A concentric lube arrangement, for which the inner and outer diameters are 8 0 mm and 100 mm . respectively, is used to remove heat from a biochemical reaction occurring in a 1 − m -long settling tank. Heat is generated uniformly within the tank at a rate of 10 5 W/m 3 , and water is supplied to the annular region at a rate of 0. 2 kg / s . (a) Determine the inlet temperature of the supply water that will maintain an average tank surface temperature of 37 ° C . Assume fully developed flow and thermal conditions. Is this assumption reasonable? (b) It is desired to have a slight, axial temperature gradient on the tank surface, since the rate of the biochemical reaction is highly temperature dependent. Sketch the axial variation of the water and surface temperatures along the flow direction for the following two cases: (i) the fully developed conditions of part (a), and (ii) conditions for which entrance effects are important. Comment on features of the temperature distributions. What change to the system or operating conditions would you make to reduce the surface temperature gradient?
A concentric lube arrangement, for which the inner and outer diameters are 8 0 mm and 100 mm . respectively, is used to remove heat from a biochemical reaction occurring in a 1 − m -long settling tank. Heat is generated uniformly within the tank at a rate of 10 5 W/m 3 , and water is supplied to the annular region at a rate of 0. 2 kg / s . (a) Determine the inlet temperature of the supply water that will maintain an average tank surface temperature of 37 ° C . Assume fully developed flow and thermal conditions. Is this assumption reasonable? (b) It is desired to have a slight, axial temperature gradient on the tank surface, since the rate of the biochemical reaction is highly temperature dependent. Sketch the axial variation of the water and surface temperatures along the flow direction for the following two cases: (i) the fully developed conditions of part (a), and (ii) conditions for which entrance effects are important. Comment on features of the temperature distributions. What change to the system or operating conditions would you make to reduce the surface temperature gradient?
Solution Summary: The author calculates the water properties at temperature 304 k and the convection rate equation applied to the inner surface.
A concentric lube arrangement, for which the inner and outer diameters are
8
0
mm
and
100
mm
. respectively, is used to remove heat from a biochemical reaction occurring in a
1
−
m
-long settling tank. Heat is generated uniformly within the tank at a rate of
10
5
W/m
3
, and water is supplied to the annular region at a rate of
0.
2 kg
/
s
.
(a) Determine the inlet temperature of the supply water that will maintain an average tank surface temperature of
37
°
C
. Assume fully developed flow and thermal conditions. Is this assumption reasonable?
(b) It is desired to have a slight, axial temperature gradient on the tank surface, since the rate of the biochemical reaction is highly temperature dependent. Sketch the axial variation of the water and surface temperatures along the flow direction for the following two cases: (i) the fully developed conditions of part (a), and (ii) conditions for which entrance effects are important. Comment on features of the temperature distributions. What change to the system or operating conditions would you make to reduce the surface temperature gradient?
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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