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001 on1081304382
003 OCoLC
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006 m o d
007 cr cnu|||unuuu
008 190109s2019 nju ob 001 0 eng d
040 _aN$T
_beng
_erda
_epn
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_dN$T
_dDG1
_dYDX
_dEBLCP
_dRECBK
_dOCLCF
_dMERER
_dOCLCQ
_dUKAHL
_dOCLCQ
019 _a1081353180
_a1082185645
_a1084620011
020 _a9781119579090
_q(electronic bk.)
020 _a1119579090
_q(electronic bk.)
020 _a9781119476962
_q(electronic bk.)
020 _a1119476968
_q(electronic bk.)
020 _z9781786302762
020 _z1786302764
029 1 _aAU@
_b000065068731
029 1 _aCHNEW
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029 1 _aCHVBK
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035 _a(OCoLC)1081304382
_z(OCoLC)1081353180
_z(OCoLC)1082185645
_z(OCoLC)1084620011
050 4 _aTJ260
072 7 _aTEC
_x009070
_2bisacsh
082 0 4 _a621.40223
_223
049 _aMAIN
100 1 _aBenallou, Abdelhanine.
_98039
245 1 0 _aEnergy Transfers by Convection /
_cAbdelhanine Benallou.
264 1 _aHoboken, NJ :
_bJohn Wiley and Sons, Inc. :
_bWiley-ISTE,
_c2019.
300 _a1 online resource
336 _atext
_btxt
_2rdacontent
337 _acomputer
_bc
_2rdamedia
338 _aonline resource
_bcr
_2rdacarrier
490 1 _aEnergy series. Energy engineering set ;
_vvolume 3
504 _aIncludes bibliographical references and index.
588 0 _aOnline resource; title from PDF file page (EBSCO, viewed January 11, 2019).
505 0 _aCover; 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
505 8 _a2.1. 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
505 8 _a2.4.5. 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
505 8 _a3.5. 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
505 8 _a4.5.1. 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
520 _aWhether in a solar thermal power plant or at the heart of a nuclear reactor, convection is an important mode of energy transfer. This mode is unique; it obeys specific rules and correlations that constitute one of the bases of equipment-sizing equations. In addition to standard aspects of convention, this book examines transfers at very high temperatures where, in order to ensure the efficient transfer of energy for industrial applications, it is becoming necessary to use particular heat carriers, such as molten salts, liquid metals or nanofluids. With modern technologies, these situations are becoming more frequent, requiring appropriate consideration in design calculations. Energy Transfers by Convection also studies the sizing of electronic heat sinks used to ensure the dissipation of heat and thus the optimal operation of circuit boards used in telecommunications, audio equipment, avionics and computers.
650 0 _aHeat
_xConduction.
_95143
650 0 _aHeat
_xTransmission.
_94039
650 0 _aHeat engineering.
_95144
650 0 _aRenewable energy sources.
_94906
650 7 _aTECHNOLOGY & ENGINEERING
_xMechanical.
_2bisacsh
_98040
650 7 _aHeat
_xConduction.
_2fast
_0(OCoLC)fst00953780
_95143
650 7 _aHeat engineering.
_2fast
_0(OCoLC)fst00953853
_95144
650 7 _aHeat
_xTransmission.
_2fast
_0(OCoLC)fst00953826
_94039
650 7 _aRenewable energy sources.
_2fast
_0(OCoLC)fst01094570
_94906
655 4 _aElectronic books.
_93294
776 0 8 _iPrint version:
_aBenallou, Abdelhanine.
_tEnergy Transfers by Convection.
_dHoboken, NJ : John Wiley and Sons, Inc. : Wiley-ISTE, 2019
_z1786302764
_z9781786302762
_w(OCoLC)1076549954
830 0 _aEnergy series (ISTE Ltd.).
_pEnergy engineering set ;
_vv. 3.
_98041
856 4 0 _uhttps://doi.org/10.1002/9781119476962
_zWiley Online Library
942 _cEBK
994 _a92
_bDG1
999 _c69005
_d69005