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CHE 4 4 7 : Heat and Mass Transfer in Chemical Engineering Processes Homework Problem Set # 1 Due Thursday January 1 8 , 2

CHE 447: Heat and Mass Transfer in Chemical Engineering Processes
Homework Problem Set #1
Due Thursday January 18,2024 before 11:59 PM on Blackboard.
Consider a stagnant, conical pipe containing "species A" with the concentration profile
and L=10cm. At z=0, the radius of the pipe 1
cm and at z=10cm, the radius of the pipe is 3cm. Assume that the concentration profile
is radially uniform for a given value of z. Calculate the total moles of species A within the
pipe.
Consider an open-top, well-mixed tank. At time =0s, the contents are drained by gravity
through a circular hole at the bottom with area A1=0.1m2. Also at time =0s, a stream
containing species A at a concentration CA0=10molm3 is pumped into the top of the tank
at a constant flow rate Fin=0.8m3s. The tank has a cross-sectional area A2=10m2 and
is initially filled with water at a height h=5m. The initial concentration of species A in the
tank is 0molm3.
a. Perform an overall mass balance on the liquid contents of the tank to derive an
equation for dhdt, the rate of change of the liquid level, as a function of Fin, A2,
A1,h, and g(the gravitational constant). Assume that the velocity of the liquid level
in the tank (v2) is significantly less than the exit velocity of the fluid through the
drainage hole (v1). Assume that the density of the liquid is constant and unaffected
by the mixing of species A.
b. Solve the differential equation in part a and plot h as a function of time over the
interval 0t600 seconds.
c. Perform a mass balance on species A to derive an equation for dCAdt as a
function of Fin,A2,A1,h,g,CA and CA0. Solve this differential equation and plot CA
as a function of time over the interval 0t600 seconds. Also plot the total moles
in the system or {:A2**h**CA) in a separate plot, using the same time interval.
d. Is the assumption v1v2 valid? Justify your answer.
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