傳遞現(xiàn)象：英文本

CHAPTER1INTRODUCTIONTOPHYSICALTRANSPORTPHENOMENA
I.1Conservationlaws
1.2Rateofmoleculartransportprocesses
1.3Microbalances
1.4Dimensionsandmagnitude
1.5Dimensionalanalysis
1.6Problems
CHAPTERIIFLOWPHENOMENA
II.1Laminarflow
II.1.1Stationarylaminarflowbetweentwoflathorizontalplates
II.1.2Stationarylaminarflowthroughahorizontalcirculartube
II.1.3Stationarylaminarflowthroughahorizontalannulus
II.1.4Flowcausedbymovingsurfaces
II.1.5Flowthroughpipeswithothercross-sections
II.1.6Non-stationaryflow
II.1.7Problems
II.2Turbulentflow
II.2.1Turbulentflowinpipes
II.2.2Pressuredropinstraightchannels
II.2.3Pressuredropinpipesystems
II.2.4Problems
II.3Flowwithnegligibleenergydissipation
II.3.1Flowofaliquidfromanorifice
II.3.2Flowofgasesthroughorifices
II.3.3Flowthroughweirs
II.3.4Flowmeters
II.3.5Problems
II.4Flowaroundobstacles
II.4.1Generalapproach
II.4.2Sphericalparticles
I1.4.3Freefallofdroplets
II.4.4Particlesinnon-stationaryflow
II.4.5Rateofsedimentationofaswarmofparticles
II.4.6Cylindersperpendiculartothedirectionofflow
II.4.7Problems
II.5Flowthroughbedsofparticles
II.5.1Fixedbed
II.5.2Filtrationthroughabedofparticles
II.5.3Fluidizedbed
II.5.4Problems
II.6Stirring，mixingandresidencetimedistribution
II.6.1Typesofstirrerandflowpatterns
II.6.2Powerconsumption，pumpingcapacityandmixingtime
II.6.3Residencetimedistribution：theFandEfunctions
II.6.4SimpleapplicationsofFandEfunctions
II.6.5Continuousflowmodels
II.6.6Dispersionandsegregationinflowsystems
II.6.7Problems
CHAPTERIIIHEATTRANSPORT
III.1Stationaryheatconduction
III.1.1Heatconductionthroughawall
III.1.2Heatconductionthroughcylindricalwalls
III.1.3Heatconductionaroundasphere
III.1.4Generalapproachforthecalculationoftemperature
distributions
III.1.5Temperaturedistributioninacylinderwithuniformheat
production
III.1.6Problems
III.2Non-stationaryheatconduction
III.2.1Heatpenetrationintoasemi-infinitemedium
III.2.2Heatpenetrationintoafinitemedium
III.2.3Influenceofanoutsideheattransfercoefficient
III.2.4Problems
III.3Heattransferbyforcedconvectioninpipes
III.3.1Heattransferduringlaminarflowinpipes
III.3.2Heattransferduringturbulentflow
III.3.3Partialandtotalheattransfercoefficients
III.3.4Problems
III.4Heatexchangers
III.4.1Determinationofmeantemperaturedifference
III.4.2Heightofatransferunit
111.4.3Designofheatexchangers
111.4.4Problems
Ili.5Heattransferbyforcedconvectionaroundobstacles
III.5.1Flowalongaflatplate
111.5.2Heattransfertofallingfilms
Ili.5.3Flowaroundspheresandcylinders
111.5.4Heattransferinpackedbeds
111.5.5Heattransferinfluidizedbeds
Ili.5.6Problems
Ill.6Heattransferduringnaturalconvection
II1.6.1Naturalconvection
III.6.2Problems
III.7Heattransferduringcondensationandboiling
III.7.1Filmcondensation
II1.7.2Dropwisecondensation
1II.7.3Boiling
II1.7.4Heattransferinevaporators
III.7.5Problems
111.8Heattransferinstirredvessels
111.8.1Problem
Ili.9Heattransportbyradiation
111.9.1Problems
CHAPTERIVMASSTRANSPORT
IV.1Stationarydiffusionandmasstransfer
IV.1.1Stationarydiffusion
IV.1.2Masstransfercoefficients
IV.1.3Generalapproachforthecalculationof
concentrationdistributions
IV.1.4Filmmodel
IV.1.5Problems
IV.2Non-stationarydiffusion
IV.2.1Problems
IV.3Masstransferwithforcedconvection
IV.3.1Analogywithheattransfer
IV.3.2Masstransferduringlaminarflow
IV.3.3Masstransferduringturbulentflow
IV.3.4Problems
IV.4Massexchangers
IV.4.1Thermodynamicequilibrium
IV.4.2Choiceoftheapparatus
IV.4.3Sizedeterminationofthemassexchanger
IV.4.4Theconceptoftheoreticalplates
IV.4.5Problems
IV.5Masstransferwithchemicalreaction
IV.5.1Slowhomogeneousfirst-orderreactions
IV.5.2Fasthomogeneousfirst-orderreactions
IV.5.3Non-linearhomogeneousreactions
IV.5.4Homogeneoussecond-orderreactions
IV.5.5Masstransferwithheterogeneouschemicalreaction
IV.5.6Problems
IV.6Combinedheatandmasstransport
IV.6.1Drying
IV.6.2Problems
NOTATION
INDEX