A mass transfer Operation is preceded by laminar flow of a gaseous species B through a circular tube that is sufficiently long to achieve a fully developed velocity profile. Once the fully developed condition is reached. The gas enters a section of the tube that is wetted with a liquid film (A). The film maintains a uniform vapor density ρ A,s , along the tube surface. (a) Write the differential equation and boundary conditions that govern the species A mass density distribution, ρ A ( x , r ) , for x > 0 . (b) What is the heat transfer analog to this problem? From this analog, write an expression for the average Sherwood number associated with mass exchange over the region 0 ≤ x ≤ L . (c) Beginning with application of conservation of species to a differential control volume of extent π r o 2 d x , derive an expression (Equation 8.86) that may be used to determine the mean vapor density ρ A , m , o at x = L . (d) Consider conditions for which species B is air at 25 ° C and 1 atm and the liquid him consists of water,also at 25 ° C . The flow rate is m ˙ = 2.5 × 10 − 4 kg/s , and the tube diameter is D = 10 mm . What is the mean vapor density at the tube outlet if L = 1 mm ?
A mass transfer Operation is preceded by laminar flow of a gaseous species B through a circular tube that is sufficiently long to achieve a fully developed velocity profile. Once the fully developed condition is reached. The gas enters a section of the tube that is wetted with a liquid film (A). The film maintains a uniform vapor density ρ A,s , along the tube surface. (a) Write the differential equation and boundary conditions that govern the species A mass density distribution, ρ A ( x , r ) , for x > 0 . (b) What is the heat transfer analog to this problem? From this analog, write an expression for the average Sherwood number associated with mass exchange over the region 0 ≤ x ≤ L . (c) Beginning with application of conservation of species to a differential control volume of extent π r o 2 d x , derive an expression (Equation 8.86) that may be used to determine the mean vapor density ρ A , m , o at x = L . (d) Consider conditions for which species B is air at 25 ° C and 1 atm and the liquid him consists of water,also at 25 ° C . The flow rate is m ˙ = 2.5 × 10 − 4 kg/s , and the tube diameter is D = 10 mm . What is the mean vapor density at the tube outlet if L = 1 mm ?
Solution Summary: The author explains the governing differential equation and boundary conditions for the species.
A mass transfer Operation is preceded by laminar flow of a gaseous species B through a circular tube that is sufficiently long to achieve a fully developed velocity profile. Once the fully developed condition is reached. The gas enters a section of the tube that is wetted with a liquid film (A). The film maintains a uniform vapor density
ρ
A,s
, along the tube surface.
(a) Write the differential equation and boundary conditions that govern the species A mass density distribution,
ρ
A
(
x
,
r
)
,
for
x
>
0
. (b) What is the heat transfer analog to this problem? From this analog, write an expression for the average Sherwood number associated with mass exchange over the region
0
≤
x
≤
L
. (c) Beginning with application of conservation of species to a differential control volume of extent
π
r
o
2
d
x
, derive an expression (Equation 8.86) that may be used to determine the mean vapor density
ρ
A
,
m
,
o
at
x
=
L
. (d) Consider conditions for which species B is air at
25
°
C
and
1 atm
and the liquid him consists of water,also at
25
°
C
. The flow rate is
m
˙
=
2.5
×
10
−
4
kg/s
, and the tube diameter is
D
=
10
mm
. What is the mean vapor density at the tube outlet if
L
=
1
mm
?
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.
(a) Write short notes about the following as they are applied in fluid mechanics
(i) Uniform flow
(ii) Uniform stead flow
(b)Consider a cylinder of fluid of length L and radius R flowing steadily in the centre of a pipe of radius r as shown below
L
r R
Show that when the flow in the pipe is laminar the pressure loss is directly proportional to the velocity and obeys the equation
Where v is the velocity D is the diameter of the pipe
A large cone-shaped container (height H and radius R) is fed a liquid solution of density ρ at aconstant flow rate q0 . The solution evaporates from its top surface exposed to the sun.(a) Assuming that the rate of evaporation is proportional to the area of the surface with aconstant K (kg/m 2 .s), develop a differential equation for the variation with time of the level ofthe liquid in the container.(b) What should be the feed flow rate to maintain the fluid level constant once it reaches adesired value h*?(c) If the feed was zero, would the rate of change of the level of the fluid depend on the shapeof the cone-shaped container (H,R dimensions)
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