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Titlebook: Direct-Contact Heat Transfer; Frank Kreith,R. F. Boehm Conference proceedings 1988 Springer-Verlag Berlin Heidelberg 1988 development.ener

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41#
發(fā)表于 2025-3-28 18:23:41 | 只看該作者
42#
發(fā)表于 2025-3-28 21:42:26 | 只看該作者
https://doi.org/10.1007/978-3-540-71095-0 phenomenon was the principal application of this direct-contact process for many years and may remain so today. The thrust of the current workshop has been the examination of fundamental heat transfer phenomena, however, so the situation with chemically reacting species will not be considered here
43#
發(fā)表于 2025-3-29 00:15:23 | 只看該作者
Springer Lexikon Kosmetik und K?rperpflegecient speed to break through the interfacial surface tension; i. e., they possess kinetic energy exceeding the work function of cohesion at the surface. Since only a small portion of the molecules is at any instant located near enough to the surface and moving in the proper direction to escape, the
44#
發(fā)表于 2025-3-29 04:47:03 | 只看該作者
Springer Lexikon Kosmetik und K?rperpflege and “bubble type” and classifies typical equipment that falls under the classifications. Next, it reviews the current state of our ability to analyze the processes and points out the uncertainties related to our knowledge of the basic mechanisms. In doing so, it points out the needed additional res
45#
發(fā)表于 2025-3-29 11:11:44 | 只看該作者
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發(fā)表于 2025-3-29 12:00:33 | 只看該作者
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發(fā)表于 2025-3-29 17:54:51 | 只看該作者
48#
發(fā)表于 2025-3-29 22:56:11 | 只看該作者
Mass Transfer Effects in Heat Transfer Processes,nd gas adsorption are examples. Gas-liquid, liquid-liquid, or fluid-solid systems are passed through devices such as packed towers, plate towers, fixed or fluidized beds, spray, and bubble towers designed to promote physical contact of the phases.
49#
發(fā)表于 2025-3-30 00:45:01 | 只看該作者
50#
發(fā)表于 2025-3-30 06:29:39 | 只看該作者
Solids Motion and Heat Transfer in Gas Fluidized Beds, fluid-like in a number of respects and is said to be fluidized. Because of the very large surface area, heat and mass exchange between the fluid and the solids are extremely efficient. In the case of typical gas fluidized beds, the solids also possess large mean and fluctuating velocities, thus pro
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