By Manfred Nitsche, Raji Olayiwola Gbadamosi
Heat Exchanger layout advisor: a realistic advisor for making plans, deciding upon and Designing of Shell and Tube Exchangers takes clients on a step by step advisor to the layout of warmth exchangers in day-by-day perform, exhibiting the best way to be sure the potent using temperature distinction for warmth move.
Users will methods to calculate warmth move coefficients for convective warmth move, condensing, and evaporating utilizing basic equations. Dew and bubble issues and contours are coated, with all calculations supported with examples.
This functional advisor is designed to aid engineers clear up standard difficulties they could come upon of their day by day paintings, and also will function an invaluable reference for college kids studying concerning the box. The ebook is broadly illustrated with figures in help of the textual content and contains calculation examples to make sure clients are absolutely built to choose, layout, and function warmth exchangers.
- Covers layout approach and useful correlations had to layout functional warmth exchangers for procedure application
- Includes geometrical calculations for the tube and shell facet, additionally overlaying boiling and condensation warmth transfer
- Explores warmth move coefficients and temperature differences
- Designed to aid engineers clear up general difficulties they could come upon of their daily paintings, but in addition perfect as an invaluable reference for college students studying concerning the field
Read or Download Heat Exchanger Design Guide: A Practical Guide for Planning, Selecting and Designing of Shell and Tube Exchangers PDF
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Additional resources for Heat Exchanger Design Guide: A Practical Guide for Planning, Selecting and Designing of Shell and Tube Exchangers
With increasing Reynolds number the laminar thickness of the boundary layer on the tube wall decreases and the quotient a z l/s becomes higher. 6 A sufﬁciently high ﬂow velocity is the required condition for a good heat transfer coefﬁcient. 5e2 m/s for liquids and 10e25 m/s for gases. With viscous media the shell-side heat transfer coefﬁcients are higher than the a-values on the tube side. This is why viscous products are preferably located at the shell side. 2 Calculation equations for the convective heat transfer.
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. S. Pressburg, Heat transfer to moving ﬂuids, Chem. Eng. Dez. 66 (1959) 67e72. P. Chopey, Heat transfer, in: Handbook of Chemical Engineering Calculations, McGraw-Hill, New York, 1993. Q. Y, 1950.  L. L. Y, 1962.
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. S. Pressburg, Heat transfer to moving ﬂuids, Chem. Eng. Dez. 66 (1959) 67e72. P. Chopey, Heat transfer, in: Handbook of Chemical Engineering Calculations, McGraw-Hill, New York, 1993. Q. Y, 1950.  L. L. Y, 1962. 00004-3 © 2016 Elsevier Inc.