Name _________________________________
Final Exam
December 21, 2006
Closed book, 3 sheets of notes allowed.
Show all work. Be
neat, and box-in your answer.
If you cannot
finish a problem (e.g., due to lack of time, or a missing formula), explain on
your exam paper how you would have completed it.
Answer:
·
Question #1 (20%)
·
Question #2 (15%)
·
one from the next three questions (#3 - #
5) (15%) ________________
·
Question #6 (30%)
·
Question
#7 (5%)
·
one from the last four questions #8 - #11
(15%) ________________
total is 100%
**********************************************************************
Answer both of the first two questions #1 & #2
1.
Stoichiometry (20 points)
Aerobic heterotrophic bacteria can facilitate the following unbalanced
biochemical transformation of glucose:
C6H12O6
+ O2 ® CO2 + H2O
A. Which element (and in which chemical
species) is being oxidized in this reaction and what is its initial and final
oxidation state?
B. Which element (and in which chemical
species) is being reduced in this reaction and what is its initial and final
oxidation state?
C. Balance the glucose-oxygen reaction.
D. Determine the Theoretical Oxygen Demand
(ThOD) of a 25 mg/L solution of glucose.
2.
Reactor Kinetics (15 points)
A. A flow of 20 L/min of water
is to be treated in a plug flow reactor (PFR).
What reactor volume (L) is needed to achieve 95% removal of a
contaminant with a first order decay rate of 0.20 min-1?
B. Calculate the volume needed
if the water is to be treated for 95% removal in an ideal complete mix flow
reactor (CMFR).
Answer one of the next three questions #3 - #5
3.
Solid Waste (15 points)
A. How much sawdust (total
weight) must be added to a waste sludge to lower the moisture content to 60% so
that it can be composted? Assume you
have 1000 kg of sludge (dry weight). The
sludge (as discarded) is 12% dry solids, 88% moisture, and the sawdust is 75% dry
solids, 25% moisture.
B. If the sludge were dewatered
such that the total solids were 30% (rather than 12%) how much sawdust (total
weight) would be needed for the same situation?
4. Hazardous
Waste (15 points)
Chlorine may be used to destroy cyanide ion (CN-) in industrial
wastes, producing nitrogen gas and bicarbonate.
The chlorine is commonly added as sodium hypochlorite (NaOCl). The reactions that occur are as follows:

And:

A. If you had 100 kg of cyanide, how many kilograms of sodium
hypochlorite would be needed?
B. How many moles of sodium hydroxide (NaOH) or hydrochloric
acid (HCl) would also be needed to neutralize the reaction mixture if you
started with 1 mole of cyanide and the requisite amount of sodium hypochlorite?
5. Air
Pollution & Hazardous Waste, short answer (15 points)
A. Describe at least two ways
that particulate air contaminants can be removed from gaseous emissions. Be as specific as possible.
B. Describe how acidic gases
can be removed from incinerator waste gases.
Include a diagram with your description.
C. Describe two in-situ cleanup
methods for site remediation of soil contaminated with hazardous wastes.
D. Describe the characteristics
of a hazardous waste, and how a waste might be defined as "hazardous"
under the law.
Answer questions #6 and #7
6. Water
Quality Modeling (30 points)
The Intercontinental Paper Co. is discharging its wastewater directly into
the Mill River.
The discharge flow is 3.8 ft3/s (cfs) the discharge D.O. is 5.5
mg/L and the discharge ultimate BOD (BODult) is 35 mg/L. They obtain half of this water from an intake
0.5 miles upstream of the wastewater outfall, and half from groundwater via a
nearby well field. On average, the Mill River
water upstream of the IPC outfall has an ultimate BOD (BODult) of
2.5 mg/L and a D.O. of 8.5 mg/L. If the
Mill River has a flow of 12 cfs upstream of the IPC intake, and if the state
permits a minimum DO of 7.5 mg/L in the Mill River, will the state have to
further restrict the BOD in IPC's wastewater (i.e., is the stream out of
compliance)? Calculate the minimum
stream D.O. expected as a result of the IPC discharge.
Additional assumptions: BOD deoxygenation rate: k1(or
kd) = 0.23 d-1
reaeration
rate constant (k2 or kr) of 0.82 d-1
D.O
saturation concentration = 9.5 mg/L
River
flow velocity = 0.5 ft/s

7. BOD
(5 points)
If the ultimate BOD of a wastewater is 350 mg/L and the kL is
0.25 d-1, what is the BOD5 ?
Answer one of the following four
questions #8 - #11
8. Chemical
Oxidation (15 points)
The oxidation of ferrous iron (Fe+2) by oxygen occurs in readily
in water forming ferric hydroxide precipitate (Fe(OH)3(s)):
A. Write the two half cell reactions and balance each one.
B. Write the overall balanced reaction
C. How much oxygen (in mg/L)
is required to oxidize 1.5 mg/L of ferrous iron and how much ferric hydroxide
precipitate is formed?
9. Groundwater
Flow (15 points)
The flow velocity (Darcy velocity) of water between two wells spaced 100 m
apart has been documented at 0.003 m/day during a long dry period. During this time, the water surface elevation
in the two wells was 335.93 m and 335.49 m.
During periods of heavy recharge, the water levels rise to 342.85 m and
340.79 m respectively. What is the Darcy
velocity between these wells under the heavy recharge period?
10. Biological
Growth Kinetics (15 points)
You have been studying the performance of a CMFR biological reactor. Your wastewater supports a specific bacterial
growth rate of 0.25 d-1. Under
these conditions, the effluent substrate (waste) concentration is 0.4
mg/L. When you increase your wastewater
strength such that the final substrate concentration leaving the CMFR is
doubled to 0.8 mg/L, you observe a specific growth rate of 0.35 d-1. From these data estimate the two Monod
coefficients, Ks and mmax.
11. Reactor
Kinetics (15 points)
You have a wastewater flow rate of 1000 L/hr. To treat this wastewater you have constructed
a concrete tank of 100,000 liters. The
wastewater contains the deadly compound, 2-methyl-3-chloro-4-anisole sulfonate
(MCAS). Kinetic studies have shown the
MCAS to degrade by a 1st order reaction with a half-life of 40
hours.
a. What
is the % removal of MCAS if the reactor is operated as a plug flow reaction (PRF)?
b. What
is the % removal of MCAS if the reactor is operated as a completely mixed flow
reactor (CMFR)?
Appendix
Some physical
constants of Water:
Temp., oC
|
Density, kg/m3
|
Viscosity,
N-s/m2
|
Kinematic
Viscosity, m2/s
|
0
|
999.8
|
1.781x10-3
|
1.785x10-6
|
5
|
1000.0
|
1.518 x10-3
|
1.519x10-6
|
10
|
999.7
|
1.307 x10-3
|
1.306 x10-6
|
15
|
999.1
|
1.139 x10-3
|
1.139 x10-6
|
20
|
998.2
|
1.002 x10-3
|
1.003 x10-6
|
25
|
997.0
|
0.890 x10-3
|
0.893 x10-6
|
30
|
995.7
|
0.798 x10-3
|
0.800 x10-6
|
35
|
994.0
|
0.725 x10-3
|
0.729 x10-6
|
40
|
992.2
|
0.653
x10-3
|
0.658
x10-6
|
Selected Chemical
Constants
Element
|
Symbol
|
Atomic #
|
Atomic Wt.
|
Valence
|
Electronegativity
|
Aluminum
|
Al
|
13
|
26.98
|
3
|
1.47
|
Boron
|
B
|
5
|
10.81
|
3
|
2.01
|
Calcium
|
Ca
|
20
|
40.08
|
2
|
1.04
|
Carbon
|
C
|
6
|
12.01
|
2,4
|
2.50
|
Cerium
|
Ce
|
58
|
140.12
|
3,4
|
1.06
|
Chlorine
|
Cl
|
17
|
35.453
|
1
|
|
Holmiuum
|
Ho
|
67
|
164.93
|
3
|
1.10
|
Hydrogen
|
H
|
1
|
1.01
|
1
|
2.20
|
Iron
|
Fe
|
26
|
55.85
|
2,3
|
|
Magnesium
|
Mg
|
12
|
24.31
|
2
|
1.23
|
Manganese
|
Mn
|
25
|
54.94
|
2,3,4,6,7
|
1.60
|
Nitrogen
|
N
|
7
|
14.0067
|
3
|
|
Osmium
|
Os
|
76
|
190.2
|
2,3,4,8
|
1.52
|
Oxygen
|
O
|
8
|
16.00
|
2
|
3.50
|
Potassium
|
K
|
19
|
39.10
|
1
|
0.91
|
Sodium
|
Na
|
11
|
22.99
|
1
|
1.01
|
Sulfur
|
S
|
16
|
32.06
|
2,4,6
|
2.44
|
|
|
|
|
|
|
|
Useful
conversion factors

1 ft = 0.305 m