Chapter 7 External Forced Convection Flashcards

1
Q

What does a Nu number of 100 mean

A

100 x more convection than conduction, 100 x more heat transfer than if fluid was not moving

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2
Q

What is drag

A

the force a flowing fluid exerts on a body in the flow direction

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3
Q

What makes up lift

A

components of the pressure and wall shear forces in the normal direction to flow tend to move the body in that direction

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4
Q

What does the drag force depend on

A

the density of the fluid, the upstream velocity V, the size, shape and orientation of the body among other things

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5
Q

Drag coefficient =

A

Cd = Fd/ 0.5rhoV^2*A

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6
Q

what is the part of the drag that is due directly to wall shear stress

A

skin friction drag (or just friction drag)

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7
Q

what is the part of the drag that is due directly to pressure

A

pressure drag

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8
Q

What is the total drag coefficient equal to

A

Cd = Cdfriction + Cdpressure

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9
Q

What is most drag due to at low reynolds numbers

A

friction drag

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10
Q

What is friction drag proportional to

A

surface area

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11
Q

what is pressure drag proportional to

A

frontal area and the difference between pressures acting on the front and back of the immersed body

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12
Q

Pressure drag is usually dominant and negligible for what type of bodies

A

dominant for blunt bodies and negligible for streamlined bodies

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13
Q

When a fluid separates from a body it forms a

A

separated region between the body and the fluid stream

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14
Q

What happens as the separated region increases

A

the pressure drag increases

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15
Q

Critical reynolds number for flat plate

A

5e5, where the distance is from the start of the plate

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16
Q

Local nusselt number for laminar =

isothermal and smooth

A

0.332 Re(x)^0.5 * Pr ^1/3 for Pr >0.6

17
Q

Local nusselt number for turbulent=

isothermal and smooth

A

0.0296 Re(x)^085 * Pr ^1/3 for 0.6<= Pr <= 60 and 5e5 <= Re <= e7

18
Q

How do the local friction and heat transfer coefficient compare in laminar and turbulent flow

A

both are higher in turbulent flow

19
Q

Draw the diagram of convection heat transfer coefficient and local friction coefficients over a flat plate
(isothermal and smooth)

A

see diagram

20
Q

Average nusselt number for laminar =

isothermal and smooth

A

0.664 Re(L)^0.5 * Pr ^1/3 for Re(L) < 5e5

21
Q

Average nusselt number for turbulent=

isothermal and smooth

A

0.037 Re(L)^0.8 * Pr ^1/3 for 0.6 < Pr < 60 and 5e5 < Re(L) < e7

22
Q

Laminar and turbulent Nu

isothermal and smooth

A

(0.037 Re(L)^0.8 - 871) Pr^1/3 for 0.6 < Pr < 60 and 5e5 < Re(L) < e7

23
Q

Why do we normally not consider the transition region

A

as it occurs so quickly we cant see it

24
Q

What is the peclet number

A

Pe(x) = Re(x)*Pr

25
Nu for laminar | flat plate subject to uniform heat flux
0.453 Re(x)^0.5 * Pr ^1/3 for Pr > 0.6 Re(x) < 5e5
26
Nu for turbulent | flat plate subject to uniform heat flux
0.0308Re(x)^0.8 * Pr ^1/3 for 0.6 < Pr < 60 and 5e5 < Re(L) < e7
27
When heat flux is prescibed the rate of heat transfer to form the plate and the surface temperature at a distance x can be determined from
q.s = h(x) (Ts(x) - Tinf)
28
Critical reynolds number for flow across a cylinder or sphere
2e5, but laminar boundary layer separation with a turbulent wake flow over a cirular cylinder at 2000
29
What two things are significant for flow over a cylinder or sphere
friction and pressure drag
30
Effect of surface roughness on drag coefficient
increases it in turbulent flow in general, however for blunt bodeies such a circular clylinder of sphere an increase in surface roughness may increase or decrease the drag coefficient depending on the reynolds number
31
What is it difficult to use an analytical approach to find the heat transfer coefficient of a cylinder or sphere
generally involved flow separation which is difficult to analyse, instead several empirical correlations have been developed for the heat transfer coefficient
32
At what temperature are fluid properties evaluated for when calculating Nu over a cylinder
film temperature Tf = 1/2 (Tinf + Ts)