A double-wall heat exchanger is used to transfer heat between liquids flowing through semicircular copper tubes. Each tube has a wall thickness of r i = 20 mm and an inner radius of r = 2 0 mm . and good contact is maintained at the plane surfaces by lightly wound straps. The lube outer surfaces are well insulated. (a) If hot and cold water at mean temperatures of T h , m = 330 K and T c , m = 290 K flow through the adjoining tubes m h = m c = 0.2 kg/s, what is the rate of heat transfer per unit length of tube? The wall contact resistance is 10 − 5 m 2 ⋅ K/W . Approximate the properties of both the hot and cold water as μ = 800 × 10 − 6 kg/s ⋅ m , k = 0.625 W/m ⋅ K , and Pr = 5.35. Hint: Heat transfer is enhanced by conduction through the semicircular portions of the tube walls, and each portion may be subdivided into two straight fins with adiabatic tips. (b) Using the thermal model developed for part (a), determine the heat transfer rate per unit length when the fluids are ethylene glycol. Also, what effect will fabricating the exchanger from an aluminum alloy have on the heat rate? Will increasing the thickness of the tube walls have a beneficial effect’?
A double-wall heat exchanger is used to transfer heat between liquids flowing through semicircular copper tubes. Each tube has a wall thickness of r i = 20 mm and an inner radius of r = 2 0 mm . and good contact is maintained at the plane surfaces by lightly wound straps. The lube outer surfaces are well insulated. (a) If hot and cold water at mean temperatures of T h , m = 330 K and T c , m = 290 K flow through the adjoining tubes m h = m c = 0.2 kg/s, what is the rate of heat transfer per unit length of tube? The wall contact resistance is 10 − 5 m 2 ⋅ K/W . Approximate the properties of both the hot and cold water as μ = 800 × 10 − 6 kg/s ⋅ m , k = 0.625 W/m ⋅ K , and Pr = 5.35. Hint: Heat transfer is enhanced by conduction through the semicircular portions of the tube walls, and each portion may be subdivided into two straight fins with adiabatic tips. (b) Using the thermal model developed for part (a), determine the heat transfer rate per unit length when the fluids are ethylene glycol. Also, what effect will fabricating the exchanger from an aluminum alloy have on the heat rate? Will increasing the thickness of the tube walls have a beneficial effect’?
Solution Summary: The author explains the rate of heat transfer per unit length of the tube. The temperature of hot water at mean is T_h=330K.
A double-wall heat exchanger is used to transfer heat between liquids flowing through semicircular copper tubes. Each tube has a wall thickness of
r
i
=
20
mm and an inner radius of
r
=
2
0
mm
. and good contact is maintained at the plane surfaces by lightly wound straps. The lube outer surfaces are well insulated.
(a) If hot and cold water at mean temperatures of
T
h
,
m
=
330
K and
T
c
,
m
=
290
K flow through the adjoining tubes
m
h
=
m
c
=
0.2
kg/s, what is the rate of heat transfer per unit length of tube? The wall contact resistance is
10
−
5
m
2
⋅
K/W
. Approximate the properties of both the hot and cold water as
μ
=
800
×
10
−
6
kg/s
⋅
m
,
k
=
0.625
W/m
⋅
K
, and Pr = 5.35. Hint: Heat transfer is enhanced by conduction through the semicircular portions of the tube walls, and each portion may be subdivided into two straight fins with adiabatic tips.
(b) Using the thermal model developed for part (a), determine the heat transfer rate per unit length when the fluids are ethylene glycol. Also, what effect will fabricating the exchanger from an aluminum alloy have on the heat rate? Will increasing the thickness of the tube walls have a beneficial effect’?
Two large tanks, each holding 100 L of liquid, are interconnected by pipes, with the liquid flowing from tank
A into tank B at a rate of 3 L/min and from B into A at a rate of 1 L/min (see Figure Q1). The liquid inside each
tank is kept well stirred. A brine solution with a concentration of 0.2 kg/L of salt flows into tank A at a rate of
6 L/min. The diluted solution flows out of the system from tank A at 4 L/min and from tank B at 2 L/min. If,
initially, tank A contains pure water and tank B contains 20 kg of salt.
A
6 L/min
0.2 kg/L
x(t)
100 L
4 L/min
x(0) = 0 kg
3 L/min
B
y(t)
100 L
y(0) = 20 kg
2 L/min
1 L/min
Figure Q1 - Mixing problem for interconnected tanks
Determine the mass of salt in each tank at time t > 0:
Analytically (hand calculations)
Two springs and two masses are attached in a straight vertical line as shown in Figure Q3. The system is set
in motion by holding the mass m₂ at its equilibrium position and pushing the mass m₁ downwards of its
equilibrium position a distance 2 m and then releasing both masses. if m₁ = m₂ = 1 kg, k₁ = 3 N/m and
k₂ = 2 N/m.
www.m
k₁ = 3
(y₁ = 0).
m₁ = 1
k2=2
(y₂ = 0)
|m₂ = 1
Y2
y 2
System in
static
equilibrium
(Net change in
spring length
=32-31)
System in
motion
Figure Q3 - Coupled mass-spring system
Determine the equations of motion y₁(t) and y₂(t) for the two masses m₁ and m₂ respectively:
Analytically (hand calculations)
100
As a spring is heated, its spring constant decreases. Suppose the spring is heated and then cooled so that the
spring constant at time t is k(t) = t sin N/m. If the mass-spring system has mass m = 2 kg and a
damping constant b = 1 N-sec/m with initial conditions x(0) = 6 m and x'(0) = -5 m/sec and it is
subjected to the harmonic external force f(t) = 100 cos 3t N. Find at least the first four nonzero terms in
a power series expansion about t = 0, i.e. Maclaurin series expansion, for the displacement:
Analytically (hand calculations)
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