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Handbook for Heat Exchangers and Tube Banks design - Donatello Annaratone
Vergriffenes Buch, derzeit bei uns nicht verfügbar.
(*)
Donatello Annaratone:
Handbook for Heat Exchangers and Tube Banks design - neues Buch

ISBN: 9783642133084

[ED: Buch], [PU: Springer-Verlag GmbH], Neuware - The recently published book by the author, Engineering Heat Transfer , already dealt with exact computation of heat exchangers and tube banks. In design c- putationthisisaccomplishedviacorrectivefactorsthelattermakesitpossibleto compute the actual mean temperature difference by starting from the logarithmic onerelativeto uidsinparallel oworcounter ow. As far as veri cation computation is concerned, corrective factors were int- ducedtocomputeacertaincharacteristicfactorcorrectly,asisfundamentalforthis typeofcomputation. Basedontheabove,theauthordecidedtoinvestigatefurther,re ne,andwiden thistopic:theoutcomeofthisworkhasresultedinthishandbook. Newtypesofexchangerswereexaminedthecalculationwasre nedtoproduce practicallyexactvaluesforthefactors. Thescopeoftheinvestigationwasincreased by widening the range of the starting factors. Furthermore, a greater number of valuestobeincludedinthetableswasconsidered. Finally,afewcharacteristicsof certainvaluesofthecorrectivefactorswerehighlighted. The rstsectionisanintroductionitsummarizesthefundamentalcriteriaofheat transferandproceedstoillustratethebehaviorof uidsinbothparallelandcounter ow. Italsoshowshowtocomputethemeanisobaricspeci cheatforsome uids itillustratesthesigni canceofdesigncomputationandveri cationcomputation. In addition,itillustrateshowtoproceedwithheatexchangersandtubebankstocarry outbothdesignandveri cationcomputationcorrectly. AppendixAthenincludes36tablesasareferencefordesigncomputation,The tablescontainthecorrectivefactorsrequiredtoobtaintheactualmeantemperature differencebystartingfromthemeanlogarithmictemperaturedifferencerelativeto uidsinparallel oworcounter ow. Finally, Appendix B includes 35 tables for veri cation computation. As far as heatexchangers areconcerned, itshowsthevaluesoffactor whichisrequired forthistypeofcomputation. Thevaluesofthecorrectivefactorsforcoilsandtube banksarealsopresented. Milano,Italy DonatelloAnnaratone v Notation c=speci cheat(J/kgK) d=diameter(m) E=ef ciencyfactor h=enthalpy(kJ/kg) k=thermalconductivity(W/mK) M=mass owrate(kg/s) m=massmoisturepercentage(%) q=heatpertimeunit(W) 2 S=surface(m ) t=temperature( C) 2 U=overallheattransfercoef cient(W/m K) x=thickness(m) 2 =heattransfercoef cient(W/m K) =characteristicfactor =characteristicfactor =ef ciency =correctivefactor =correctivefactor =characteristicfactor t=temperaturedifference( C) vii viii Notation Superscripts =heating uid =heated uid Subscripts c=counter ow e=exchanger i=inside l=logarithmic m=mean o=outside p=constantpressure(isobaric),parallel ow w=wall 1=inlet(forheatingorheated uid) 2=outlet(forheatingorheated uid) Contents 1 Introduction to Computation . . . . . . . . . . . . . . . . . . . . . 1 1. 1 GeneralConsiderations . . . . . . . . . . . . . . . . . . . . . . 1 1. 2 MeanIsobaricSpeci cHeat . . . . . . . . . . . . . . . . . . . . 3 1. 2. 1 WaterandSuperheatedSteam . . . . . . . . . . . . . . . 4 1. 2. 2 AirandOtherGases. . . . . . . . . . . . . . . . . . . . 4 2 Design Computation. . . . . . . . . . . . . . . . . . . . . . . . . . 7 2. 1 Introduction . . . . . . . . . . . . . . . . . . . . . . . . . . . . 7 2. 2 FluidsinParallelFloworinCounterFlow . . . . . . . . . . . . 8 2. 3 TheMeanDifferenceinTemperatureinReality . . . . . . . . . 12 2. 3. 1 FluidsinCrossFlow. . . . . . . . . . . . . . . . . . . . 14 2. 3. 2 HeatExchangers. . . . . . . . . . . . . . . . . . . . . . 15 2. 3. 3 Coils. . . . . . . . . . . . . . . . . . . . . . . . . . . . 19 2. 3. 4 TubeBankswithVariousPassagesoftheExternalFluid . 21 3 Veri cation Computation . . . . . . . . . . . . . . . . . . . . . . . 25 3. 1 Introduction . . . . . . . . . . . . . . . . . . . . . . . . . . . . 25 3. 2 FluidsinParallelFloworinCounterFlow . . . . . . . . . . . . 25 3. 3 Factor inRealCases. . . . . . . . . . . . . . . . . . . . . . . 33 3. 3. 1 FluidswithCrossFlow . . . . . . . . . . . . . . . . . ., DE, [SC: 0.00], Neuware, gewerbliches Angebot, 241x165x20 mm, 176, [GW: 424g], offene Rechnung (Vorkasse vorbehalten), PayPal, Kreditkarte, Banküberweisung, Interntationaler Versand

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Handbook for Heat Exchangers and Tube Banks design - Donatello Annaratone
Vergriffenes Buch, derzeit bei uns nicht verfügbar.
(*)
Donatello Annaratone:
Handbook for Heat Exchangers and Tube Banks design - neues Buch

1, ISBN: 9783642133084

[ED: Buch], [PU: Springer-Verlag GmbH], Neuware - The recently published book by the author, Engineering Heat Transfer , already dealt with exact computation of heat exchangers and tube banks. In design c- putationthisisaccomplishedviacorrectivefactorsthelattermakesitpossibleto compute the actual mean temperature difference by starting from the logarithmic onerelativeto uidsinparallel oworcounter ow. As far as veri cation computation is concerned, corrective factors were int- ducedtocomputeacertaincharacteristicfactorcorrectly,asisfundamentalforthis typeofcomputation. Basedontheabove,theauthordecidedtoinvestigatefurther,re ne,andwiden thistopic:theoutcomeofthisworkhasresultedinthishandbook. Newtypesofexchangerswereexaminedthecalculationwasre nedtoproduce practicallyexactvaluesforthefactors. Thescopeoftheinvestigationwasincreased by widening the range of the starting factors. Furthermore, a greater number of valuestobeincludedinthetableswasconsidered. Finally,afewcharacteristicsof certainvaluesofthecorrectivefactorswerehighlighted. The rstsectionisanintroductionitsummarizesthefundamentalcriteriaofheat transferandproceedstoillustratethebehaviorof uidsinbothparallelandcounter ow. Italsoshowshowtocomputethemeanisobaricspeci cheatforsome uids itillustratesthesigni canceofdesigncomputationandveri cationcomputation. In addition,itillustrateshowtoproceedwithheatexchangersandtubebankstocarry outbothdesignandveri cationcomputationcorrectly. AppendixAthenincludes36tablesasareferencefordesigncomputation,The tablescontainthecorrectivefactorsrequiredtoobtaintheactualmeantemperature differencebystartingfromthemeanlogarithmictemperaturedifferencerelativeto uidsinparallel oworcounter ow. Finally, Appendix B includes 35 tables for veri cation computation. As far as heatexchangers areconcerned, itshowsthevaluesoffactor whichisrequired forthistypeofcomputation. Thevaluesofthecorrectivefactorsforcoilsandtube banksarealsopresented. Milano,Italy DonatelloAnnaratone v Notation c=speci cheat(J/kgK) d=diameter(m) E=ef ciencyfactor h=enthalpy(kJ/kg) k=thermalconductivity(W/mK) M=mass owrate(kg/s) m=massmoisturepercentage(%) q=heatpertimeunit(W) 2 S=surface(m ) t=temperature( C) 2 U=overallheattransfercoef cient(W/m K) x=thickness(m) 2 =heattransfercoef cient(W/m K) =characteristicfactor =characteristicfactor =ef ciency =correctivefactor =correctivefactor =characteristicfactor t=temperaturedifference( C) vii viii Notation Superscripts =heating uid =heated uid Subscripts c=counter ow e=exchanger i=inside l=logarithmic m=mean o=outside p=constantpressure(isobaric),parallel ow w=wall 1=inlet(forheatingorheated uid) 2=outlet(forheatingorheated uid) Contents 1 Introduction to Computation . . . . . . . . . . . . . . . . . . . . . 1 1. 1 GeneralConsiderations . . . . . . . . . . . . . . . . . . . . . . 1 1. 2 MeanIsobaricSpeci cHeat . . . . . . . . . . . . . . . . . . . . 3 1. 2. 1 WaterandSuperheatedSteam . . . . . . . . . . . . . . . 4 1. 2. 2 AirandOtherGases. . . . . . . . . . . . . . . . . . . . 4 2 Design Computation. . . . . . . . . . . . . . . . . . . . . . . . . . 7 2. 1 Introduction . . . . . . . . . . . . . . . . . . . . . . . . . . . . 7 2. 2 FluidsinParallelFloworinCounterFlow . . . . . . . . . . . . 8 2. 3 TheMeanDifferenceinTemperatureinReality . . . . . . . . . 12 2. 3. 1 FluidsinCrossFlow. . . . . . . . . . . . . . . . . . . . 14 2. 3. 2 HeatExchangers. . . . . . . . . . . . . . . . . . . . . . 15 2. 3. 3 Coils. . . . . . . . . . . . . . . . . . . . . . . . . . . . 19 2. 3. 4 TubeBankswithVariousPassagesoftheExternalFluid . 21 3 Veri cation Computation . . . . . . . . . . . . . . . . . . . . . . . 25 3. 1 Introduction . . . . . . . . . . . . . . . . . . . . . . . . . . . . 25 3. 2 FluidsinParallelFloworinCounterFlow . . . . . . . . . . . . 25 3. 3 Factor inRealCases. . . . . . . . . . . . . . . . . . . . . . . 33 3. 3. 1 FluidswithCrossFlow . . . . . . . . . . . . . . . . . ., DE, [SC: 0.00], Neuware, gewerbliches Angebot, 241x165x20 mm, 176, [GW: 424g], PayPal, Banküberweisung, Interntationaler Versand

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Handbook for Heat Exchangers and Tube Banks design - Donatello Annaratone
Vergriffenes Buch, derzeit bei uns nicht verfügbar.
(*)
Donatello Annaratone:
Handbook for Heat Exchangers and Tube Banks design - neues Buch

ISBN: 9783642133084

[ED: Buch], [PU: Springer-Verlag GmbH], Neuware - areconcerned, itshowsthevaluesoffactor whichisrequired forthistypeofcomputation. Thevaluesofthecorrectivefactorsforcoilsandtube banksarealsopresented. Milano,Italy DonatelloAnnaratone v Notation c=speci cheat(J/kgK) d=diameter(m) E=ef ciencyfactor h=enthalpy(kJ/kg) k=thermalconductivity(W/mK) M=mass owrate(kg/s) m=massmoisturepercentage(%) q=heatpertimeunit(W) 2 S=surface(m ) t=temperature( C) 2 U=overallheattransfercoef cient(W/m K) x=thickness(m) 2 =heattransfercoef cient(W/m K) =characteristicfactor =characteristicfactor =ef ciency =correctivefactor =correctivefactor =characteristicfactor t=temperaturedifference( C) vii viii Notation Superscripts =heating uid =heated uid Subscripts c=counter ow e=exchanger i=inside l=logarithmic m=mean o=outside p=constantpressure(isobaric),parallel ow w=wall 1=inlet(forheatingorheated uid) 2=outlet(forheatingorheated uid) Contents 1 Introduction to Computation . . . . . . . . . . . . . . . . . . . . . 1 1. 1 GeneralConsiderations . . . . . . . . . . . . . . . . . . . . . . 1 1. 2 MeanIsobaricSpeci cHeat . . . . . . . . . . . . . . . . . . . . 3 1. 2. 1 WaterandSuperheatedSteam . . . . . . . . . . . . . . . 4 1. 2. 2 AirandOtherGases. . . . . . . . . . . . . . . . . . . . 4 2 Design Computation. . . . . . . . . . . . . . . . . . . . . . . . . . 7 2. 1 Introduction . . . . . . . . . . . . . . . . . . . . . . . . . . . . 7 2. 2 FluidsinParallelFloworinCounterFlow . . . . . . . . . . . . 8 2. 3 TheMeanDifferenceinTemperatureinReality . . . . . . . . . 12 2. 3. 1 FluidsinCrossFlow. . . . . . . . . . . . . . . . . . . . 14 2. 3. 2 HeatExchangers. . . . . . . . . . . . . . . . . . . . . . 15 2. 3. 3 Coils. . . . . . . . . . . . . . . . . . . . . . . . . . . . 19 2. 3. 4 TubeBankswithVariousPassagesoftheExternalFluid . 21 3 Veri cation Computation . . . . . . . . . . . . . . . . . . . . . . . 25 3. 1 Introduction . . . . . . . . . . . . . . . . . . . . . . . . . . . . 25 3. 2 FluidsinParallelFloworinCounterFlow . . . . . . . . . . . . 25 3. 3 Factor inRealCases. . . . . . . . . . . . . . . . . . . . . . . 33 3. 3. 1 FluidswithCrossFlow . . . . . . . . . . . . . . . . . ., DE, [SC: 0.00], Neuware, gewerbliches Angebot, 241x165x20 mm, 176, [GW: 424g], offene Rechnung (Vorkasse vorbehalten), PayPal, Banküberweisung

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(*) Derzeit vergriffen bedeutet, dass dieser Titel momentan auf keiner der angeschlossenen Plattform verfügbar ist.
Handbook for Heat Exchangers and Tube Banks design - Donatello Annaratone
Vergriffenes Buch, derzeit bei uns nicht verfügbar.
(*)
Donatello Annaratone:
Handbook for Heat Exchangers and Tube Banks design - neues Buch

ISBN: 9783642133084

[ED: Buch], [PU: Springer-Verlag GmbH], Neuware - areconcerned, itshowsthevaluesoffactor whichisrequired forthistypeofcomputation. Thevaluesofthecorrectivefactorsforcoilsandtube banksarealsopresented. Milano,Italy DonatelloAnnaratone v Notation c=speci cheat(J/kgK) d=diameter(m) E=ef ciencyfactor h=enthalpy(kJ/kg) k=thermalconductivity(W/mK) M=mass owrate(kg/s) m=massmoisturepercentage(%) q=heatpertimeunit(W) 2 S=surface(m ) t=temperature( C) 2 U=overallheattransfercoef cient(W/m K) x=thickness(m) 2 =heattransfercoef cient(W/m K) =characteristicfactor =characteristicfactor =ef ciency =correctivefactor =correctivefactor =characteristicfactor t=temperaturedifference( C) vii viii Notation Superscripts =heating uid =heated uid Subscripts c=counter ow e=exchanger i=inside l=logarithmic m=mean o=outside p=constantpressure(isobaric),parallel ow w=wall 1=inlet(forheatingorheated uid) 2=outlet(forheatingorheated uid) Contents 1 Introduction to Computation . . . . . . . . . . . . . . . . . . . . . 1 1. 1 GeneralConsiderations . . . . . . . . . . . . . . . . . . . . . . 1 1. 2 MeanIsobaricSpeci cHeat . . . . . . . . . . . . . . . . . . . . 3 1. 2. 1 WaterandSuperheatedSteam . . . . . . . . . . . . . . . 4 1. 2. 2 AirandOtherGases. . . . . . . . . . . . . . . . . . . . 4 2 Design Computation. . . . . . . . . . . . . . . . . . . . . . . . . . 7 2. 1 Introduction . . . . . . . . . . . . . . . . . . . . . . . . . . . . 7 2. 2 FluidsinParallelFloworinCounterFlow . . . . . . . . . . . . 8 2. 3 TheMeanDifferenceinTemperatureinReality . . . . . . . . . 12 2. 3. 1 FluidsinCrossFlow. . . . . . . . . . . . . . . . . . . . 14 2. 3. 2 HeatExchangers. . . . . . . . . . . . . . . . . . . . . . 15 2. 3. 3 Coils. . . . . . . . . . . . . . . . . . . . . . . . . . . . 19 2. 3. 4 TubeBankswithVariousPassagesoftheExternalFluid . 21 3 Veri cation Computation . . . . . . . . . . . . . . . . . . . . . . . 25 3. 1 Introduction . . . . . . . . . . . . . . . . . . . . . . . . . . . . 25 3. 2 FluidsinParallelFloworinCounterFlow . . . . . . . . . . . . 25 3. 3 Factor inRealCases. . . . . . . . . . . . . . . . . . . . . . . 33 3. 3. 1 FluidswithCrossFlow . . . . . . . . . . . . . . . . . ., DE, [SC: 0.00], Neuware, gewerbliches Angebot, FixedPrice, 176, [GW: 424g], offene Rechnung (Vorkasse vorbehalten), PayPal, Banküberweisung

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Handbook for Heat Exchangers and Tube Banks design - Annaratone, Donatello
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Annaratone, Donatello:
Handbook for Heat Exchangers and Tube Banks design - gebunden oder broschiert

2010, ISBN: 3642133088

ID: A10320558

Gebundene Ausgabe Bau / Entwurf, Konstruktion, Chemische Industrie, Industrie / Chemische Industrie, Energietechnik, Dynamik (physikalisch) / Thermodynamik, Thermodynamik, Wärmelehre / Thermodynamik, mit Schutzumschlag neu, [PU:Springer-Verlag GmbH; Springer Berlin]

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Details zum Buch
Handbook for Heat Exchangers and Tube Banks design

When a heating fluid transfers heat to a heated fluid through a wall, if the fluids are in parallel flow or counter flow it is possible to compute exactly both the transferred heat and the temperatures of the fluids via well-known equations. This holds true both for design and verification computation. However, the motion of the fluids is never in parallel flow or counter flow in heat exchangers and in tube banks. Instead, it is rather complex and consists of a combination of various cross flows. Hence, a precise design of the above components requires, on a case-by-case basis, the availability of the value of certain crucial factors or of corrective factors so as to make it possible to use the equations relative to parallel flow or counter flow. This handbook contains the introduction to the problem, its design criteria, and about 70 tables for the exact design and verification computation. It also indicates how to proceed in the case of cross flow.

Detailangaben zum Buch - Handbook for Heat Exchangers and Tube Banks design


EAN (ISBN-13): 9783642133084
ISBN (ISBN-10): 3642133088
Gebundene Ausgabe
Erscheinungsjahr: 2010
Herausgeber: Springer-Verlag GmbH
176 Seiten
Gewicht: 0,424 kg
Sprache: eng/Englisch

Buch in der Datenbank seit 05.07.2009 13:16:56
Buch zuletzt gefunden am 04.10.2017 15:47:10
ISBN/EAN: 9783642133084

ISBN - alternative Schreibweisen:
3-642-13308-8, 978-3-642-13308-4


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