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By Adrian Bejan(auth.)
A re-creation of the bestseller on convection warmth transfer
A revised variation of the vintage, Convection warmth move, Fourth variation, chronicles how the sphere of warmth move has grown and prospered over the past twenty years. This re-creation is extra obtainable, whereas now not sacrificing its thorough remedy of the main up to date info on present study and functions within the box.
One of the key leaders within the box, Adrian Bejan has pioneered and taught some of the equipment and practices common within the this present day. He keeps this book's long-standing function as an inspiring, optimum examine instrument by way of delivering:
- Coverage of the way convection impacts functionality, and the way convective flows may be configured in order that functionality is enhanced
- How convective configurations were evolving, from the flat plates, gentle pipes, and single-dimension fins of the sooner versions to new populations of configurations: tapered ducts, plates with multiscale positive aspects, dendritic fins, duct and plate assemblies (packages) for warmth move density and compactness, etc.
- New, up-to-date, and more desirable examples and difficulties that replicate the author's learn and advances within the box because the final edition
- A suggestions manual
Complete with enormous quantities of informative and unique illustrations, Convection warmth move, Fourth version is the main accomplished and approachable textual content for college kids in faculties of mechanical engineering.Content:
Chapter 1 primary rules (pages 1–29):
Chapter 2 Laminar Boundary Layer circulate (pages 30–95):
Chapter three Laminar Duct stream (pages 96–167):
Chapter four exterior common Convection (pages 168–232):
Chapter five inner traditional Convection (pages 233–294):
Chapter 6 Transition to Turbulence (pages 295–319):
Chapter 7 Turbulent Boundary Layer circulation (pages 320–368):
Chapter eight Turbulent Duct circulate (pages 369–397):
Chapter nine loose Turbulent Flows (pages 398–427):
Chapter 10 Convection with swap of section (pages 428–488):
Chapter eleven Mass move (pages 489–536):
Chapter 12 Convection in Porous Media (pages 537–605):
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Extra resources for Convection Heat Transfer, Fourth Edition
Example text
Derive the mass conservation equation in cylindrical coordinates [eq. 1) to an elementary control volume of size r(r θ) z in Fig. 1b (assume that ρ = constant). 3. Derive the mass conservation statement for spherical coordinates [eq. 10)] by writing eq. 1) for the elementary control volume ( r)(r sin φ θ)(r φ) around point (r, θ, φ) in Fig. 1c (assume that ρ = constant). 4. Consider a flow in which ρ and µ may be regarded as constant. 18) follows from eq. 17) through proper use of the mass conservation principle.
Morega and A. Bejan, Heatline visualization of forced convection boundary layers, Int. J. Heat Mass Transfer, Vol. 36, 1993, pp. 3957–3966. 32. A. M. Morega and A. Bejan, Heatline visualization of forced convection in porous media, Int. J. Heat Fluid Flow, Vol. 15, 1994, pp. 42–47. 33. V. A. F. Costa, Double diffusive natural convection in a square enclosure with heat and mass diffusive walls, Int. J. Heat Mass Transfer, Vol. 40, 1997, pp. 4061–4071. 34. V. A. F. Costa, Double diffusive natural convection in enclosures with heat and mass diffusive walls, in G.
The hottest is the furnace, which is enclosed by a surface of area AH and high temperature TH . The thickness of the insulation mounted on AH is tH . This thickness is sufficiently small so that the volume of the insulation on AH is AH tH . 13 The rest of the hot components (pipes, feed water heaters, turbines) are not as hot as the furnace. They are inside an enclosure with area AL , temperature TL , insulation thickness tL , and insulation volume AL tL . The heat leaks qH and qL are by pure conduction and are driven by the temperature differences TH = TH − T0 and TL = TL − T0 , respectively.