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Handbook for Heat Exchangers and Tube Banks design - Donatello Annaratone

(*)

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 b… Mehr…

[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- putationthisisaccomplishedviacorrectivefactors;thelattermakesitpossibleto 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. Newtypesofexchangerswereexamined;thecalculationwasre nedtoproduce practicallyexactvaluesforthefactors. Thescopeoftheinvestigationwasincreased by widening the range of the starting factors. Furthermore, a greater number of valuestobeincludedinthetableswasconsidered. Finally,afewcharacteristicsof certainvaluesofthecorrectivefactorswerehighlighted. The rstsectionisanintroduction;itsummarizesthefundamentalcriteriaofheat 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], Banküberweisung, PayPal, Skrill/Moneybookers, Selbstabholung und Barzahlung, Klarna-Sofortüberweisung, Offene Rechnung (Vorkasse vorbehalten)<

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Handbook for Heat Exchangers and Tube Banks design - Donatello Annaratone

(*)

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 banksar… Mehr…

[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], Banküberweisung, PayPal<

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Handbook for Heat Exchangers and Tube Banks design / Donatello Annaratone / Buch / Englisch / 2010 / Springer Berlin / EAN 9783642133084 - Annaratone, Donatello

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Handbook for Heat Exchangers and Tube Banks design / Donatello Annaratone / Buch / Englisch / 2010 / Springer Berlin / EAN 9783642133084 - gebunden oder broschiert

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[ED: Gebunden], [PU: Springer Berlin], areconcerned, itshowsthevaluesoffactor ? whichisrequired forthistypeofcomputation. Thevaluesofthecorrectivefactorsforcoilsandtube banksarealsopresen… Mehr…

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Annaratone, Donatello:
Handbook for Heat Exchangers and Tube Banks design | Donatello Annaratone | Buch | Englisch | 2010 | Springer Berlin | EAN 9783642133084 - gebunden oder broschiert

2010, ISBN: 9783642133084

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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 b… Mehr…

[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- putationthisisaccomplishedviacorrectivefactors;thelattermakesitpossibleto 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. Newtypesofexchangerswereexamined;thecalculationwasre nedtoproduce practicallyexactvaluesforthefactors. Thescopeoftheinvestigationwasincreased by widening the range of the starting factors. Furthermore, a greater number of valuestobeincludedinthetableswasconsidered. Finally,afewcharacteristicsof certainvaluesofthecorrectivefactorswerehighlighted. The rstsectionisanintroduction;itsummarizesthefundamentalcriteriaofheat 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], Banküberweisung, PayPal, Skrill/Moneybookers, Selbstabholung und Barzahlung, Klarna-Sofortüberweisung, Offene Rechnung (Vorkasse vorbehalten)<

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Handbook for Heat Exchangers and Tube Banks design - Donatello Annaratone

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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 banksar… Mehr…

[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], Banküberweisung, PayPal<

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ISBN: 9783642133084

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Annaratone, Donatello:
Handbook for Heat Exchangers and Tube Banks design | Donatello Annaratone | Buch | Englisch | 2010 | Springer Berlin | EAN 9783642133084 - gebunden oder broschiert

2010, ISBN: 9783642133084

[ED: Gebunden], [PU: Springer Berlin], areconcerned, itshowsthevaluesoffactor ? whichisrequired forthistypeofcomputation. Thevaluesofthecorrectivefactorsforcoilsandtube banksarealsopresen… Mehr…

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Handbook for Heat Exchangers and Tube Banks design - gebrauchtes Buch

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Handbook for Heat Exchangers and Tube Banks design

Autor:	Donatello Annaratone
Titel:	Handbook for Heat Exchangers and Tube Banks design
ISBN-Nummer:	9783642133084

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
Taschenbuch
Erscheinungsjahr: 2010
Herausgeber: Springer Berlin
176 Seiten
Gewicht: 0,424 kg
Sprache: eng/Englisch

Buch in der Datenbank seit 2009-07-05T13:16:56+02:00 (Vienna)
Detailseite zuletzt geändert am 2023-03-08T14:53:29+01:00 (Vienna)
ISBN/EAN: 9783642133084

ISBN - alternative Schreibweisen:
3-642-13308-8, 978-3-642-13308-4
Alternative Schreibweisen und verwandte Suchbegriffe:
Autor des Buches: donatello annaratone
Titel des Buches: heat exchangers, little design possible, looking design, eat for heat, the handbook, donatello, berlin heat

Daten vom Verlag:

Autor/in: Donatello Annaratone
Titel: Handbook for Heat Exchangers and Tube Banks design
Verlag: Springer; Springer Berlin
176 Seiten
Erscheinungsjahr: 2010-07-31
Berlin; Heidelberg; DE
Gedruckt / Hergestellt in Niederlande.
Gewicht: 0,980 kg
Sprache: Englisch
139,09 € (DE)
142,99 € (AT)
153,50 CHF (CH)
POD
X, 176 p.

BB; Engineering Thermodynamics, Heat and Mass Transfer; Hardcover, Softcover / Technik/Allgemeines, Lexika; Technische Thermodynamik; Verstehen; Industrielle Fertigung; cross flows; design criteria; heat exchanger; heat exchangers; heat transfer; tube banks; Industrial Chemistry/Chemical Engineering; Engineering Design; Energy Systems; Energy, general; Energy Policy, Economics and Management; Engineering Thermodynamics, Heat and Mass Transfer; Industrial Chemistry; Engineering Design; Electrical Power Engineering; Mechanical Power Engineering; Energy Policy, Economics and Management; Industrielle Chemie und Chemietechnologie; Konstruktion, Entwurf; Elektrotechnik; Energietechnik, Elektrotechnik und Energiemaschinenbau; Umwelt; BC; BC; EA

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.

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