• Title/Summary/Keyword: Decomposition Products

Search Result 377, Processing Time 0.029 seconds

Effect of $H_2O_2$ and Metals on The Sonochemical Decomposition of Humic Substances in Wastewater Effluent

  • Jung, Oh-Jun
    • Environmental Sciences Bulletin of The Korean Environmental Sciences Society
    • /
    • v.10 no.S_3
    • /
    • pp.127-137
    • /
    • 2001
  • The sonochemical Process has been applied as a treatment method and was investigated its effect on the decomposition of humic substances(HS). The reaction kinetics and mechanisms in the Process of sonochemical treatment for humic substances(HS) in wastewater have also been discussed. It was observed that the metal ions such as Fe(II) and Mn(II) showed catalytic effects, while Al(III), Ca(II), and Mg(II) had inhibitory effects on the decomposition of humic substances in sonochemical reaction with hydrogen peroxide. Experimental results also showed factors such as hydrogen peroxide dose affected the formation of disinfection by-products. Two trihalomethanes, chloroform and dichlorobromomethane were formed as major disinfection by-products during chlorination. The mechanism of radical reaction is controlled by an oxidation process. The radicals are so reactive that most of them are consumed by HS radicals and hydroxyl radicals can be acted on organic solutes by hydroxyl addition, hydrogen abstraction, and electron transfer. The depolymerization and the radical reaction of HS radicals appear to occur simultaneously. The final steps of the reaction are the conversion of organic acids to carbon dioxide.

  • PDF

Decomposition of Chlorofluorocarbon by Sonication (초음파조사에 의한 염화불화탄소(CFC)의 분해)

  • ;;Kyozo Hirai;Yasuaki Maeda
    • Journal of Korean Society for Atmospheric Environment
    • /
    • v.19 no.3
    • /
    • pp.307-314
    • /
    • 2003
  • The sonolytic decomposition of chlorofluorocarbon (CFC 113) and several alternative compounds, such as HCFC 225ca, HCFC 225cb, and HFC 134a, in.aqueous solutions was investigated. The CFC 113 with a high volatility and a low solubility in water was rapidly decomposed with increasing sonication time. The decomposition rates were influenced by the initial concentration of CFC 113, the reaction temperature, and the gas/liquid phase volume ratio but were independant of the pH of solution. The predominant pathway of the decomposition of CFC 113 by sonication was not the oxidation by OH radicals but the pyrolysis with high temperature and pressure inside of the cavitation bubble. The pyrolysis in the cavitation bubble resulted in an almost complete mineralization of CFC 113 with the high efficient formation of inorganic products (Cl$^{[-10]}$ , F$^{[-10]}$ , CO, $CO_2$). The addition of zinc powder on the decomposition of CFC 113 by sonication caused an acceleration of the decomposition. Also, HCFCs and HFC 134a were found to be readily decomposed by the pyrolysis induced from the sonication.

Thermal Decomposition Reaction of Gas-phase Uranyl Complexes as Studied by in-Situ IR Spectroscopy

  • Cho, Young-Hwan;Choi, In-Kyu;Kim, Won-Ho
    • Proceedings of the Korean Nuclear Society Conference
    • /
    • 2002.05a
    • /
    • pp.420.1-420
    • /
    • 2002
  • Thermal decomposition reaction of gas-phase UO2(hfacac)2. THF was investigated in a static cell. IR spectroscopic method was used to study the thermal decomptsition of gas phase uranyl complexes. The decomposition reaction products were separated by using thermal-gradient fractional sublimation method utilizing the differences in their volatility.

  • PDF

Oxidative Decomposition of TCE over TiO2-Supported Metal Oxide Catalysts (TiO2에 담지된 금속 산화물 촉매상에서 TCE 산화분해반응)

  • Yang Won-Ho;Kim Moon-Hyeon
    • Journal of Environmental Science International
    • /
    • v.15 no.3
    • /
    • pp.221-227
    • /
    • 2006
  • Oxidative TCE decomposition over $TiO_2$-supported single and complex metal oxide catalysts has been conducted using a continuous flow type fixed-bed reactor system. Different types of commercial $TiO_2$ were used for obtaining the supported catalysts via an incipient wetness technique. Among a variety of titanias and metal oxides used, a DT51D $TiO_2\;and\;CrO_x$ would be the respective promising support and active ingredient for the oxidative TCE decomposition. The $TiO_2-based\;CrO_x$ catalyst gave a significant dependence of the catalytic activity in TCE oxidation reaction on the metal loadings. The use of high $CrO_x$ contents for preparing $CrO_x/TiO_2$ catalysts might produce $Cr_2O_3$ crystallites on the surface of $TiO_2$, thereby decreasing catalytic performance in the oxidative decomposition at low reaction temperatures. Supported $CrO_x$-based bimetallic oxide systems offered a very useful approach to lower the $CrO_x$ amounts without any loss in their catalytic activity for the catalytic TCE oxidation and to minimize the formation of Cl-containing organic products in the course of the catalytic reaction.

Thermal Decomposition of Ammonia Borane for $H_2$ Release (수소 발생을 위한 암모니아 보레인의 열분해)

  • Lee, Ji-Hong;Lee, Hyun-Joo;Ahn, Byoung-Sung;Kim, Chang-Soo
    • Transactions of the Korean hydrogen and new energy society
    • /
    • v.19 no.4
    • /
    • pp.299-304
    • /
    • 2008
  • Thermal decomposition of Ammonia Borane have been investigated with various analytical methods including TGA, TP-MS, DSC. By-products such as aminoborane and borazine were identified during hydrogen release by TGA, TP-MS analysis. $H_2$ release amount was measured at each temperature isothermally, which resulted in 7 wt% $H_2$ release at 130$^{\circ}C$. Moreover, higher temperature enhanced hydrogen release kinetics leading to shortened induction period from 20 min at 95$^{\circ}C$ to 0 min at 130$^{\circ}C$. Melting and decomposition at close temperature (4$^{\circ}C$ difference) caused the formation of thin foam during hydrogen release. Suppression of by-products and thin foam formation during hydrogen release is suggested as critical issues to realize chemical hydrogen storage system with ammonia borane.

Gamma-Radiolysis of Carbon Dioxide (IV). Effect of the Addition of Alcohols on the Gamma-Radiolysis of Gaseous Carbon Dioxide$^+$

  • Jin Joon Ha;Choi Jae Ho;Pyun Hyung Chick;Choi Sang Up
    • Bulletin of the Korean Chemical Society
    • /
    • v.9 no.1
    • /
    • pp.55-59
    • /
    • 1988
  • The gaseous carbon dioxide has been irradiated with Co-60 gamma-radiation in the presence and absence of various alcohols, and the radiolysis products analyzed by gas chromatography. Experimental results indicate that no detectable amount of carbon monoxide is formed when pure carbon dioxide is irradiated. By adding small quantities of alcohols to carbon dioxide, however, considerable amount of carbon monoxide, ketones, alcohols and other organic products have been detected. By adding 0.1% of methanol, ethanol, 1-propanol, 2-propanol, 1-butanol, 2-methyl-l-propanol, 2-butanol, and 2-methyl-2-propanol, G(CO) values obtained are 4.4, 4.5, 5.2, 4.4, 5.2, 5.0, 4.7 and 4.1, respectively. These high yields of carbon monoxide suggest that the oxidation reactions of carbon monoxide may be suppressed by scavenging oxygen atom with the alcohols. The main radiolytic decomposition reactions of the alcohols present in small quantity in carbon dioxide may be supposed to be the reactions with the oxygen atom produced by the radiolysis of carbon dioxide. The decomposition reactions seems to follow pseudo-first order kinetics with respect to the alcohols. The decomposition rate measured with 2-propanol is the fastest and that with 2-methyl-2-propanol the slowest. The mechanisms of the radiolytic decomposition reactions of the alcohols present in carbon dioxide are discussed on the basis of the experimental results of the present study.

Effect of the Diisocyanate Type on the Hydrolysis Behavior of Polyurethane

  • Dong-Eun Kim;Seung-Ho Kang;Sang-Ho Lee
    • Elastomers and Composites
    • /
    • v.58 no.3
    • /
    • pp.121-127
    • /
    • 2023
  • The effect of diisocyanate type on the decomposition temperature of polyurethane (PU) hydrolysis was investigated in a subcritical water medium up to 250℃. PU samples were prepared using different types of diisocyanate: two aromatic diisocyanates (4,4'-methylene diphenyl diisocyanate (MDI) and methyl phenylene diisocyanate (TDI)), one unbranched aliphatic diisocyanate (hexamethylene diisocyanate (HDI)), and two cyclic aliphatic diisocyanates (4,4'-methylene dicyclohexyl diisocyanate (H12MDI) and isophorone diisocyanate (IPDI)). The pressure had no effect on hydrolysis in the range of 70-250 bar. The decomposition temperature of the PU samples increased in the following order: TDI-PU (199℃) < H12MDI ≈ IPDI ≈ HDI (218-220℃) < MDI-PU (237℃). This order of increase in temperature is related to the electron-donating ability of the group to connected to the nitrogen of the urethane unit. When the temperature of the (PU + water) mixture reached the specific decomposition temperature, the PU samples hydrolyzed completely within 5 min into primary amine and 1,4-butanediol. The hydrolysis products from MDI-PU and H12MDI-PU were separated into a liquid phase rich in (BD + water) and a solid low phase rich in amine, whereas the products from TDI-, IPDI-, and HDI-PU existed in a single aqueous phase.

Hydorgen Production by Catalytic Decomposition of Propane Over Cabon-Based Catalyst (탄소계 촉매를 이용한 프로판 분해 반응에 의한 수소 생산)

  • Yoon, Suk Hoon;Han, Gi Bo;Lee, Jong Dae;Park, No-Kuk;Ryu, Si Ok;Lee, Tae Jin;Yoon, Ki June;Han, Gui Young
    • Korean Chemical Engineering Research
    • /
    • v.43 no.6
    • /
    • pp.668-674
    • /
    • 2005
  • It is reported that a method for the hydrogen production from the propane decomposition using carbon black as a catalyst is more effective than from the methane decomposition. Since the by-products like CO and $CO_2$ are not produced by the direct decomposition of propane, it is considered as an environmentally sustainable process. In this study, hydrogen was produced by the direct decomposition of propane using either commercial activated carbon or carbon black at atmospheric pressure in the temperature range of $500-1,000^{\circ}C$. Resulting products in our experiment were not only hydrogen but also several by-products such as methane, ethylene, ethane, and propylene. Hydrogen yield increased as temperature increased because the amount of those by-products produced in the experiment was inversely proportional to temperature. The achieved hydrogen yield at $750^{\circ}C$ with commercial DCC N330 catalyst was 22.47% in this study.

Studies on Stability of Ftorafur (항암제제(抗癌製劑) 개발(開發)에 관(關)한 연구(硏究) -Ftorafur의 안전성(安定性)에 관(關)한 연구(硏究)-)

  • Baik, Chia-Sun;Choi, Jun-Shik;Yu, Young-Jong
    • Journal of Pharmaceutical Investigation
    • /
    • v.15 no.1
    • /
    • pp.40-44
    • /
    • 1985
  • The stability of ftorafur in artificial gastric juice and its major decomposition product were studied quantitatively by the combination of TLC technique and UV-recording spectrophotometry. The decomposition proceeded in first-order reaction. The decomposition rate was accelerated by the increase of temperature. The major decomposition products were identified as 5-fluorouracil. The apparent activation energy for the decomposition was found to he approximately 24.3kcal/mole from Arrhenius plot.

  • PDF

Decomposition Characteristics of Benzene by Microwave

  • Kim, Dong-Sik;Kim, Jeong-Young;Lee, Dong-Kyu
    • Carbon letters
    • /
    • v.1 no.3_4
    • /
    • pp.143-147
    • /
    • 2001
  • Under the irradiation of radiofrequency wave, the dipole materials vibrate as microwave phase changes. This causes friction between adjacent molecules and enables an unique characteristics of interior heating of the materials. Using this principle, when harmful material pass through anthracite- bed which play a role as a absorber of radiofrequency wave, the material can be easily decomposed by the microwave energy. To remove benzene vapour and other solvents in the process of industry, we examined decomposition of benzene in this manner. It was found that benzene was decomposed to the methane, ethane, propane and butane, etc. during passing through the carbon-bed under the microwave impingement and distribution of methane in the products reached about 85 vol.%. The decomposition rate of benzene was high within 5 minutes from start of reaction. For a lower concentration of benzene gas, general cases in the field of industry, almost complete decomposition of benzene is believed possible and this method is surely expected to be useful for the prevention of air pollution and improvement of ambient condition.

  • PDF