Advanced Chemical Engineering Analysis: Problem Sets for CHEE 502 (University of Arizona) , Assignments of Chemistry

Problem sets for the university of arizona's chee 502 advanced chemical engineering analysis course, focusing on topics such as algae growth in stagnant ponds and non-newtonian fluid flow between parallel plates. Students are expected to apply advanced chemical engineering principles and analytical methods to solve these problems.

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Pre 2010

Uploaded on 08/26/2009

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UNIVERSITY OF ARIZONA
DEPARTMENT OF CHEMICAL AND ENVIRONMENTAL ENGINEERING
CHEE 502 - ADVANCED CHEMICAL ENGINEERING ANALYSIS
FALL 2008
Problem Set 8
1. Consider the spontaneous growth of algae in water, in the region close to the surface of a
stagnant pond. We will assume that the only factor limiting algal growth is light, and we will
also consider that diffusion of algae is very slow. Under these conditions, at any point in the
pond, the rate of growth of algae is a first order process with respect to algae concentration, with
a rate constant that is proportional to the intensity of light. A mass balance in algae leads to
bIN
t
N=
where N is algae concentration, I is intensity of light, b is a constant, and t is time measured so
that t=0 represents sunrise. If we assume that the most important factor that affects light
attenuation is the presence of algae, the change of light intensity with position is given by Beer's
law, with an extinction coefficient directly proportional to algae concentration,
aIN
z
I=
where a is a constant and z represents depth in the pond. Initial and boundary conditions are
N=N
*
, t=0
where N
*
is a constant (i.e., algae concentration in the pond at sunrise is uniform); and
I=I
*
sin(
π
t/T), z=0
where T is the length of the day, and I
*
is the maximum incident light, which occurs at midday.
(a) Formulate the problem in terms of the following dimensionless variables:
T
t
=τ
x=aN
*
z
*
I
I
u
=
*
N
N
v
=
(b) Find u(
τ
,x) and v(
τ
,x) for the case in which algae growth is slow (
ε
=bI
*
T
0). Formulate
your results in terms of asymptotic expansions that include terms of O(
ε
1
).
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UNIVERSITY OF ARIZONA DEPARTMENT OF CHEMICAL AND ENVIRONMENTAL ENGINEERING CHEE 502 - ADVANCED CHEMICAL ENGINEERING ANALYSIS FALL 2008

Problem Set 8

  1. Consider the spontaneous growth of algae in water, in the region close to the surface of a stagnant pond. We will assume that the only factor limiting algal growth is light, and we will also consider that diffusion of algae is very slow. Under these conditions, at any point in the pond, the rate of growth of algae is a first order process with respect to algae concentration, with a rate constant that is proportional to the intensity of light. A mass balance in algae leads to

bIN t

N

where N is algae concentration, I is intensity of light, b is a constant, and t is time measured so that t=0 represents sunrise. If we assume that the most important factor that affects light attenuation is the presence of algae, the change of light intensity with position is given by Beer's law, with an extinction coefficient directly proportional to algae concentration,

aIN z

I

where a is a constant and z represents depth in the pond. Initial and boundary conditions are

N=N*, t=

where N*^ is a constant (i.e., algae concentration in the pond at sunrise is uniform); and

I=I*sin(πt/T), z=

where T is the length of the day, and I*^ is the maximum incident light, which occurs at midday.

(a) Formulate the problem in terms of the following dimensionless variables:

T

t τ = x=aN*z (^) * I

I

u = (^) * N

N

v =

(b) Find u(τ,x) and v(τ,x) for the case in which algae growth is slow (ε=bI*T→0). Formulate your results in terms of asymptotic expansions that include terms of O(ε^1 ).

  1. The steady state, pressure-driven flow of a non-Newtonian fluid between parallel plates can be represented in dimensionless form by the ODE

dy

dv dy

d =− 

η

where y is dimensionless position in the direction perpendicular to the flow, v is the dimensionless velocity, and η is the dimensionless non-Newtonian viscosity. Appropriate boundary conditions for this model are

v=0, y=0 (no-slip condition)

dy

dv = , y=1 (symmetry)

We will consider the onset of non-Newtonian effects, i.e. we will analyze the velocity profile for a fluid whose viscosity exhibits a weak dependence on shear rate, given by

  • ε

η=

dy

dv 1

where ε«1. Use a regular perturbation analysis to find the velocity profile with an accuracy of O(ε^1 ).