• Title/Summary/Keyword: oxidation process

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A Comparison between the Decomposition of Bisphenol A and the Concentration of Hydrogen Peroxide Formed during Ozone/Catalyst Oxidation Process (오존/촉매 산화공정에서 비스페놀 A의 분해와 생성된 과산화수소의 농도 비교)

  • Choi, Jae Won;Lee, Hak Sung
    • Applied Chemistry for Engineering
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    • v.28 no.6
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    • pp.619-625
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    • 2017
  • In this study, the formation of hydroxyl radical and decomposition characteristics of bisphenol A (BPA) was investigated by quantifying hydrogen peroxide formed as a reaction by-product during the formation stage of hydroperoxyl radical. The direct oxidation reaction by ozone only decomposed BPA just like the Criegee mechanism under the condition where radical chain reactions did not occur. Non-selective oxidation reactions occurred under the conditions of pH 6.5 and 9.5 where radical chain reactions do occur, confirming indirectly the formation of hydroxyl radical. The decomposition efficiency of BPA by the added catalysts appeared in the order of $O_3$/PAC ${\geq}$ $O_3/H_2O_2$ > $O_3$/high pH > $O_3$ alone. 0.03~0.08 mM of hydrogen peroxide were continuously measured during the oxidation reactions of ozone/catalyst processes. In the case of $O_3$/high pH process, BPA was completely decomposed in 50 min of the oxidation reaction, but reaction intermediates formed by oxidation reaction were not oxidized sufficiently with 29% of the removal ratio for total organic carbon (TOC, selective oxidation reaction). In the case of $O_3/H_2O_2$ and $O_3$/PAC processes, BPA was completely decomposed in 40 min of the oxidation reaction, and reaction intermediates formed by the oxidation reaction were oxidized with 57% and 66% of removal ratios for TOC, respectively (non-selective oxidation reactions).

Chemistry of persulfates for the oxidation of organic contaminants in water

  • Lee, Changha;Kim, Hak-Hyeon;Park, Noh-Back
    • Membrane and Water Treatment
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    • v.9 no.6
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    • pp.405-419
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    • 2018
  • Persulfates (i.e., peroxymonosulfate and peroxydisulfate) are capable of oxidizing a wide range of organic compounds via direct reactions, as well as by indirect reactions by the radical intermediates. In aqueous solution, persulfates undergo self-decomposition, which is accelerated by thermal, photochemical and metal-catalyzed methods, which usually involve the generation of various radical species. The chemistry of persulfates has been studied since the early twentieth century. However, its environmental application has recently gained attention, as persulfates show promise in in situ chemical oxidation (ISCO) for soil and groundwater remediation. Persulfates are known to have both reactivity and persistence in the subsurface, which can provide advantages over other oxidants inclined toward either of the two properties. Besides the ISCO applications, recent studies have shown that the persulfate oxidation also has the potential for wastewater treatment and disinfection. This article reviews the chemistry regarding the hydrolysis, photolysis and catalysis of persulfates and the reactions of persulfates with organic compounds in aqueous solution. This article is intended to provide insight into interpreting the behaviors of the contaminant oxidation by persulfates, as well as developing new persulfate-based oxidation technologies.

Wet oxidation of polycrystalline $Ge_{0.2}Si_{0.8}$ (다결정 $Ge_{0.2}Si_{0.8}$의 습식 열산화)

  • 박세근
    • Electrical & Electronic Materials
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    • v.8 no.1
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    • pp.71-76
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    • 1995
  • The thermal oxidation of Ge$_{0.2}$Si$_{0.8}$ in wet ambient has been investigated by Rutherford Backscattering Spectrometry(RBS). A uniform Ge$_{0.2}$Si$_{0.8}$O$_{2}$ oxide is formed at temperatures below 650.deg. C for polycrystalline and below 700.deg. C for single crystalline substrates. At higher temperatures Ge becomes depleted from the oxide and finally SiO$_{2}$ oxide is formed with Ge piled-ub behind it. The transition between the different oxide types depends also on the crystallinity of Ge$_{0.2}$Si$_{0.8}$. When a uniform Ge$_{0.2}$Si$_{0}$8/O$_{2}$ oxide grows, its thickness is proportional to the square root of the oxidation time, which suggests that the rate noting process is the diffusive transport of oxidant across the oxide. It is believed the oxidation is controlled by the competition between the diffusion of Ge or Si in Ge$_{0.2}$Si$_{0.8}$ and the movement of oxidation front.t.oxidation front.t.

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An Experimental Study on the Oxidation Process of Silicon (실리콘 산화공정에 대한 실험적 고찰)

  • 최연익;김충기
    • Journal of the Korean Institute of Telematics and Electronics
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    • v.16 no.1
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    • pp.26-32
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    • 1979
  • Dry oxidation and wet oxidation processes of silicon have been examined experimentally. The oxidation temperatures were 1.10$0^{\circ}C$, 1.15$0^{\circ}C$, and 1.200 $^{\circ}C$, and oxygen flow rate was changed from 0.2 liter/min to 2.8 liter/min. From the experimental measurements, oxidation temperaturel time and oxygen flow rate have been tabutated for oxide layers 0.1$\mu$ - 1.0$\mu$ in thickness. The quality of the grown oxide layer has been investigated In terms of the dielectric constant, breakdown voltage, fixed surface charge densify (Qss/q) and mobile charge density (Q /q). From these measurements, it is concluded that the quality of the oxide layer is sufficient to expect the normal operation of MOS transistors.

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Structural Changes during Oxidation Process of Anisotopic Mesophase Carbon Fibers(II)-Surface Texture Observation by Scanning Electron Microscopy (산화반응에 의한 이방성 메조페이스 탄소섬유의 구조 변화(II)-주사전자현미경을 이용한 표면구조 관찰)

  • Roh, J.S.
    • Korean Journal of Materials Research
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    • v.13 no.12
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    • pp.831-838
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    • 2003
  • Anisotropic mesophase carbon fiber(AMCFs) was exposed to isothermal oxidation in air and $CO_2$atmosphere, and burn-off rates have measured by TGA. The microstructure changes of oxidized carbon fibers, were observed by SEM. It was observed that oxidation rate in the air is over 100 times faster than that in $CO_2$atmosphere. The activation energy obtained in air was about 43.4 Kcal/mole in the temperature range of $600∼800^{\circ}C$, and in $CO_2$was about 55.2 Kcal/mole in the temperature range of $950∼1200^{\circ}C$. Therefore, the oxidation reaction in both atmospheres was under chemical reaction regime in the above temperature ranges. It was shown that the oxidation of the AMCFs is initiated at the end of fibers at high temperature($1100^{\circ}C$) with developing the large pores, and the small pores are developed on the fiber surface at low temperature($900^{\circ}C$). In conclusion, the oxidation of the AMCFs is progressed through the imperfection.

Comparison of Land Farming and Chemical Oxidation based on Environmental Footprint Analysis (환경적 footprint 분석을 통한 토양경작법과 화학적산화법의 비교)

  • Kim, Yun-Soo;Lim, Hyung-Suk;Park, Jae-Woo
    • Journal of Soil and Groundwater Environment
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    • v.20 no.3
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    • pp.7-14
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    • 2015
  • In this study, land farming and chemical oxidation of a diesel-contaminated site is compared to evaluate the environmental impact during soil remediation using the Spreadsheet for Environmental Footprint Analysis by U.S. EPA. Each remediation process is divided into four phases, consisting of soil excavation, backfill and transportation (Phase 0), construction of remediation facility (Phase 1), remediation operation (Phase 2), and restoration of site and waste disposal (Phase 3). Environmental footprints, such as material use, energy consumption, air emission, water use and waste generation, are analyzed to find the way to minimize the environmental impact. In material use and waste generation, land farming has more environmental effect than chemical oxidation due to the concrete and backfill material used to construct land farming facility in Phase 1. Also, in energy use, land farming use about six times more energy than chemical oxidation because of cement production and fuel use of heavy machinery, such as backhoe and truck. However, carbon dioxide, commonly considered as important factor of environmental impact due to global warming effect, is emitted more in chemical oxidation because of hydrogen peroxide production. Water use of chemical oxidation is also 2.1 times higher than land farming.

Control of size and physical properties of graphene oxide by changing the oxidation temperature

  • Kang, Dong-Woo;Shin, Hyeon-Suk
    • Carbon letters
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    • v.13 no.1
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    • pp.39-43
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    • 2012
  • The size and the physical properties of graphene oxide sheets were controlled by changing the oxidation temperature of graphite. Graphite oxide (GO) samples were prepared at different oxidation temperatures of $20^{\circ}C$, $27^{\circ}C$ and $35^{\circ}C$ using a modified Hummers' method. The carbon-to-oxygen (C/O) ratio and the average size of the GO sheets varied according to the oxidation temperature: 1.26 and 12.4 ${\mu}m$ at $20^{\circ}C$, 1.24 and 10.5 ${\mu}m$ at $27^{\circ}C$, and 1.18 and 8.5 ${\mu}m$ at $35^{\circ}C$. This indicates that the C/O ratio and the average size of the graphene oxide sheets respectively increase as the oxidation temperature decreases. Moreover, it was observed that the surface charge and optical properties of the graphene oxide sheets could be tuned by changing the temperature. This study demonstrates the tunability of the physical properties of graphene oxide sheets and shows that the properties depend on the functional groups generated during the oxidation process.

CO Oxidation of Catalytic Filters Consisting of Ni Nanoparticles on Carbon Fiber

  • Seo, Hyun-Ook;Nam, Jong-Won;Kim, Kwang-Dae;Kim, Young-Dok;Lim, Dong-Chan
    • Bulletin of the Korean Chemical Society
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    • v.33 no.4
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    • pp.1199-1203
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    • 2012
  • Catalytic filters consisting of Ni nanoparticle and carbon fiber with different oxidation states of Ni (either metallic or oxidic) were prepared using a chemical vapor deposition process and various post-annealing steps. CO oxidation reactivity of each sample was evaluated using a batch type quartz reactor with a gas mixture of CO (500 mtorr) and $O_2$ (3 torr) at $300^{\circ}C$. Metallic and oxidic Ni showed almost the same CO oxidation reactivity. Moreover, the CO oxidation reactivity of metallic sample remained unchanged in the subsequently performed second reaction experiment. We suggested that metallic Ni transformed into oxidic state at the initial stage of the exposure to the reactant gas mixture, and Ni-oxide was catalytically active species. In addition, we found that CO oxidation reactivity of Ni-oxide surface was enhanced by increase in the $H_2O$ impurity in the reactor.

High Temperature Oxidation Behavior of Cr-Mo Low Alloy Steel According to Atmospheric Pressures in Humid Air (Humid air 분위기로부터 대기 압력에 따른 Cr-Mo 저합금강의 고온 산화 거동)

  • Kwon, Gi-hoon;Park, Hyunjun;Lee, Young-Kook;Moon, Kyoungil
    • Journal of the Korean Society for Heat Treatment
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    • v.35 no.5
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    • pp.246-254
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    • 2022
  • The high-temperature oxidation behavior of Cr-Mo steel AISI 4115 in air at different temperatures (600, 850, 950℃) for 120 min was studied by mass gain analysis, phase analysis (optical microscopy, electron probe micro-analysis, x-ray diffraction) and hardness measurement of each iron oxide-phase. The oxidation scales that formed on oxidation process consisted outer layer (Hematite), middle layer (Magnetite) and the inner layer (Chromite). In the case of 850 and 950℃, the oxidation mass gain per unit area of AISI 4115 steel increased according to the logarithmic rate as atmospheric pressure increased. Especially, It has been observed that with an increase in the atmospheric pressure at 600℃, the oxidation mass gain per unit area changed from a linear to logarithmic relationship.

A study on production of dry oxidant by decomposition of H2O2 on K-Mn/Fe2O3 catalyst and NO oxidation process according to simulated flue gas flow (K-Mn/Fe2O3 촉매 상 H2O2 분해에 의한 건식산화제 생성 및 모사 배가스 유량에 따른 NO 산화공정)

  • Choi, Hee Young;Shin, Woo Jin;Jang, Jung Hee;Han, Gi Bo
    • Journal of the Korean Applied Science and Technology
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    • v.34 no.2
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    • pp.367-375
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    • 2017
  • In this study, NO oxidation process was studied to increase the NO treatment efficiency of pollutant present in exhaust gas. $H_2O_2$ catalytic cracking was introduced as a method of producing dry oxidizing agents with strong oxidizing power. The $K-Mn/Fe_2O_3$ heterogeneous catalysts applicable to the $H_2O_2$ decomposition process were prepared and their physico-chemical properties were investigated. The prepared dry oxidant was applied to the NO oxidation process to treat the simulated exhaust gas containing NO, NO conversion rates close to 100% were confirmed at various flow rates (5, 10, 20 L/min) of the simulated flue gas.