By Manfred Nitsche, Raji Olayiwola Gbadamosi
Heat Exchanger layout consultant: a realistic consultant for making plans, identifying and Designing of Shell and Tube Exchangers takes clients on a step by step consultant to the layout of warmth exchangers in day-by-day perform, exhibiting the way to confirm the potent using temperature distinction for warmth move.
Users will how one can calculate warmth move coefficients for convective warmth move, condensing, and evaporating utilizing basic equations. Dew and bubble issues and contours are lined, with all calculations supported with examples.
This useful consultant is designed to assist engineers remedy general difficulties they could come upon of their daily paintings, and also will function an invaluable reference for college students studying concerning the box. The ebook is commonly illustrated with figures in aid of the textual content and contains calculation examples to make sure clients are absolutely built to choose, layout, and function warmth exchangers.
- Covers layout strategy and sensible correlations had to layout sensible warmth exchangers for procedure application
- Includes geometrical calculations for the tube and shell facet, additionally masking boiling and condensation warmth transfer
- Explores warmth move coefficients and temperature differences
- Designed to assist engineers remedy commonplace difficulties they could stumble upon of their day by day paintings, but in addition excellent as an invaluable reference for college students studying concerning the field
Read Online or Download Heat Exchanger Design Guide: A Practical Guide for Planning, Selecting and Designing of Shell and Tube Exchangers PDF
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Extra resources for Heat Exchanger Design Guide: A Practical Guide for Planning, Selecting and Designing of Shell and Tube Exchangers
With condensers vertical bafﬂe, cuts with vertical chord are advantageous in order to avoid condensate built-up and allow the noncondensable gases to escape and ﬂow out upward. If the pressure loss on the shell side is to be reduced disc and doughnutdor double segmental bafﬂes are used. The full circle bafﬂes have the advantage that there is no bypass streams through the diametrical gap between the tube bundle and the shell; however, the mainly horizontal streams deteriorate the heat transfer coefﬁcient.
J. J. Picozzi, Specifying and selecting, Chem. Eng. (Octomber 1980). N. E. Tate, Ind. Eng. Chem. 28 (1936) 1429. A. Donohue, Heat transfer and pressure drop in heat exchangers, Ind. Eng. Chem. 41 (1949) 2499. Ref. 34 (1955), No. 10 und No. 11. T. Tinker, Shell-side characteristics of shell and tube heat exchangers, Trans. ASME 80 (1958) 36 (f f ). J. Bell, Thermal design of heat transfer equipment, in: Perry’s Handbook, 1973. VDI-W€armeatlas, Aufkage, 5, VDI-Verlag, D€ usseldorf, 1988. Lord, Minton, Slusser, Design of heat exchangers, Chem.
A. Donohue, Heat transfer and pressure drop in heat exchangers, Ind. Eng. Chem. 41 (1949) 2499. Ref. 34 (1955), No. 10 und No. 11. T. Tinker, Shell-side characteristics of shell and tube heat exchangers, Trans. ASME 80 (1958) 36 (f f ). J. Bell, Thermal design of heat transfer equipment, in: Perry’s Handbook, 1973. VDI-W€armeatlas, Aufkage, 5, VDI-Verlag, D€ usseldorf, 1988. Lord, Minton, Slusser, Design of heat exchangers, Chem. Eng, 26 ( January 1970). M. Jakob, Trans. ASME 60 (1938), 381/392.