Transcript ENVS4450 - Robert Morris University

Environmental Modeling
Chapter 7:
Dissolved Oxygen Sag Curves in Streams
Copyright © 2006 by DBS
Quote
“[Mathematics] The handmaiden
of the Sciences”
-Eric Temple Bell
Concepts
•
•
•
•
•
Introduction
Input sources
Mathematical Model
Sensitivity analysis
Limitations
Case Study: Any Stream, Anywhere
•
Every stream has inputs of
organic waste
– Spreads disease
– Consumes DO on
decomposition
•
Ancient communities built
near flowing water
e.g. NY City, London,
W. Europe
Meadows et al., 2004
ChemicalCase
process:Study:
Any Stream, Anywhere
MO’s consume DO
Physical process:
Re-aeration by
atmosphere
The Problem: D.O. < BOD
Sewage treatment begins
Introduction
•
Modeling the effects of release of oxidizable organic matter into a
flowing body of water
– DO = chemical measurement of dissolved oxygen (mg L-1)
– BOD = total DO needed to oxidize organic matter in a water sample
= change from initial DO at saturation to amount after 5 days
BOD
time
Wipple and Wipple (1911)
Introduction
•
Standard of living ~ adequate water and
wastewater treatment
Human Risks
• Challenge of preventing rapid spead of disease
e.g. typhoid fever (bacteria), hepatitis (viruses),
cryptosporidosis (protozoa)
• Removed by sand filtration and
chlorination/ozonation
Aquatic Risks
• Aerobic organisms depend on DO
• 8-12 mg L-1
• Affected by temperature and salt
Inc. salt dec. DO
Organic matter is oxidized,
stream re-aerates
The Streeter-Phelps
Equation
without trmt:
with trmt:
End
• Review
Basic Input Sources
•
Parameters for S-P equation:
– Wastewater: Flow rate, temperature, DO, BOD
•
BOD measured in lab – DO measured after several days (flat portion
of curve)
• The following material and model is
covered in:
CHEM3500/3550
Basic Input Sources
Sewage Treatment Plants
•
Remove turbidity, oxidizable organic matter, and pathogens
– Turbidity – settling tanks and filters
– Organic matter – trickling filters, activated sludge
– Pathogens – filtration, chloination, ozonation
ftp://ftp.wiley.com/public/sci_tech_med/pollutant_fate/
Basic Input Sources
Sewage Treatment Plants
•
Prelininary - screening of large materials
•
Primary - sedimentation - settling tanks
•
Secondary - biological aeration – trickling
filters, activated sludge - metabolizes and
flocculates dissolved organics
•
Tertiary – e.g. P removal
http://www.waterencyclopedia.com/Tw-Z/Wastewater-Treatment-and-Management.html
Basic Input Sources
•
Wastewater Treatment Plant
Model
Movie
1. Wastewater Treatment and Discharge (2000)
2. Wastewater Generation and Collection (2000)
3. Our Urban Environment: Water Quality (2000)
End
• Review
Mathematical Model
Take a river: What parameters and processes would be important in
developing a model for the oxidation of organic waste?
Amount DO consumed
our model river: draw in parameters
Re-aeration by atmosphere
Consumption DO by MO’s
Ultimate BODLof mix
Stream DO deficit
The Streeter-Phelps Equation
D = k’BODL [exp(-k’(x/v) – exp(-k2’(x/v))] + D0exp(-k2’(x/v))
k2’ – k’
Consumption by MO’s
where:
Re-aeration by atmos. O2
D = DO concentration deficit (value below saturation) (mg L-1),
k’2= the re-aeration constant (in d-1),
BODL= the ultimate BOD (in mg L-1),
k’= the BOD rate constant for oxidation (d-1),
x = distance downstream from the point source (km),
v = average water velocity (km d-1)
Do= initial oxygen deficit of mixed stream and wastewater (mg L-1)
D is not the remaining DO content but the amount of original DO
consumed…must be subtracted from original DO without BOD waste
The Streeter-Phelps Equation
DO at a given distance below the input:
The Streeter-Phelps Equation
• k2’ = first-order rate constant for re-aeration
• Eact measurements are difficult, get from tables:
The Streeter-Phelps Equation
• BODL = ultimate BOD or maximum O2 required to oxize the
waste sample
• Determined from 5 day BOD test or using equation:
BODL =
BOD5
1 – exp(-k’(x/v))
• Where k’ is obtained from a 20 day BOD experiment
• D0 = DO level in the stream upstream from input - initial DO of
stream-waste mixture
Algae, fungi, protozoa, worms,
larger planst die
Gray/black, H2S, CH4, NH3
productions,
The Streeter-Phelps Equation
Zone of Clean Water (Zone 1)
Zone of Degradation (Zone 2)
Zone of Active Decomposition (Zone 3)
Zone of Recovery (Zone 4)
Zone of Cleaner Water (Zone 5)
Minimum D = critical
dissolved oxygen = Dc
The Streeter-Phelps Equation
tc =
1
k2’ – k’
ln k2’ 1 – D0(k2’-k’)
k’
k’ BODL
and xc = vtc
Critical DO concentration, Dc:
Dc =
k’ BODL exp(-k’(xc/v))
k 2’
Problem
Example Problem: A city discharges 25 million gallons per day of domestic
sewage into a stream whose typical rate of flow is 250 cubic feet per second.
The velocity of the stream is appoximately 3 miles per hour. The temperature
of the sewage is 21 °C, while that of the stream is 15 °C. The 20 °C BOD5 of
the sewage is 180 mg/L, while that of the stream is 1.0 mg/L. The sewage
contains no DO, but the stream is 90% saturated upstream of the discharge.
At 20 °C, k’ is estimated to be 0.34 per day while k2’ is 0.65 per day.
1. Determine Dc and its location.
2. Estimate the 20 °C BOD5 of a sample taken at xc.
3. Plot the curve.
1. Determine DO in stream before discharge (=upstream DO):
Saturation conc. at 15 °C = 10.2 mg/L
Upstream is 90% saturated = 10.2 mg/L x 0.90 = 9.2 mg/L
2. Determine mixture, T, DO, and BOD using mass balance:
Flow rate stream: = 250 ft3/s = 612 x 106 L/d
Flow rate sewage: 25 x 106 gallons/d = 94.8 x 106 L/d
Temperature of mixture:
T = stream input + sewage input – output effect
0 = (stream flow)(stream temp.) + (sewage flow)( sewage temp) – (mix flow)(mix temp)
0 = (612 x 106 L/d)(15 °C) + (94.8 x 106 L/d)(20 °C) – (612 x 106 L/d + 94.8 x 106 L/d)Tmix
Tmix = (612 x 106 L/d)(15 °C) + (94.8 x 106 L/d)(20 °C) = 15.7 °C
(612 x 106 L/d +94.8 x 106 L/d)
DO in mixture
Net change in DO = Stream input + Sewage output – Output
0 = (stream flow)(stream DO) + (sewage flow)(sewage DO) – (mix flow)(mix DO)
0 = (612 x 106 L/d)(9.2 mg/L) + (94.8 x 106 L/d)(0.0) - (612 x 106 L/d + 94.8 x 106 L/d)(Domix)
DOmix = (612 x 106 L/d)(9.2 mg/L) + (94.8 x 106 L/d)(0.0 mg/L)
(612 x 106 L/d + 94.8 x 106 L/d)
= 7.97 mg/L
BOD5 of mixture:
Net change in BOD5 = BOD5 = Stream input + Sewage output – Output
0 = (stream flow)(stream BOD5) + (sewage flow)(sewage BOD5) – (mix flow)(mix BOD5)
0 = (612 x 106 L/d)(1.0 mg/L) + (94.8 x 106 L/d)(80 mg/L) - (612 x 106 L/d + 94.8 x 106
L/d)(BOD5)
BOD5mixture = (612 x 106 L/d)(1.0 mg/L) + (94.8 x 106 L/d)(80 mg/L) = 25.0 mg/L
(612 x 106 L/d + 94.8 x 106 L/d)
BODL of mixture (at 20 °C)
BODL =
BOD5
1 – exp(-k’(x/v)
= 25.0 mg/L
1 – exp(-0.34/d)(5 d)
= 30.6 mg/L
3. Correct rate constants to 15.7 °C
k’ = 0.34(1.135)15.7-20 = 0.197 d-1
k2’ = 0.65(1.024)15.7-20 = 0.587 d-1
4. Determine tc and xc:
D0 = (initial stream O2 - O2 of mixture)
= (9.2 – 7.97) = 1.23 mg O2 L-1
4. Determine tc and xc:
tc =
1
k2’ – k’
ln k2’
k’
1 – D0(k2’-k’)
k’ BODL
= 2.42 d
xc = vtc = 3 mi/h x 24 h/d x 2.42 d = 174.2 mi = 280 km
5. Determine Dc:
5. Determine Dc:
V = 3 mi/h = 72 mi/d
Dc =
k’ BODL exp(-k’(xc/v)
k2’
= 0.197 d-1 (30.6 mg/L) exp(-(0.197 d-1)(174.2 mi / 72 mi d-1)))
0.587 d-1
= 6.37 mg L-1
The DO will be depressed 6.37 mg L-1 from saturation.
Minimum DO = 9.2 mg L-1 - 6.37 mg L-1 = 2.83 mg L-1
6. Determine BOD5 at critical point, xc:
BOD5 = BODL exp(-k’(x/v))
= (30.6 mg L-1) exp(-0.197 d-1)(174.2 mi)/(72 mi d-1) = 19.0 mg L-1
20 °C BOD5
= BOD5 [1 – exp(-k’)(5)]
= 19.0 mg L-1 [1 – exp(-0.34 d-1)(5 d)] = 15.5 mg L-1
Easier method
• Use Fate!!!
• Much easier than by hand
End
• Review
Sensitivity Analysis
Limitations
•
It uses average re-aeration rates of the stream (problem in alternating
riffle and pool areas)
•
Sedimentation is not allowed in the basic model, but can be
incorporated with additional experimental data
Remediation
•
Problems are:
•
Source removal! (install treatment plant)
including BOD, NO3-, NH3/NH4+, PO43removal, but you still will have organic rich
sediments for some time
•
Time (flowing aquatic systems can be very resilient)
•
Notice the difference between the recovery of a biodegradable pollutant
versus nonbiodegradable!
-Eutrophication
-Odors
-Low/no D.O.
-Aquatic death
-Microbes/Pathogens
End
• Review
Further Reading
Journals and Reports
• Wipple, G.C. and Wipple, M.C. (1911) Solubility of oxygen in sea
water. Journal of the American Chemical Society, Vol. 3 pp 362.
Books
•
•
•
•
•
•
•
•
Craun, G. (1986) Waterborne Diseases in the United States. CRC Press, Boca Raton, FL.
Meadows, D., Randers, J., and Meadows, D. (2004) Limits to Growth: The 30-Year Update.
Chelsea Gren Publishing Compnay, White River Junction, VT.
Metcalf and Eddy Inc. (1991) Wastewater Engineering, 3rd Ed. McGraw-Hill, New York.
Sawyer, C.N. and McCarty, P.L. (1978) Chemistry for Environmental Engineering. McGrawHill, New York.
Snoeyink, V.L. and Jenkins, D. (1980) Water Chemistry. John Wiley & Sons, New York.
Standard Methods for the Examination of Water and Wastewater, 20th Ed. (1998) American
Waterworks Association, Washington D.C.
Streeter, H.W. and Phelps, E.B. (1925) A Study of the Pollution and natural Purification of
the Ohio River. United States Public Health Service, U.S. Department of Health, Education
and Welfare.
Tchobanoglous, G. and Burton, F.L. (1991) Wastewater Engineering: Treatment, Disposal,
and Reuse. McGraw-Hill, New York.