Spelling suggestions: "subject:"[een] MASS TRANSFER"" "subject:"[enn] MASS TRANSFER""
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Heat and mass transfer in semi-porous channelsMassey, William Moore 08 1900 (has links)
No description available.
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Sublimation dehydration in the continuum, transition, and free-molecule flow regimesHill, James Edward 12 1900 (has links)
No description available.
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Heat and mass transfer mechanisms in freeze-dryingHardin, Thurman Craig 05 1900 (has links)
No description available.
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Heat and mass transfer in a semi-porous textile compositeFrancis, Nicholas Donald 05 1900 (has links)
No description available.
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Transport phenomena in sublimation dehydrationDyer, David Fairfield 12 1900 (has links)
No description available.
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Combined heat and mass transfer in gas-liquid two-phase systemsEghbali, Davoud A. 12 1900 (has links)
No description available.
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Model-based design optimization of heterogeneous micro-reactors and chemical sensorsPhillips, Cynthia Michelle 08 1900 (has links)
No description available.
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Simultaneous heat, momentum and mass transfer in the through-flow drying of agricultural productsBrock, James Donald 05 1900 (has links)
No description available.
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Influence of vapor mass flux on simultaneous heat and mass transfer in moist porous mediaBoo, Joonhong 12 1900 (has links)
No description available.
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Coupled heat and mass transfer during condensation of high-temperature-glide zeotropic mixtures in small diameter channelsFronk, Brian Matthew 27 August 2014 (has links)
Zeotropic mixtures exhibit a temperature glide between the dew and bubble points during condensation. This glide has the potential to increase system efficiency when matched to the thermal sink in power generation, chemical processing, and heating and cooling systems. To understand the coupled heat and mass transfer mechanisms during phase change of high-glide zeotropic mixtures, a comprehensive investigation of the condensation of ammonia and ammonia/water mixtures in small diameter channels was performed. Condensation heat transfer and pressure drop experiments were conducted with ammonia and ammonia/water mixtures. Experiments on ammonia were conducted for varying tube diameters (0.98 < D < 2.16 mm), mass fluxes (75 < G < 225 kg m⁻² s⁻¹) and saturation conditions (30 < Tsat < 60°C). Zeotropic ammonia/water experiments were conducted for multiple tube diameters (0.98 < D < 2.16 mm), mass fluxes (50 < G < 200 kgm⁻² s⁻¹) and bulk ammonia mass fraction (xbulk = 0.8, 0.9, and > 0.96). An experimental methodology and data analysis procedure for evaluating the local condensation heat duty (for incremental ∆q), condensation transfer coefficient (for pure ammonia), apparent heat transfer coefficient (for zeotropic ammonia/water mixtures), and frictional pressure gradient with low uncertainties was developed. A new heat transfer model for condensation of ammonia in mini/microchannels was developed. Using the insights derived from the pure ammonia work, an improved zeotropic condenser design method for high-temperature-glide mixtures in small diameter channels, based on the non-equilibrium film theory, was introduced. The key features of the improved model were the consideration of annular and non-annular flow effects on liquid film transport, including condensate and vapor sensible cooling contributions, and accounting for mini/microchannel effects through the new liquid film correlation. By understanding the behavior of these mixtures in microchannel geometries, highly efficient, compact thermal conversion devices can be developed.
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