By Paul E. Minton
This glorious quantity combines loads of information in simple terms formerly to be had from many alternative resources right into a unmarried, informative quantity. It offers evaporation know-how because it exists at the present time. even if evaporation is likely one of the oldest unit operations, it's also a space with dramatic adjustments within the final region century. even if different tools of separation can be found, evaporation continues to be the simplest technique for plenty of purposes. All elements has to be evaluated so one can decide upon the simplest evaporator sort. This booklet should be super helpful in comparing and identifying which evaporation know-how will meet a selected set of necessities.
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Extra info for Handbook of Evaporation Technology
Sample text
The following equation has been widely used to predict nucleate boiling heat transfer. The equation includes a term to treat variation of coefficient with pressure. A special Reynolds number is also defined. 48) G = (W,lA)bil&) (Note that A is the surface area, not a cross-sectional a numerical correlating factor, varies with the nature struction) of the surface. ) $I, which is (material of con- for commercial copper and steel surfaces for stainless steel or chromium and nickel alloys for polished surfaces 34 Handbook of Evaporation Technology Surface conditions have a profound effect on boiling phenomena.
51. At the upper limit, nucleation is diminished because of the insulating effects of a vapor film. At the lower limit, nucleation is inhibited because of natural convection effects. For horizontal tubes, the criterion for determining the upper limit is the maximum allowable value of vapor velocity. Vapor bubbles can escape at a velocity determined by the pressure of the system. When vapor is generated faster than it can escape, all or a portion of the tube or tube bundle will become blanketed by a film of vapor.
Heat For laminar flow, Di = inside tube diameter DC = diameter the ratio of length Reynolds number required Re, where Sensible the heat-transfer phenomena largely tubes. The in flow in flow over is more tube gradual transition banks than from for in the minimum at a Reynolds flow those exterior of heat Experiments from laminar whereas for of about 100, 3,000. that, flow tube flow. 8) in-line where case based banks. 7) The heat transfer analytically. 6) flow of the flow. to be treated staggered be calculated 12(Di/DJ”*] number on the flow is too complex over + of the velocity equations should Tubes to the nature depends cients the related are functions the flow Reynolds 13 (De/Di)1’6 turbulent = 2100[1 Outside The in turn for Heat Transfer are closely bundles = critical Ret = in Evaporators or coil to diameter (L/Di)1’3 The of helix Transfer as below: rate and ac is given below.
Handbook of Evaporation Technology by Paul E. Minton
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