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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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UNIVERSITY OF ARIZONA DEPARTMENT OF CHEMICAL AND ENVIRONMENTAL ENGINEERING CHEE 502 - ADVANCED CHEMICAL ENGINEERING ANALYSIS FALL 2008
Problem Set 8
bIN t
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
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 τ = x=aN*z (^) * I
u = (^) * 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 ).
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
η=
dy
dv 1
where ε«1. Use a regular perturbation analysis to find the velocity profile with an accuracy of O(ε^1 ).