Air flowing through a tube of 75 − mm diameter passes over a 150-nuniong roughened Section that is constructed from naphthalene having the properties M = 128.16 kg / kmol and p s a t ( 300 K ) = 1.31 × 10 − 4 bar. The air is at 1 atmand 3 00 K , and the Reynolds number is R e D = 35 , 000 . In an experiment for which flow was maintained for 3 h. mass loss due to sublimation from the roughened surface was determined to be 0.0 1 kg . What is the associated convection mass transfer coefficient? What would be the corresponding convection heat transfer coefficient? Contrast these results with those predicted by conventional smooth tube correlations.
Air flowing through a tube of 75 − mm diameter passes over a 150-nuniong roughened Section that is constructed from naphthalene having the properties M = 128.16 kg / kmol and p s a t ( 300 K ) = 1.31 × 10 − 4 bar. The air is at 1 atmand 3 00 K , and the Reynolds number is R e D = 35 , 000 . In an experiment for which flow was maintained for 3 h. mass loss due to sublimation from the roughened surface was determined to be 0.0 1 kg . What is the associated convection mass transfer coefficient? What would be the corresponding convection heat transfer coefficient? Contrast these results with those predicted by conventional smooth tube correlations.
Solution Summary: The author compares the results with conventional smooth tube correlations. The convection mass transfer coefficient is 3.89times 10-4m/s
Air flowing through a tube of
75
−
mm
diameter passes over a 150-nuniong roughened Section that is constructed from naphthalene having the properties
M
=
128.16
kg
/
kmol
and
p
s
a
t
(
300
K
)
=
1.31
×
10
−
4
bar. The air is at 1 atmand
3
00
K
, and the Reynolds number is
R
e
D
=
35
,
000
. In an experiment for which flow was maintained for 3 h. mass loss due to sublimation from the roughened surface was determined to be
0.0
1 kg
. What is the associated convection mass transfer coefficient? What would be the corresponding convection heat transfer coefficient? Contrast these results with those predicted by conventional smooth tube correlations.
Net movement of mass from one location, usually meaning stream, phase, fraction, or component, to another. Mass transfer occurs in many processes, such as absorption, evaporation, drying, precipitation, membrane filtration, and distillation.
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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