Consider the microchannel cooling arrangement ofProblem 8.107. However, instead of assuming theentire chip and cap to be at a uniform temperature.adopt a more conservative (and realistic) approach thatprescribes a temperature of T s = 350 K at the base ofthe channels ( x = 0 ) and allows for a decrease in temperature with increasing x along the side walls of eachchannel. (a) For the operating conditions prescribed in Problem 8.107 and a chip thermal conductivity of k c h = 140 W/m ⋅ K , determine the water outlet temperature and the chip power dissipation. Heat transfer from the sides of the chip to the surroundings and from the side walls of a channel to the cap may be neglected. Note that the spacing between channels. δ = S − W , is twice the spacing between the side wall of an outer channel and the outer surface of the chip. The channel pitch is S = L / N , where L = 1 0 mm is the chip width and N = 5 0 is the number of channels (b) The channel geometry prescribed in Problem 8.107 and considered in part (a) is not optimized, and larger heat rates may be dissipated by adjusting related dimensions. Consider the effect of reducing the pitch to a value of S = 100 μ m . while retaining a width of W = 50 μ m and a flow rate per channel of m 1 = 10 − 4 kg/s.
Consider the microchannel cooling arrangement ofProblem 8.107. However, instead of assuming theentire chip and cap to be at a uniform temperature.adopt a more conservative (and realistic) approach thatprescribes a temperature of T s = 350 K at the base ofthe channels ( x = 0 ) and allows for a decrease in temperature with increasing x along the side walls of eachchannel. (a) For the operating conditions prescribed in Problem 8.107 and a chip thermal conductivity of k c h = 140 W/m ⋅ K , determine the water outlet temperature and the chip power dissipation. Heat transfer from the sides of the chip to the surroundings and from the side walls of a channel to the cap may be neglected. Note that the spacing between channels. δ = S − W , is twice the spacing between the side wall of an outer channel and the outer surface of the chip. The channel pitch is S = L / N , where L = 1 0 mm is the chip width and N = 5 0 is the number of channels (b) The channel geometry prescribed in Problem 8.107 and considered in part (a) is not optimized, and larger heat rates may be dissipated by adjusting related dimensions. Consider the effect of reducing the pitch to a value of S = 100 μ m . while retaining a width of W = 50 μ m and a flow rate per channel of m 1 = 10 − 4 kg/s.
Solution Summary: The author describes the water outlet temperature, chip power dissipation, and thermal conductivity of the chip. The expression for the hydraulic diameter is given as, mathrmRe_D
Consider the microchannel cooling arrangement ofProblem 8.107. However, instead of assuming theentire chip and cap to be at a uniform temperature.adopt a more conservative (and realistic) approach thatprescribes a temperature of
T
s
=
350
K at the base ofthe channels (
x
=
0
) and allows for a decrease in temperature with increasing x along the side walls of eachchannel.
(a) For the operating conditions prescribed in Problem 8.107 and a chip thermal conductivity of
k
c
h
=
140
W/m
⋅
K
, determine the water outlet temperature and the chip power dissipation. Heat transfer from the sides of the chip to the surroundings and from the side walls of a channel to the cap may be neglected. Note that the spacing between channels.
δ
=
S
−
W
, is twice the spacing between the side wall of an outer channel and the outer surface of the chip. The channel pitch is
S
=
L
/
N
, where
L
=
1
0
mm
is the chip width and
N
=
5
0
is the number of channels
(b) The channel geometry prescribed in Problem 8.107 and considered in part (a) is not optimized, and larger heat rates may be dissipated by adjusting related dimensions. Consider the effect of reducing the pitch to a value of
S
=
100
μ
m
. while retaining a width of
W
=
50
μ
m
and a flow rate per channel of
m
1
=
10
−
4
kg/s.
1. A 40 lb. force is applied at point E. There are pins at
A, B, C, D, and F and a roller at A.
a. Draw a FBD of member EFC showing all the known and
unknown forces acting on it.
b. Draw a FBD of member ABF showing all the known and
unknown forces acting on it.
c. Draw a FBD of member BCD showing all the known and
unknown forces acting on it.
d. Draw a FBD of the entire assembly ADE showing all the
known and unknown forces acting on it.
e. Determine the reactions at A and D.
f. Determine the magnitude of the pin reaction at C.
40 lbs.
B
A
6 in.
4 in.
D
F
-5 in.4 in 4.
A crude oil of specific gravity0.85 flows upward at a volumetric rate of flow of 70litres per
second through
a vertical
venturimeter,with an inlet diameter of 250 mm and a throat
diameter of 150mm. The coefficient
of discharge of venturimeter is 0.96. The vertical
differences betwecen the pressure toppings is
350mm.
i)
Draw a well labeled diagram to represent the above in formation
i)
If the two pressure gauges are connected at the tapings such that they are
positioned at the levels of their corresponding tapping points,
determine the
difference of readings in N/CM² of the two pressure gauges
ii)
If a mercury differential
manometer
is connected in place of pressure gauges,
to the tappings such that the connecting tube up to mercury are filled with oil
determine the difference in the level of mercury column.
Can you solve it analytically using laplace transforms and with Matlab code as well please. Thank You
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