LEADER 05358nam 2200673Ia 450 001 9910458110003321 005 20200520144314.0 010 $a1-281-02506-2 010 $a9786611025069 010 $a0-08-054441-X 035 $a(CKB)1000000000364034 035 $a(EBL)296619 035 $a(OCoLC)469606488 035 $a(SSID)ssj0000228157 035 $a(PQKBManifestationID)11216599 035 $a(PQKBTitleCode)TC0000228157 035 $a(PQKBWorkID)10149536 035 $a(PQKB)10178511 035 $a(MiAaPQ)EBC296619 035 $a(Au-PeEL)EBL296619 035 $a(CaPaEBR)ebr10178565 035 $a(CaONFJC)MIL102506 035 $a(EXLCZ)991000000000364034 100 $a20070104d2007 uy 0 101 0 $aeng 135 $aur|n|---||||| 181 $ctxt 182 $cc 183 $acr 200 10$aProcess heat transfer$b[electronic resource] $eprinciples and applications /$fR.W. Serth 210 $aAmsterdam ;$aLondon $cElsevier Academic Press$dc2007 215 $a1 online resource (770 p.) 300 $aIncludes index. 311 $a0-12-373588-2 327 $aFront Cover; Process Heat Transfer Principles and Applications; Copyright Page; Contents; Preface; Conversion Factors; Physical Constants; Acknowledgements; Chapter 1: Heat Conduction; 1.1 Introduction; 1.2 Fourier's Law of Heat Conduction; 1.3 The Heat Conduction Equation; 1.4 Thermal Resistance; 1.5 The Conduction Shape Factor; 1.6 Unsteady-State Conduction; 1.7 Mechanisms of Heat Conduction; Chapter 2: Convective Heat Transfer; 2.1 Introduction; 2.2 Combined Conduction and Convection; 2.3 Extended Surfaces; 2.4 Forced Convection in Pipes and Ducts; 2.5 Forced Convection in External Flow 327 $a2.6 Free ConvectionChapter 3: Heat Exchangers; 3.1 Introduction; 3.2 Double-Pipe Equipment; 3.3 Shell-and-Tube Equipment; 3.4 The Overall Heat-Transfer Coefficient; 3.5 The LMTD Correction Factor; 3.6 Analysis of Double-Pipe Exchangers; 3.7 Preliminary Design of Shell-and-Tube Exchangers; 3.8 Rating a Shell-and-Tube Exchanger; 3.9 Heat-Exchanger Effectiveness; Chapter 4: Design of Double-Pipe Heat Exchangers; 4.1 Introduction; 4.2 Heat-Transfer Coefficients for Exchangers without Fins; 4.3 Hydraulic Calculations for Exchangers without Fins; 4.4 Series/Parallel Configurations of Hairpins 327 $a4.5 Multi-tube Exchangers4.6 Over-Surface and Over-Design; 4.7 Finned-Pipe Exchangers; 4.8 Heat-Transfer Coefficients and Friction Factors for Finned Annuli; 4.9 Wall Temperature for Finned Pipes; 4.10 Computer Software; Chapter 5: Design of Shell-and-Tube Heat Exchangers; 5.1 Introduction; 5.2 Heat-Transfer Coefficients; 5.3 Hydraulic Calculations; 5.4 Finned Tubing; 5.5 Tube-Count Tables; 5.6 Factors Affecting Pressure Drop; 5.7 Design Guidelines; 5.8 Design Strategy; 5.9 Computer Software; Chapter 6: The Delaware Method; 6.1 Introduction; 6.2 Ideal Tube Bank Correlations 327 $a6.3 Shell-Side Heat-Transfer Coefficient6.4 Shell-Side Pressure Drop; 6.5 The Flow Areas; 6.6 Correlations for the Correction Factors; 6.7 Estimation of Clearances; Chapter 7: The Stream Analysis Method; 7.1 Introduction; 7.2 The Equivalent Hydraulic Network; 7.3 The Hydraulic Equations; 7.4 Shell-Side Pressure Drop; 7.5 Shell-Side Heat-Transfer Coefficient; 7.6 Temperature Profile Distortion; 7.7 The Wills-Johnston Method; 7.8 Computer Software; Chapter 8: Heat-Exchanger Networks; 8.1 Introduction; 8.2 An Example: TC3; 8.3 Design Targets; 8.4 The Problem Table; 8.5 Composite Curves 327 $a8.6 The Grand Composite Curve8.7 Significance of the Pinch; 8.8 Threshold Problems and Utility Pinches; 8.9 Feasibility Criteria at the Pinch; 8.10 Design Strategy; 8.11 Minimum-Utility Design for TC3; 8.12 Network Simplification; 8.13 Number of Shells; 8.14 Targeting for Number of Shells; 8.15 Area Targets; 8.16 The Driving Force Plot; 8.17 Super Targeting; 8.18 Targeting by Linear Programming; 8.19 Computer Software; Chapter 9: Boiling Heat Transfer; 9.1 Introduction; 9.2 Pool Boiling; 9.3 Correlations for Nucleate Boiling on Horizontal Tubes; 9.4 Two-Phase Flow 327 $a9.5 Convective Boiling in Tubes 330 $aThe First Law of Thermodynamics states that energy can neither be created nor destroyed. Heat exchangers are devices built for efficient heat transfer from one fluid to another. They are widely used in engineering processes and include examples such as intercoolers, preheaters, boilers and condensers in power plants. Heat exchangers are becoming more and more important to manufacturers striving to control energy costs.Process Heat Transfer Rules of Thumb investigates the design and implementation of industrial heat exchangers. It provides the background needed to unde 606 $aHeat$xTransmission 606 $aHeat exchangers 606 $aHeat exchangers$xDesign 606 $aHeat$xTransmission$xComputer programs 608 $aElectronic books. 615 0$aHeat$xTransmission. 615 0$aHeat exchangers. 615 0$aHeat exchangers$xDesign. 615 0$aHeat$xTransmission$xComputer programs. 676 $a621.4022 700 $aSerth$b R. W$0503603 801 0$bMiAaPQ 801 1$bMiAaPQ 801 2$bMiAaPQ 906 $aBOOK 912 $a9910458110003321 996 $aProcess heat transfer$9716682 997 $aUNINA LEADER 01500cam a2200325 i 4500 001 991003558039707536 005 20020503200014.0 008 930923s1991 caua 001 0 eng 020 $a012182103X (v.202) 020 $a0121821048 (v.203) 035 $ab1052339x-39ule_inst 035 $aEXGIL122957$9ExL 040 $aBiblioteca Interfacoltà$bita 245 00$aMolecular design and modeling :$bconcepts and applications 260 $aSan Diego [etc.] :$bAcademic press,$cc1991 300 $a2 v. :$bill. ;$c24 cm 490 0 $aMethods in enzymology ;$v202 490 0 $aMethods in enzymology ;$v203 504 $aInclude referenze bibliografiche ed indici 505 00$gPt.A:$tProteins, peptides, and enzyme /$redited by John J.Langone. - 1991. - xxxi, 824 p. 505 00$gPt.B:$tAntibodies and antigens, nucleic acids, polysaccarides, and drugs /$redited by John J. Langone. - 1991. - xxxi, 764 p. 650 4$aMolecola 700 1 $aLangone, John Joseph 907 $a.b1052339x$b21-02-17$c27-06-02 912 $a991003558039707536 945 $aLE002 Coll. 21.202 [dislocato c/o Biblioteca DiSTeBA]$cPt. A$g1$i2002000003171$lle003$o-$pE0.00$q-$rl$s- $t0$u0$v0$w0$x0$y.i10602021$z27-06-02 945 $aLE002 Coll. 21.203 [dislocato c/o Biblioteca DiSTeBA]$cPt. B$g1$i2002000003188$lle003$o-$pE0.00$q-$rl$s- $t0$u0$v0$w0$x0$y.i10602033$z27-06-02 996 $aMolecular design and modeling$9216874 997 $aUNISALENTO 998 $ale003$b01-01-93$cm$da $e-$feng$gcau$h0$i2