WQ0005763_2008 Annual Report_20090226

n ' 1
zoo?- 11(a1C)9
Annual Report Review Class A Distribution
1. Class A Annual Distribution and Marketing/Surface Disposal Certification Form
® Was a certification form submitted? I es
® Was distribution conducted during the reported year? y 2S
® How many dry tons were distributed? 270 CST
® Were the distributions within the permitted amount? k4o hw{` ��r:r b w O-S
® Were recipients information listed`? �S & —,4 e s
'i Co�r$ts� l c �1
Did it indicate compliance? y'P_5 t 0
,
® Was form complete?. y �Q �� l
® Was it signed by the appropriate people? e5
2. Monitoring
® Were the analyses conducted at the required frequency?��
® Were the metals analyses reported on the Residual. Sampling Summary Form?y-,_PS
® Were the results reported in mg/kg.?YES
® Were the metals within ceiling concentration permit limits? 14.5
® Were the metals within monthly average concentration permit limits? yes
® If no, were the lab analyses attached?
® Were all the required parameters tested?yes
® Was TCLP analysis conducted? Y e,S
® Were the TCLP contaminants within regulatory limits? ,y e5
3. Pathogen and Vector Attraction Reduction
® Was a signed copy of the Pathogen and Vector Attraction Reduction Form submitted? yeS
® Did the form indicate the period of coverage, the residual class, and the pathogen reduction alternative and the
vector attraction reduction option used?
Was the appropriate docupsntation to show pathogen and vector attraction reduction included in the report?
® Was pathren and vector attraction reduction demonstrated according to 40 CFR Part 503 or 2T?
4. General
© Was the report in the proper format? YZ-S
® Were any parts of the annual report missing? No
® Was the report submitted on time? y eS

Class A Pathogen Review
To be Class A, residuals shall meet either fecal coliform density or salmonella density.
Fecal coliforn density
® Was the sampling conducted at the required frequency? 10s o^«11, ©J�S'oj 0'7
® Were multiple samples taken? 14rw
® Was each sample less than 1000 MPN/gram of total solids?
Or
Salmonella density
9 Was the sampling conducted at the required frequency?
® Were multiple samples taken?
Was each sample less than 3 MPN/4 grams of total solids?
r
To be Class A, residuals shall meet one of the following alternatives:
Alternative 1 - Time/Temperature
® Were the residuals maintained for correct time and temperature?
®. Were logs submitted showing time and temperature?
® Were temperatures within range for complete time period?
Alternative 2 - Alkaline Treatment
m Were logs submitted showing time and temperature?
® Was the pH raised to 12 or greater and maintained for 72 hours or longer?
6 Was the temperature 52°C (126°F) for 12 hours or longer while the pH was 12 or greater?
® Were logs submitted showing time and pH?
e Was the temperature corrected to 25°C (770F)?
Alternative 3 -Prior Testing for. Enteric Viruses/Viable Helminth Ova
® Were residuals analyzed prior to the pathogen reduction treatment?
. Prior to treatment were, the density of enteric viruses less than one Plaque -forming Unit per four grams of
total solids; or
was the resultant density after pathogen treatment less than one Plaque -forming Unit per four grams of
total solid?
OR
o Prior to treatment were, the density of viable helminth ova less than one per four grams of total solids; or
was the resultant density after pathogen treatment of viable helminthova less than one per four grams of
total solids?
® Were the. operating parameters documented to the satisfaction of the Division?
Alternative 4 -No Prior Testing for Enteric Viruses/Viable Helminth Ova
® Was the density of enteric viruses less than one Plaque -forming Unit per four grams of total solids at the
tune the residuals were prepared for sale or given away?
OR
® Was the density of viable helminth ova -less than one per four, grams of total solids at the time the
residuals were prepared for sale or given away?

Alternative 5 —Process To Further Reduce Pathogens
PFRP Composting
® Were the within -vessel method or static aerated pile methods used?
® Was the residuals temperature maintained at 55°C (131T) or higher for three consecutive days or longer
in the within -vessel method or static aerated pile method?
OR
® Was the windrow composting method used?
Was the residuals temperature maintained at 55°C or higher for 15 consecutive days or longer in the
windrow method, and the windrow turned a minimum of five times during this time?
PFRP Heat Drying
® Was the residuals dried by direct or indirect with hot gases and moisture content of residuals reduced to
10% or lower?
® Did the temperature of the residuals or the of the wet bulb temperature of the gas in contact with the
residuals as they leave the dryer exceed 80°C (176°F)?
PFRP Heat Treatment
® Were the residuals liquid during treatment?
m Were the residuals heated to a temperature of 180°C (356T) or higher, for 30 minutes?
PFRP Thermophilic Aerobic Di esg tion
® Were the residuals liquid during treatment?
® Was it an aerobic process with agitation?
Was the mean cell residence time 10 consecutive days. at 55°C (131°F) to 60°C (140°F)?
PFRP Beta Ray Irradiation
Were residuals radiated with beta rays at dosages of at least 1.0 megarad at room temperature
[approximately 20°C (68°F)]?
PFRP Gamma Ray Irradiation
m Were residuals radiated with gamma rays from certain isotopes, such as Cobalt 60 and Cesium 137; at
dosages of at least 1.0 megarad at room temperature [approximately 20°C (68°F)]?
PFRP Pasteurization
. ® Was the temperature of the residuals maintained at 70°C (158T) for 30 minutes or longer? jl &S

Vector Attraction Reduction Review
• Was the sampling conducted at the required frequency?
38% Volatile Solids Reduction
• Was there 38% reduction?
Were lab sheets/calculations in report.
• Was the reduction on volatile solids (not"total solids)?
• Was the samples taken at beginning of digestion process and before application
(Inspection)?
• Were calculations correct?,.-.
40-Day Bench Scale Test
• Were residuals from anaerobically digested treatment (Inspection)?
• Were residuals anaerobically digested in lab?
Was the test run for 40 days?
• Was the test done between 30°C (86°F) and 37C (99°F)?
• Was. the reduction on volatile solids (not total solids)?
• Was the reduction less than 17%?
• Were lab sheets/calculations in report? .
• Were calculations correct?
30-Day Bench Scale Test
• Were residuals from aerobically digested treatment (Inspection)?
• Were residuals aerobically digested in lab?
• Were residuals 2% or less total solids?
• Was the test run for 30 days?
• Was the test done at 200C (680F)?
• Was the reduction on volatile solids (not total solids)?
• Was the reduction less than 15%?.
• . Were lab sheets/calculations in report?
• Were calculations correct?
Specific Oxygen Uptake Rate (SOUR)
• - Were residuals from aerobically digested treatment (Inspection)?
• Were residuals 2% or less total solids (dry weight basis).(riot diluted)?
• Was the test done between 10°C (56°F) and 3.0°C (86-F)?
• Was the temperature corrected to 20°C (686F)?
• Was the SOUR equal to or less than 1.5 mg of oxygen per hour per gram of total residual
solids (dry weight basis)?
• Was the sample holding time under two hours?
• Was the test started within15 minutes of sampling or aeration maintained?

14-Day Aerobic Process
® Were residuals from aerobically digested treatment (Inspection)?
® Were the residuals treated for 14 days?
® Was the residuals temperature higher than 400C (104°F) for the 14-day period?
® Was the average residuals temperature higher than.45°C (113T)?
Alkaline Stabilization
® Was the pH of the residuals raised to 12 or higher by the addition of alkali? yea
Did the pH of residuals remain at 12 or higher for two hours without the addition yes
of more alkali?
® Did the pH of residuals remain at 11.5 or higher for an additional twenty-two 14 S
hours without the addition of more alkali?
v Was the pH corrected to 250C (770F)? yd5
Drying of Stabilized Residuals
o Does the residuals contain any unstabilized residuals?
® Were the residuals mixed with any other materials?
® Were the residuals dried to 75% total solids?
Drying of Unstabilized Residuals
Were the residuals mixed with any other materials?
• Were the residuals dried to 90% total solids? . .
Injection
• Was there any significant. amount of residuals on land surface one hour after
injection (Inspection)?
• Was injection done on pasture or hay field?
® Was injection done at time that crop was growing?
• If Class A with respect to pathogen, were residuals injected within eight hours
after discharge from pathogen treatment?
Incorporation
Were the residuals incorporated into the soil within six hours after application?
® Was incorporation done on pasture or hay field?
o Was incorporation done at time that crop was growing?
® If Class A with respect to pathogen, were residuals incorporated within eight
___----____hours-after-dischar-ge-from-pathogen-.tr-eatment?.-_-__--._.___.-_-_-..._.._..__.__._..__-__------.___

Tuckaseigee Water & Sewer Authority
Serving Jackson County
1246 West Main Street
Sylva, NC 28779
Ph. [phone]
Fax [phone]
February 5, 2009
DENR/DWQ/Water Quality Section
Non -Discharge Compliance Unit
1617 Mail Service Center
Raleigh NC 27699-1617
Attn: Non -Discharge Compliance Unit,
4 �
R`' E C �'
MAR 17 2659
fA hevilfe Regional Office
Enclosed is the Annual Residuals Report for the Tuckaseigee Water and Sewer Lime
Stabilization facility (permit #WQ0005763) for the period of January 1, 2008 - December
31, 2008.
Should you have any questions or if I can provide you any additional information, please
don't hesitate to contact me.
Sincer ly,
Stan Bryson °
Wastewater Plant Operations Superintendent
Tuckaseigee Water & Sewer Authority
Enc.
C _j
FEB 2 6 2009
information Pr `ng Unit

ANNUAL SEWAGE SLUDGEhtEPORT
OF
TUCKASEIGEE WATER, AND SEWER
AUTHORITY.
PLANT # 1-NPDES # NC0039578
(WQ0005763)
for the period of
January 1, 2008-December 31 2008
as required by
40 CFR, . PART 5.03
STANDARDS FOR THE USE OR
DISPOSAL OF SEWAGE SLUDGE

CERTIFICATION
" I certify under penalty of law, that the Class A pathogen requirements in 40 CFR, Part
503. 32 have been met and the vector attraction reduction requirement in 40 CFR, Part
[503. 33(b)(6)] has been met. I am aware that there are significant penalties for false
certification including fine and imprisonment."
Signed this 5th day of February, 2009
Stan Bryson, Was water Superintendent

Appendix (a)
Distribution and
Marketing
Summary

ANNUAL DISTRIBUTION AND MARKETING/ SURFACE DISPOSAL CERTIFICATION AND SUMMARY FORM
PERMIT #: WQ 005763 FACILITY NAME: Tuckaseigee Water and Sewer Authority
PHONE: [phone] COUNTY: Jackson OPERATOR: - Stan Bryson
FACILITY TYPE (please check one): ❑ Surface Disposal (complete Part A (Source(s) and "Residual In" Volume only) and Part C)
EY'bistribution and Marketing (complete Parts A, B, and C)
Was the facility in operation during the past calendar year? 2-*,Yes ❑ No No If No skip parts A, B, C and certify.form below
Part
A*:
Part B*:
Recipient Information
.Volume (dry
Name(s) Intended use s
tons) ( )
Month
Sources(s) (include NPDES # if
applicable)
Volume (dry tons)
Amendment/
Residual In Product Out
Bulking Agent
January
22.67
10.15
32.82
0
February
9.92
5.65
15.57
0
March
37.98
18.2
56.18
30.35
April
May
June
See Appendix A
Part A
45.97
3 5.27
40.04
23.8
17.3
18.17
69.77
52.57 .
58.21
See Appendix A
Part B
106.77
35.23
15.18
July
31.2
15.43 ,
46.63
21.68
August
13:5
7.97
21.47
0
September
0
0
0
0
October
0
0
0
2.4.4 4
November
December
Totals:
Annual (dry tons):
0
0
236.55
0
0
116.67
.7
0
0
353 2 .2
5 4
0
270.19 9
Nmenamen
t1s2 use AO +(quick lime Bulkin Agent(s) used: none
,*If more space than given is required, please attach additional information sheet(s). W Check box if additional sheet(s) are attached
Part C.-
Facility was compliant during calendar year with all conditions of the permit (including but not limited to items 1-3 below) issued by the
Division of Water Quality. M-`Y s ❑ No If No, please provide a written description why the facility was not compliant.
1. All monitoring was done in accordanc � t and reported for the year as required and three (3) copies of certified laboratoryresults are attached
2. All operation and maintenance requiredr e� we'Te�c ' e with or, in case of a deviation, prior authorization was received from the Division of Water
Quality. 262009
3. No contravention of Ground WateNy � oandards occurred at a monitoring well.
"I certify, under penalty of law, that the W d jf 'a*ion is, to the best of my knowledge and belief, true, accurate and complete. I am aware
tha a are s' ificant penalties for submitting false information, including the possibility of fines and imprisonment for knowing violations."
Signature of Permi ee D� S' ignature of Preparer**
Date
(if different from Permittee) **Preparer is defined in 40 CFR Part 503.9(r)
DENR FORM DMSDF (11/2005)

Appendix A
-TWSA PLANT #.1
ANNUAL DISTRIBUTION AND MARKETING SUMMARY
2008
Part A,
Residual Sources and Volume
Class A
Sludge Volume Sludge Volume Sludge Volume Residual Volume
Produced Dewatered Treated Lime Added Produced .
Month Source (dry tons(dry tons(dry tons(dry tons(dry tons
January
TWSA Plant # 1 (NC0039578)
23.31
TWSA Plant# 2 (NC0020214)
2.27
TWSA Plant# 3 (NC0063321)
0.00
Septage Received
1.71
Monthly TotalF
27.29
10.15
10.15 22.67
32.82
February
TWSA Plant # 1 (NC0039578)
17.86
TWSA Plant # 2 (NC0020214)
5.18
TWSA Plant # 3 (NC0063321)
0.00
Septage Received
3.42
Monthly Totall
26.46
24.101
5.65
9.92
15.67
March
TWSA Plant# 1 (NC0039578)
TWSA Plant # 2 (NC0020214)
TWSA Plant # 3 (NC0063321)
Septage Received
Monthly Total
23.30
2.34
2.87
1.87
30.38
19.37
18.2
37.98
56.18
April
TWSA Plant # 1 (NC0039578)
TWSA Plant # 2 (NC0020214)
TWSA Plant # 3 (NC0063321)
Septage Received
Monthly Total
. 29.76
3.37
0.19
Z03
35.35
27.49
23.8
45.97
69.77
May
TWSA Plant # 1 (NC0039578)
22.98
TWSA Plant # 2 (NC0020214) ,
- 4.26
TWSA Plant # 3 (NC0063321)
0.00
Septage Received
1.93
Monthlv Total
29.17
17.30
17.30
35.27
52.57
June
TWSA Plant # 1 (NC0039578)
- 22.52
TWSA Plant #2 (NC0020214)
3.69 -
TWSA Plant # 3 (NC0063321)
0.00
Septage Received
3.41
29.62
18.17
18.17
40.04
68.21
Monthly Totall

Part A
Residual
Sources and Volume
Class A
Sludge Volume
Sludge Volume
Sludge Volume
Residual Volume
Month Source
Produced
(dry tons)
Dewatered
(dry tons)
Treated
(dry tons)
Lime Added
(dry tons)
Produced
(dry tons)
July
TWSA Plant # 1 (NC0039578)
18.93
TWSA Plant # 2 (NC0020214)
0.00
TWSA Plant # 3 (NC0063321)
1.95
Septage Received
2.41
Monthly Total
23.29
15.43
15.43
31.20
46.63
August
TWSA Plant # 1 (NC0039578)
19.90
TWSA Plant # 2 (NC0020214)
4.22
TWSA Plant # 3 (NC0063321)
0.00
Septage Received
1.06
Monthly Total
26.18
16.14
7.97
13.6
21.47
September
TWSA Plant # 1 (NC0039578)
28.40
TWSA Plant # 2 (NC0020214)
0.00
TWSA Plant# 3 (NC0063321)
0.71
Septage Received
2.53
Monthly Total
31.64
25.82
0
0
0
October
TWSA Plant # 1 (NC0039578)
25.11
TWSA Plant # 2 (NC0020214)
3.39
TWSA Plant # 3 (NC0063321)
1.95
Septage Received
3.96
34.41
17.82
0
0
0
Monthly Total
November
TWSA Plant # 1 (NC0039578)
19.05
TWSA Plant # 2 (NC0020214)
0.00
TWSA Plant# 3 (NC0063321)
0.00
Septage Received
0.86
MonthIV Total
19.91
9.17
0
0
0
December
TWSA Plant # 1 (NC0039578)
19.45
TWSA Plant # 2 (NC0020214)
0.00
TWSA Plant .# 3 (NC0063321)
0.00
Septage Received
2.12
Mnnthiv Tntall
21.67
16.78
0
0
0
Total "sludge" produced by all sources for 2008= 310.98 dry tons
Total "sludge" dewatered by belt press in 2008= 217.74 dry tons
Total "sludge" treated in pastuerization process in 2008= 116.67 dry tons
Total lime added in pastuerization process in 2008= 236.55 dry tons
Total "residual' produced for distribution in 2008= 353.22 DRY TONS

Appendix A
TWSA PLANT # 1
ANNUAL DISTRIBUTION AND MARKETING SUMMARY
2008
Part B
Recipient Information
'Est. Volume
Month Name Address (wet tons) Intended Use
January
Monthly Total
0
February
_ _
-
Monthly Totall.
0
March
Tom Kelley
56
Pasture/Hayfields
Webster NC. 28788-
Monthl Total
56
April
Steve Hansen
Old Still Rd.
2.
Pasture/Hayfields
Franklin NC 28734
Robert Medlin
PO Box 3155
120
Pasture/Hayfields
Cullowhee NC 28723
Chester Sorrells
274 Davis Cove Rd.
63
Commercial Hauler
Waynesville NC 28786
Felicia Stewart..
PO Box 384
.12
Pasture/Hayfields
Robbinsville NC 28771
Monthly Totall
197 T
May
Manuel Cooper
PO Box 945
9
Commercial Hauler
Sylva NC 2877.9
Chester Sorrells
274 Davis Cove Rd.
56
Commercia_f Hauler
Waynesville NC 28786
Monthly Total
65 T
June
Chester Sorrells
274 Davis Cove Rd.
28
Commercial Hauler
Waynesville NC 28786
Monthl Totall
28 T

July
Morriss Edwards
1219 Toccoa Hwy
Mt. Airy GA 30563 .
40
Pasture/Hayfields
Monthly Total
40 T
August
_
.
MonthlyTotal
0
September
Monthly Total
0
October
Arnold Frady
270 Christmas Tree Lane
Sylva NC 28779
4.5
Pasture/Hayfields
Monthl Total
4.5 T
November
R.L. Morgan
149 Gilbert Rd.
80
Pasture/Hayfields
Leiceister NC 28740
Chester Sorrells
274 Davis Cove Rd.
28
Commercial- Hauler
Waynesville NC 28786
Monthl----
y Total
108 T`
December
Monthl Total
0 77

Appendix (b)
Residuals Sampling
Summary
Form
f:,

,� 6r7U0
Annual F lual Sampling Summary Form
Attach fts-Tbrm to the corresponding Annual Report
Please note that your permit may contain additional parameters to be analyzed than those required to be summarized on this form.
Permit Number: WQ 0005763
Facility Name: Tuckaseigee Water and Sewer Auth
NPDES # NC 0039578
WQ #: WQ 0005763
WWTP Name: TWSA Plant # 1
P
A
Sample
Date
Percent Solids
Aluminum
Arsenic
2/22
44.2
7,390
<1.1
3/25
53.5
4/8
50.4
5/13
54.5
5,880
0.91
8/19
54.6
9,250
2.1
11/4
58.4
8,880
< 0.88
12/22
0842
57.5
12/22
0845
56.2
12/29
58.2
Avg.
54.2
7,850
0.75
Cadmium
0.47
0.37
< 0•.1
0.34
0.30
R
A
M
Calcium
Chromium
4,360
6.0
404,000
4.8
64,100
12.5
364,000.-
7.7
209,115
7.8
Copper
71.8
64.3
134
117
97
E
T
E
R
S
Lead
4.7
5.2
5.2
7.0
5.5
Magnesium
Mercury
2,640
0.023
2,650
0.017
2,120
0.390
2,540
0.120
2,488
0.138
Molybdenum
2.7
1.8
2.5
2.4
2.4
Nickel
4.9
3.7
6.2
4.7
4.9
h
12
11.7
11.9
12
Potassium
Selenium
2,870
< 2.2
3,100
2.2
3,790
<1
3,070
< 1.8
3,208
0.6
Sodium
< 1110
<1
535
< 880
134
Zinc
224
202
291
295
253
mg/
TKN
Ammonia -Nitrogen
64,900
222
145,000
62.2
8,210 .
163
12,500
261
57,653
177
kg
Nitrate -Nitrite
115.9
<1.9
18.6
17.3
13.2
Plant Available N
Total Phosphorous
Fecal Coliform
19,500
147
1
< 200 1
< 20 1
' 43,500
463
< 2
2,500
43.3
< 20
3,800
1,750
< 3 1
< 20
< 20
17,325
601
<.2
< 12
I certify, under penalty of law, that this document was prepared under my direction or supervision in accordance with a system
designed to assure that qualified personnel properly gathered and evaluated the information submitted. I am aware that there are
significant penalties for submitting false information, including the possibility of fines and imprisonment for knowing violations."
A
Signature of Preparer
-�%- %- ate

Appendix (c)
Residuals Analysis
Lab Sheets

.. analytical
s.
www pagelabscom;
✓✓✓ March 07, 2008
Mr. Stan Bryson
Tuckaseigee Water- & Sewer Co.
1246 West Main Street
Sylva, NC 28779
Pace Analytical Services, Inc.
2225 Riverside Dr.
Asheville, NC 28804
[phone]
Pace Analytical Services, Inc.
9800 Kincey Ave. Suite 100
Huntersville, NC 28078
[phone]
RE: Project: Lime Residual 2/22
r
Pace Project No.: 92.14100
Dear Mr. Bryson:
Enclosed are the analytical results for sample(s) received by the laboratory on February 22, 2008.
The results relate only to the samples included in this report. Results reported herein conform to the
most current NELAC standards, where applicable, unless otherwise narrated in the body of the
report.
Inorganic Wet Chemistry and Metals analyses were performed at our Pace Asheville laboratory and
Organic testing was performed' at our Pace Huntersville laboratory unless otherwise footnoted. All
Microbiological analyses were performed at the, laboratory where the samples were received. .
If you have any questions concerning this report, please feel free,to contact me.
Si ce ely,
T Willams
[e-mail]-
Project Manager
Enclosures
REPORT. OF LABORATORY ANALYSIS
This report shall not be reproduced; except in full,
without the written consent of Pace Analytical Services, Inc..
� p ACCCgC' .
Page 1 of 14

race hnaiyncaraernces, Inc. Pace Analytical Services, Inc.- ,
®
.fC�IICC'
2225 Riverside Dr.
9800 Kincey Ave. Suite 100
" wwwpacetabs M.
Asheville,. NC 28804
Huntersville, NC 28078 -
[phone]
[phone] .
ANALYTICAL
RESULTS
Project: -Lime Residual 2/22 ,
Pace Project No.: 9214100
Sample: TWSA LIME RESIDUAL
Lab ID: 9214100001, Collected:
02/22/08 09:30
Received: 02/22/08 15:26 Matrix: Solid
Results reported on a "dry -weight" basis
Parameters
Results Units Report Limit
DF •
Prepared
Analyzed `
CAS No. Qual
6010 MET ICP
Analytical Method: EPA 6010 Preparation
Method: EPA 3050 ,
"- Aluminum
7390,:mg/kg
22.2
1
'03/05/08 13:20
03/06/0811:56
7429-90-5
Arsenic
ND mg/kg,'
1.1
1
03/05/08 13:20
03/06/08 11:56
7440-38-2
Cadmium
0.47 mg/kg
0.22
_ 1
03/05/08 13:20
03/06/08 11:56
7440-43-9
- Calcium _
�•_- -° y__4360_mg/kg._..
443
20
03/05/08 13:20
03/06/08 15:56
7440-70-2
Chromium
6.0 mg/kg
1.1
1 -03/05/08
13:20
03/06/08 11:56
7440-47-3
Copper
71.8 mg/kg
1.1
1
03/05/08 13:20
03/06/08 11:56
.7440-50-8
Lead
4.7 mg/kg
1.1
1
03/05/0813:20
03/06/08 11:56
7439-92-1
-` Magnesium
2640 mgft
22.2
1
03/05/08 13:20
03/06/08 11:56
7439-95-4
Molybdenum
2.7,mg/kg
1.1
1 •
03/05/08 13:20
03/06/08 11:56
7439-98-7
Nickel
4.9 mg/kg
1.1
1
03/05/08 13:20
03/06/08 11:56
1440-02-0
Potassium
2870 mg/kg
1110
1
03/05/08 13:20
03/06/08 11:56
7440-09-7
Selenium
ND mg/kg
2.2
1
03/05/0& 13:20
03/06/08 11:56
7782-49-2
Sodium
ND mg/kg
1110
1
03/05/08 13:20
03/06/08 11:56
7440-23-5
Zinc
224 m6/kg
2.2' .
1
03/05/08 13:20
03/06/08 11:56
7440-66-6
7471 Mercury
_ Analytical Method: EPA 7471 Preparation Method: EPA 7471
Mercury
0.023 mg/kg "
0.014
1
02/26/08 13:24
02/26/68 16:57 '
7439-97-6 `4
cent Moisture
Analytical, Method: ASTM D297487
Percent Moisture
55.8 %
0.10
1
02/29/08 08:31
9045 pH Soil
Analytical Method: EPA 9045
pH at 25 Degrees C
12.0 Std. Units
0.10
1
02/29/08 20:55
Plant Available Nitrogen
Analytical Method: 40CFRPART 503
Plant Available Nitrogen
19500 mg/kg
1.0
1
03/07/0815:44
Total Nitrogen Calculation
Analytical Method: 40CFR PART 503 .
.
r.
Nitrogen
64900 mg/kg
40.0
1
03/07/0815:37,
7727-37-9
350A Ammonia ,
Analytical Method: EPA 350.1
Nitrogen, Ammonia
222 mg/kg
4.5
1
03/02/08 20:08
7764-41-7
351.2 Total Kjeldahl Nitrogen
Analytical Method: EPA 351.2
Nitrogen, Kjeldahl, Total
64900 mg/kg
1570
140 •
03/04/08 17:46
7727-37-9
353.2 Nitrogen, NO2/NO3
-Analytical Method: EPA 353.2
Nitrogen, Nitrate'
ND mg/kg
.16.9
1
02/26/08 11:55
Nitrogen, Nitrite'
ND mg/kg
16.9 ,
1
02/26/08 11'55
Nitrogen, NO2 plus NO3
ND mg/kg
16.9
1
02/26/0811:55
365.1 Phosphorus, Total
Analytical Method: EPA365.1
Phosphorus
147 mg/kg
9.0
- 2.
02/25/08 20:47 .7723-140
L?tlie: 03/07/2008 03:44 PM
REPORT OF LABORATORY ANALYSIS
This report shall not be reproduced, except in full,
without the written consent of Pace Analytical Services, Inc..
1N ACCO,
41
ti n
Vx
Page 4 of 14

Pace Analytical Services, Inc.
2225 Riverside Dr.
Cei4FIc?�)/�lCail Asheville, NC 28804
www.paceJabs:com:
r [phone]
,ter
April 14, 2008
Mr. Stan Bryson .
Tuckaseigee Water & Sewer Co.
1246 W6st Main Street
Sylva, NC 28779
RE: Project: TWSA Lime Residual 3/25
Pace Project No.: 9216028
Pace Analytical Services, Inc.
9800 Kincey Ave. Suite 100
Huntersville, NC 28078
[phone]
Dear Mr. Bryson:
Enclosed are the analytical results for sample(s) received by the laboratory on March 25, 2008. The
results relate only to the samples included in this report. Results reported herein conform to the
most current NELAC standards, where applicable, unless otherwise narrated in the body of the
report.
Inorganic Wet Chemistry and Metals analyses were performed at our Pace Asheville laboratory and
Organic testing was performed at our Pace Huntersville laboratory unless otherwise footnoted. All
Microbiological analyses were performed at the laboratory where the samples were received.
If you have any questions concerning this report, please feel free to contact me.
Sin rely,
L
a
T Williams
[e-mail]
Project Manager
Enclosures
J REPORT OF LABORATORY ANALYSIS
This report shall not be reproduced, except in full,
without the written consent of Pace Analytical Services, Inc..
M •CCOy ,
it • ��l�Js
Page 1 of 2

Analytical Results
Pace AnalyticalAsIheville For: 9216028
2225 Riverside Drive
Asheville NC 28804
Entered 3/26/2008
Reported:. 4/3/2008
Sample Remark
Sample ID Parameter Cu$t 'ID 12esult Units Method. Date Analyzed Analyst
080326-2 % Solids 9216028001 53.5 % SM2540B 3/26/08 CL
080326-2 Fecal Coliform IVITF 9216028001 <200 MPN/g SM92210E 3/26/08 CL
Respectfully submitted,
f�
.L?na Myers
NC Cert ##440,
NCDW Cert ##37755,
EPA NC00909
P.O. Box 228 9 Statesville, North Carolina 28687. 704/872/4697

.Pace Analytical Services, Inc. Pace Analytical Services, Inc.''
p 2225 Riverside Dr. 9800 KinceyAve. Suite 100
nCZr ��ia', Asheville, NC'28804 Huntersville, NC 28078`
�nnvwpecethbs com;
[phone] [phone]'
April 18, 2008
Mr. Stan Bryson
L Tuckaseigee Water & Sewer Co.
1246 West Main Street
Sylva;-NC 28779
RE: .Project:. TWSA Lime Residual 4/8'.'
Pace Project No.: 9216926 :
Dear Mr. Bryson:
Enclosed are the analytical results for sample(s) received by the laboratory on April 08, 2008. The
results relate only to the samples included in this report. Results reported herein conform to the
most current NELAC standards, where applicable, unless otherwise narrated in the body of the
report.
Inorganic Wet Chemistryand Metals analyses were performed at our Pace Asheville laboratory -and
Organic testing was performed at our Pace Huntersville laboratory unless otherwise footnoted. All
Microbiological analyses were performed at the laboratory where the samples were received.
If you have any questions concerning this report, please feel free to -contact me.
Sinc - ely,
To Williams
+^ [e-mail]
Project Manager
Enclosures
REPORT OF LABORATORY ANALYSIS' . Page 1 of 2
This report shall not be reproduced, except in full,
without the written consent of Pace Analytical Services,Inc..
M CCOgp -

f fv
Analytical Results
Pace Analytical -Asheville For: 921696
2225 Riverside Drive
Asheville NC 28804
Entered 4/9/2008
---Reported: . 4/15/2008
Sample Remark
Sample ID Parameter , Cust ID Result Units Method Date Analyzed Analyst
08049-1 % Solids 9216926001 50.4 % SM2540B 4/9/08 MD
08049-1 Fecal Coliform MTF 9216926001 <20 MPN/g SM92210E 4/9/08 MD
Respectfully submitted,
�Uena Myers
NC Cert #440,
NCDW Cert #37755,
EPA NCO0909
C)
P.O. Box 228 • Statesville, North Carolina 28687. 704/872/4697"

Pace Analytical Services, Inc. Pace Analytical Services, Inc..
`a 2225 Riverside Dr. Kincey Ave Suite 100
ice, Anal ifcal i 9800
Asheville, NC 28804 - Huntersville, NC 28018
wwwpacelabscom; [phone] [phone]
May 29, 2008
Mr. Stan Bryson
Tuckaseigee Water & Sewer Co.
1246 West Main Street
Sylva, NC 28779
RE: Project: Lime Residual' 05/13
Pace Project No.: 9219197
Dear Mr. Bryson:
Enclosed are the analytical results,for sample(s) received by the laboratory on May 13, 2008. The
results relate only to the samples included in this report. Results reported herein conform to the
most current NELAC standards, where applicable, unless otherwise narrated in the body of the
report.
Inorganic Wet Chemistry and Metals analyseswere performed at our Pace Asheville laboratory and
Organic testing was "performed at our Pace Huntersville laboratory unless otherwise footnoted. All
Microbiological analyses were at
at the laboratory where the samples Were received.
If you have any questions concerning this report, please feel free to contact me.
Sin ely, .
T illiams
[e-mail]
Project Manager
Enclosures
REPORT OF LA86RATORY ANALYSIS Page 1. of 14
This report "shall not be reproduced, except in full,
without the written consent of Pace Analytical Services, Inc..

rnaly_tical
lam,
Pace Analytical Services, Inc.
2225 Riverside Dr.
Asheville, NC 28804
[phone]
ANALYTICAL RESULTS
Pace Analytical Services, Inc.
9800 Kincey Ave. Suite 100
Huntersville, NC 28078
[phone]
Project: Lime Residual 05/13
Pace Project No.: 9219197
Sample: TWSA LIME RESIDUAL Lab ID: 9219197001 Collected: 05/13/08 09:45 Received: 05/13/08 12:00 Matrix: Solid
Results reported on a "dry -weight" basis
Parameters Results Units Report Limit DF Prepared Analyzed CAS No.
6010 MET ICP
Analytical Method: EPA 6010 Preparation Method: EPA 3050
Aluminum-
f
Arsenic
5880 m /k
9 g
15.9
1
05/20/08 08:35
05/21/08 01:50
7429-90-5
-Cadmium ----
0.91 mg/kg
0.80
1
05/20/08 08:35
05/21/08 01:50
7440-38-2
Calcium
0.37 mg/kg
0.16
1
05/20/08 08:35
05/21/08 01:50
7440-43-9
Chromium
404000 mg/kg
1590
100
05/20/08 08:35
05/21/08 16:51
7440-70-2
Copper
4.8 mg/kg
0.80
1
05/20/08 08:35
05/21/08 01:50
7440-47-3
_
Lead
64.3 mg/kg
0.80
1
05/20/08 08:35
05/21/08 01:50
7440-50-8
Magnesium
5.2 mg/kg
0.80
1
05/20/08 08:35
05/21/08 01:50
7439-92-1
Molybdenum
2650 mg/kg
15.9
1
05/20/08 08:3.5
05/21/08 01:50
7439-95-4
Nickel
1.8 mg/kg
0.80
1
05/20/08 08:35
05/21/08 01:50
7439-98-7
Potassium
3.7 mg/kg
0.80
1
05/20/08 08:35
05/21/08 01:50
7440-02-0
Selenium
3100 mg/kg
797
1
05/20/08 08:35
05/21/08 01:50
7440-09-7
Sodium
2.2 mg/kg
1.6
1
05/20/08 08:35
05/21/08 01:50.
7782-49-2
Zinc
ND mg/kg
797
1
05/20/08 08:35
05/21/08 01:50
7440-23-5
202 mg/kg
1.6
1
05/20/08 08:35
05/21/08 01:50
7440-66-6
7471 Mercury
Analytical Method: EPA 7471
Preparation Method: EPA 7471
i
Mercury
0.017 mg/kg
0.010
1
05/15/08.11:00
05/15/0818:09
7439-97-6
1 Arcent Moisture
Analytical Method: ASTM D2974-87
Percent Moisture
47.7 % 0.10 1
05/19/08 09:17
9045 pH Soil
Analytical Method: EPA 9045
pH at 25 Degrees C
11.7 Std. Units 0.10 1
05/19/08 12:04
Plant Available Nitrogen
Analytical Method: 40CFR PART 503
Plant Available Nitrogen
43500 mg/kg 1.0 1
05/29/08 08:59
Total Nitrogen Calculation
Analytical Method: 40CFR PART 503
Nitrogen
145000 mg/kg 40.0 1
05/29/08 15:46 7727-37-9
350.1 Ammonia
Analytical Method: EPA 350.1
Nitrogen, Ammonia
62.2 mg/kg 19.1 1
05/21/08 21:53 7764-41-7
351.2 Total Kjeldahl Nitrogen
Analytical Method: EPA 351.2
Nitrogen, Kjeldahl, Total
145000 mg/kg 2680 70
05/28/08 20:04 7727-37-9
353.2 Nitrogen, NO2/NO3
Analytical Method: EPA 353.2
Nitrogen, NO2 plus NO3
ND mg/kg 1.9 1
05/27/08 15:30
365.1 Phosphorus, Total -
Analytical Method: EPA 365.1
Phosphorus
463 mg/kg 34.8 4
05/23/0819:37 7723-14-0
Date: 05/29/2008 03:47 PM
REPORT OF LABORATORY ANALYSIS
This report shall not be reproduced, except in full,
without the written consent of Pace Analytical Services, Inc..
E C,
I 1 IGI�.S.I=
Qual
Page 4 of 14
4F

Analytical Results
Pace Analytical -Asheville
2225 Riverside Drive
Asheville NC 28804
Entered 5/14/2008
—Reported,-5/21/2008
Sample Remark
For 9219197
Sample ID Parameter Cust ID Result Units Method Date Analyzed Analyst
080514-9 % Solids 9219197001 54.5 % SM2540B 5/14/08 CL
080514-9 Fecal Coliform MTF 9219197001 <2 MPN/g SM92210E 5/14/08 CL
Respectfully submitted,
Oena Myers
NC Cert #440,
NCDW Cert #37755,
EPA NCO0909
P.O. Box 228 •Statesville, North Carolina 28687. 7041872/4697

Pace Analytical Services, Inc.
m 2225 Riverside Dr.
.,aee Ialytical Asheville, NC 28804
www. pa&16bs —.
[phone]
September 11, 2008
Pace Analytical Services, Inc.
9800 Kincey Ave. Suite 100
Huntersville, NC 28078
[phone]
Mr. Stan Bryson :
Tuckaseigee Water•& Sewer Co.
1246 West Main Street
Sylva, NC 28779 _
RE: Project: Lime Residual'8/19
Pace Project No.: 9225884
Dear Mr. Bryson:
Enclosed are the analytical results for sample(s) received by the laboratory on August 19, 2008. The
results relate only to the samples included in this report. Results reported herein conform to the
most current NELAC standards, where applicable, unless otherwise narrated in the body of the
report.
0
Inorganic Wet Chemistry and Metals analyses were performed at our Pace Asheville laboratory and
Organic testing was performed at our Pace Huntersville laboratory unless otherwise footnoted. All
Microbiological analyses were performed at the laboratory where the samples were received.
If you have any questions concerning this report, please feel free to contact me.
Sincerely,
Tom Williams
[e-mail]
Project Manager
Enclosures
REPORT OF LABORATORY ANALYSIS
This report shall not be reproduced, except in full,
without the written consent of Pace Analytical Services, Inc..
n
AI I IGitls.l=
T-
Page 1 of 14

Pace Analytical Services, Inc. Pace Analytical Services, Inc.
® 2225 Riverside Dr. 9800 Kincey Ave. Suite 100
ANALYTICAL RESULTS
Project: Lime Residual 8/19
Pace Project No.: 9225884
Asheville, NC 28804 Huntersville, NC 28078
[phone] [phone]
Sample: TWSA Lime Residual Lab ID: 9225884001 Collected: 08/19/08 10:45 Received: 08/19/08 12:54 Matrix: Solid
Results reported on a "dry -weight" basis
Parameters Results Units Report Limit DF Prepared Analyzed CAS No
6010 MET ICP
Aluminum
Arsenic
-Cadmium-- - -
Calcium
Chromium
Copper
Lead
Magnesium
Molybdenum
Nickel
Potassium
Selenium
Sodium
Zinc
7471 Mercury
Me
rcury
�• ti�
Percent Moisture
9045 pH Soil
pH at 25 Degrees C
Plant Available Nitrogen
Plant Available Nitrogen
Total Nitrogen Calculation
Nitrogen
350.1 Ammonia
Nitrogen, Ammonia
351.2 Total Kjeldahl Nitrogen
Nitrogen, Kjeldahl, Total
353.2 Nitrogen, NO2/NO3
Nitrogen, Nitrate
Nitrogen, Nitrite
Nitrogen, NO2 plus NO3
365.1 Phosphorus, Total
Phosphorus
Date: 09/11/2008 11:01 AM
Analytical Method: EPA 6010 Preparation Method: EPA 3050
9250 mg/kg
10.2
1
08/21/08 11:30
08/22/08 04:08
7429-90-5
2.1 mg/kg
0.51
1
08/21/08 11:30
08/22/08 04:08
7440-38-2
ND mg/kg
0.10
1 '
08/21/08 11:30
08/22/08 04:08
7440-43-9
64100 mg/kg
1020
100
08/21/08 11:30
08/22/08 11:27
7440-70-2
12.5 mg/kg
0.51
1
08/21/08 11:30
08/22/08 04:08
7440-47-3
134 mg/kg
0.51
1
08/21/08 11:30
08/22/08 04:08
7440-50-8
5.2 mg/kg
0.51
1
08/21/08 11:30
08/22/08 04:08
7439-92-1
2120 mg/kg
10.2
1
08/21/08 11:30
08/22/08 04:08
7439-95-4
2.5 mg/kg
0.51
1
08/21/08 11:30
08/22/08 04:08
7439-98-7
6.2 mg/kg
0.51
1
08/21/08 11:30
08/22/08 04:08
7440-02-0
3790 mg/kg
511
1
08/21/08 11:30
08/22/08 04:08
7440-09-7
ND mg/kg
1.0
1
08/21/08 11:30
08/22/08 04:08
7782-49-2
535 mg/kg
511
1
08/21/08 11:30
08/22/08 04:08
7440-23-5
291 mg/kg
9.0
1
08/21/08 11:30
08/22/08 04:08
7440-66-6
Analytical Method: EPA 7471 Preparation Method: EPA 7471
0.39 mg/kg
0.032
5
08/20/0811:35
08/21/0813:06
7439-97-6
Analytical Method: ASTM D2974-87
46.2 %
0.10
1
09/02/08 14:52
Analytical Method: EPA 9045
11.9 Std. Units
0.10
1
08/26/08 17:10
Analytical Method: 40CFR PART 503
2500 mg/kg
1.0
1
09/11/08 11:01
Analytical Method: 40CFR PART 503
8210 mg/kg
40.0
1
09/09/08 13:52
7727-37-9
Analytical Method: EPA 350.1
163 mg/kg
9.2
1
08/21/08 20:50
7764-41-7
Analytical Method: EPA 351.2
8210 mg/kg
930
50
09/07/08 10:22
7727-37-9
Analytical Method: EPA 353.2
s
ND mg/kg
18.6
1
08/25/0814:35
ND mg/kg
18.6
1
08/25/08 14:35
ND mg/kg
18.6
1
08/25/0814:35
Analytical Method: EPA 365.1
43.3 mg/kg
7.4
2
08/29/08 14:54
7723-14-0
REPORT OF LABORATORY ANALYSIS
This report shall not be reproduced, except in full,
without the written consent of Pace Analytical Services, Inc..
Qual
Page 4 of 14
.r.
M

Analytical Results
Pace Analytical For: 9225884
9800 Kincey Suite 100
Huntersville NC 28078
Entered 8/20/2008
__Reported: 9/3/2008
Sample Remark
Sample ID
Parameter
Cust ID
Result
Units
Method
Date Analyzed
Analyst
080820-6
% Solids
9225884
54.6
%
SM2540B
8/20/08
CL
080820-6
Fecal Coliform MTF
9225884
<20
MPN/g
SM92210E
8/20/08
CL
Respectfully submitted,
rrh
Dena Myers
NC Cert #440,
NCDW Cert #37755,
EPA NCO0909
P.O. Box 228 e Statesville, North Carolina 28687. 704/872/4697

Pace Analytical Services, Inc.
2225 Riverside Dr.
Asheville, NC 28804
Pace Analytical Services, Inc.
9800 Kincey Ave. Suite 100
Huntersville, NC 28078
Inw.pacelabs:eom:
November 18, 2008
Mr. Stan Bryson ;
__. __Tuckas_eigee Water & Sewer Co.
1246 West Main Street
Sylya,_NC_28779
RE: Project: TWSA Lime Residual 11/4
Pace Project No.: 9231371
[phone]
[phone]
Dear Mr. Bryson:
Enclosed are the analytical results for sample(s) received by the laboratory on November 04, 2008.
The results relate only to the samples included in this report. Results reported herein conform to the
most current NELAC standards, where applicable, unless otherwise narrated in the body of the
report.
Inorganic Wet Chemistry and Metals analyses were performed at out Pace Asheville laboratory and
:Organic testing was performed at our Pace Huntetsville'.laboratory unless otherwise footnoted. All
Microbiological analyses were performed at the laboratory` Where the samples were received.
If you have any questions concerning this report, please feel free to contact me.
ZSJ erely,
T 00 Williams
[e-mail]
Project Manager
Enclosures
REPORT OF LABORATORY ANALYSIS
This report shall not be reproduced, except in full,
without the written consent of Pace Analytical Services, Inc..
ry •CCoy
G�Q1.J=
Page'1 of 14

Pace Analytical Services, Inc. Pace Analytical Services, Inc.
2225 Riverside Dr. 9800 Kincey Ave. Suite 100
Asheville, NC 28804 Huntersville, NC 28078
[phone] [phone]
ANALYTICAL RESULTS
Project: TWSA Lime Residual 11/4
Pace Project No.: 9231371
Sample: TWSA Lime Residual Lab ID: 9231371001 Collected ,,',41/04/08 08:00 Received: 11/04/08 13:14 Matrix: Solid
Results reported on a "dry -weight" basis
Parameters Results Units Report Limit DF Prepared Analyzed CAS No. Qual
6010 MET ICP
Analytical Method: EPA 6010 Preparation Method: EPA 3050
Aluminum
8880 mg/kg
17.6
1
11/06/08 12:55
11/08/08 04:45
7429-90-5
Arsenic
ND mg/kg
0.88-
1
11/06/08 12:55
11/08/08 04:45
7440-38-2
-Cadmium-
0.34 mg/kg
0.18
1
11/06/08 12:55
11/08/08 04:45
7440-43-9
Calcium
364000 mg/kg: v°.
1760
. 100
11/06/08 12:55
11/10/0812:49
7440-70-2
Chromium
7.7 mg/kg
0.88
1
11/06/08 12:55
11/08/08 04:45
7440-47-3
Copper
117 mg/kg
0.88
1
11/06/08 12:55
11/08/08 04:45
7440-50-8
Lead
7.0 mg/kg
0.88
1
11/06/08 12:55
11/08/08 04:45
7439-92-1
Magnesium
2540 mg/kg
17.6
1
11/06/08 12:55
11/08/08 04:45
7439-95-4
Molybdenum
2.4 mg/kg
0.88
1
11/06/08 12:55
11/08/08 04:45
7439-98-7
Nickel
.4.7 mg/kg
0.88
1
11/06/08 12:55
11/08/08 04:45
7440-02-0
Potassium
3070 mg/kg
880
1
11/06/08 12:55
11/08/08 04:45
7440-09-7
Selenium
ND mg/kg
1.8
1
11/06/08 12:55
11/08/08 04:45
7782-49-2
Sodium
ND mg/kg
880
1
11/06/08 12:55
11/08/08 04:45
7440-23-5
Zinc
205 mg/kg
1.8
1
11/06/08 12:55
11/08/08 04:45
7440-66-6
7471 Mercury
Analytical Method: EPA 7471 Preparation Method: EPA 7471
Mercury
0.12 mg/kg •
0.0089
1
11/11/08 16:25
11/12/08 11:22
7439-97-6
-bcent Moisture
Analytical Method: ASTM D2974-87
Percent Moisture
45.4 %
`0.10
1
11/06/08 08:42
9045 pH Soil
Analytical Method: EPA 9045
pH at 25 Degrees C
12.2 Std. Units
0.10
1
11/07/08 12:55
H1
Plant Available Nitrogen
Analytical Method: 40CFR PART 503
Plant Available Nitrogen
3800 ing/kg
1.0
1
11/18/08 15:36
Total Nitrogen Calculation
_ Analytical Method: 40CFR PART 503
Nitrogen
12500- mg/kg
40.0
1
11/18/08 15:30
7727-37-9
350.1 Ammonia
Analytical Method: EPA 350.1
Nitrogen, Ammonia
261 mg/kg.
32.7
1
11/14/08 14:24
7764-41-7
351.2 Total Kjeldahl Nitrogen
Analytical Method: EPA 351.2
Nitrogen, Kjeldahl, Total
12500 mg/kg
728
20
11/06/08 13:37
7727-37-9
R1
353.2 Nitrogen, NO2/NO3
Analytical Method: EPA 353.2
Nitrogen, Nitrate
ND mg/kg
17.3
1
11/17/08 15:39
Nitrogen, Nitrite
ND mg/kg
17.3
1
11/17/08 15:39
MO
Nitrogen, NO2 plus NO3
ND mg/kg
17.3
1
11/17/08 15:39
0,;89
365.1 Phosphorus, Total
Analytical Method: EPA 365.1
Phosphorus
1750 mg/kg
: J 147
0,
20
11/18/08 12:09
7723-14-0
MO
11/18/2008 03:36 PM
REPORT OF LABORATORY
ANALYSIS
Page 4 of 14
This report shall not be reproduced, except in full,
without the written consent of Pace Analytical Services, Inc..
a
V��M.YJi

Analytical Results
Pace Analytical -Asheville For 9231371
2225 Riverside Drive
Asheville NC 28804
Entered 11/5/2008
_ Reported:. .11 /6/2008
Sample Remarks
Sample ID Parameter Cust ID Result Units Method Date Analyzed Analyst
081105-11 % Solids 9231371001 58.4 % SM2540B 11/5/08 DM
081105-11 Fecal Coliform MTF 9231371001 <3 MPNIg SM92210E 11/5/08 DM
Respectfully submitted,
�na Myers
NC Cert #440,
NCDW Cert #37755,
EPA NCO0909
F
P.O. Box 228 o Statesville, North Carolina 28687. 704/872/4697 r
' I

naIX cal
www.pecolabs.com:
January 02, 2009
Mr. Stan Bryson
Tuckaseigee Water & Sewer Co.
1-246-West Main Street
Sylva, NC 28779
Pace Analytical Services, Inc.
2225 Riverside Dr.
Asheville, NC 28804
[phone]
Pace Analytical Service's, Inc.
9800 Kincey Ave. Suite 100
Huntersville, NC 28078
[phone]
RE: Project: Lime Residual 12/22
Pace Project No.: 9234854
Dear Mr. Bryson:
Enclosed are the analytical results for sample(s)'received by the laboratory on December 22, 2008.
The results relate only to the samples included in this report. Results reported herein conform to the
most current NELAC standards, where applicable, unless otherwise narrated in the body of the
report,
Inorganic Wet Chemistry and Metals analyses were performed at our Pace Ashevjlle laboratory and
Organic testing was performed at our Pace Hunter$ville laboratory unless otherwise footnoted'. All
Microbiological analyses were performed at the laboratory where the samples were received.
If you have any questions concerning this report, -please feel free to contact me.
Si rely,
r
;y
T ilHarris
[e-mail]
Project Manager
Enclosures
J REPORT OF LABORATORY ANALYSIS
This report shall not be reproduced, except in full,
without the written consent of Pace Analytical Services, Inc..
1VC M Lcc Oq'
0
u��1
,74
Page 1 of 2

f Analytical Resilts
Pace Analytical
9800 Kincey Suite 100
Huntersville
Entered 12/23/2008.
Reported: 12/30/2008
--Sample-Remark
NC. 28078
For: 9234854
Sample ID Parameter Cust ID Result Units Method Date Analyzed Analyst
081223-11.1 % Solids 9234854001
57.5
%
SM2540B
12/23/08
MD
081223-11.1 Fecal Coliform MTF 9234854001
<20
MPN/g
SM92210E
12/23/08
MD
081223-11.2 % Solids 9234854002 '
56.2
%
SM2540B
12/23/08
MD
081223-11.2 Fecal Coliform MTF 9234854002
<20
MPN/g
SM9221 CE
12/23/08
MD ;
-:_'` pectfully submitted,
Dena Myers
NC Cert #440,
NCDW Cert #37755,
EPA NCO0909
P.O. Box 228 9 Statesville, North Carolina 28687 • 704/872/4697

Pace Analytical Services, Inc. Pace Analytical -Services, Inc.
1aceAnalytical -
2225 Riverside Dr. 9800 KinceyAve. Suite "100
wwwpacelabs,cprn Asheville, NC 28804 Huntersville, NC 28078
[phone] [phone]
January 16,-2009
Mr. Stan Bryson
_Tuckaseigee Water & Sewer Co.
1246 West Main Street.
Sylva, NC 28779
RE: Project: Lime -Residual,
Pace Project. No.: 9235081 -
Dear Mr. Bryson:
Enclosed are the'analytical results for sample(s) received by the laboratory on December 29, 2008.
The results relate only to the samples included in this report. Results reported herein conform to the
most current NELAC standards, where applicable, unless otherwise narrated in the body of the
report: i
Inorganic Wet Chemistry and Metals analyses were performed at our Pace Asheville laboratory and
Organic testing was performed at our Pace Huntersville laboratory unless otherwise footnoted_. All
Microbiological analyses were performed at the laboratory where the samples were received.
If you have any questions concerning this report, please feel free to contact me.
Sincerely,
Tom Williams
[e-mail].
Project Manager
Enclosures
REPORT OF LABORATORY ANALYSIS Page 1 of
(� This report shall not be reproduced, except in full,
without the written consent of Pace Analytical Services, Inc.."

Analytical Results
q,"
Pace Analytical -Asheville
2225 Riverside Drive
Asheville NC 28804
Entered 12/30/20.08
Reported: 1/5/2009
Sample Remark
Sample ID Parameter Cust ID
For: 9235081
Result Units Method Date Analyzed Analyst
081230-4 % Solids TWSA Lime 58.2 % SM2540B 12/30/08 CL
081230-4 Fecal Coliform MTF TWSA Lime <2 MPN/g SM9221 CE 12/30/08 CL
Respectfully submitted,
Dena Myers
NC Cert #440,
NCDW Cert #37755,
EPA NCO0909
P.O. Box 228 • Statesville, North Carolina 28687 0 704/872/4697

Appendix (d)
TCLP Analysis

aceAnalytical
www.pacelabs.com
0
September 17, 2008
Mr. Stan Bryson
- - Tuckaseigee Water & Sewer Co.
1246 West Main Street
Sylva, NC-28779
RE: Project: Sludge TCLP
Pace Project No.: 9226256
Pace Analytical Services, Inc.
2225 Riverside Dr.
Asheville, NC 28804
[phone]
Pace Analytical Services, Inc.
9800 Kincey Ave. Suite 100
Huntersville, NC 28078
[phone]
SEP 2 3 2008 I I
U
Dear Mr. Bryson:
Enclosed are the analytical results for sample(s) received by the laboratory on August 22, 2008. The
results relate only to the samples included in this report. Results reported herein conform to the
most current NELAC standards, where applicable, unless otherwise narrated in the body of the
„ report.
Inorganic Wet Chemistry and Metals analyses were performed at our Pace Asheville laboratory and
Organic testing was performed at our Pace Huntersville laboratory unless otherwise footnoted. All
Microbiological analyses were performed at the laboratory where the samples were received.
If you have any questions concerning this report, please feel free to contact me.
Sin el,
T Williams
[e-mail]
Project Manager
Enclosures
REPORT OF LABORATORY ANALYSIS
Av� \')eYe'
Page 1 of 15
This report shall not be reproduced, except in full,
without the written consent of Pace Analytical Services, Inc..
„.«oq
%r'iplar�4

Pace Analytical Services, Inc. Pace Analytical Services, Inc.
P . +
2225 Riverside Dr. 9800 Kincey Ave. Suite 100
8�11alytlCal Asheville, NC 28804 Huntersville, NO 28078
w mvwpacelabs.com
[phone] [phone]
ANALYTICAL RESULTS
Project: Sludge TCLP
Pace Project No.: 9226256
Sample: TWSA Raw Sludge
Parameters
Lab ID: 9226256001 Collected: 08/22/08 09:50'
Results Units Report Limit DF
Received: 08/22/08 11:42 Matrix: Water
Prepared - Analyzed CAS No. Qua[
8081 GCS Pesticides, TCLP `SPE
Analytical Method: EPA 8081
Preparation Method: EPA 3535
gamma-BHC (L[ndane)
ND ug/L
0.50
1
09/03/08 00:00 09/04/08 21:08 58-89-9
Chlordane (Technical)
ND ug/L
3.0
1
09/03/08 00:00 09/04/08 21:08 57-74-9
Endrin --^ —
ND ug/L
0.50
1
09/03/08 00:00 09/04/08 21:08 72-20-8
Heptachlor epoxide
ND ug/L
0:50
1
09/03/08 00:00 09/04/08 21:08 1024-57-3
Methoxychlor
ND ug/L
1000
1
09/03/08 00:00 09/04/08 21:08 72-43-5
. Toxaphene
ND ug/L
3.0
1
09/03/08 00:00 09/04/08 21:08 8001-35-2
Decachlorobiphenyl IS)
58 %
10-138
1
09/03/08 00:00 09/04/08 21:08 2051-24-3
Tetrachloro-m-xylene (S)
29 %
10-110
1
09/03/08 00:00 09/04/08 21:08 877-09-8
6010 MET ICP, TCLP Analytical Method: EPA 6010 Preparation Method: EPA 3010
Arsenic
NDmg/L
0.025
1
08/29/08 11:00 08/30/08 01:34 7440-38-2
Barium
0.12 mg/L
0.025
1
08/29/08 11:00 08/30/08 01:34 7440-39-3
Cadmium
ND mg/L
0.0050
1
08/29/08 11:00 08/30/08 01:34 7440-43-9
Chromium
ND mg/L
0.025
1
08/29/08 11:00 08/30/08 01:34 7440-47-3
Lead
ND mg/L
0.025
1
08/29/08 11:00 08/30/08 01:34 7439-92-1.
Selenium
ND mg/L
0.050
1
08/29/08 11:00 08/30/08 01:34 7782-49-2
Silver
ND mg/L
0.025
1
08/29/08 11:00 08/30/08 01:34 7440-22-4
t 70 Mercury, TCLP
Analytical Method: EPA 7470
Preparation Method:
EPA
7470
Mercury
ND ug/L
0.20
1
08/29/0813:20 08/30/08 13:10 7439-97-6
8270 MSSV TCLP Sep Funnel
Analytical Method: EPA 8270
Preparation Method: EPA
3510
1,4-Dichlorobenzene
ND ug/L
50.0
1
09/03/08 00:00 09/05/08 00:25 106-46-7
2,4-Dinitrotoluene
ND ug/L
50.0
1
09/03/08 00:00 09/05/08 00:25 121-14-2
Hexachloro-1,3-butadiene
ND ug/L
50.0
1
09/03/08 00:00 09/05/08 00:25 87-68-3
Hexachlorobe nzene
ND ug/L
50.0
1
09/03/08 00:00 09/05/08 00:25 118-74-1
Hexachloroethane
ND ug/L
50.0
1
09/03/08 00:00 09/05/08 00:25 67-72-1
2-Methylphenol(o-Cresol)
ND ug/L
50.0
1
09/03/08 00:00 09/05/08 00:25 95-48-7
3&4-Methylphenol(m&p Cresol)
ND ug/L
50.0
1
09/03/08 00:00 09/05/08 00:25 '
Nitrobenzene
ND ug/L
50.0
1
09/03/08 00:00 09/05/08 00:25 98-95-3
Pentachlorophenol
ND ug/L
50.0
1
09/03/08 00:00 09/05/08 00:25 87-86-5
Pyridine
ND ug/L
50.0
1
09/03/08 00:00 09/05/08 00:25 110-86-1
2,4,5-Trichlorophenol
ND ug/L
50.0
1
09/03/08 00:00 09/05/08 00:25 95-95-4
2,4,6-Trichlorophenol
ND ug/L
50.0
1
09/03/08 00:00 09/05/08 00:25 88-06-2
Nitrobenzene-d5 (S)
71 %
30-150
1
09/03/08 00:00 09/05/08 00:25 4165760-0
2-Fluorobiphenyl IS)
68 %
30-150
1
09/03/08 00:00 09/05/08 00:25 321-60-8
Terphenyl-d14 (S)
81 %
30-150
1
09/03/08 00:00 09/05/08 00:25 1718-51-0
Phenol-d6 IS)
26 %
25-150
1
09/03/08 00:00 09/05/08 00:25 13127-88-3
2-Fluorophenol IS)
33 %
25-150
1
09/03/08 00:00 09/05/08 00:25 367-12-4
2,4,6-Tribromophenol IS)
91 %
25-150
1
09/03/08 00:00 09/05/08 00:25 118-79-6
8260 MSV TCLP
Analytical Method: EPA 8260
Benzene
ND ug/L
125
25
08/31/08 11:28 71-43-2
2-Butanone (MEK)
348 ug/L
250
25
08/31/08 11:28 78-93-3
Carbon tetrachloride
ND ug/L
125
25
08/31/08 11:28 56-23-5
C'-olorobenzene
ND ug/L
125
25
08/31/08 11:28 108-90-7
1'
Date: 09/17/200810:10 AM
REPORT OF LABORATORY ANALYSIS Page 5 of 15
This report shall not be reproduced, except
in full,
without the written consent
of Pace Analytical Services, Inc..

Analytical
www.pacelabsxom
Project: Sludge TCLP
Pace Project No.: 9226256
Pace Analytical Services, Inc.
2225 Riverside Dr.
Asheville, NC 28804
[phone]
ANALYTICAL RESULTS
Pace Analytical Services, Inc.
9800 Kincey Ave. Suite 100
Huntersville, NC 28078
[phone]
Sample: TWSA Raw Sludge
Lab ID: 9226256001 Collected: 08/22/08 09:50
Received: 08/22/08 11:42 Matrix: Water
Parameters
Results Units
Report Limit
DF
Prepared Analyzed CAS No. Qua]
8260 MSV TCLP
Analytical Method: EPA 8260
Chloroform
ND ug/L
125
25
08/31/08 11:28 67-66-3
1,4-Dichlorobenzene
ND ug/L
125
25
08/31/08 11:28 106-46-7
^I;2=Di`chlor0ethane
ND ug/L
125
25
08/31/08 11:28 107-06-2
1,1-Dichloroethene
ND ug/L
125
25
08/31/08 11:28 75-35-4
'Tetrachloroethene
ND ug/L
125
25
08/31/08 11:28 127-18-4
Trichloroethene
ND ug/L
125
25
08/31/08 11:28 79-01-6
Vinyl chloride
ND ug/L
125
25
08/31/08 11:28 75-01-4
1,2-Dich]oroethane-d4 (S)
95 %
79-120
25
08/31/08 11:28 17060-07-0
Toluene-d8 (S)
96 %
70-120
25
08/31/08 11:28 2037-26-5
4-BromofIuorobe nzene (S)
93 %
87-109
25
08/31/08.11:28 460-00-4
Dibromofluoromethane (S)
92 %
85-115
25
08/31/08 11:28 1868-53-7
9095 Paint Filter Liquid Test
Analytical Method: EPA 9095
Free Liquids
0
1.0
1
08/27/08 14:52
i
Date: 09/17/2008 10:10 AM
REPORT OF LABORATORY ANALYSIS
This report shall not be reproduced, except in full,
without the written consent of Pace Analytical Services, Inc..
M CCyC+
Trmftl`nff
Page 6 of 15

:..Pace Analytical Services, Inc. Pace Analytical Services, Inc.
aceA alytica% _.. , r 2225 Riverside Dr. 9800 Kincey Ave. Suite 100
J Asheville, NC 28804 Huntersville, NC 28078
www.pecela6s:com
[phone] [phone]
November 13, 2008 NOV 2 4 208 t
Mr. Stan Bryson ;
_. Tuckaseigee Water& Sewer -Co.
1246 West Main Street,
_ - Sy"Iv_a, NC 28779
RE: Project: Wastewater 11/4 .
Pace Project No.: 9231377
Dear Mr. Bryson:
Enclosed are the analytical results for sample(s) received by the laboratory on November 04, 2008.
The results relate only to the samples included in this report. Results reported herein conform to the
most current NELAC standards, where applicable, unless otherwise narrated in the body of the i
report.
Inorganic Wet Chemistry'and Metals'analyses were performed at our -Pace Asheville laboratory and
Organic testing was performed at our Pace Huntersville laboratory unless otherwise footnoted. All
Microbiological analyses were performed: at the laboratoy where the samples were received.
If you have any questions concerning this report, please feel free to contact me.
Si rely,
To li ms
[e-mail]
Project Manager
Enclosures
REPORT OF LABORATORY ANALYSIS Page 1 of 3
This report shall not be reproduced, except in full,
without the written consent of Pace Analytical Services, Inc..

i
Analytical Environmental Services, Inc. Date: 13-Nov-08
CLIENT:.
Pace Analytical Services, Inc.
Client Sample ID: RAW SLUDGE
Lab Order:
0811364
Tag Number:
Project:
9231377
Collection Date: 11/4/2008 11:30:00 AM
.Lab ID:
0811364-001A
Matrix: SLUDGE
Analyses
Result
Limit Qual Units BatchID DF Date Analyzed
HERBICIDES, TCLP
SW1311/8161A (SW3510B) Analyst: El
2,4,5-TP (Silvex)
BRL
0.20 mg/L 106417 1 11/12/2008 1:17:00 PP
2,47D
BRL
0.20 mg/L 106417 1 11/12/2008 1:17:00 PP
Surr: DCAA
91.3
36.6-149 %REC 106417 1 11/12/2008 1:17:00 PP
Qualifiers: * Value exceeds Maximum Contaminant Level
> Greater than Result value
BRL Below Reporting Limit
H Holding times for preparation or analysis exceeded
f ; N Analyte not NELAC certified
< Less than Result value
B 4nalyte detected in the associated Method Blank
E Estimated value above quantitation range
J Estimated value detected below Reporting Limit
Rpt Lim Reporting Limit rage I of I

Appendix (e)
Pathogen and
Vector Attraction
Reduction Forms

ANNUAL PATHOGEN AND VECTOR ATTRACTION REDUCTION FORM
Facility Name: Tuckaseigee Water and Sewer Authority Permit Number: WQ 005763
WWTP Name: TWSA Plant #1 NPDES Number: NC 0039578
Monitoring Period: From 1/1/2008 To 12/31/2008
Pathogen Reduction (40 CFR 503.32) - Please indicate level achieved and alternative performed:
Class A: Alternative 1 ❑
Alternative 4 a ❑
If applicable to alternative performer
Compost ❑ Heat Drying ❑
Beta Rav ❑ Gamma Rav ❑
Alternative 2 ❑ 1 Alternative 3
Alternative 5 N I Alternative 6 ❑
Class A only) indicate "Process to Further Reduce Path(
Heat Treatment ❑ 1 Thermophilic ❑
Pasteurization ®.
Class B: Alternative 1 ❑ Alternative 2 ❑ Alternative 3 ❑
If applicable to alternative performed (Class B only) indicate "Process to Significantly Reduce Pathogens":
Lime Stabilization ❑ Air Drying ❑ 1 Composting ❑ Aerobic Digestion ❑
Anaerobic Digestion❑ .:.::::::...>:.;::;::.::.;:>:
..:..:.:.::::::.
If applicable to alternative performed (Class A or Class B) complete the following monitoring data:
al
Parameter Allowable Level Pathogen Density NumBer Emcee o regofncy Sample AnalyuTech-
in
Sludge Minimum Geo. Mean MaximumUnitsences Type
niaiie
2x10tothe 6th
power MPN per
gram of total
solids or 2 x 10 to
Fecal Coliform the 6th power
1000 mpn per
gram of total solid < 2 1 < 12 1 < 200 1 mpn/gm
Salmonella bacterial 3 NWN per 4
(in lieu of fecal grams total solid
0 I 8/year I Grab 1-5 M
C?,Q ,Q
Vector Attraction Reduction (40 CFR 503.33) - Please indicate option performed:
Option 5 Option Ot ❑ 3 O to ❑ Option 1 ❑ Option 2 ❑ Option ❑
p
P pp
O tion 10 8 Option ❑ 7 in Oto ❑ 6 Option Option o Option ❑ ❑
p p
p p
No vector
r attraction reduction options were perform
ed ❑
CERTIFICATION STATEMENT (please check the appropriate statement)
® "I certify, under penalty of law, that the pathogen requirements in 40 CFR 503.32 and the vector
attraction "reduction requirement in 40 CFR 503.33 have been met."
❑ "1 certify, under penalty of law, that the pathogen requirements in 40 CFR 503.32 and the vector
attraction reduction requirement in 40 CFR 503.33 have not been met." (Please note if you check
this statement attach an explanation why you have not met one or both of the requirements.)
"This determination has been made under my direction and supervision in accordance with the
system designed to ensure that qualified personnel properly gather and evaluate the information
used to determine that the pathogen and vector attraction reduction requirements have been met. I
am aware that there are significant penalties for false certification including fine and imprisonment."
Stan Bryson, WWTP Supt.
Preparer Name and Title (type or print)
��E S:2� -
Signature of Pre rer
g p
Land Applier Name and Title (if applicable)(type or print)
Signature of Land Applier (if applicable) Date
DENR FORM RF (5/2003)

Appendix (f)
Pathogen and
Vector Attraction
Reduction
Lab Sheets/
Records

TWSA LIME.STABILIZATION .
DAILY RECORD
..DATEID fl .
r"*
START, STOP TOTAL,
RUN TIME, HRS no
F ,
DRY TON
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDS a PRESS, °% SOLIDS ,
LIME/SLUDGE RATIO TOTAL PRODUCTION, DRY TONS
Inlet reached temp @ ,
Outlet reached temp @ d'
PATHOGEN REDUCTION VECTOR ATTRACTION -REDUCTION
TEMPERATURE of
TIME
INTO
VESSEL.
OUT OF
VESSEL
OPERATOR
1.5
END'
TIME
OPERATOR
r s
INITIAL PH
-5x.03=,450 -
.
, ,.I�,Gro�tiSa=►�.51�.
'S
2 HRS.-
1, .3.11I,o3 =. )1.7
1 ;2,. 5 7 117 = 1.2, 473
e{
22 HRS. 1 Z 570 .
OPERATIONAL
BELT PRESS SPEED, % "Coto
POLYMER PUMP SPEED, %16
SLUDGE PUMP' SPEED, % CGb GPM �1
LIME FEED AUGER, % LBS/HR 0 .

TWSA LIME STABILIZATION
DAILY RECORD yy
DATE
START STOP TOTAL
1-5-4 -7 D
RUN TIME, HRS 10
SLUDGE FEED, GAL L/ 0�
LIME FEED, LBS
SLUDGE FEED % SOLIDS PRESS , % SOLIDS1
LIM I E/SLUDGE RATIO TOTAL PRODUCTION, DRY TONS r75
Inlet reached temp
Outlet reached temp
PATHOGEN REDUCTION VECTOR'ATTRACTION REDUCTION
TFMPFRATLJRF'nF
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
0
q9.
3
ry.TIME
'INITIAL PH' I oo7,q 7
ff o
— f36'
2 HRS.
I -!S-oq
A5 - .7 1. 1 3,61 Y. 6 -5
!;;Z,553
22 HRS. 155
...................... ; ................ ......................................................... ......................................................
OPERATIONAL
-6 BELT PRESS SPEED, %
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, % GPM
LIME FEED AUGER, % Q LBS/H'
MIXER SPEED, % Q0 o
Revised BMW
TON
OPERATOR
-
rV1
PE USED-44?6'�/"464 W60
ANKS MIXED

TWSA LIME STABILIZATION
DAILY RECORD
i
DATE'—/
START STOP TOTAL
RUN TIME, HRS T
SLUDGE FEED,.GAL
-- .4, Cl
LIME FEED; LBS 'h
SLUDGE FEED % SOLIDS
PRESS , % SOLIDSI
LIME/SLUDGE RATIO
J.o
TOTAL PRODUCTION, DRY TONS
Inlet reached temp .p_
Outlet reached temp @
0
PATHOGEN REDUCTION
VECTOR ATTRACTION REDUCTION
TFIVIPFRATI IPF `nl=
TIME
INTO -
VESSEL
OUT OF.
VESSEL
OPERATOR
q:
Aar
V,
01
0,6 0L
fm
t q7
TON
TIME
OPERATOR
12,3 10.
UlJ
INITIAL PH
'aS - aol
2 HRS. - A,9, 3
Rp- Olt
03
4 q, 12, 3 41
T,60
22t*H*RS.
lel
7h4
OPERATIONAL
BELT PRESS SPEED, % _ 3S Z'.
POLYMER PUMP SPEED, % 960/e�
SLUDGE PUMP SPEED, % 'Kld GPM D
LIME FEED AUGER, LBS/HR 1056;
MIXER SPEED, %
R6vised 8112103
................................................................................
POLYMER USAGE
PE USED A'/
ANkS MIXED
_iTERSrrANiK- .1"'14
45-

TWSA LIME STABILIZATION
DAILY RECORD
DATE
�. START STOP TOTAL
RUN TIME, HRS - I (� , r,
SLUDGE FEED, GAL 5
LIME FEED, LBS
SLUDGE FEED °% SOLIDS
LIME/SLUDGE RATIO
Inlet reached temp @
G)!
Outlet reached temp @
I P, o
PATHOGEN REDUCTION
TEMPERATURE OF
INTO
OUT OF
TIME VESSEL
VESSEL OPERATOR
mmm I
mmmm
PRESS , °% SOLIDS
TOTAL PRODUCTION, DRY TONS
VECTOR ATTRACTION REDUCTOOf
•
TIME
Ia�61-o 13ot = ,a,y�g
315
INITIAL PH
95- ad. F= 4,-21(03
I�.b3=.ice = la SO
q
2 HRS. Sy
22 HRS.
OPERATIONAL
BELT PRESS SPEED, % _ !�Q DZ
POLYMER PUMP SPEED, %
.SLUDGE PUMP SPEED, % . c2, C b GPM
LIME FEED AUGER, % (� ��6 LBS/HR a�
MIXER SPEED, % I no �D
Revised 8/12103
OPERATOR
fe-1
I?13 /-•Z'17-o0
POLYMER USAGE
PE USED Y16 C
TANKS MIXED
R�:i «s

TWSA LIME STABILIZATION
DAILY RECORD j
DATE
RUN TIME, HRS; C�
SLUDGE FEED, GAL
LIME FEED-, LBS
SLUDGE FEED °% SOLIDS
LIME/SLUDGE RATIO
Inlet reached -temp @
Outlet reached temp @ `
PATHOGEN REDUCTION
TEMPERATURE of
INTO ; . OUT OF
TIME VESSEL VESSEL OPERATOR.
I okuo
3 . ray
- 1
: o?D 0
606
STOP
49 4Q
PRESS , °% SOLIDS
TOTAL PRODUCTION, DRY TONS 4
)RY TON
1•35-
VECTOR ATTRACTION REDUCTION .
TIME 1 2,'v7, l `{..f = . I.;C OPERATOR
2 �t INITIAL PH
.2 HRS:i, 0 21_L-L(2)
57,£3X
22 HRS. , /4 4
OPERATIONAL
BELT PRESS SPEED, la .
POLYMER PUMP SPEED, .% g
SLUDGE PUMP SPEED, % GPM
LIME FEED AUGER, % LBS/HR 1 (�
MIXER SPEED, %
Revised BMW
PE USED
ANKS MIXED
_ITERS/TANK % 14
f

.POLYMER USAGE /
TYPE USED
TANKS MIXED
TWSA LIME STABILIZATION
DAILY RECORD
DATE
START STOP TOTAL.
RUN TIME, HRS
SLUDGE FEED, GAL I 1 * 1 (7 q I�
LIME FEED; LBS.1, 9 45_77—T;
(a
SLUDGE FEED % SOLIDS PRESS S. % SOLIDS "
7
LIMEfSLUDGE RATIO �� TOTAL PRODUCTION, DRY TO
- Inlet reached temp @ �U l
Outlet reached temp @ .
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION .
TEMPERATURE of
TIME
INTO :
VESSEL
OUT OF
VESSEL
OPERATOR,
' /mil
%J
�0
92.
Gas
64,
TIME
OPERATOR
71' 1� : INITIAL PH1Z,Z9 .
t-1
2 HRS.
ZS-Z(;?._' 3.3A ..0,75 .0'5�\
22 MS.
OPERATIONAL
BELT PRESS SPEED, % Co
POLYMER PUMP SPEED, % 3
SLUDGE PUMP SPEED, % 77S GPM 1
LIME FEED AUGER, % S LBS/HR 5
MIXER SPEED, % t o o

TWSA LIME STABILIZATION
DAILY RECORD
DATE
j
RUN TIME, HRS
SLUDGP_''.FEED, GAL
LIME FEED; LBS
SLUDGE FEED °h SOLIDS
LIME/SLUDGE RATIO
Inlet reached temp @
Outlet reached temp @
91
PATHOGEN REDUCTION
TEMPERATURE nF
TIME
INTO .
VESSEL
OUT OF
VESSEL
OPERATOR
d�
(710
ofln
1' �
l91
C2
/q
199
146
' 1 CO .
09 9 .
q1b
STOP
DRY TON
1417.
PRESS .% SOLIDS
TOTAL PRODUCTION, DRY TONS ` C�
VECTOR ATTRACTION REDUCTION
TIME OPERATOR
.21 '30 INITIAL PH I Z • Z 2_.
4' 2 HRS.'2 �
PC, 66 ' 22 HRS.
OPERATIONAL
BELT PRESS -SPEED, % 5 JC
POLYMER PUMP SPEED, % '7? U
SLUDGE PUMP SPEED, .% b GPM t0
LIME FEED AUGER, % �-� LBS/HR
MIXER SPEED, % DID
Revised 8/12103
POLYMER USAGE
TYPE USED ` bAiS v Y,'/4-0
TANKS MIXED
.T q_
I (0;5

TVVSA LIME STABILIZATION
DAILY RECORD
DATE
START STOP TOTAL
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDS a PRESS, . % SOLIDS1
LIME/SLUDGE RATIO TOTAL PRODUCTION, DRY TONS -
Inlet reached temp Q
outlet -reached temp @ J Q,
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TEMPERATURE'oF
TIME
INTO
VESSEL
OUT OF
VESSEL'
OPERATOR
tovi
TIME-
AS- 91-11-3,14on =,,oq3 OPERATOR
j,2. (P(—, 6q3 12-517
INITIAL PH
09-
2 HRS.
t103= Jzn
22'HRS.
.... UID .........................................................................................................................
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, % GPM P"n
.LIME FEED AUGER, LBS/HR
MIXER SPEED, % I Q0_10
Revised 8/12103
TYPE USED
TANKS MIXED
ILITERS/TANK _50�3 _j

TWSA LIME STABILIZATION o V
DAILY RECORD
DATE
START_ t-� STOP TOTAL
RUN TIME, HRS'
DRY TON
SLUDGE FEED, GAL Ion �3
LIME FEED, LBS
SLUDGE FEED % SOLIDS . C-) PRESS, % SOLIDS
LIMEISLUDGE RATIO a TOTAL PRODUCTION, DRY TONS
Inlet reached temp @ dial
Outlet reached temp @ •�
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TEMPERATURE 'oF
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
193
/111)9
199
A03
C--014.
3 `jg
Ob
��
C 11v
5 I' a9
0
7,100
�C)q
9,65
cm
la�x�b3=�I
TIME
19 - If 'F
OPERATOR
y�-�
l' 36
INITIAL PHIc, 3S---
6l
As ao�=y,�IGo3=�13a
3�
2 HRS.
rn
'S- =4J1,o3 =, jai
U'qq -, tz:-1a.3��F
3C
22 HRS.
.........................................................................................................................................
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, PJ
SLUDGE PUMP SPEED, % 59 GPM % c�
LIME FEED AUGER, % ` 0 LBS/HR 3
MIXER SPEED, % ( D /,
Revised 8/12103
POL
71 PE USED // Q � "Li5
TANKS MIXEDW!!ff It

TWSA LIME STABILIZATION ;
DAILY RECORD
DATE " (�
START STOP TOTAL
RUN TIME, HRS o
DRY TON
SLUDGE FEED,GAL
I.
LIME FEED, LBS
SLUDGE FEED % SOLIDS
'
PRESS °� SOLIDS 1
7771
LIME/SLUDGE RATIO
TOTAL PRODUCTION, DRY TONS
" 0
Inlet reached temp
Outlet reached temp 0-
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TFMPFRATURF'nF
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
c�d 3
1413
� L
a0 7.
�Mq
�m
- i
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, %° 3�
SLUDGE PUMP SPEED, % 30 GPM 7
LIME FEED AUGER, % 70 LBSA-IR f
MIXER SPEED, % l Q aIa
Revised W12/03
TIME 025. a 3sX.03 `.11y OPERATOR
116.z. 114=�
7 3D. INITIAL" PH
s^ al, o y u, 03 - ,1 I
l : 3 6 2 HRS.
22 HRS:
TYPE USED % C) + 4Lq_ f3
TANKS MIXED
LITERS/TANK
`I, tF. I vto —5

TWSA LIME STABILIZATION
DAILY RECORD
DATE 0t-7
START
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDS 1 0 �
LIME/SLUDGE RATIO
Inlet reached temp Q 9:09,
Outlet reached temp @ IV3 3
PATHOGEN REDUCTION
TEMPERATURE'oF
TIME
INTO -
VESSEL
OUT OF
VESSEL
.
OPERATOR
-33-1
0
0'33
9-D
Igo
I R
��;�
5 % 3s,
dog
900-
Fvn
17; o o
3
TOTAL
�nl �-
DRYTON
c2,7 -7
PRESS, % SOLIDS1
ToWd. PRODUCTION, DRY TONS
VECTOR ATTRACTION REDUCTION
TIME OPERATOR
1az Sol-. It/
'T30 INITIAL PH'
HR& [a, qq-
ASS%,,qr,63- t3a
.139 qoZ
22 HRS.
......................................................................................................................... ........... .........................
OPERATIONAL
BELT PRESS SPEED; '%
POLYMER PUMP SPEED, % SO
SLUDGE PUMP SPEED.% GPM
LIME FEED AUGER, LBS/H
o 61
MIXER SPEED, % 0/t,
ReAsed 8/12/03
POLYMER USAGE
TYPE USED ,$//&Og
TANKS MIXED
ul ILiTERS/TAN'K -i 3 I
q 5-. ( Pb _5

TWSA LIME STABILIZATION
DAILY RECORD
DATE ®-
START
STOP TOTAL
RUN TIME, HRS �° � � O0
DRY TON
SLUDGE FEED, GAL
LIME FEED; LBS 55
SLUDGE FEED % SOLIDS 3 PRESS, % SOLIDS
LIME/SLUDGE RATIO e4 TOTAL PRODUCTION, DRY TONS F-,? •
Inlet reached temp @ b
Outlet reached temp @ %13
PATHOGEN REDUCTION
TEMPERATURE :oF
TIME' _
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
�32„
o�
l SW
�C
e4y
L.4
(? e
/479
51 32-
EV%.A
i`��(JOD3
9•0(
VECTOR ATTRACTION REDUCTION
TIME pIS-. 3;y ^— L�.(P 1C, 63-" 616OPERATOR.
ra. la. q7a
TL 2 INITIAL PH (a."t-7 fv�
2HRS. f�Z
�5= 11.b=3,Kx; 03 _ ,10a
12.55—,loa=ta,y
22 HRS.
................................... .................................................................................... :............................................
OPERATIONAL
BELT PRESS SPEED, % S
POLYMER PUMP SPEED, % �)
SLUDGE PUMP SPEED, % 3 S GPM �� O
LIME FEED AUGER, % �� LBS/HR ( c� D
MIXER SPEED, %
Revised 8112103
TYPE USED
ANKS MIXED
LITERS/TANK -5 4-_

TWSA LIME STABILIZATION
DAILY RECORD
DAT
START >> STOP TOTAL
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED %SOLIDS - 131 PRESS , °% SOLIDS
LIMEISLUDGE RATIO TOTAL PRODUCTION, DRY TONS
- Inlet reached temp @ �'
e -
Outlet reached temp-@
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TEMPERATURE 'oF
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
i.
3; �/
;6
S 51"7
90&��
Cl
!7
1
TIME
ia, rod. - , o� = OPERATOR
'"T�.QI)
INITIAL PH
AS-a31= ),-A
(? U
2 HRS. l
3-14-og
95-a1.Lt=3.ioX.0-5
Fr;.
fa,(pq ".10`+j�: 1.7
7: UO .
22.HRS.. /1.5
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, % �O
SLUDGE PUMP SPEED, % lz(J GPM S
LIME FEED AUGER, %" CD LBS/HR 1
MIXER SPEED, %
l I
Revised 8112103
POLYMERUSAGE
TYPEUSEDi
TANKS MIXED
g5rI

RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED; LBS
TWSA LIME STABILIZATION
DAILY RECORD
DATE-3 Zj&
START" STOP TOTAL
--t SD I
".7 c9 3k Z "73 0
DRYTON
SLUDGE FEED % SOLIDS ' o` PRESS, % SOLIDS
LIME/SLUDGE RATIO - O TOTAL PRODUCTION, DRY TONS
inlet reached temp @ G
Outlet reached temp @
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TEMPERATURE"oF
'TIME
INTO -
VESSEL
OUT OF,
VESSEL
-OPERATOR
i'
1 0
ISM"�
TIME
�5=al�3=3.711/ OPERATOR
5
INITIAL PH
la.3a- . ►a3= I�.a��i
�O
-
'2SSHR^S.j
: 22 HRS.
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, %
SLUDGE PUMP. SPEED, % GPM
LIME FEED AUGER, % iaU LBS/HR I{�
MIXER SPEED, % 16 0
POLYMER USAGE
TYPE USED
TANKS MIXED
Revised 81171D3 j
A NUJ f03.
1�5

RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, _LBS
TWSA LIME STABILIZATION
DAILY RECORD
DATE T f
START STOP TOTAL
7► 55 1)
SLUDGE FEED eb SOLIDS
LIME/SLUDGE RATIO
Inlet reached temp @
Outlet reached temp @
PATHOGEN REDUCTION
TFMPFRATI IRF nF
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
1
315d-
5 Sol
-�,03
Rod-
f-r6-1
a D
DRY TO
PRESS. % SOLIDS
TOTAL PRODUCTION, DRY TONS
VECTOR ATTRACTION REDUCTION
TIME ls-a)'to=3,4>I,�3=� . OPERATOR
I� la.� (Oa= 1:2 33T
TOO INITIAL PH 19. 3q . I C 0-1_
d0 2 HRS.
Ia.gL-,1302 ,329'6
7 %/5' 22 HRS:
OPERATIONAL
BELT PRESS SPEED,
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, % ipO GPM
LIME FEED AUGER, %_lp LBS/HR�_
MIXER SPEED, %
Revised 8112103
POLYMER USAGE /
TYPE USED
TANKS MIXED
1 -. \ tb s
L

RUN TIME, HRS
SLUDGE FEED, GAL
-LIME FEED, LBS
TWSA LIME STABILIZATION
DAILY RECORD/
DATE ! ��
START STOP TOTAL
'2 ,00 1.56 1Q, :
SLUDGE FEED % SOLIDS ® (�
LIME/SLUDGE RATIO I I
Inlet reached temp @ . ,t3 o
Outlet reached temp @ .° b
PATHOGEN REDUCTION
TEMPERATURE 'nF
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
a
`0 3
d}
, 001��:
-To`-
.9,D7
9 (p
DRY
PRESS. % SOLIDS -
TOTAL PRODUCTION, DRY TONS
VECTOR ATTRACTION REDUCTION .
TIME ;tS-aa,3=,7X.b3=,.Q1 OPERATOR
► : 5a-O S'I 12.4 39
30, INITIAL PH
a1g=3.�Y.d3=.aYI�
30 2 HRS. 1Z 3T_
.214= 3,11Y,03 =40.1
77 30 22 HRS. _
5 .1L®C3.............. 2 fl: .............. C?.5...................w►............... :........................................................................................................................................................
OPERATIONAL P[)I YMFR I Icnrr;
BELT PRESS SPEED, %(�
� F
POLYMER PUMP SPEED, % J
SLUDGE PUMP SPEED, % GPM �• 23
LIME FEED AUGER, %_ 50 LBS/HR 1 d i
MIXER SPEED, % 10 d
Revised 8/12103
YPE USED 4R4,48ti-S16
ANKS MIXED

TWSA LIME STABILIZATION
DAILY RECORD
DATE -
START
RUN TIME, HRS S�
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED °% SOLIDS
S
_ LIME/SLUDGE RATIO
Inlet reached temp @
Outlet reached temp @
PATHOGEN REDUCTION
TEMPERATURE OF
INTO
OUT OF
TIME VESSEL
VESSEL OPERATOR
q-�.��tj
t
/1: ff4
cn,
9b011
1- Lia
,a® 6
05
e'
TOTAL
',®o
PRESS, °% SOLIDS
TOTAL PRODUCTION, DRY TONS ,9
m
VECTOR ATTRACTION REDUCTION
TIME 157-:21.1 lz-319,o3'=:Og4,
®�
INITIAL PH11,1p
,t17= 1140
D ©
2 HRS.
.,DL-
22 HRS:
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, % GPM
LIME FEED AUGER, %_ LBS/HR
MIXER SPEED, % f ©C)
}
Revised 8112103
OPERATOR
POLYMER USAGE
TYPE USED
TANKS MIXED
ILITERS/TANK .

TWSA LIME STABILIZATION
DAILY RECORD
DATE __ /�► / tf /_
START STOP TOTAL
RUN TIME, HRS 7 f 0 0 I
DRY TON
SLUDGE FEED, GAL
LIME FEED; LBS
SLUDGE FEED °% SOLIDS L I • 1 PRESS , °% SOLIDS
LIME/SLUDGE RATIO TOTAL PRODUCTION, DRY TONS
Inlet reached temp
1 q:14
Outlet reached temp @
o
PATHOGEN
REDUCTION
TEMPERATURE oF_
INTO
OUT OF
TIME
VESSEL
VESSEL
OPERATOR
A0 -T
3,
9,o�
�wi
0
To 1)
9-
VECTOR ATTRACTION REDUCTION
TIME5�19;7-5.3X.o3-,ISg . OPERATOR
' o D INITIAL PH
12,'14 -, N7. = 0.313
06 2 HRS. 2. 31
�S=a►.�=3,�K.o3=,a22
�� � O o 22 HRS. [ 9. 33
OPERATIONAL
BELT PRESS SPEED,
POLYMER PUMP SPEED, % S�
SLUDGE PUMP SPEED, % tUU CS GPM qV , ol*,J
LIME FEED AUGER, %_ (9� LBS/HR
MIXER SPEED, % O D
Revised 8/12/03
POLYMER USAGE
YPE USED 4
ANKS MIXED

TWSA LIME STABILIZATION
DAILY RECORD.
DATE
START STOP TOTAL
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED °% SOLIDS U
LIM JSLUDGE RATIO
Inlet reached temp @ "i
Outlet reached temp @
PATHOGEN REDUCTION
TFMPFRATI IPF'nF
TIME
INTO
OUT OF
VESSEL
OPERATOR
VESSEL
tt-/!
Coo
Co
1
/99
a 0.3
TON
PRESS, °% SOLIDS
TOTAL PRODUCTION, DRY TONS p
VECTOR ATTRACTION REDUCTION
TIME Xrd'3 IDS OPERATOR
ra,30-,ros= sar�s
of 3 INITIAL PH
T i 36 2 HRS.'
-a
9. d3= 2x, ,It7
3 D 22 HRS.
OPERATIONAL
BELT PRESS SPEED, % IJ
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, % ` `' ~ S O GPM 6 .
LIME FEED AUGER, %- l LBS/HR 13
MIXER SPEED, % © Q
Revised 8112/03
POLYMER USAGE
YPE USED IK f 8m 0 to t,
ANKS .MIXED

j SS}TAW
RUN TIME, .HRS 9 ' 15
SLUDGE FEED, GAL
TWSA LIME STABILIZATION
DAILY RECORD ,
DATE '7 A2
STOP TOTAL
DRY TON
LIME FEED', LBS
SLUDGE FEED °% SOLIDS
LIME/SLUDGE RATIO
- Inlet reached temp @
Outlet reached temp
PATHOGEN REDUCTION
TFMPFRATI IRF'nF
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
CD
-�
`ra
s�
r
t v �
e o
aS
o
y
;k64m
�,
PIN
PRESS , % SOLIDS
TOTAL PRODUCTION, DRY TONS
VECTOR ATTRACTION REDUCTION
TIME
=3��SX�03-�1 OPERATOR
3
!
INITIAL PH j Q
25-mo='ix.v3=..i
3
2 HRS. 1�, qj— rryL
fa, 56-,►�=1a,4a�
` 3
22 HRS. L J Cry"
.........................................................................................................................:...............................:..........
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, %D
SLUDGE PUMP SPEED,. % GPM 2,
LIME FEED AUGER, %, to ') LBS/HR
MIXER SPEED, %
j
Revised'8112/03
TYPE USED �� �� OL
TANKS MIXED
_ITERS/TANK ��'�

TWSA LIME STABILIZATION
DAILY RECORD
DATE 41A q lo k-
START STOP TOTAL
RUN TIME, HRS U TOO
DR)
SLUDGE FEED, GAL Qi
LIME FEED', LBS L Lo
SLUDGE FEED % SOLIDS PRESS .% SOLIDS�-
LIME/SLUDGE RATIO TOTAL PRODUCTION, DRY TONS
Inlet reached temp p—
Outlet reached temp
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TEMPERATURE'oF
TIME
I INTO
VESSEL
I OUT OF
VESSEL-
.
OPERATOR
R: �
1 �
�0-
Aoa
R9 -
�..
I.,
L403.
13 V.
5 V
0 . 0
OPERATIONAL
BELT PRESS SPEED 4011/0
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, .% oGPM
LIME FEED AUGER, % rl 0 alb LBS/HR
MIXER SPEED, %
Revised 8112103
TIME •OPERATOR
INITIAL PH —IFLA
X-Aid = 3AX. 0 3 17
t2 --,-117 (RA3
pd
2 HRS.
Iq
22 HRS.
IJL)LYMF-R USAGE
YPE USEDt6%� �lk)
ANKS . MIXED-tKL
IJ-6111. A �(03

TWSA LIME STABILIZATION
DAILY RECORD
DATE
START STOP TOTAL
RUN TIME, HRS F-7-6
DRY TON
3-7 Lf 9,
SLUDGE FEED, GAL 6
C
LIME FEED, LBS 1�q
SLUDGE FEED % SOLIDS r-Q, PRESS OA SOLIDS1
LIME/SLUDGE RATIO TOTAL PRODUCTION, DRY TONS
Inlet reached temp Q 9, 47—
Outlet reached temp @I
PATHOGEN REDUCTION VECTOR ATTRACTION- REDUCTION
TEMPERATURE of
INTO OUT OF
TIME VESSEL VESSEL OPERATOR TIME OPERATOR
PA
o 95
rI ob
............................................................................................................... ........
OPERATIONAL
BELT PRESS SPEED, %
POLYMERPLIMP SPEED, % 40%
SLUDGE PUMP SPEED, %-55'/o GPM 61, aq
LIME FEED AUGER, 9/b_L5_!/_C_) LBS/HR I:Xrl(o
MIXER SPEED, 100%
Revised 8/12/03
INITIAL PH LI - . .frn
-IS-;?h&= 3A X.63.=.)69,
O;L,:: 12 - 525.
.2 HRS. )A. 5 3
25-22 2K, S- X, 0 .3 0 7'S-
0 22 HRS.
.............................................. ........
POLYMER USAGE,
6y IF,
TYPE USED Wo YR
TANKS MIXED
Lq.

TWSA LIME STABILIZATION
DAILY RECORD
&., 3 3
DATE
START STOP TOTAL
RUN TIME, HRS 7 17
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDS a PRES9 % SOLIDSI
, TOTAL PRODUCTIONDRY TONS
LIME/SLUDGE RATIO r)
Inlet reached temp @ T 51,
Outlet reached temp 1114
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TEMPERATURE'oF
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
14
;o3
AoL�
TON
TIME b X, 0 S- .077—OPERATOR
I. -Z 7,5' .0 72
6;404 M INITIAL PH 0 J �>
5
12-- 0 — -
2. HRS. Z, 2Q
In 124".241.
2 . .
17.0 2 HRS.
:A os-
..........
X.5y .............
�47 ...........
dks .................... ...................................................... ................................................................
OPERATIONAL.
BELT PRESS SPEED, %
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEEb,% GPM
LIME FEED AUGER, % G LBS/HR/3719,
MIXER SPEED,
Revised 8/12103
POLYMER USAGE
TYPE USED+'9448 1 '3160
TANKS MIXED

TWSA LIME STABILIZATION
DAILY RECORD
DATE �
-
f
START
STOP: TOTAL
RUN TIME,. HRS
�i
2
r
DRY'TON
SLUDGE FEED, GAL
�b
- -
�
`-;
LIME FEED; LBS
SLUDGE FEED % SOLIDS
�® Q�
PRESS , °,6 SOLIDS
LIME/SLUDGE RATIO ,
�1/
TOTAL PRODUCTION, DRY TONS
Inlet' reached temp @
r.10
Outlet reached temp
PATHOGEN REDUCTION
VECTOR ATTRACTION
:REDUCTION
TEMPERATURE F
TIME Y
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
3 a 5
F'-7
� 53
oQ_
:
,7 ' O.P 19,0-7'
c;0J
TIME -al,� _�lY, �.�a l� OPERATOR
1�.33-.t0.1 Ca.aa
: 00
INITIAL PH. , 3`_ 1 ;!
S—�i,:a-3,Td ,63-,I(q
q'.aa
2HRS. _�,a5
�s=ah,=3��.x,®�=eel-? .
7= P 113
;.
22 HRS. l`�. —6�=-

TWSA. LIME STABILIZATION
DAILY RECORD Q. U
DATE. s,, lbw
pSTART STOP TOTAL
RUN TIME, HRS
DRY TON
SLUDGE FEED, GAL .
LIME FEED, LBS
SLUDGE FEED % SOLIDS OS Ot Q PRESS, °%SOLIDS
LIME/SLUDGE RATIO . TOTAL PRODUCTION, DRY TONS U J
Inlet reached temp @ 4l
Outlet reached temp @
r
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TEMPERATURE OF
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
l _
q4
c
T 0 0
TIME
I=.�i•wX,®3-•C)7 OPERATOR
la. 4q-.©T7 12.36-3
0 d
INITIAL PH 2,3
f�,�1.-.lobs= Ia•3°�
Y
�Q
2 HRS.
�4t3� [17 = 6�• .
r d
22 HRS.

TWSA LIME STABILIZATION'
DAILY RECORD
DATE
START STOP TOTAL
RUN TIME, HRS
Pi
SLUDGE FEED, GAL 39, 59
LIME FEED, LBS
Y TON
SLUDGE FEED %SOLIDS �a O lb PRESS , % SOLIDS .
LIME/SLUDGE RATIO Ov TOTAL PRODUCTION, DRY TONS
Inlet reached temp it ®t `
Outlet reached temp @ S. /
-PATHOGEN .REDACTION VECTOR ATTRACTION REDUCTION
TEMPERATURE of
TIME
INTO'
VESSEL
OUT OF
VESSEL
OPERATOR.
l� �l
J�D
!sue
C
TIME
93- .,.3= iQ. .63=.Otsl OPERATOR
ya9
O
INITIAL PH I 4
I ; 4G- 011 = ia.3(A
6�.
2 HRS. 12 36. '
3A.i.03-. I1
b.,
22 HRS: .
................................................................................................;.:......................................:........
OPERATIONAL
BELT PRESS SPEED,
POLYMER PUMP SPEED,%
SLUDGE PUMP SPEED, %_ GPM
LIME FEED AUGER, LBS/HR_t
i
MIXER SPEED, % 10
Revised 8/12103 ,
POLYMER USAGE
TYPE .USED
TANKS MIXED
VK . 5

TWSA LIME STABILIZATION
DAILY RECORD
DATE'S
START STOP TOTAL
RUN TIME, HRS i 3� ' l
DRYTON
SLUDGE -FEED, GAL r% � 4 6 (0 . _ -
-----------
LIME FEED, LBS "� o
SLUDGE FEED % SOLIDS c PRESS, % SOLIDS
LIME/SLUDGE RATIO L TOTAL PRODUCTION, DRY TONS #
Inlet reached temp
Outlet reached temp @
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TEMPERATURE of
'TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
57,36�
y
40Y
TIME
BLS—�2a:=�,�'X" �1
OPERATOR
Ia, P-2_ a 040 Ia,131
INITIAL PH 13
.
o�S-a`LL6.=3.WIC,03= � i0a
! @O
2 HRS. 6 Alp-
X.
��.
22HRS.`'S
c-R

TWSA LIME
STABILIZATION
-DAILY RECORD
j
DATE
START
STOP, TOTAL
RUN TIME, HRS '.
7 r
SLUDGE FEED, GAL
DRY TON
•
LIME FEED, LBS
t 7�
SLUDGE FEED °% SOLIDS -
©�
PRESS, % SOLIDS
LIME/SLUDGE RATIO
r
n
TOTAL PRODUCTION, DRY TONS
Ip�
inlet reached temp @
& 3
Outlet reached temp
PATHOGEN REDUCTION
VECTOR ATTRACTION REDUCTION
TEMPERATURE of
INTO
J,OUT OF .
TIME VESSEL
VESSEL OPERATOR
TIME 679 OPERATOR
INITIAL PH ,
4� 1--11
r ,.1��'7= la, S,
'`w
Sba;3=2.7X,03.._ ; off►
Qi0 1965-1
"r✓1
1 �1�3~•p�p�
i 22 HRS.. 1, -
-�
ems.
OPERATIONAL POLYMER USAGE
BELT PRESS SPEED, % (t3a
TYPE USED
POLYMER PUMP SPEED, %
TANKS MIXED
SLUDGE PUMP SPEED,
% 4o GPM_
%TE Cal
LIME FEED AUGER, %o Q LBS/HR 1616LITERS/TANK
.MIXER SPEED, % - !on
_ .. / 0 7
Revised 8/72/03'
-
-

��13
TWSA LIME
STABILIZATION,
,
DAILY RECORD
DATE
START
STOP
TOTAL
RUN TIME, HRS .
-t L�
T ' 13
SLUDGE FEED, GAL
DRY TON
1,
LIME FEED, LBS
4�
SLUDGE FEED % SOLIDS
f BGa
PRESS. %' . SOLIDS
`
LIME/SLUDGE RATIO
TOTAL PRODUCTION, DRY TONS
Inlet reached temp @
-
Outlet reached temp @
, <s--
PATHOGEN
:REDUCTION
VECTOR -ATTRAC'II.ON :REDUCTION
TEMPERATURE of
INTO
OUT OF .
TIME' VESSEL
VESSEL OPERATOR
TIME
�t5- 2a, 7 =02,3 X, 03'_, �feq OPERATOR
I
PH
;Q®
INITIAL
13
R077,
aJ�
f7rr3
alS��ll, Q =3,) XE0:3=dq3
1 a o'ft4 : 643 )2. NO
2 HRS.,_
gx,03 =`1yv
P,5o �. ►� = .r . �s�
-17F®O 22 HRS. `1 rJ

TWSA'LIME STABILIZATION
DAILY RECORD
DATE
RUN TIME, HRS
SLUDGE FEED, GAL CJt! I I 7 c
LIME FEED, LBS o gq
d
A ,
SLUDGE FEED %SOLIDS o9' to PRESS , %SOLIDS
LIME/SLUDGE RATIO �. TOTAL PRODUCTION, DRY TONS O 1
k
Inlet reached temp @ dr
Outlet,teached temp @ �
PATHOGEN REDUCTION, VECTOR -ATTRACTION REDUCTION
TEMPERATURE OF
INTO I OUT OF
TIME VESSEL VESSEL
13 -d-
OPERATOR
TIME
Xi03_.r057 OPERATOR
�a.33 ; 057 = O.A73 .
]�00.. INITIAL PH
0
:-
osl
1©6 2 HRS.
3,t,,.33.
�
aac�
'7,o6
;�
.22 HRS. 1 . �a�,
.5 33C
6 00
'
A61
fill
............................. :...........................................
...........................................
.........................................................
OPERATIONAL POLYMER USAGE
BELT PRESS SPEED, 35 TYPE USEDI���
POLYMER PUMP SPEED, % _ ANKS MIXED
SLUDGE PUMP SPEED, % to cJ GPM_
LIME FEED AUGER,' % L0 LBS/HR I (, Jr LITERS/TANK
MIXER SPEED, % t 00(d
Revised 8112103 - - - -

TWSA LIME STABILIZATION
- -
DAILY RECORD
DATE ll�
_
START
STOP TOTAL
RUN TIME, HRS
.�` j
71
SLUDGE FEED, GAL
DRY TON
.
LIME FEED, LBS:
SLUDGE FEED % SOLIDS
V
PRESS, % SOLIDS
LIME/SLUDGE RATIO
cY
TOTAL PRODUCTION, DRY TONS
_ Inlet reached temp @
_-_ Outlet reached temp
3
IiHllf
-- PATHOGEN REDUCTION,
_ - TEMPERATURE 'OF
VECTOR ATTRACTION REDUCTION
INTO,
OUT OF
_
TIME VESSEL
VESSEL OPERATOR
TIME OPERATOR .
T 00 INITIAL PH I
t�
ao
J ,-'fox= /9,258
i C� 221-1RS:
I
s 1�
p���%&v►

TWSA LIME STABILIZATION.
DAILY RECORD o
DATE- -6- I(` Oe
START STOP TOTAL
RUN TIME, HRS' 6o
DRY TON
- SLUDGE FEED, GAL I G P
LIME FEED, LBS
SLUDGE FEED %SOLIDS /Q U! b �o PRESS. % SOLIDS
LIME/SLUDGE RATIO Y TOTAL PRODUCTION, DRY TONS
Inlet reached temp
Outlet reached temp @
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TEMPERATURE of
TIME
INTO
VESSEL
OUT OF.
VESSEL
OPERATOR;
t,
F q
7100
3
2,61
TIME OPERATOR
LZ-5 �-1. osr=`1a,459
6 INITIAL-.PH-1 9,.
R5-aa,i=2.9X,03 a617
i.1, 5 7 — &S7 =42. 453
2 HRS. L
t5-ZZ.3=Z7_5 =.Og\
12.,3-I .orb _ iZ 2— ,A
> � SO 22HRS. . k Zc)
OPERATIONAL -
BELT PRESS SPEED, %
POLYMER PUMP SPEED, %•l'1
SLUDGE PUMP SPEED; % GPM %O
LIME FEED AUGER, % LBS/HR ��

TWSA LIME STABILIZATION
DAILY RECORD
I
DATE b
START STOP TOTAL
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDS
LIME/SLUDGE RATIO
Inlet reached temp @
Outlet reached temp @
PATHOGEN REDUCTION
TFMPFRATURFoF
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
Q31
®
l �
��
133,
1 V
1`3 1
[ W
���►-�
~T:
PRESS, % SOLIDS
TOTAL PRODUCTION, DRY TONS
VECTOR ATTRACTION REDUCTION
TIME
o`Dc5-23.:3 = Lly,03=1OSI
(� 06
INITIAL PH
aS — .;L'7. ( a-)-,4 X. 6'? =.U`e
9460
2 HRS.
I �!,3(� -. Ivy
t-�
l aD
22 HRS. ,
.....................................................................................................................................................I...............
OPERATIONAL
f ice- /17
BELT PRESS SPEED, % `�C�,� 0G'
POLYMER PUMP SPEED, % j®Yr
/� Ca
SLUDGE PUMP SPEED, % S++ V L) GPM G
LIME FEED AUGER, % LBS/HR ``�
Ai !R SPEED, % 6 o %C'
TON
OPERATOR
POLYMER USAGE
TYPE USED O6 0 I R14
TANKS MIXED
LITERS/TANK
96�(D 09-�
Revised 8/12/03

TWSA LIME STABILIZATION
DAILY RECORD
DATE
START STOP TOTAL
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS j 6
v ,
SLUDGE FEED % SOLIDS .O PRESS, % SOLIDS
LIME/SLUDGE RATIO ' ` J� TOTAL PRODUCTION,, DRY TONS
Inlet reached temp @
Outlet reached temp @ la
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TFMPFRATI IRF nF
TIME .
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
5;�Z(
fq6
19(o
f7',66
f qq
TON
TIME a34 = OPERATOR
INITIAL PH l2. 3 `lL
3�
2 HRS. VA. lq
IMP: ca•3sa
fi ram®
22 HRS. ja.. �
OPERATIONAL
BELT PRESS SPEED, % U
POLYMER PUMP SPEED,
SLUDGE PUMP SPEED, % _416GPM
LIME FEED AUGER, % q 5 LBS/HR
11 '�R SPEED, % 06
POLYMER USAGE
TYPE USED ` b N1 TI
TANKS MIXED
- �/b17• i�� -
Revised 8/12/03

RUN TIME, HRS
SLUDGE. FEED, GAL
LIME FEED, LBS
TWSA LIME STABILIZATION
DAILY RECORD
/
DATE
START STOP TOTAL
DRY TON
SLUDGE FEED % SOLIDS PRESS, % SOLIDS
LIME/SLUDGE RATIO .lY TOTAL PRODUCTION, DRY TONS
Inlet reached temp @
Outlet reached temp @
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TEMPERATURE of
TIME
"INTO
VESSEL
OUT OF
VESSEL
OPERATOR
Icy
1b
`3
_
OW
%3
ff
;o.51316
®�
01oa
......................................................
OPERATIONAL
TIME Z--;0,3.9=I=l.X;63=.033
/ 0 .INITIAL PH 12.56
J.=3,kX,03=",(62
1a;55 �aa=1�• ��f8
%. 30 2 HRS.
22 HRS.
BELT PRESS SPEED, % �)
POLYMER PUMP SPEED, % 30
SLUDGE PUMP SPEED, % GPM
LIME FEED AUGER, % J LBS/HR
11 JR SPEED, % % ( 0
OPERATOR
�tM
POLYMER USAGE
TYPE USED /4? y,, N zr 16 o
TANKS MIXEDIW
J0 7
Revised 8/12103

TWSA LIME STABILIZATION
DAILY RECORD
DATE- 1-36* e3
START
STOP
TOTAL
RUN TIME, HRS
' --
DO
0
DRY TON
SLUDGE FEED, GALI
D---T
-(953o-T-
LIME FEED, LBS
SLUDGE FEED % SOLIDS
PRESS, % SOLIDS
[
LIME/SLUDGE RATIO
TOTAL PRODUCTION,
DRY -TONS
Inlet reached temp @
Outlet reached temp @
PATHOGEN REDUCTION
VECTOR ATTRACTION REDUCTION
TEMPERATURE of
lKrrf,%
n"-r
TIME
VESSEL
OF
VESSEL
OPERATOR
90
1.5(y
6—j)
Q:4
3
51'e
� ((S
- � lJ
(
TIME
OPERATOR
36
INITIAL PH'
9s.ZU =11 19 9163= 00
2 HRS. 1�,43
t4.S'X,(J,3
22 HRS. r),, 3$
.............................. ....... ............................................ m ......................... .......................................................
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, % gIC)
SLUDGE PUMP SPEED, % 3 -GPM -7(9,.6
LIME FEED AUGER, % LBS/HR -275
I." fR SPEED, %
POLYMER USAGE
TYPE USED w l 6
TANKS MIXEDA I
LITERS/TANK
q. ;2-
Revised 8/12103

TWSA LIME STABILIZATION
DAILY RECORD
DATE 1 02
START STOP TOTAL
RUN TIME, HRS 1 2 1 Z',- 0 d b'
SLUDGE FEED, GAL
LIME FEED, LBS I ® I � 0 rJ
SLUDGEFEED % SOLIDS F 1
LIME/SLUDGE RATIO -�
Inlet reached temp @
Outlet reached temp @
PATHOGEN REDUCTION
TFIUPP:PAT1 IRF nF
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
A
,
e
dd
PRESS , % SOLIDS
TOTAL PRODUCTION, DRY TONS
DRY TON
i - 9 U
VECTOR ATTRACTION REDUCTION
TIME
a5-2"3,1=0 OPERATOR.
7,30
INITIAL PH
ta, o(,91la.All
91.30
2 HRS. 12,
aS— adz='t 5"X'03 = e35
7 C'50
22 HRS. -)_Z l
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, % GPM I h
LIME FEED AUGER, % 6 LBS/HR 1 Q`t
N'' �R SPEED, % I Q C)
POLYMER USAGE
/
TYPE USED 'i U VY16
TANKS MIXED
LITERS/TANK
a5-:(.a- tto5
Revised 8/12103

0 � 6
TWSA LIME STABILIZATION
�� 1
DAILY RECORD
:DATE ® ..
START
STOP TOTpAL
RUN TIME, HRS
I'S
�� -o o-
j
i o -
DRY TON
FEED,
D
//
�O S 0
SLUDGE GAL
LIME FEED, LBS
(.J.
SLUDGE FEED % SOLIDS
v
PRESS, % SOLIDS
TOTAL PRODUCTION, DRY TONS 1 i
+
LIME/SLUDGE RATIO
Inlet reached temp @
Outlet reached temp @
PATHOGEN REDUCTION
VECTOR ATTRACTION REDUCTION
TPRAPPPATI IRF nF
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
AIDS
U
/ M T
llj `1'
A06
6
�f o®
TIME
a5-a=rgX,0'6D 0 ' OPERATOR
.3
-
1 r
INITIAL PH
1 q1,45
2 HRS. I a�
'e
22 HRS. 1 �5
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, % GPM + `
LIME FEED AUGER, %(06 LBS/HR
k. )R SPEED, % ��6
V
TYPE USED
TANKS MIXED
AN
Revised 8/12103

TWSA LIME STABILIZATION
DAILY RECORD
DATE l —.AJL ` O
START STOP TOTAL
RUN TIME, HRS 8�-5y 1 ; 00 1 /0- 5
ca lf, L O
i DRY TON j.s4
SLUDGE FEED, GAL 19 --T".S. O
01
LIME FEED, LBS
SLUDGE FEED % SOLIDS ✓ A
LIME/SLUDGE RATIO
Inlet reached temp @
I j � A- I
qb Z3
Outlet reached temp @
PATHOGEN REDUCTION
TFMPFRATI IRF nF
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR.
.k
,t455
aab
aoC,
/3
3;S1
�-b'�)
267-
1413
5; 55
;'�6 j
Ewt-
PRESS , % SOLIDS
TOTAL PRODUCTION, DRY TONS 1 3 a
4 1
VECTOR ATTRACTION REDUCTION
TIME
Z- A3, T^f„t%, 03; � 63 j0 OPERATOR
y .
I 1
INITIAL PH 1,2, 7
9-5-aa,r-2M},63=,OT7
t2,6&_,697. la,97,3
r 1
2 HRS. b2, Y7
°7`a3ja8
a5-ao.�=��sta3=,t3�
19,.53,l3�=/a.317
i/
22 HRS. —a, 40ln�_
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, % `i `O
SLUDGE PUMP SPEED, % r % GPM
LIME FEED AUGER, % (116 1`o LBS/HR
h )R SPEED, % I 0 V /6
I POLYMER USAGE I
YPE USED //,9 & V13tr9149
ANKS MIXED
ITERS/TAN
.76.1
Revised 8/12/03

TWSA LIME. STABILIZATION.
DAILY RECORD '!
DATE F. G�
T-
START STOP TOTAL
RUN TIME, HRS I e c/ I , l! 0
2 DRYTON
SLUDGE FEED; GAL
- - -LIME FEED, LBS
SLUDGE FEED % SOLIDS
—I
PRESS, % SOLIDS
•
O
LIME/SLUDGE RATIO
2
TOTAL PRODUCTION, DRY TONS s
Inlet reached temp
Outlet reached temp @
PATHOGEN REDUCTION
VECTOR ATTRACTION. REDUCTION
TFMPFRATt 1RF nF
TIME
INTO
VESSEL
OUT OF
VESSEL '
OPERATOR
A
02o
J•"fir)„
7
?b
,6 t
TIME z.' 1 �3 =1 o7Z
OPERATOR
DO INITIAL PH
.IZL_
r. 2 HRS. �.22
4.,0 K, 6`3 I'Z
r�k.q5=12. 3
cL'r( 22HRS.
OPERATIONAL
BELT PRESS SPEED, % Li
POLYMER PUMP SPEED,
SLUDGE PUMP SPEED, %° (-' GPM' (6
LIME FEED AUGER, % LBS/HR 2
fl'. L'R.,SPEED, %
Revised.8/12/63 •-
POLYMER USAGE
TYPE USED 13
TANKS MIXED �� f
LITERS/TANK
76 lb�

TWSA LIME STABILIZATION
DAILY RECORD
115-1 W
I
1
RUN TIME, HRS
SLUDGE FEED, GAL
DATE 'I - 2-91 - 0 9
START STOP TOTAL
' ®D � � V e V
DRY TON
xq•5�
se
9115
, V 9/' 1 ('1 --A q t s'- I 'h o o b 1 1
LIME FEED, LBS
SLUDGE FEED %SOLIDS PRESS , °ti SOLIDS
I LIME/SLUDGE RATIO TOTAL PRODUCTION, DRY TONS
Inlet reached temp @
f Outlet reached temp @ Q
PATHOGEN REDUCTION
TFMPFRATI IRF nF
INTO
OUT OF
TIME
VESSEL
VESSEL
OPERATOR
q,1
65
VECTOR ATTRACTION REDUCTION
TIME
of a��l = •'3 %- 03 '' d ! OPERATOR
• 1
INITIAL PH� �Gi.►
A5-0,14=3,q X.03-.lva
am v, rda= Boas
2 HRS. +1 a 9
A5`16-3=�►�7 �o3=,i�►l
'7- 36 -0'9
to ►33-. i!q1=
22 HRS. J
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, % d
SLUDGE PUMP SPEED, % 14 GPM
LIME FEED AUGER, % ( LBS/HR
11, �R SPEED, % w 0
POLYMER USAGE
TYPE USED
TANKS MIXED_,
41
oj,y5
Revised 8/12/03

TWSA LIME STABILIZATION `•-��
.. DAILY RECORD -,
DATE
—T�
START STOP TOTAL
RUN TIME; HRS g' t3 0 r7 ; 00
DRY TON
SLUDGE FEED, GAL O _ �j % 2, 3 �%
LIME FEED, LBS
SLUDGE FEED % SOLIDS
LIME/SLUDGE RATIO •� cY
Inlet reached temp @
Outlet reached temp @
PATHOGEN REDUCTION
TFMPFRATI IRF nF
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
1--3
a64
u'�
(-11fj
5 f X
a 05
aQ o
wV
Euo 10,05,-
-gog-
PRESS , % SOLIDS
I 771
TOTAL PRODUCTION, DRY TONS
VECTOR ATTRACTION REDUCTION
TIME
OPERATOR
17! 30
INITIAL PH
.
p1a `^V�?
•"'r a l 'tea eq x, J 0 TCJ
laa�a�.OTT=-12,513
2HRS.
late58 _o lib =1� �9�"�p
�d
.........................................................................................................................................................
22 HRS. .45
OPERATIONAL
BELT PRESS SPEED,
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, % ,) GPM,
:.
LIME FEED AUGER, % LBS/HR-�
h', !R SPEED, % ©®
POLYMER USAGE
TYPE USED 3�19(V �
TANKS MIXED
LITERS/TANK
Revised 8112/03

ST
RUN TIME, HRS 17 2
SLUDGE FEED, GAL
LIME FEED, LBS
TWSA LIME STABILIZATION
DAILY RECORD
DATE
STOP TOTAL
Plk Of 6 .1
SLUDGE FEED SOLIDS PRESS, % SOLIDSI
LIME/SLUDGE RATIO a TOTAL PRODUCTION, DRY TONS
Iftlet reached temp @
Outlet reached temp Q L It) pb 13 1
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TEMPERATURE of
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
.115.
9105-
boo
r7 f
TIME S g3,6=- j,qX,63=,, (349, OPERATOR
INITIAL PH
2HR&
Z--,�,a q = q-,
Q. LCC 13?
'J'
............... ............... m .................................................. I ........ ........................... : ................................. ................. .........
OPERATIONAL
BELT PRESS SPEED, 41r
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, % GPM 7q, 53
LIME FEED AUGER, % LBS/HR 1613
k --R SPEED, % I 106
POLYMER USAGE
TYPE USED
TANKS MIXED I
LITERS/TANK A4 q' 4
,Revised 8/12/03

TWSA LIME STABILIZATION
DAILY RECORD
DATE_
�- ((-
START STOP TOTAL
RUN TIME, HRS
DRY TON
SLUDGE FEED, GAL J. 'I
LIME FEED, LBS
SLUDGE FEED % SOLIDS I OP-
LIME/SLUDGE RATIO
Inlet reached temp @
l b: 3 (a
Outlet reached temp @ Z
PATHOGEN REDUCTION
TFhAPFRATI IRF nF
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
2. 2
;26 5
C71
2-Z
fig
#13
• 'Z-:2-
,z Z') /
�9
Oo
PRESS, % SOLIDS
TOTAL PRODUCTION, DRY TONS I 6 ° 56-
VECTOR ATTRACTION REDUCTION
TIME
a5� p3.& --- 1,gK,03-,oLta OPERATOR
1�3q'-beta= ta,3�$
INITIAL PH ila,3s
=a9)(,03=,0$7
12.353
3b
2 HRS.
%f r-03 -.)3a
-,139=/a.9,79
r V
hh
22 HRS. Q, a 3-
OPERATIONAL
BELT PRESS SPEED, % _
55T
POLYMER PUMP SPEED, % 140
SLUDGE PUMP SPEED, % 60 GPM 70, A2
LIME FEED AUGER, % 5 LBS/HR 7
R SPEED,
POLYMER USAGE
TYPE USED��,Q
TANKS MIXED
LITERS/TANK -
Revised 8/12/03

--;? 0 7i;
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
TWSA LIME STABILIZATION
DAILY RECORD.
DATE 9 - / Z - Q
START STOP TOTAL
O C n -7 f ^A I/'\ f
SLUDGE FEED % SOLIDS
-- LIME/SLUDGE RATIO _
Inlet reached temp @ q`,
Outlet reached temp @
PATHOGEN REDUCTION
TFMPFRATI IPP nF
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
b
of
'
6 3
OPERATIONAL
BELT PRESS SPEED, % 45
POLYMER PUMP SPEED, %�
PRESS, % SOLIDS
TOTAL PRODUCTION, DRY TONS
VECTOR ATTRACTION REDUCTION
TIME �5--•3=.7X,D-,QSI OPERATOR
00 INITIAL PH
aS-a0.I" 1- ov.03 126
<a,35--o/a(-= �a.aay
Od 2 HRS.
aS=aO.gT-q. 1603= .138
12,3q-•138= l�.asa
5<00 22 HRS. -----.
SLUDGE PUMP SPEED, % GPM___(p,5, %%
LIME FEED AUGER, %(QO LBS/HR
iV ,R SPEED, % L ©n
POLYMER USAGE
TYPE USED 4'QUW l-, ft-0 [lob
TANKS MIXED
LITERS/TANK it /
%o � V
Zevised 8112/03

Appendix (g)
Sludge Production

Appendix (g)
..2008 SLUDGE DATA
- -�
TWSA PLANT '# 1 (1.5 mgd)
NPDES # NC0039578.
SLUDGE TO DIGESTOR.....:. :...............:._...,. ..........13,059,900 gallons
-
total lbs............:........:..........:........:........::.........,......541,163 lbs
total tons................. :.......270.6 tons
total metric tons .............. .............. ........245.4 metric. tons
_
TWSA PLANT # 2 :. (.5 mgd)
:..
NPDES # "NC0020214 , .
-SLUDGE HAULED TO PLANT # 1.:.......:.. ...........:...:. ... 422;593 gallons
total tons....: .........................................................28.72 tons
total metric tons. ....................... ........:.. .. 26.05 metric tons
TWSA PLANT # 3 , (.1- mgd)
'
NPDES # NC0063321
SLUDGE HAULED TQ PLANT # 1: :..., 74;206 gallons
........_.
total tons............ .....:. 7.67 tons
............
total metric tons...:........... .......".............. ;...._ ......_._...6.96 metric tons
Septage Receiving. Station :. .............. ..:-.468,223 gallons
.......
total tons............. ..........................-:27-_31 tons.
total metric tons........:`.... ........24.77 metric tons
A portion of the,sludge that was generated at.the Tuckaseigee Water and..Sewer Authority
during`2008 was hauled by a private contractor to a designated landfill. ,
Landfill: R&B. Landfill
610 Frank Bennett Road
. Homer GA 30080
A total of.4651 wet tons were hauled to the landfill during 2008.
Copies of haul tickets can be provided if needed..