• 환경위생공학
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• 제16권4호
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• pp.62-68
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• 2001

The advantages of hydrogen peroxide dissolution method were no discharge of noxious matter when dissolution of iron wire which used as the center supporter, reactions occur in room temperature and easy to recover dissolved iron. This study was aimed at gathering the basic data of iron wire dissolution- recovery process and proposes the reaction condition of iron wire dissolution- recovery process rind the factors influencing those reactions. The results were as follows : 1 . Hydrogen peroxide dissolution method used hydrochloric acid as the catalyst. 1. In the dissolution of iron wire(1.668 g), the condition of reaction was E1702(30 ml), HCI(20 ml) and $H_2O$(200 ml) ; time of the reaction was 18 min. P.W.(Piece weight) was 7.75 mg, and C.R. was $2.34{\;}{\Omega}$ 2. In the dissolution of iron wire(1.529 g), the condition of reaction was H7O2(30 ml), HCI(20 ml) and $H_2O$(200 ml), time of the reaction was 21 min., P.W.(Piece weight) was 7.73 mg, and C.R. was $2.35{\;}{\Omega}$. Hydrogen peroxide dissolution method used sulfuric acid as the catalyst. 1. In the dissolution of iron wire(0.834 g), the condition of reaction was $H_2O$(65 ml), $H_2SO_4$(5 ml) and 1702(5 ml) ; time of the reaction was 5 min.30 sec, P.W.(Piece weight) was 7.74 mg, and C.R. was $2.33{\;}{\Omega}$ 2. In the dissolution of iron wire(1.112 g), the condition of reaction was $H_2O$(65 ml), $H_2SO_4$(5 ml) and $H_2O_2$(5 ml) ; time of the reaction was 4 min.30 sec, P.W.(Piece weight) was 7.75 mg, and C.R. was $2.33{\;}{\Omega}$. Hydrogen peroxide dissolution method used hydrochloric acid and sulfuric acid as the catalyst confirmed a clean technology, because there were not occurred a pollutant discharged in the existing method.

• 한국환경과학회지
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• 제8권2호
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• pp.227-231
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• 1999

This study was conducted to investigate the removal characteristics of $PO_4^{3-}-P$ contained in livestock wastewater using waste concrete. With small particle size, increased dosage and temperature of water, $PO_4^{3-}-P$ was well removed by waste concrete.$PO_4^{3-}-P$ was removed by adsorption reaction in low pH of the primary phase, but the crystallization reaction predominated for increasing pH with passed time. As a result of adapting the adsorption isotherm equation, $PO_4^{3-}-P$ removal was more affected by the crystallization reaction than the adsorption reaction. In the SEM micrograph, there was no evident change on the waste concreter surface. Particle size was plate-phase before reaction but appeared a dense form to progress in the crystallization reaction.

• Bulletin of the Korean Chemical Society
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• 제24권3호
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• pp.306-310
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• 2003

Hydrolysis reactions of S-phenyl-S-vinyl-N-p-tosylsulfilimine (VSI) and its derivatives at various pH have been investigated kinetically. The hydrolysis reactions produced phenylvinylsulfoxide and p-toluene sulfonamide as the products. The reactions are first order and Hammett ρ values for pH 1.0, 6.0, and 11.0 are 0.82, 0.45, and 0.57, respectively. This reaction is not catalyzed by general base. The plot of k vs pH shows that there are three different regions of the rate constants $(k_t)$ in the profile.; At pH < 2 and pH > 10, the rate constants are directly proportional to the concentrations of hydronium and hydroxide ion catalyzed reactions, respectively. The rate constant remains nearly the same at 2 < pH < 10. On the bases of these results, the plausible hydrolysis mechanism and a rate equation have been proposed: At pH < 2.0, the reaction proceeds via the addition of water molecule to sulfur after protonation at the nitrogen atom of the sulfilimine, whereas at pH > 10.0, the reaction proceeds by the addition of hydroxide ion to sulfur directly. In the range of pH 2.0-10.0, the addition of water to sulfur of sulfilimine appears to be the rate controlling step.

• 대한화학회지
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• 제33권1호
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• pp.127-134
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• 1989

${\beta},\;{\beta}$-diethoxycarbonylstryene 유도체(H, p-OCH$_3$, 3,4,5-(OCH$_3)_3$), 3,4,5-methylenedioxy)에 대한 3-mercaptopropionic acid의 친핵성 첨가반응 속도상수를 자외선 분광법으로 측정하여 넓은 pH 범위에서 적용될수 있는 속도식을 구하였다. pH에 따르는 속도상수의 변화, 일반염기촉매작용등을 바탕으로 이 첨가반응 메카니즘을 제안하였다. 즉 pH 6.0 이하에서는 중성인 3-mercaptopropionic acid 분자의 첨가로 이 반응이 시작되며 pH 6.0∼8.0영역에서는 이 중성분자와 황화음이온의 첨가가 경쟁적으로 일어나며, pH 8.0이상에서는 황화음이온에 의해서만 첨가반응이 진행된다.

• Nuclear Engineering and Technology
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• 제56권6호
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• pp.2079-2091
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• 2024

In this paper, a model is developed for calculating pH in the presence of organic impurities due to dissolution of paint and/or continuous injection of organic impurities in the sump. The model is implemented in the AnCheBi code for the analysis of chemical behaviors of the iodine in the containment when the pH changes during a severe accident. Validation of the model is performed with P10T2 and P11T1 experiments carried out by AECL in Canada under the BIP project. Importance analyses of the pH calculation model in the AnCheBi code are then performed with the aforementioned experimental data via Latin hypercube sampling on the reaction coefficients, sensitivity analyses of AnCheBi, and calculation of the correlation coefficients between the reaction coefficients and figure of merits (the pH and the concentrations of the various iodine species). From the importance analyses, we provide the sensitivity of the pH calculation model to the change of pH and the concentrations of the various iodine species and the reaction coefficients related with the dominant phenomena underlying the change of pH and the concentrations of the species.

• 공업화학
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• 제28권6호
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• pp.619-625
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• 2017

본 연구에서는 하이드로퍼옥시 라디칼 생성단계에서 반응 부산물로 생성되는 과산화수소를 정량하여 수산화라디칼의 생성 및 비스페놀 A (BPA)의 분해특성을 조사하였다. 라디칼 연쇄반응이 일어나지 않는 조건에서는 Criegee mechanism과 동일하게 오존에 의한 직접산화반응만이 BPA를 분해시키는 것으로 나타났다. 라디칼 연쇄반응이 일어나는 pH 6.5 및 9.5의 조건에서는 비선택적 산화반응이 일어나 수산화라디칼의 생성을 간접적으로 확인할 수 있었다. 투입된 촉매에 의한 BPA의 분해효율은 $O_3$/PAC ${\geq}$ $O_3/H_2O_2$ > $O_3$/high pH > $O_3$ alone 공정 순으로 나타났다. 오존/촉매공정들의 산화반응 동안에는 0.03~0.08 mM의 과산화수소가 지속적으로 측정되었다. $O_3$/high pH 공정의 경우, BPA가 반응시작 50 min 만에 완전히 분해되었지만, TOC (총유기탄소) 제거율은 29%로 산화반응 중 생성된 중간물질을 충분히 산화시키지 못하는 것으로 나타났다(선택적 산화반응). $O_3/H_2O_2$ 및 $O_3$/PAC 공정에서는 BPA가 반응시작 40 min 만에 완전히 분해되었으며, TOC 제거율은 각각 57% 및 66% 정도로 반응 중간체들을 산화(비선택적 산화반응)시키는 것으로 나타났다.

• 공업화학
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• 제8권3호
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• pp.502-509
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• 1997

방향족 오염물을 UV산화-고도산화처리기술로 처리할 때, 여러 가지 반응조건에 따른 분해효율에 대해 고찰하였다. 벤젠 50ppm, 에틸벤젠 150ppm, 크실렌 250ppm을 각각 초기농도로하여 UV조사 하에서 시간변화에 따른 분해실험을 행한 결과, 반응 1시간 후 약 95% 이상의 분해율을 나타내었으나, 톨루엔의 경우에는 43%의 분해율을 보였다. 단일성분이 혼합성분에서 보다 분해가 좋았으며, pH변화에서는 벤젠은 pH변화에 관계없이 분해가 잘 되었으며, 에틸벤젠 92%(pH 4.0), 90%(pH 6.4), 91%(pH 10.0), 크실렌 95%(pH 4.0), 90%(pH 6.4), 92%(pH 10.0), 그러나 톨루엔은 80%(pH 4.0), 43%(pH 6.4), 70%(PH 10.0)의 분해율을 나타내었다. 방향족 오염물의 TOC 감소는 에틸벤젠을 제외하고는 유사 1차 반응속도식에 일치하였으며, 이로부터 속도상수를 결정할 수 있었다.

• Preventive Nutrition and Food Science
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• 제13권2호
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• pp.134-137
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• 2008

This study was conducted to investigate the effect of pH on the formation of acrylamide and acrylate from glucose and fructose reacting with amino acid enantiomers by the Maillard reaction. The acrylamide content was increased with increasing pH, except for Fru/D-Asn system. Both acrylamide and acrylate contents were higher in the glucose-based system compared to the fructose-based system at pH 10.0. However, according to amino acid enantiomers, only the acrylamide content showed a difference in the fructose-based system. In addition, the acrylate content was increased with increasing pH except in the Glc/L-Asn system. Acrylate formation was observed specifically at pH 4.0 for both the Glc/D-Asn and Fru/D-Asn systems.

• 한국세라믹학회지
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• 제31권10호
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• pp.1231-1239
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• 1994

In this study, gel powder which had relatively high hydration reactivity in CaO and P2O5 rich composition of CaO-P2O5-SiO2-H2O system was prepared by sol-gel process and its hydrated specimen was manufactured. The it was investigated to appropriate calcination temperature in sol-gel process which hydrated specimen of gel powder have proven to strength and the effect of factors influenced strength in hydration process. The major product of before and after hydration reaction was hydroxyapatite, and crystalline phase of C-S-H was already formed during gelation process. After hydration reaction of pressed specimen, crystalline phase of C-S-P-H was formed. It was hydrated product of silicocarnotite (5CaO.P2O5.SiO2). Gel phases of C-S-H and C-S-P-H occured as a result of partial substitution of amorphous silica by P2O5 was formed. The strength of hydrated hardened body is developed by strong bonding and bridging between the gel phases of C-S-H or C-S-P-H and the crystalline products such as hydroxyapatite, Ca(OH)2 C-S-H and C-S-P-H. In addition, the ultrafine gel powder have an great effect on increase of hydration reaction.

• Bulletin of the Korean Chemical Society
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• 제32권3호
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• pp.964-972
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• 2011

This work investigated the difference between $Fe^{2+}$ autoxidation-induced and Fenton-type cleavage of pBR322 plasmid DNA. $^{\cdot}OH$ generation reactions in the absence and presence of $H_2O_2$ under various conditions were also investigated. Although both the $Fe^{2+}$ autoxidation and Fenton-type reactions showed DNA cleavage and $^{\cdot}OH$ generation, there were significant differences in their efficiencies and reaction rates. The rate and efficiency of the cleavage reaction were higher in the absence of 1.0 mM of $H_2O_2$ than in its presence in 20 mM phosphate buffer. In contrast, the $^{\cdot}OH$ generation reaction was more prominent in the presence of $H_2O_2$ and showed a pH-independent, fast initial reaction rate, but the rate was decreased in the absence of $H_2O_2$ at across the entire tested pH range. Studies using radical scavengers on DNA cleavage and $^{\cdot}OH$ generation reactions in both the absence and presence of $H_2O_2$ confirmed that both reactions spontaneously involved the active oxygen species $^{\cdot}OH$, ${O_2}^{\cdot-}$, $^1O_2$ and $H_2O_2$, indicating that a similar process may participate in both reactions. Based on the above observations, a new mechanism for the $Fe^{2+}$ autoxidation-induced DNA cleavage reaction is proposed.