725_11 - 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20...

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1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 [Fi r s [79 7 Lin e * 17 . 2 —— No r m * PgE [79 7 CHAPTER 11 Heat Exchangers ALLAN D. KRAUS University of Akron Akron, Ohio 11.1 Introduction 11.2 Governing relationships 11.2.1 Introduction 11.2.2 Exchanger surface area 11.2.3 Overall heat transfer coef±cient 11.2.4 Logarithmic mean temperature difference 11.3 Heat exchanger analysis methods 11.3.1 Logarithmic mean temperature difference correction factor method 11.3.2 e N tu method Speci±c e N tu relationships 11.3.3 P N tu ,c method 11.3.4 ψ P method 11.3.5 Heat transfer and pressure loss 11.3.6 Summary of working relationships 11.4 Shell-and-tube heat exchanger 11.4.1 Construction 11.4.2 Physical data Tube side Shell side 11.4.3 Heat transfer data Tube side Shell side 11.4.4 Pressure loss data Tube side Shell side 11.5 Compact heat exchangers 11.5.1 Introduction 11.5.2 Classi±cation of compact heat exchangers 11.5.3 Geometrical factors and physical data 11.5.4 Heat transfer and flow friction data Heat transfer data Flow friction data 11.6 Longitudinal ±nned double-pipe exchangers 11.6.1 Introduction 797
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798 HEAT EXCHANGERS 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 [798 Lin e 0.9 7 —— Nor m PgE n [798 11.6.2 Physical data for annuli Extruded Fns Welded U-Fns 11.6.3 Overall heat transfer coefFcient revisited 11.6.4 Heat transfer coefFcients in pipes and annuli 11.6.5 Pressure loss in pipes and annuli 11.6.6 Wall temperature and further remarks 11.6.7 Series–parallel arrangements 11.6.8 Multiple Fnned double-pipe exchangers 11.7 Transverse high-Fn exchangers 11.7.1 Introduction 11.7.2 Bond or contact resistance of high-Fn tubes 11.7.3 ±in efFciency approximation 11.7.4 Air-Fn coolers Physical data Heat transfer correlations 11.7.5 Pressure loss correlations for staggered tubes 11.7.6 Overall heat transfer coefFcient 11.8 Plate and frame heat exchanger 11.8.1 Introduction 11.8.2 Physical data 11.8.3 Heat transfer and pressure loss 11.9 Regenerators 11.9.1 Introduction 11.9.2 Heat capacity and related parameters Governing differential equations 11.9.3 e N tu method 11.9.4 Heat transfer and pressure loss Heat transfer coefFcients Pressure loss 11.10 ±ouling 11.10.1 ±ouling mechanisms 11.10.2 ±ouling factors Nomenclature References 11.1 INTRODUCTION A heat exchanger can be deFned as any device that transfers heat from one fluid to another or from or to a fluid and the environment. Whereas in direct contact heat exchangers, there is no intervening surface between fluids, in indirect contact heat exchangers, the customary deFnition pertains to a device that is employed in the trans- fer of heat between two fluids or between a surface and a fluid. Heat exchangers may be classiFed (Shah, 1981, or Mayinger, 1988) according to (1) transfer processes,
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GOVERNING RELATIONSHIPS 799 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 [79 9 Lin e 1.7 p —— No r m PgE [79 9 (2) number of fluids, (3) construction, (4) heat transfer mechanisms, (5) surface com- pactness, (6) flow arrangement, (7) number of fluid passes, and (8) type of surface.
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This note was uploaded on 12/03/2010 for the course ECON 089907 taught by Professor Mikey during the Spring '10 term at Nashville State Community College.

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725_11 - 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20...

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