Transport Processes Flashcards
Formula for Conduction
Q/A = -kΔT/Δx
resistance = Δx/k
Heat in Conduction
Qᴛ = Qᴀ = Qʙ = Qc
Conduction in Hollow Cylinder
. - 2πkLΔT
Q= ———————
ln (r2/r1)
E5-7
Conduction in Sphere
. - 4πkΔT
Q= ———————
1/r2 - 1/r1
E5-8
Conduction in Sphere with more than 3 insulation
Uses the cylinder formula
. - 2πLΔT
Q= ——————————————-
1/kᴀ·ln(r₂/r₁) + 1/kʙ·ln(r₃/r₂)+…+
E5-8
Conduction in Series
E5-9
Formula for Convection
Q/A = -hΔT
resistance = 1/h
h = individual heat transfer coeff.
Heat and Resistance in Convection
Qᴛ = Qᴀ + Qʙ + Qc
1/Rᴛ = 1/Rᴀ = 1/Rʙ = 1/Rc
Combination in Series
Q/A = -ΔT/(1/U)
Q/A = -ΔT/ (Δx/k) + (1/h)
where 1/U = 1/k + 1/h
U = overall heat transfer coeff. (both resistance of conduction and convection)
Conduction with Internal Heat Generation for Cylinder
Ex. Wire
. q̇r ²
To = ———- + Tw
4k
where:
q̇ = Q/V = I²R/ πr²L
r = radius
To = Center Temperature
Tw = Outside Temperature
Conduction with Internal Heat Generation for a Flat Slab
. q̇x²
To = ———- + Tw
2k
where:
q̇ = Q/V
x = thickness
To = Center/Max Temperature
Tw = Surface Temperature
Double Pipe Heat Exchanger
withour Ft
Q = UAΔTₗₘ
where:
Q = mCpΔT
-Qloss = Qgain
ΔTₗₘ = T1-T2/ln(T1/T2)
if not given: A = πDL (not cross-sectional)
1/U = 1/h,o + 1/h,cw; h=coeff.
Counter-current Flow
T1 ———-> T2
t2 <———- t1
Parallel Flow
T1 ———-> T2
t1 ———-> t2
Heat Exchanger
with Ft
Q = UAΔTₗₘ · Ft
Q = UᵢAᵢΔTₗₘ = UₒAₒΔTₗₘ
where:
Q = mCpΔT
ΔTₗₘ = T1-T2/ln(T1/T2)
A = πDL
Ft = ? R = T₁ - T₂ / t₂ - t₁
S = t₂ - t₁ / T₁ - t₁
1-2 HE –> 1 shell and 2 tubes
Heat Transfer Coefficient
Convection
Q/A = -hΔT
Use:
Re, Pr, and Nu formulas
**
T2-144 if Pr for air
T2-145 for k**