• 한국세라믹학회지
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• 제32권7호
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• pp.853-857
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• 1995

ZrSiO4 powders were prepared from partially hydrolyzed solution of Si(OC2H5)4 and ZrOCl2.8H2O solution by the sol-gel method and formation rate of ZrSiO4 on the reaction parameter was investigated. In order to prepare homogeneous ZrSiO4 precursor gels, the H2O/Si(OC2H5)4 molar ratio of about 2, the pH of the ZrOCl2.8H2O solution fo about 4 and stirring time of the mixed solutions of about 2 hrs were appropriate. Formation of temperature of ZrSiO4 reduced about 15$0^{\circ}C$ by milling and formation of ZrSiO4 at 1300~135$0^{\circ}C$ showed an accelerative increase through the hedvall effect by silica.

• 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.

• 한국지하수토양환경학회지:지하수토양환경
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• 제7권2호
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• pp.73-81
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• 2002

전통적인 펜톤반응에서 Superoxide radical (${O_2}^-$.)에 의한 사염화탄소의 환원반응을 조사하였으며 과산화수소의 농도구배와 pH의 변화에 따른 ${O_2}^-$.의 생성률을 측정하였다. 펜톤반응에서 1-헥산올의 분해율은 pH가 증가함에 따라 90% (pH3) 에서 5% (pH5) 급격하게 감소한 반면 사염화탄소의 분해율은 pH가 증가함에 따라서 증가하였다. 이러한 결과는 펜톤반응이 Hydroxyl radical (${O_2}^-$.)의 산화반응과 ${O_2}^-$.의 환원반응이 공존하는 반응임을 보이는 결과이다. ${O_2}^-$.의 생성률은 pH 11에서 $H_2$O$_2$의 농도가 29.4mM에서 294mM로 증가함에 따라 (45.3$\pm$7.8) X $10^{-6}$ M/s에서 (151.0$\pm$26.2) X $10^{v}$ / M/s로 증가하였으며 294mM의 H$_2$$O_2$에서 pH가 7에서 11로 증가함에 따라 (22.1$\pm$3.8) x $10^{-6}$ / M/s에서 (151.0$\pm$26.2) x $10^{-6}$ M/s 증가하였다. 이러한 결과는 ${O_2}^-$.의 환원력을 적용한 펜톤반응이 넓은 pH영역에서 적용될 수 있음을 나타내는 결과이다. 특별히 토양내 흡착력이 약하고 지하수내에 쉽게 용해될 수 있으며 독성 및 발암성물질로 알려진 사염화탄소와 같은 염소계 유기화합물의 제거에 효과적으로 적용될 수 있을 것으로 사료된다.

• 한국환경과학회지
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• 제15권1호
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• pp.67-75
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• 2006

The degradation of Rhodamine B (RhB) in water was investigated in laboratory-scale experiments, using five advanced oxidation Processes (AOPs) $UV/H_2O_2$, lenten, photo-lenten, $UV/TiO_2,\;UV/TiO_2/H_2O_2$. The photodegradation experiments were carried out in a fluidized bed photoreactor equipped with an immersed 32 W UV-C lamp as light source. initial decolorization rate and COD removal efficiency were evaluated and compared. The results obtained showed that the initial decolorization rate constant was quite different for each oxidation process. The relative order of decolorization was: photo-fenton > $UV/TiO_2/H_2O_2$ > fenton > $UV/H_2O_2$ > $UV/TiO_2$ > UV > $H_2O_2$. The relative order of COD removal was different from decolorization: photo-fenten ${\fallingdotseq}$ $UV/TiO_2/H_2O_2\;>\;UV/TiO_2\;>\;fenton\;>\;UV/H_2O_2$. The Photo-lenten and $UV/TiO_2/H_2O_2$ processes seem to be appropriate for decolorization and COD removal of dye wastewater.

• 한국재료학회지
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• 제22권11호
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• pp.620-625
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• 2012

A general synthetic method to make $Fe_3O_{4-{\delta}}$ (activated magnetite) is the reduction of $Fe_3O_4$ by $H_2$ atmosphere. However, this process has an explosion risk. Therefore, we studied the process of synthesis of $Fe_3O_{4-{\delta}}$ depending on heat-treatment conditions using $FeC_2O_4{\cdot}2H_2O$ in Ar atmosphere. The thermal decomposition characteristics of $FeC_2O_4{\cdot}2H_2O$ and the ${\delta}$-value of $Fe_3O_{4-{\delta}}$ were analyzed with TG/DTA in Ar atmosphere. ${\beta}-FeC_2O_4{\cdot}2H_2O$ was synthesized by precipitation method using $FeSO_4{\cdot}7H_2O$ and $(NH_4)_2C_2O_4{\cdot}H_2O$. The concentration of the solution was 0.1 M and the equivalent ratio was 1.0. ${\beta}-FeC_2O_4{\cdot}2H_2O$ was decomposed to $H_2O$ and $FeC_2O$4 from $150^{\circ}C$ to $200^{\circ}C$. $FeC_2O4$ was decomposed to CO, $CO_2$, and $Fe_3O_4$ from $200^{\circ}C$ to $250^{\circ}C$. Single phase $Fe_3O_4$ was formed by the decomposition of ${\beta}-FeC_2O_4{\cdot}2H_2O$ in Ar atmosphere. However, $Fe_3C$, Fe and $Fe_4N$ were formed as minor phases when ${\beta}-FeC_2O_4{\cdot}2H_2O$ was decomposed in $N_2$ atmosphere. Then, $Fe_3O_4$ was reduced to $Fe_3O_{4-{\delta}}$ by decomposion of CO. The reduction of $Fe_3O_4$ to $Fe_3O_{4-{\delta}}$ progressed from $320^{\circ}C$ to $400^{\circ}C$; the reaction was exothermic. The degree of exothermal reaction was varied with heat treatment temperature, heating rate, Ar flow rate, and holding time. The ${\delta}$-value of $Fe_3O_{4-{\delta}}$ was greatly influenced by the heat treatment temperature and the heating rate. However, Ar flow rate and holding time had a minor effect on ${\delta}$-value.

• 대한환경공학회지
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• 제22권7호
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• pp.1307-1318
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• 2000

원자력 발전소에서 발생되는 제염폐수에 함유된 Oxalic acid와 Citric acid를 고급산화방법(Advanced Oxidation Process) 중의 하나인 $UV/H_2O_2$를 적용하여 이들 물질의 분해특성 및 최적처리조건을 파악하고자 하였다. 이를 위하여 각각의 물질에 대하여 $H_2O_2$나 UV를 단독사용할 경우, pH 및 과산화수소의 주입량 변화, Oxalic acid와 Citric acid의 농도변화에 따른 분해특성에 대하여 조사하였다. $H_2O_2$나 UV만으로도 완전분해가 가능한 반면 Citric acid는 같은 파장의 UV만으로는 분해가 잘되지 않는 것으로 조사되었다. 또한 과산화수소와는 두 물질 모두 반응성이 없는 것으로 조사되었다. 산화공정에서 반응속도상수, 반응시간, 제거효율, 과산화수소 소모량 등에 대한 결과를 종합한 결과 Oxalic acid의 경우 pH 4 이하의 낮은 pH에서, Citric acid는 pH 4~6 정도의 약산성 부근에서 높은 분해효율을 나타내는 것으로 조사되었다. 최적 pH에서는 과산화수소의 주입량이 증가할수록 두 물질 모두 제거효율이 증가하는 것으로 조사되었으나 과산화수소의 주입량이 200 mg/L 이상을 초과하는 경우에는 과산화수소에 의한 OH radical trap에 의하여 제거효율이 감소하는 것으로 조사되었다. 이상의 결과 $UV/H_2O_2$ 광분해에 의한 Oxalic acid와 Citric acid의 처리시 pH 4에서 과산화수소 주입량 200 mg/L일 경우 가장 효율적인 것으로 조사되었다.

• Bulletin of the Korean Chemical Society
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• 제30권3호
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• pp.667-670
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• 2009

The understanding of behaviors of hydroperoxyl/superoxide anion radicals (${H_2O_2}^./{O_2}^{-.}$) generated from a photoirradiated $TiO_2$ surface is essential to improve the efficiency of $TiO_2$ photocatalytic reactions by decreasing the recombination of photoinduced electron-hole ($e^--h^+$) pairs. In contrast with previous studies, we found that ${H_2O_2}^./{O_2}^{-.}$ generated on the surface of illuminated $TiO_2$ particles are mobile. ${H_2O_2}^./{O_2}^{-.}$ formed by the photocatalysis of $TiO_2$ particles immobilized onto the inner surface of a coil-quartz tube were forced under a continuous flow through a knotted tubing reactor (KTR) and into the aqueous phase completely separated from the $TiO_2$ particles, and were measured by a chemiluminescence (CL) technique using 2-methyl-6-(p-methoxyphenyl)-3,7-dihydroimidazo[ 1,2-a]pyrazin-3-one (MCLA) as the reagent. The initial concentration of the ${H_2O_2}^./{O_2}^{-.}$ stream entering the KTR was determined by its half-life (98 s) at pH 5.8. We suggests that the efficiency of $TiO_2$ photocatalytic reactions may be further improved by utilizing the mobility of ${H_2O_2}^./{O_2}^{-.}$.

• Environmental Engineering Research
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• 제16권3호
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• pp.131-136
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• 2011

The degradation of 30 pharmaceuticals and personal care products (PPCPs) subjected to $O_3$, $O_3$/UV, and $O_3/H_2O_2$ treatments were investigated using semi-batch tests and evaluated by their pseudo-first-order rate constants. The additional application of UV or $H_2O_2$ during $O_3$ treatment significantly improved the degradation rate of most of the PPCPs. At the same $O_3$ feed rate, $O_3$/UV treatment exhibited much higher PPCP degradation efficiency than that of $O_3$ treatment. This was probably due to degradation of the PPCPs by $O_3$, direct UV photodegradation, and OH radicals that formed from the photodegradation of $O_3$ during $O_3$/UV treatment. PPCP degradation by $O_3$ was also promoted by adding $H_2O_2$ during the $O_3$ treatment. However, when the initial $H_2O_2$ concentration was high during $O_3$ treatment, OH radicals were likely to be scavenged by excess $H_2O_2$, leading to low PPCP degradation. Therefore, it is important to determine the appropriate $H_2O_2$ dosage during $O_3$ treatment to improve PPCP degradation when adding $H_2O_2$ during $O_3$ treatment.

• 대한화학회지
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• 제48권4호
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• pp.358-366
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• 2004

두개의 sulphato로 다리걸친 착물 $[Cr_2(NH_2)_2(H_2O)_2(SO_4)_2]{\cdot}2H_2O$, 말단 3개의 isocyanato $[Cr(NCO)_3(H_2O)]{\cdot}3H_2O$ 화합물과 갈철광 $[FeO(OH)]{\cdot}0.2H_2O$ 화합물들은 각각의 $Cr_2(SO_4)_3{\cdot}xH_2O, Cr(CH_3COO)_3, Fe_2(SO_4)_3$과 $80^{\circ}C$, 수용액에서 요소와 반응으로 합성되었다. 생성물들의 IR 스펙트럼에서 요소(urea)의 띠가 나타나지 않지만, 결합된 아마이드(amide), 물, 연결된 sulphato와 isocyanato 그룹에 대해서 특징적인 띠를 보인다. 착물들에 대한 열무게분석(TG)과 시차열분석법(DTA) 측정을 기록하였다. 얻어진 데이터들은 예상했던 구조화 잘 일치한다. 형성에 대한 설명과 화합물의 열역학적 분해에 대한 일반적인 메커니즘을 제시하였다.

• Bulletin of the Korean Chemical Society
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• 제34권10호
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• pp.3065-3072
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• 2013

Direct synthesis of $H_2O_2$ and in situ oxidative desulfurization of model fuel over Au/Ti-HMS and Au/TS-1 catalysts has been comparatively investigated in water or methanol. Maximum amount (82%) of active $Au^0$ species for $H_2O_2$ synthesis was obtained. Au/Ti-HMS and Au/TS-1 exhibited the contrary performances in $H_2O_2$ synthesis as $CH_3OH/H_2O$ ratio of solvent changed. $H_2O_2$ decomposition and hydrogenation in water was inhibited by the introduction of methanol. Effect of $O_2/H_2$ ratio on $H_2O_2$ concentration, $H_2$ conversion and $H_2O_2$ selectivity revealed a relationship between $H_2O_2$ generation and $H_2$ consumption. The highest dibenzothiophene removal rate (83.2%) was obtained over Au/Ti-HMS in methanol at 1.5 of $O_2/H_2$ ratio and $60^{\circ}C$. But removal of thiophene over Au/TS-1 should be performed in water without heating to obtain a high removal rate (61.3%). Meanwhile, $H_2$ conversion and oxidative desulfurization selectivity of $H_2$ were presented.