CL 351 Homework # 3
Due date:
1.
The dissolution of lead from lead-soldered joints in
household piping is a possible health problem.
If the water flowing through the pipe is mildly acidic, then some of the
lead will dissolve from the inner surface of the lead-soldered pipe section
into the water. New drinking water
requirements stipulate that soluble lead concentration levels should not exceed
0.015 g/m3. At present, water
flows through a 0.025 m
2.
A stirred tank fermenter is used to cultivate
aerobic micro-organisms in aqueous suspension.
The aerobic cells require dissolved oxygen for respiration, which is
supplied by aerating the liquid medium.
An important design parameter for specifying the oxygen mass transfer
rate in the fermenter is the volumetric mass transfer coefficient, kLa. Based on power per unit volume of 1572 W/m3,
aeration rate of 1m3 per minute, tank diameter of 1.5 m and liquid
volume of 2 m3, determine the volumetric mass transfer coefficient
and the oxygen mass transfer rate in .
Assume that the cells immediately consume the dissolved oxygen, so that
the oxygen concentration in the liquid medium is essentially zero. The Henry’s law constant for oxygen in water
is 52, 500 bars. Use correlation
developed in the class.
3.
A disk of radioactively tagged benzoic acid 1 centimeter
in diameter is spinning at 20 revolutions per minute in 94 cc of initially pure
water. We find that the solution
contains benzoic acid at 7.3 x 10-4 g/cc after 10 hours 4 minutes
and 3.43 x 10-3 g/cc after a long time. What is the mass transfer coefficient? How long will it take to reach fourteen
percent saturation? How closely does
this mass transfer coefficient agree with that expected from correlation? For correlation of mass transfer coefficient from
a spinning disk, see handouts available in Hostel 10 photocopy room.
4.
Trichloroethylene (TCE), a common industrial
solvent, is often found at low concentrations in industrial waste waters. Stripping is a common process for removing
sparingly soluble, volatile organic solutes such as TCE from aqueous
solution. A wetted wall column is used
to study the stripping of TCE from water to air at a constant temperature of
293 K and a total system pressure of 1 atm.
The column inner diameter is 4 cm and height is 2 m. In the present process, the volumetric air
flow rate into the column is 2000 cm3/sec and water is falling at a
velocity of 0.5 m/sec. Estimate, the
overall liquid side mass transfer coefficient for TCE across the liquid and gas
film. To predict mass transfer
coefficient on gas side use the correlation given in Problem 1. For mass transfer coefficient from a falling
film (liquid side), see handouts available in Hostel 10 photocopy room.
The process is dilute so that the bulk gas has properties
of air and bulk liquid has properties of water.
The Henry’s law constant for TCE is 550 atm at 293 K. Diffusivity of TCE in air is 8.08 x 10-6 m2/sec
and that in water is 2 x 10-9 m2/sec.