منو
رکورد قبلیرکورد بعدی

" Energy Transfers by Convection / "


Document Type : BL
Record Number : 840635
Main Entry : Benallou, Abdelhanine.
Title & Author : Energy Transfers by Convection /\ Abdelhanine Benallou.
Publication Statement : Hoboken, NJ :: John Wiley and Sons, Inc. :: Wiley-ISTE,, 2019.
Series Statement : Energy series. Energy engineering set ;; volume 3
Page. NO : 1 online resource
ISBN : 1119476968
: : 1119579090
: : 9781119476962
: : 9781119579090
: 1786302764
: 9781786302762
Bibliographies/Indexes : Includes bibliographical references and index.
Contents : Cover; Half-Title Page; Title Page; Copyright Page; Contents; Preface; Introduction; 1. Methods for Determining Convection Heat Transfer Coefficients; 1.1. Introduction; 1.2. Characterizing the motion of a fluid; 1.3. Transfer coefficients and flow regimes; 1.4. Using dimensional analysis; 1.4.1. Dimensionless numbers used in convection; 1.4.2. Dimensional analysis applications in convection; 1.5. Using correlations to calculate h; 1.5.1. Correlations for flows in forced convection; 1.5.2. Correlations for flows in natural convection; 2. Forced Convection inside Cylindrical Pipes
: 2.1. Introduction2.2. Correlations in laminar flow; 2.2.1. Reminders regarding laminar-flow characteristics inside a pipe; 2.2.2. Differential energy balance; 2.2.3. Illustration: transportation of phosphate slurry in a cylindrical pipe; 2.2.4. Correlations for laminar flow at pipe entrance; 2.3. Correlations in transition zone; 2.4. Correlations in turbulent flow; 2.4.1. Dittus-Boelter-McAdams relation; 2.4.2. Colburn-Seider-Tate relation; 2.4.3. Illustration: improving transfer by switching to turbulent flow; 2.4.4. Specific correlations in turbulent flow
: 2.4.5. Illustration: industrial-grade cylindrical pipe2.5. Dimensional correlations for air and water; 3. Forced Convection inside Non-cylindrical Pipes; 3.1. Introduction; 3.2. Concept of hydraulic diameter; 3.3. Hydraulic Nusselt and Reynolds numbers; 3.4. Correlations in established laminar flow; 3.4.1. Pipes with rectangular or square cross-sections in laminar flow; 3.4.2. Pipes presenting an elliptical cross-section in laminar flow; 3.4.3. Pipes presenting a triangular cross-section in laminar flow; 3.4.4. Illustration: air-conditioning duct design; 3.4.5. Annular pipes with laminar flow
: 3.5. Correlations in turbulent flow for non-cylindrical pipes3.5.1. Pipes with rectangular or square cross-sections in turbulent flow; 3.5.2. Pipes with elliptical or triangular cross-sections in turbulent flow; 3.5.3. Illustration: design imposes the flow regime; 3.5.4. Annular pipes in turbulent flow; 4. Forced Convection outside Pipes or around Objects; 4.1. Introduction; 4.2. Flow outside a cylindrical pipe; 4.3. Correlations for the stagnation region; 4.4. Correlations beyond the stagnation zone; 4.5. Forced convection outside non-cylindrical pipes
: 4.5.1. Pipes with a square cross-section area4.5.2. Pipes presenting an elliptical cross-section area; 4.5.3. Pipes presenting a hexagonal cross-section area; 4.6. Forced convection above a horizontal plate; 4.6.1. Plate at constant temperature; 4.6.2. Plate with constant flow density; 4.7. Forced convection around non-cylindrical objects; 4.7.1. Forced convection around a plane parallel to the flow; 4.7.2. Forced convection around a sphere; 4.8. Convective transfers between falling films and pipes; 4.8.1. Vertical tubes; 4.8.2. Horizontal tubes; 4.9. Forced convection in coiled pipes
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