60
7.4 CASE STUDY #3 – TREATING MIB IN SQUAW PEAK WTP INFLUENT WATER
7.4.1 Process Control Monitoring
By late July 2001 MIB concentrations entering Squaw Peak WTP were approaching 30
ng/L (Figure 7-5). During July 2001 no PAC was added.
MIB in the Squaw Peak WTP
0
10
20
30
40
50
60
70
80
8/1
8/16
8/30
9/13
9/27
10/18
11/2
11/15
MIB, ng/L
Inlet
Outlet
Figure 7-5. MIB in raw (SP-IN) and finished (SP-OUT) water at the Squaw Peak WTP
7.4.2 Diagnosis
Options to minimize MIB production in the upstream canal were being implemented.
However, elevated MIB levels (> 30 ng/L) still entered the WTP. It was determined that
in-plant MIB control was required.
7.4.3 Treatment Selection
Squaw Peak WTP had no documented in-plant production of MIB, therefore chlorine or
copper addition in the WTP would not be effective at reducing MIB levels. Squaw Peak
WTP does not have ozone or chlorine dioxide feed capabilities. Since the WTP feeds
chlorine prior to filtration, biological filtration was not an option. This left powdered
activated carbon (PAC) addition as the only means of MIB treatment.
7.4.4 Treatment Application
Squaw Peak WTP had residual Norit HDB PAC in slurry storage tanks and used that
supply up by the end of July. Norit 20B was ordered; this PAC was deemed more
61
effective at removing MIB from the local water source based upon laboratory
performance comparisons. However, Norit HDB was delivered and had to be used
during early September. PAC ran out around September 20, 2001, and no MIB removal
was achieved. It is important to monitor PAC supplies and coordinate new deliveries
accordingly. Once Norit 20B was delivered the PAC dose was calculated based upon
laboratory dose-removal nomographs (Figure 5-10) verified the prior year at Val Vista
WTP in full-scale tests. The following equation can be used for PAC dose calculation:
C/C
0
= 0.95 x EXP (-0.18 x PAC_Dose)
Equation 7.1
OR
Equation 7.2
An example Norit B PAC dose calculation for September 12, 2001, to achieve 10 ng/L
of MIB in finished water (C) when a MIB concentration of 55 ng/L was present in the raw
water (C
0
)
follows:
C = 10 ng/L
C
0
= 55 ng/L
PAC Dose (mg/L) = - [ ln(0.95 *10/55) ] / 0.079 = 22 mg/L
The WTP was operating near capacity (120 MGD) and detention time in the
presedimentation basins where the PAC was added was only one hour. However, the
nomographs were developed based upon a three-hour contact time. Revised
nomographs for shorter contact times were required to determine PAC doses.
7.4.5 Follow-up Monitoring
PAC (8 to 16 mg/L doses) removed MIB, but not to below 10 ng/L (Figure 7-5). PAC
doses of greater than 16 mg/L were necessary to achieve 10 ng/L MIB in the finished
water, but the PAC feed facilities were not rated for a feed rate this high.
Recommendation: improve and increase capacity of PAC feed system.
Once, after November 2001, Norit 20B was used and detention times in the
presedimentation basins were above 1.25 hours the observed and predicted MIB
removal was adequate and the target of 10 ng/L of MIB in finished water was achieved.
The experience suggested that slight refinements in PAC dose-removal nomographs
may be necessary to account for varying hydraulic retention times, and that scheduling
delivery of PAC was critical.
−
=
079
.
0
*
95
.
0
ln
_
0
C
C
Dose
PAC
62
REFERENCES
American Public Health Association, American Water Works Association and Water
Environment Federation. (1999) Standard Methods for the Examination of Water and
Wastewater. 20
th
Edition.
Baker, L., Westerhoff, P., Sommerfeld, M., Bruce, D., Dempster, T., Qiang, H. and
Lowry, D. (2000) Multiple barrier approach for controlling taste and odor in Phoenix's
water supply system, Water Quality Technology Conference, Salt Lake City, Utah,
November, 2000.
Baker, L. A., Westerhoff, P. and Sommerfeld, M. (1999) Multibarrier concept for taste
and odor control, North American Lake Management Society Conference, Reno,
Nevada, Dec. 1-4, 1999.
Bruce, D., Westerhoff, P., Sommerfeld, M., Baker, L., Nguyen, M. L., Lowry, D.,
Dempster, T. and Hu, Q. (2000) Occurrence of MIB and geosmin in Arizona drinking
waters, Arizona Water Pollution Control Association Conference, May 4-5, 2000.
Lloyd, S. W., Lea, J. M., Zimba, P. V., and Grimm, C. C. (1998) Rapid analysis of
geosmin and 2-methylisoborneol in water using solid phase micro extraction
procedures. Wat. Res. 37(7):2140-2146.
Means, E. G. and McGuire, M. J. (1986) An early warning system for taste and odor
control. Journal AWWA: March, 1986, 77-83.
Nguyen, M. L. (2002) Sources and characteristics of dissolved organic carbon in arid
region water supplies, Ph.D. Dissertation, Civil and Environmental Engineering, Tempe,
Arizona State University, .
Nguyen, M. L., Baker, L. A. and Westerhoff, P. (2002) Sources of DOC and DBP
precursors in western U.S. watersheds and reservoirs. J. Am. Water Works Assoc.
94(5):98-112.
Suffet, I. H., Khiari, D. and Bruchet, A. (1999) The drinking water taste and odor wheel
for the millenium: beyond geosmin and 2-methylisoborneol. Wat. Sci. Tech. 40(6):1-13.
Taylor, W. D., Losee, R. F., Isaguirre, G., Crocker, D. J., Otsuka, D. J., Whitney, R. D.,
Kemp, J. and Faulconer, G. (1994) Application of limnological principles for
management of taste and odor in drinking water reservoirs: a case study, Water Quality
Technology Conference, San Francisco, CA, Nov. 6-10, 1994.
Watson, S. B., Brownlee, B., Satchwill, T., and Hargesheimer, E. E. (2000) Quantitative
Analysis of trace levels of geosmin and MIB in source and drinking water using
headspace SPME. Wat. Res. 34(10): 2818-2828.
63
APPENDIX A
SAMPLE DATA SHEETS FOR LAKE, CANAL AND WTP SAMPLES
Taste and Odor Project – Lake Sampling
Site #: ____________ Location: _________ Date: __________Time: ________
Personnel: __________Weather: ____________________________ Elevation: ___
Description of water:
Description: ______________________________________ Water Depth ____________ m
(circle): Turbid clear
green blue-green brown yellow-brown
white floc
white foam
Secchi Disk Reading 1 __ m Secchi Disk Reading 2 __m Average Reading ___m
Field measurements:
Depth (m)
T (
o
C - D.O.)
D.O. (mg/L)
pH
sample (yes/no)
comments
0
5
10
15
20
25
30
35
40
45
64
Description of phytoplankton (free-floating):
____________________________________________________________________________
Color (circle): Green Brown
yellow-brown Blue-green Pink Other:
____________________
Visible clumps: yes no
Comments: ________________________________
Water Odor Characteristics:
Odor in epilimnion composite water sample:
Odor strength (circle one): Strong Medium Weak Absent
Odor (circle): musty earthy moldy fishy sulfidic grassy chlorine Other
Comments:
______________________________________________________________________
Odor in hypolimnion composite water sample:
Odor strength (circle one): Strong Medium Weak Absent
Odor (circle): musty earthy moldy fishy sulfidic grassy chlorine Other
Comments:
______________________________________________________________________
Samples collected:
Comments:
____________________________________________________________________________
____________________________________________________________________________
____________________________________________________________________________
____________________________________________________________________________
____________________________________________________________________________
____________________________________________________________________________
65
Taste and Odor Project – Canal Sampling
Site #: Specify Site ID Location: Specify location Date: ____________Time: ________
Personnel: ____________Weather: ___________________________ Elevation: _____
Description of water:
Description:
____________________________________________________________________________
(circle): Turbid clear
green blue-green brown yellow-brown
white floc
white foam
Description of phytoplankton (free-floating):
Description: _______________________________________________________________
Color (circle): Green Brown/yellow-brown Blue-green Pink Other:
Visible clumps: yes no Comments: _______________________________
Description of periphyton (attached to canal walls):
Description:
______________________________________________________________________
Depth less than 15 cm:
Approximate thickness of mat: _____ cm Comments: ________________________
Color of mat (circle): Green Blue-green Brown or goldish-brown Black Other:
________________
Depth 15 – 30 cm:
Approximate thickness of mat: __________ cm Comments: __________________
Color of mat (circle): Green Blue-green Brown or goldish-brown Black Other:
________________
Depth greater than 30 cm:
Approximate thickness of mat: ______ cm Comments: ______________________
Color of mat (circle): Green Blue-green Brown or goldish-brown Black Other:
________________
Field measurements:
Temp (
o
C - DO): ______ D.O. (mg/L): ______ Temp (
o
C - pH meter): ________ pH: ______
Odor in water sample:
Odor strength (circle one): Strong Medium Weak Absent
Odor (circle): musty earthy moldy fishy sulfidic grassy chlorine Other
66
Samples collected:
Used scraping device? (yes or no) _________ # of scrapes (2 if possible) _____________
Comments:
____________________________________________________________________________
____________________________________________________________________________
____________________________________________________________________________
____________________________________________________________________________
____________________________________________________________________________
____________________________________________________________________________
67
APPENDIX B
DESIGN AND OPERATION OF PERIPHYTON SAMPLER
A periphyton sampler was designed for this project. The periphyton sampler is a
rectangular chamber, measuring 25 cm long, 18 cm wide and 18 cm high. The upper
part of the chamber is made of a clear PVC plate, whereas the bottom is a metal plate
with a 10 x 15 cm open area (0.015 m
2
). The side of the chamber facing the canal bank
is a small slot through which a wire pool brush inside the chamber is attached to a
telescoping pole. The upstream side of the chamber has a large opening that is
covered by a fine plastic screen that allows water to flow through the chamber. The
downstream side of the chamber is a large circular opening with an attached plankton
net (80 um mesh). Two people are required to collect samples. The sampler is placed
on the canal wall and held into position with the telescoping pole by one person. A
second individual brushes the wall a predetermined number of times. As periphyton
mats are removed from the canal wall, they are carried by water flow into the plankton
net. Because vertical zonation of periphyton is evident on canal walls, sampling is done
at three depths (just below the surface and at 30 cm intervals. The three samples are
composited and stored in a sterile whirl-pak bag at 4
0
C until laboratory analysis.
Diagram of the periphyton sampler. Sampler consists of A, a rectangular chamber with an open window
(10 x 15 cm) on the bottom plate; B, a plankton net; C, a plastic screen with metal frame (D); E, two
telescoping poles; and F, a wire pool brush.
A
B
F
E
C
D
E
68
APPENDIX C
SPME METHOD FOR MEASURING MIB AND GEOSMIN
Twelve (12) ml of sample is added to a 25 ml septum capped vial that contains 4 g
desiccated sodium chloride. An internal standard (10 ng/L IPMP, Sulpelco #47527 U) is
added through the septum and the vial is placed in a heat block 50
±
1.5
0
C. A SPME
fiber (Supelco # 57348 U) is introduced into the head space through the septum and the
sample is shaken for 30 minutes. The fiber is removed from the vial and inserted into
the gas chromatograph injector at 250
0
C for 5 minutes. The fiber is then retracted into
the holder, removed from the GC inlet and reused for the next sample. Compounds
from the fiber are desorbed in the column gas chromatograph (MDN-5 capillary column;
Supelco, Pennsylvania) and eluted into a mass spectrometer set for selective ion
monitoring (selective m/z values: MIB = 95, geosmin = 112 and IPMP = 124, 136).
Calibration curves are generated using MIB and geosmin standards (mixture standard:
Supelco # 47525 U). Analysis of MIB and geosmin was performed on a Varian Star
3400 CX gas chromatograph and mass spectrometer (GC/MS). (QA/QC analysis of
MIB measurements by the City of Phoenix and ASU labs has shown a nearly 1:1
correlation (actual slope was 0.95), and a statistical R
2
value of 0.72 for approximately
150 samples since inception of the project.) The method detection limit (MDL) for MIB
and geosmin is ca. 1ng/L ng/L.
69
APPENDIX D
TEST PROTOCOL FOR EVALUATING
PAC MIB ADSORPTION CAPACITY
A PAC slurry should be prepared by adding 1000 mg of PAC to 1 liter of 0.45
µ
m filtered
water and allowed to hydrate overnight while being mixed with a magnetic stir. Filter
approximately 2 liters of raw water and spike with MIB and geosmin to give a
representative concentration (e.g., 30 ng/L). Fill amber glass bottles (no headspace;
250 mL) with this water sample. The hydrated PAC slurry will have a PAC
concentration of 1 mg/ml. Select representative PAC doses for the performance-based
experiments (e.g., 15 mg/L). Calculate the volume of PAC slurry (V
PAC
) required for
addition to the 250mL sample (e.g., a PAC dose of 15 mg/L would equate to 3.75 mL of
PAC slurry); remove and add V
PAC
of the PAC slurry to the 250 mL amber bottle. Using
a magnetic stir or wrist-shaker, rapidly agitate the bottle containing the water sample
and PAC for a desired period representative of average HRT of the presedimentation
basins (e.g., 1 to 4 hours). Immediately after the prescribed agitation period use a
syringe-filter (0.2
µ
m) and filter the water sample/PAC mixture. Collect the filtrate in a
100 mL amber vial (no headspace). Conduct MIB and geosmin analysis on the filtrate.
Repeat for each PAC brand, and repeat for a blank (no PAC added). Calculate the
fraction of MIB remaining: C/C
o
where C
o
is the MIB or geosmin concentration in the
blank and C is the concentration after contact with the PAC. Compute the Index Value
based upon the fraction of MIB remaining (C/C
o
) and the unit cost of the PAC (e.g.,
$/lb):
Index Value = [C/C
o
] x [PAC unit Cost]
Equation D.1
The PAC brand with the lowest Index Value is the most cost-effective. This assumes
that there are no limitations to PAC feed rates. For example, to achieve a desired MIB
removal, one PAC brand may require 40 mg/L of PAC while a more expensive PAC
brand may only require 30 mg/L of PAC feed. Therefore, the actual fraction removed
(C/C
o
) should be examined. High PAC feed rates can increase the frequency of PAC
shipments, sludge production, handling costs and maintenance on equipment, etc.
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