Big Chemical Encyclopedia

Chemical substances, components, reactions, process design ...

Articles Figures Tables About
0 | 1 | 2 | 3 | 4 | 5 | 6 | 7 | 8 | 9 | a | b | c | d | e | f | g | h | i | j | k | l | m | n | o | p | q | r | s | t | u | v | w | x | y | z

   |<      <<      >>     > |    


O2 conversion data versus temperature for the oxidation of CH4 for three microreactor channels. Open-loop temperature control was used in this experiment with each heater set to the same heater voltage. The temperature used for the plot is the average of the measured RTD temperatures. These results come from one AIMS experiment with three

O2 dissociation in atmospheric-pressure thermal plasma. Composition of products

O2 dissociation in atmospheric-pressure thermal plasma. Energy cost of the dissociation as a function of specific energy input in the case of absolute quenching.

O2 evolution in 3M KOH, 75 C on various catalysts. Catalyst loadings were

O2 evolves but saturating with time by the deposition of Ag on the surface under the irradiation. This result suggests that the photocatalyst prepared in this work has ability for proceeding to the photocatalytic reaction under the visible light irradiation. The amount of evolved O2 for 1 hour in the initial stage is defined as the photocatalytic activity of the corresponding

O2 insertion into a tungsten cyclopentadienyl

O2 Microelectrode for Environmental Measurements, p. 370 Chapter 18

O2 N2 selectivity of the NR SBR blend membrane obtained by using different crosslinking systems.

O2 oxidation of thioethers exhibiting an induction period when using the Au 2 NOj catalyst. Conditions

O2 permeation flux within a 25 CH4 25 He thickness 81 pm. Lao.6Sro.4Coo.8Gao203 a

O2 permeation flux within a 40 porous LSC coating. Conditions

O2 product recovery .

O2 product throughput .

O2 profiles generated in a membrane reactor for the partial oxidation of alkanes, a chemical valve MR. Bottom, Evolution of permeance of the chemical valve membrane as a function of the ratio C3H8 O2 without any catalyst.

O2 reduction kinetics at a dispersed Pt Catalyst in a PEFC cathode operating at 80 C 100 RH . Pt utilization , that is, Pt catalyst surface accessed by protons and electrons was

O2 reduction on adsorbed layers of various transition metal tetrasulfonated phthalocyanines on the basal plane of stress-annealed pyrolytic graphite in O.lAfNaOH. Macrocyclic preadsorbed from aqueous 10 M MeTSPc solution. Rotating disk electrode. Rotation rate

O2 reduction on adsorbed transition metal tetrasulfonated phthalocyanine in O.O5MH2SO4. Conditions similar to those for

O2 reduction on rotating Au and Pb Au electrodes in 1 M NaOH containing 1 mM HPb02. Ring potential 0.3 V, ring area 0.049 cm sweep rate 50 mV s. Upper panel

O2 reduction on several substrates in 1 M NaOH. Tl concentrations

O2 requirement and minimum heat rejected for CH4, O2 -

O2 RIE of poly and its brominated derivatives. Etching was carried out in a Cooke Vacuum C71-3 apparatus at the following conditions

O2 sensing is preserved in CGD mice lacking the gp91 phox subunit of NADPH oxidase,

O2 sensitivity of H146 cells, Correlation between membrane potential and K current magnitude at each grade of hypoxia.

O2 solubility as a function of temperature in different electrolyte solutions. O2 pressure

O2 TPD profiles for LSFN and nanocomposite calcined at different temperatures



   |<      <<      >>     > |    

SEARCH



© 2024 chempedia.info