Results 241 to 250 of about 822,015 (305)
Selective Production of Glycolic Acid and Dihydroxyacetone From Glycerol Under Non-Thermal Plasma in Liquid Phase. [PDF]
ChemSusChemParedes-Quevedo LC +2 more
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Effect of Carbon Dioxide's Injection Concentration on the Diffusion Coefficient of Methane. [PDF]
ACS OmegaHao J, Wang S, Wen H, Liu Z, Ren L.
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Effect of Gas/Liquid Mass Ratio on the Penetration of Aerated Liquid Jet in Supersonic Cross Flow
44th AIAA Aerospace Sciences Meeting and Exhibit, 2006The success of supersonic air-breathing propulsion systems will be largely dependent on efficient injection, mixing, and combustion inside the supersonic combustion chamber. Fuel/air mixing enhancement inside the combustion chamber will depend on the strategies used to control the fuel jet penetration and droplet's size, velocity and dispersion ...
Chaouki Ghenai +2 more
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Chemical Engineering and Processing: Process Intensification, 2014
Abstract This work analyzes flow regimes and mass transfer in a miniaturized packed bed reactor under reacting conditions. The reactor consisted of a cylindrical channel with an inner diameter of 2 mm which was filled with spherical catalyst particles having an outer diameter of 0.8 mm.
Robert Langsch +3 more
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Abstract This work analyzes flow regimes and mass transfer in a miniaturized packed bed reactor under reacting conditions. The reactor consisted of a cylindrical channel with an inner diameter of 2 mm which was filled with spherical catalyst particles having an outer diameter of 0.8 mm.
Robert Langsch +3 more
openaire +2 more sources
Chemical Engineering Science, 2007
Abstract The mass transfer performance of a gas–liquid self-ingesting stirred reactor is reported both for coalescing and non-coalescing systems. The vessel features are a high aspect ratio and a rather narrow multiple-impeller draft tube, through which the gas phase is ingested and led down to the vessel bottom, where it is finely dispersed into the
F. Scargiali +3 more
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Abstract The mass transfer performance of a gas–liquid self-ingesting stirred reactor is reported both for coalescing and non-coalescing systems. The vessel features are a high aspect ratio and a rather narrow multiple-impeller draft tube, through which the gas phase is ingested and led down to the vessel bottom, where it is finely dispersed into the
F. Scargiali +3 more
openaire +2 more sources