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Transfer equipment

Even if the reactor temperature is controlled within acceptable limits, the reactor effluent may need to be cooled rapidly, or quenched, to stop the reaction quickly to prevent excessive byproduct formation. This quench can be accomplished by indirect heat transfer using conventional heat transfer equipment or by direct heat transfer by mixing with another fluid. A commonly encountered situation is... [Pg.42]

Use heat transfer equipment which requires a low inventory, such as plate heat exchangers. [Pg.271]

Fig. 17. Effect of axial dispersion in both phases on solute distribution through countercurrent mass transfer equipment. A, piston or plug flow B, axial... Fig. 17. Effect of axial dispersion in both phases on solute distribution through countercurrent mass transfer equipment. A, piston or plug flow B, axial...
George W. Gassman, Paul J. Schajhuch, Thomas J. McAvoy, Dale E. Seborg Process Economics F. A. Holland, J. K Wilkinson Transport and Storage of Fluids Meherwan P. Boyce Heat-Transfer Equipment Richard L. Shilling, Kenneth J. Bell,... [Pg.7]

Kenneth J. Bell, Ph.D., P.E., Regents Professor Emeritus, School of Chemical Engineering, Oklalioma State University Member, American Institute of Chemical Engineers (Section 11, Heat-Transfer Equipment)... [Pg.9]

Overall Coefficient of Heat Transfer In testing commercial heat-transfer equipment, it is not convenient to measure tube temperatures (t,3 or t4 in Fig. 5-6), and hence the overall performance is expressed as an overall coefficient of heat transfer U based on a convenient area dA, which may be dAi, oi an average of dAi and dA whence, by definition,... [Pg.558]

According to this analysis one can see that for gas-absorption problems, which often exhibit unidirectional diffusion, the most appropriate driving-force expression is of the form y — y tyBM,. ud the most appropriate mass-transfer coefficient is therefore kc- This concept is to he found in all the key equations for the design of mass-transfer equipment. [Pg.604]

Because heat-transfer equipment for solids is generally an adaptation of a primarily material-handhng device, the area of heat transfer is often small in relation to the overall size of the equipment. Also pecuhar to sohds heat transfer is that the At varies for the different heat-transfer mechanisms. With a knowledge of these mechanisms, the At term generally is readily estimated from temperature hmita-tions imposed by the burden characteristics and/or the construc tion. [Pg.1054]

Conauctive Heat Transfer Heat-transfer equipment in which heat is transferred by conduction is so constructed that the solids load (burden) is separated from the heating medium by a wall. [Pg.1054]


See other pages where Transfer equipment is mentioned: [Pg.67]    [Pg.68]    [Pg.168]    [Pg.368]    [Pg.189]    [Pg.12]    [Pg.17]    [Pg.19]    [Pg.560]    [Pg.1031]    [Pg.1032]    [Pg.1032]    [Pg.1033]    [Pg.1033]    [Pg.1033]    [Pg.1034]    [Pg.1034]    [Pg.1034]    [Pg.1035]    [Pg.1037]    [Pg.1038]    [Pg.1039]    [Pg.1040]    [Pg.1041]    [Pg.1042]    [Pg.1043]    [Pg.1044]    [Pg.1045]    [Pg.1046]    [Pg.1047]    [Pg.1048]    [Pg.1049]    [Pg.1050]    [Pg.1051]    [Pg.1052]    [Pg.1053]    [Pg.1054]   
See also in sourсe #XX -- [ Pg.400 ]




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