부산대학교현규
부산대학교 화공생명공학부현 규 (Kyu Hyun)
유체역학및열전달
Chapter 11. Principles of Heat Flow in Fluids
-열교환기
유체역학및열전달 1
부산대학교현규
Heat-Exchange Equipment – Using latent heat
-In this text the symbol ΔT is used to signify a temperature difference between two objects or two fluids
유체역학및열전달 2
부산대학교현규
Heat-Exchange Equipment – Using sensible heat
l Countercurrent flow (or counter flow) 향류
l Parallel flow (or counter flow) 병류
Parallel flow is used in special situations èTo change the temperature of fluid rapidly
유체역학및열전달 3
부산대학교현규
Energy Balances (1)
- Heat loss (cool down)
- Heat gain (heat up)
유체역학및열전달 4
부산대학교현규
Energy Balances (2)
유체역학및열전달 5
부산대학교현규
Heat flux and Heat-transfer coefficients (1)
-Tubular exchanger = Pipe shape-Plate type heat exchanger = Both side areas are same, only one U Value
유체역학및열전달 6
부산대학교현규
Heat flux and Heat-transfer coefficients (2)
부산대학교현규
Heat flux and Heat-transfer coefficients (3)
유체역학및열전달 8
부산대학교현규
Heat flux and Heat-transfer coefficients (4)
l LMTD is not always valid -ΔT is not a linear function of q
-Cooling and condensing superheated vapor
-Temperature patterns in Jacketed tubular reactor
유체역학및열전달 9
부산대학교현규
Individual heat-transfer coefficient (1)
유체역학및열전달 10
부산대학교현규
Individual heat-transfer coefficient (2)
-Turbulent flow effect on the temperature profile (forced convection)
-Newton’s cooling law유체역학및열전달 11
부산대학교현규
Individual heat-transfer coefficient (3)
-Tubular pipe
유체역학및열전달 12
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Individual heat-transfer coefficient (4)
-Eq. 10.15
유체역학및열전달 13
부산대학교현규
Individual heat-transfer coefficient (5)
부산대학교현규
Individual heat-transfer coefficient – Nusselt Number
Tube diameter
유체역학및열전달 15
부산대학교현규
Overall heat-transfer coefficient
유체역학및열전달 16
부산대학교현규
Individual heat-transfer coefficient -Plate
유체역학및열전달 17
부산대학교현규
Heat conduction through composite walls – Plate (1)
-Newton’s cooling law
-q0 (heat flux) = constant
부산대학교현규
Heat conduction through composite walls – Plate (2)
유체역학및열전달 19
Individual heat transfer coefficient
부산대학교현규
Heat conduction through composite walls - Pipe
-r0q0 (heat flux) = constant
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