Conduction Flashcards

(35 cards)

1
Q

General equation for conduction, Q.

A
Q. = - k A dT/dt
Q. = - k A (T1-T2)/Δx
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2
Q

What does k stand for (W/mK)

A

K = thermal conductivity

  • measure of materials ability to conduct heat
  • material property
  • temperature dependent
  • find using data books (LBOTF)
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3
Q

Definition of diffusivity, α (m^2/s)

A

α = heat conduction / heat storage = k / ρc

the larger α, the faster the propagation of heat into the medium

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4
Q

Q. =

q. =

A
Q. = heat transfer rate (W)
q. = heat flux (W/m^2)

q. = Q. / A

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5
Q

Topics thought about when engineering HX (Heat exchangers)

A
1. Experimental approach
\+ Actual physical system
\+ Real measurements are used
- Expensive, time consuming
- Often impractical
  1. Analytical approach
    + Fast
    + inexpensive assumptions and approximations
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6
Q

Definition of transient

A

implies variation with time

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7
Q

Heat generation equation

A

E. gen = ∫ e. gen dV

therefore volumetric phenomenon

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8
Q

Energy conservation equation for 1D plane wall

A

d/dx(k dT/dx) + e.gen = ρc dT/dt

for steady state, no heat gen - d2T/dx2 = 0
pg.47 LBOTF

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9
Q

Equation used to find exact temperature at any point of a material.

A

Tx = (T2-T1)x + T1

L

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10
Q

Equation for resistance

A

R = L / kA

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11
Q

For materials with varying k, how to find q.cond

A

q.cond * L = - (aT^4/4 + bT^3/3 + cT^2/2 + d*T)

a, b, c, d all vary for each material

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12
Q

Equation for energy used to change state

solid liquid

A

ρ * dδ/dt * Δh(fus)

where dδ/dt measured in m/s

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13
Q

Energy conservation equation for 1D long cylinder

A

1/r * d/dr( r k dT/dr) + e.gen = ρc dT/dt

for steady state, no heat gen:
d/dr(r dT/dr) = 0
Therfore:
T = C1 ln(r) + C2

pg.47 LBOTF

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14
Q

Equation for resistance of a cylinder

A

Rcyl = ln(r(out) / r(in))

k2πL

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15
Q

Energy conservation equation for 1D sphere

A

1/r^2 * d/dr( r^2 k dT/dr) + e.gen = ρc dT/dt

for steady state, no heat gen:
d/dr(r^2 dT/dr) = 0
or
r d^2T/dr^2 + 2 dT/dr = 0

pg.47 LBOTF

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16
Q

Definition of adiabatic system

A

system where no heat or matter is transferred.

17
Q

Equation for U - overall heat transfer coefficient

A

1
U = ——————————————–
(1/h(conv)A) + Δx/kA + 1/h(rad)A)

Q. = UAΔT(overall)

18
Q

What is thermal contact resistance, and equation for it

A

Resistance seen between two different materials meeting.
Due to surface roughness, material properties, temp and pressure interface.

R(c) = 1 / h(c)A

19
Q

What does a lumped system approach imply about heat conductivity

A

It implies high k, which would mean a uniform temperature inside a body

20
Q

Lumped system approach equation for temp variation

A

T(t) - T(∞)
————- = e^(-bt)
T(i) - T(∞)

where b = hA(s) / ρVc

21
Q

how does the temp of lumped system approach the system temp?

How does this vary with ‘b’ value

A

exponentially

larger b, means faster approach

22
Q

Definition and equation for Biot number

A

Definition:
the ratio between heat transfer resistances. i.e.

Bi = Convection resistance / Conduction resistance

Bi = hL(c) / k where L(c) = V / A(s)

23
Q

When can a lumped system analysis be applied, with respect to Bi

24
Q

Definition and equation for Fourier number

A

Definition:
characterizes transient heat conduction

Fo = αt / L(c)^2 where: t = time
α = k / ρc

25
Lumped system approach equation for temp variation, using Bi and Fo
T(t) - T(∞) ------------- = e^(-Bi * Fo) T(i) - T(∞)
26
For fin analysis, what assumptions are taken
``` steady state no heat generation in fin constant k constant h around fin constant h along fin ```
27
For the case that: fin in very long and temperature of end of fin same as T(∞) Equation for Q.
Q.longfin = -kAdT/dx = √(hpkA(c)) * (Tb - T∞) where: p = perimeter Tb = temperature at beginning of fin T∞ = surrounding temp (end of fin too) found page 47 LBOTF
28
For the case that: fin is insulated (adiabatic) Equation for Q.
Q.longfin = -kAdT/dx = √(hpkA(c)) * (Tb - T∞) * tanh(mL) found page 47 LBOTF
29
Equation to calculate fin efficiency
η = Qfin / Qfin,max Qfin,max = hA(fin)(Tb - T∞)
30
Equation for fin effectiveness, εfin
εfin = η * Afin / Ab
31
For what value of εfin is it justifiable to use a fin
εfin > 1 fin justifiable if εfin < 1 this implies fin insulates the surface
32
Equation for overall fin effectiveness, εoverall
εoverall = Aunfin + ηfinAfin ------------------------ Anofin
33
Equation for shape factor for plane wall
S = A/L
34
How to calculate shape factor of complex shape
divide into smaller shapes and then add these shape factors up. All use look up tables
35
How to use shape factor to calculate heat loss of shape
Q. = Sk(T1-T2)