191 |
Oxidative studies of emodin anthroneBoyce, James P. 08 1900 (has links)
No description available.
|
192 |
Kinetics of oxidation of aqueous sulfur (IV) as catalized by manganous ionCollins, Kenneth Robert 05 1900 (has links)
No description available.
|
193 |
Correlation of antihypertensive activity of novel DBM substrates with adrenergic catecholamine levels in spontaneously hypertensiveEvans, Chheng-Orn Ny 05 1900 (has links)
No description available.
|
194 |
Oxidative doping and characterization of electrically conductive poly(undecyl bithiophene)s with quinone based oxidantsBrooms, Christine Edmond 05 1900 (has links)
No description available.
|
195 |
The catalytic isomerization of alpha-pinene and the catalytic oxidation of the isomerized productsSmoyer, Howard Walter 05 1900 (has links)
No description available.
|
196 |
Catalytic partial oxidation of methyl acetate as a model to investigate the conversion of methyl esters to hydrogenNguyen, Betty Ngoc Thy, 1982- January 2007 (has links)
Rhodium, platinum, copper, palladium, and rhodium-ceria catalysts were investigated in the catalytic partial oxidation of methyl acetate, the simplest methyl ester, to better understand the conversion of biodiesel to hydrogen. Only rhodium and rhodium-ceria catalysts allowed for an autothermal reactor operation. Both catalysts were active in producing hydrogen, carbon monoxide, water, and carbon dioxide, although the rhodium-ceria catalyst showed the greater methyl acetate conversion and the greater hydrogen and carbon monoxide selectivities. A low C/O feed ratio favored the methyl acetate conversion, the hydrogen selectivity, and the carbon monoxide selectivity. Furthermore, a high gas hourly space velocity also improved the reactor performance. According to the experimental data, it appears that the oxidation of methyl acetate forms carbon monoxide and water as a primary step, instead of carbon dioxide and water as with the combustion reaction. In general, methyl acetate does not yield more synthesis gas than biodiesel. The methyl ester functional group limits the hydrogen yield and hence new catalysts should be developed and investigated in order to better target the decomposition of methyl esters to hydrogen.
|
197 |
Scope of microporous and mesoporous molecular sieves in the oxidation of higher alkanes with ozonePullabhotla, V. S. R. Rajasekhar. January 2008 (has links)
Alkane-rich fractions including n-paraffins are the most important chemical feedstock used in the / Thesis (Ph.D.)-University of KwaZulu-Natal, Westville, 2008.
|
198 |
Alkaline Pressure Oxidation of Pyrite in the Presence of Silica – Characterization of the Passivating FilmDani, Anirudha 22 November 2013 (has links)
Alkaline pressure oxidation, particularly in the presence of trona as additive, can be used to oxidize high carbonate refractory gold ores as it prevents the formation of CO2 in the autoclave. However, the presence of silica in the ore can lead to the encapsulation of pyrite due to the formation of a passive layer. This phenomenon occurs due to the high solubility of silica in alkaline solutions and its subsequent re-precipitation on the reacting pyrite surface. The present study investigated the chemical composition and thickness of the passive layer on a rotating pyrite surface in an aqueous slurry containing silica sand, sodium carbonate and calcium carbonate at 230°C and under 7 bar of oxygen overpressure. Results obtained from XPS and SEM show that a concentration of 2.5 g/L sodium carbonate gave the maximum thickness of passivation on pyrite and that the passive layer consisted primarily of silicates and aluminosilicates.
|
199 |
Partial oxidation of hydrocarbons over a staged catalystRekhelman, Michael Arik 12 1900 (has links)
No description available.
|
200 |
The effects of combustion CVD-applied alumina coatings on the high temperature oxidation of a Ni-Cr alloyHendrick, Michelle Renee 05 1900 (has links)
No description available.
|
Page generated in 0.0678 seconds