하여 가장 높은 효율을 나타내었다. 0.5N황산을 단독으로 사용한 경우에는 60분 반응 시 제거된 산화철이 0.68%에 불과하다. 황산만을 이용하여 1.5wt %의 산화철을 제거하기 위해서는 5N의 반응농도와 150분의 반응시간이 요구되었다. 따라서 친환경적이고, 인체친화적인 L-아스코르브산의 탈철반응이 반응농토와 반응시간에 있어서도 효율적임을 관찰하였다. 산화철 제거 후 일라이트는 백색도가 42%에서 75%로, 색도가 10YR 8/4에서 5Y, 8/1로 향상되어 CBD 처리와 같은 수준으로 증가하였다. 일라이트 입자를 교결하고 있던 산화철이 제거되어 입도가 소폭 감소하였으나 광물학적/물리 화학적 특성은 변화가 관찰되지 않았다.