WQ0005763_2007 Annual Report_20080206

Annual Report Review Class A Distribution

PV�Qass,A Pathogen Review
To be Class A, residuals shall meet either fecal coliform density or salmonella density.
Fecal coliform density
• Was the sampling conducted at the required frequency? V -
• Were multiple samples taken? ,q,25
• Was each sample less than 1000 MPN/gram of total solids? Val
Or rl
Salmonella density
• Was the sampling conducted at the required frequency?
• Were multiple samples taken?
• Was each sample less than 3 MPN/4 grams of total solids?,
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
• Were logs submitted showing time and temperature?
• Was the pH raised to 12 or greater and maintained for 72 hours or longer?
• 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?
• Was the temperature corrected to 25°C (77°F)?
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
• 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 helminth_ ova 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 Eriteric Viruses/Viable Helminth Ova
• Was the density of enteric viruses less than one Plaque -forming Unit per four grams of total solids at the
time 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?

RM
FRIECEWE0
Tuckaseigee Water & Sewer Authority
Serving Jackson County
1246 West Main Street
Sylva, NC 28779
Ph. [phone]
Fax [phone]
January- 24, 2008
DENR/DWQ/Water Quality Section
Non -Discharge Compliance Unit
1617 Mail Service Center
Raleigh NC 27699-1617
Attn: Non -Discharge Compliance Unit,
FEB 212008
Asheville Regional Office
! J L FEB 2 0 2008
Enclosed is the Annual Residuals Report for the Tuckaseigee Water and Sewer Lime
Stabilization facility (permit #WQ0005763) for the period of January 1, 2007 - December
31, 2007.
Should you have any questions or if I can provide you any additional information, please
don't hesitate to contact me.
Sincerely,
Stan Bryson
Wastewater Plant Operations Superintendent
Tuckaseigee Water & Sewer Authority
Enc.
RECoVED
Informaflon Processing unit
DW QIBOG

ANNUAL SEWAGE SLUDGE REPORT
OF
TUCKASEIGEE WATER AND SEWER AUTHORITY
PLANT # 1-NPDES # NCO039578 (WQ0005763)
for the period of January 1, 2007-December 31, 2007
as required by
40 CFR, PART 503
STANDARDS FOR THE USE OR DISPOSAL OF SEWAGE SLUDGE
:FB 0 6 2008
information Processing Unit
DWQ/BOG

TABLE OF CONTENTS
(1) REPORTING REQUIREMENTS/PERTINENT INFORMATION
(2) CERTIFICATION
APPENDIX
(a) 2007 sludge production data
(b) 2007 distribution and marketing summary
Part A&B
(c) 2007 laboratory analysis
(d) 2007 lime stabilization record of operation

REPORTING REQUIREMENTS
Facilities responsible for reporting annually are described in the regulations as:
1. Publicly Owned Treatment Works (POTW) with an average design
influent flow rate equal to or greater than 1.0 MGD.
2. POTW's serving a population of 10,000 or more.
3. Class I (facilities with an approved pretreatment program) sludge management
facilities.
The Tuckaseigee Water and Sewer Authority Wastewater Treatment Plant is a 1.5 MGD
design facility. The facility also treats the sludge from two additional plants owned by the
authority.
Pertinent information includes:
facility name: Tuckaseigee Water & Sewer Authority Plant # 1
NPDES # NCO039578
correspondence address: 1246 West Main St
Sylva NC 28779
physical address: 1871 North River Rd
Sylva NC 28779
facility operator: Stan Bryson
Wastewater Plant Operations Superintendent
ph. 828-586-9318

CERTIFICATION REQUIREMENTS
PART I - POLLUTANT CONCENTRATIONS
Ceiling Concentrations
mg/kg
Parameter
Sample
Analysis
value
Maximum
Permitted
value
Arsenic
1.2
75
Cadmium
0.8
85
Chromium
12.9
3,000
Copper
66.6
4,300
Lead
11.0
840
Mercury
0.3
57
Molybdenum
2.8
75
Nickel
17.8
420
Selenium
2.9
100
Zinc
240
7,500
PART H - PATHOGEN REDUCTION (40 CFR 503.32)
X Class A
Class B
PART HI - VECTOR ATTRACTION (40 CFR 503.33)
Option 1
Option 2
Option 3
— Option 5 X Option 6 — Option 7
Option 4
Option 8

PART IV - 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 CM 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 29th day of January , 2008.
Stan Bryson, Wastew ter Superintendent

ANNUAL PATHOGEN AND VECTOR ATTRACTION REDUCTION FORM
Facility Name: Tuckaseiaee Water and Sewer Auth ' Permit Number: —WO n fl ti
WWTP Name: TWSA Plant .# 1 NPDES Number: No on, A R
Monitoring Period: From. 1 / 0 i / 0 � To i /
Pathogen Reduction (40 CFR 503.32), - Please indicate level achieved and alternative
Class A:
Alternative 1El
Alternative.2 ❑
Alternative`3 ❑
.. ::::::: .::
Alternative 4❑
Alternative 5 ®.
Alternative 6 ❑
_
If applicable to alternative performed (Class A only) indicate "Process to Further Reduce Pathogens":
Compost ❑ Heat Drying ❑ Heat Treatment ❑ Thermophilic ❑
Beta Ray ❑
Gamma Ray❑
Pasteurization
Class: B:
Alternative 1 ❑,
Alternative 2 ❑
Alternative .3 ❑
'.
If -applicable toalternative performed (Class B only) indicate "Process to Significantly Reduce Pathogens,,:
❑ Air
Lime Stabilization - Drying ❑ Composting ❑ = Aerobic Digestion ❑
e
Ana rob" is Di e stion
g
XV
If applicable to .alternative performed (Class A or. Class B) complete the following monitoring data:
': Parameter-
.Allowable Level
Pathogen
Density -
e1 0
Excee-
Frequency
q Y
'Sam le
p
Anal cal
Yh
Geo. Mean
Maxim
TJnits
in Sludge
deuces
of Analysis
Type
Tech=pique
2 x 10 to the 6th
power WN per..::.
.
gram of total
solids or 2 x 10 to
FecalColiform
the 6thpower
CFU p,efa= of
1000 mpu per
gram of total solid
<20
C.26
< 39
cfti
0
8/Yr
grab
SM
9221 ,.
(dry weight)
: `CE
Salmonella bacteria .
3 WN per 4
.0h lieu of fecal
grams total solid
coliform)-
(dry weight) . .
Vector Attraction Reduction .(40 CFR 503.33) -Please indicate option performed:. .
Option 1 ❑ Option 2 , ❑Option 3 ❑ Option 4 ❑ Option 5 ❑
iri.6 ®IOvtion 7
■
No.vector attraction reduction options were performed ❑
❑` 1 Option 10 . ❑
......................... • .........•.,.•:.•....•.•.•. .
CERTIFICATION STATEMENT (please check the appropriate statement).
k7 "I certify, under penalty of law, that the pathogen.requirements in 40 CFR 503.32 and the vector
attraction reduction requirement -in 40 C--FR 503.33 have been met."
U "I certify,.under penalty of law, that the pathogen requirements in 40 C-FR 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-Suet.
Prepay r Name and Title (type or print)
Signature of Preparer Date
Land Applier Name and Title (if applicable)(type or print)
Signature of Land Applier (if applicable) Date

ANNUAL DISTRIBUTION AND.MARKETING/ SURFACE DISPOSAL CERTIFICATION AND SUMMARY;FORM
PERMIT #: � 26 FACILITY NAMETuckasei ee. Water
PHONE:[phone] COUNTY: Jackson g .and Sewer Authority.
FACILITY TYPE (please check one): OPERATOR: Stan. Bryson
❑ Surface Disposal:(complete Part A (Source'(s) and -"Residual In" Volume only) and Part C)
®. Distribution and Marketing (complete Parts A, B, and C)
Was the facility in operation during the past calendar. year?, Yes . ' []No No_If No skip parts A, B, C and certify form below
Part A*.
Part B*;
Month Sources(s) (include NPDES #
applicable).
,JLHY See Appendix B
une Part'A
®!
e
October
November
tons)
Residual In ' Product Out
Recipient Information
Naine(s) Volume (dry tons) Intended use(s)
1 otais: Annual (dry tons):
211,34
360.84
Amendments used: ' Lime CAO+ - Bulking Agent(s) used:
.............
* If more space than given is required, please attach additional information sheet(s):' ®- Check box if additional sheet(s) are. attached
Part C:
Facility was compliant during ealendar'year2 0 0-7 -With alttonditions .of the permit (including but not limited to items 1-3 below issued b
Division of Water Quality. -, ; ®yes ) y the
0; No If No, please provide.a written description why the facility was not compliant.
1. All monitoring_ was* done in -accordance with the permit and reported'for the -year as required and three (3) copies of certified laboratory results are attached.
2. All operation and maintenance requirements were compiled with or, in the ease of a deviation, prior authorization was received from the Division of Water
Quality.
3.. No contravention of Ground Water Quality Standards occurred at monitoring well.
"I certify, under penalty of law, that the above information is, to the best of my knowledge and belief, true, accurate and complete. I am aware
atha here a e significant penalties for submitting false information, in the possibility -of fines and imprisonment for knowing violations."
Signature of P ittee Date Signature of Preparer**
Date.
`'(if different from Permittee) **Preparer is defined in 40 .CFRPart.503.9(r)

Append x A
2007 Sludge Production Data

Appendix A
2007 SLUDGE DATA
TWSA PLANT # 1 (1.5 mgd)
NPDES # NCO039578
SLUDGE TO DIGESTOR...............................................................10,259,700 gallons
totallbs....................................................................484,185 lbs
totaltons......................................'.............................242.10 tons
total metric tons ....................................................... 219.6 metric tons
TWSA PLANT # 2 (.5 mgd)
NPDES # NCO020214
SLUDGE HAULED TO PLANT # 1................................................ 229,139 gallons
totaltons..................................................................20.04 tons
total metric tons.......................................................18.18 metric tons
TWSA PLANT # 3 (.1 mgd)
NPDES # NCO063321
SLUDGE HAULED TO PLANT # 1
total tons ..............
total metric tons....
................................................ 99,906 gallons
................................................... 6.39 tons
...................................................5.80 metric tons
Septage Receiving Station................................................505,280 gallons
totaltons................................................................29.47 tons
total metric tons......................................................26.73 metric tons
A portion of the sludge that was generated at the Tuckaseigee Water and Sewer
Authority during 2007 was hauled by a private contractor to a designated landfill.
Landfill: R&B Landfill
610 Frank Bennett Road
Homer GA 30080
A total of 595.99 wet tons were hauled to the landfill during 2007.
Copies of haul tickets can be provided if needed.

Appendix B
2007 Distribution and
Marketing Summary
l 0* v,.r.d_ A �_ i

Appendix B
TWSA PLANT # 1
ANNUAL DISTRIBUTION AND MARKETING. SUMMARY
2007
Part A
Residual Sources and Volume
Class A
Sludge Volume .Sludge Volume Residual Volume
Produced Treated Lime Added Produced
Month Source (dry tons) (dry tons) (dry tons) (dry tons)
January
TWSA Plant # 1. (NC0039578)
21.35
TWSA Plant # 2 (NC0020214)
0
TWSA Plant # 3 (NC0063321)
1
Septage Received
0.7
Monthly Totall
23.05
0
0
0
February
TWSA Plant # 1 (NC0039578)
16.35
TWSA Plant # 2 (NC0020214)
0
TWSA Plant# 3 (NC0063321)
0
Septage Received
1.74
Monthly Total
18.09 0
.0
0
March TWSA Plant # 1 (NC0039578) 22.40
TWSA Plant # 2 (NC0020214) 4.59
TWSA Plant # 3 (NC0063321) 0.95
Septage Received 2.95.
Monthly Total 30.89 23.13 42.66 65.79
April TWSA Plant # 1 (NC0039578) 22.16
TWSA Plant # 2 (NC0020214) 0
TWSA Plant # 3 (NC0063321) 1.42
Septage Received 3.08
Monthly Total 26.66 20.69 35.14 56.83
May
TWSA .Plant # 1 (NC0039578)
18.11
TWSA Plant # 2 (NC0020214)
2.04
TWSA Plant #3 (NC0063321)
0.42
Septage Received
2.56
Monthly Total
23.13
22.50
40.27
62.77
June
TWSA Plant # 1 (NC0039578)
17.66
TWSA Plant # 2 (NC0020214)
0
TWSA Plant # 3 (NC0063321)
1.27
Septage Received
1.76
20.69
3.06
2.98
6.04
Monthly Total
July
TWSA Plant # 1 (NC0039578)
23.79
TWSA Plant # 2 (NC0020214)
0
TWSA Plant # 3 (NC0063321)
1.06
Septage Received
2.29
27.14
10.92
24.1
35.02
Monthly Totall

Part A
Residual
Sources and Volume
Class A
Sludge Volume
Sludge Volume
Residual Volume
Produced
Treated Lime Added
Produced
Month Source
(dry tons)
(dry tons) (dry tons)
(dry tons)
August
TWSA Plant # 1 (NC0039578)
17.11
TWSA Plant # 2 (NC0020214)
4.15
TWSA Plant # 3 (NC0063321)
0.26
Septage Received
3.26
Monthly Total
24.78
4.54
8.59
13.13
September
TWSA Plant # 1 (NC0039578)
21.64
TWSA Plant # 2 (NC002021.4)
0
TWSA Plant # 3 (NC0063321)
0
Septage Received
2.06
Monthly Total
23.7
4.49
7.6
1.2.09
October
TWSA Plant # 1 (NC0039578)
22.61
TWSA Plant # 2 (NC0020214)
3.70
TWSA Plant # 3 (NC0063321)
0
Septage Received
2.54
28.85
0
0
0
Monthly Total
November
TWSA Plant # 1 (NC0039578)
18.80
TWSA Plant # 2 (NC0020214)
2.06
TWSA Plant # 3 (NC0063321)
0
Septage Received
5.78
'Monthly Total
26.64
16.71
33.70
50.41
December
TWSA Plant # 1 (NC0039578)
20.10
TWSA Plant # 2 .(NC0020214)
3.50
TWSA Plant # 3 (NC0063321)
0
Septage Received
2.16
-
Monthly Total
25.76
21.46
38.30
59.76
Total "sludge" produced by all sources for 2007= 299.38 dry tons
Total "sludge" treated in pastuerization process in 2007= 127.5 dry tons
Total lime added in pastuerization process in 2007= 233.34 dry tons
Total "residual' produced for distribution in 2007= 360.84 DRY TONS

Appendix B
TWSA PLANT # 1
ANNUAL DISTRIBUTION AND MARKETING SUMMARY
2007
Part B
Recipient Information
Est. Volume
Month, Name Address (wet tons) Intended Use
January
Monthly Total
0
February
Monthly Total
96
Chester Sorrells
274 Davis Cove Rd.
96
Commercial Hauler
Waynesville NC 28786
March
Monthly Total
124
Chester Sorrells
274 Davis Cove Rd.
70
Commercial Hauler
Waynesville NC 28786
Parrish Farm
3343 Bryson City Rd.
54
Pasture/Hayfields
Franklin NC 28734
April
Monthly Total
192
Chester Sorrells
274 Davis Cove Rd.
144
Commercial Hauler
Waynesville NC 28786
Smoky Mtn. Golf Club
1110 Conleys Creek Rd.
48
Golf Course
Whittier NC 28789
May
Monthly Total
161
Tony Collins
24
Pasture
Franklin NC 28734
Chester Sorrells
274 Davis Cove Rd.
60
Commercial Hauler
Waynesville NC 28786
Darrin Stewart
PO Box 384
12
Pasture
Robbinsville NC 28771
Johnny White
311 Ottinger Rd.
55
Pasture
Parrotsville TN 37834
June
Monthly Total
12
Darrin Stewart
PO Box 384
12
Pasture
Robbinsville NC 28771
July
Monthly Total
0
August
Monthly Total
60
Darrin Stewart
PO Box 384
60
Pasture
Robbinsville NC 28771

September
Monthly Total
0
October
Monthly Total
36
Chester Sorrells
274 Davis Cove Rd. 36
Waynesville NC 28786
Commercial Hauler
November
Monthly Totall 68
Sorrells Spreading
Tony Collins
274 Davis Cove Rd. 48
Waynesville NC 28786
Franklin NC 20
Commercial Hauler
Pasture
December
Monthly Total
0
Yearly Total
739 Wet Tons

Appendix C
2007
Laboratory
Analysis

kuJ7
Ann! lesidual Sampling Summary Form
Attau this form 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 Laboratory: Pace Analytical
Facility Name: Tuckaseigee Water and Sewer Auth. Asheville NC
NPDES # NC 0039578
WQ # : WQ 0005763
WWTP Name: TWSA Plant # 1
......._.._._....
......._...........
Sample
Date
1 /23
2/13
3/7
4/24
5/15
8/21
9/26
11 /13
12/27
12/31
Avg.
Percent Solids
50.9
52.5
49
53.8
45.2
55
59.5
54.4
47.4
48.5
51.6
Aluminum
10,000
3,200
5570
3,730
6,750
6420
5,945
P
Arsenic
1.2
<0.47
<0.68
<0.59
0.94
<0.97
0.4
A
Cadmium
0.80.
0.20
0.24
0.18
0.47
0.40
0.4
R
Calcium
28,0000
20,0000
256000
242,000
413,000
452,000
2atTIV
A
Chromium
9.1
2.9
5.2
3.1
12.9
4.8
6.3
M
Copper
63
38
66.6
66.3
63.3
59
E
Lead
11.0
7.0
6.2
3.6
4.2
4.5
6.1
T
Magnesium
4,800
1,300
2,060
1,550
2,800
2780
2,548
E
Mercury
0.25
0.059
0.091
0.019
0.1
R
Molybdenum
<0.98
1.1
2.5
2.7
2.8
2.4
1.9
S
Nickel
5.9
1.6
3.0
1.9
17.8
4.1
5.7
h
11.7
12.3
12.4
12.0
Potassium
2,000
1,500
2210
1,370
4,360
2880
2,387
Selenium
<2.0
1.4
2.9
1.9
<1.8
2.5
1.5
Sodium
360
250
<685
<592
<879
<973
102
Zinc
240
140
222
155
226
219
200.3333
TKN
8,100
6,500
16500
8,550
9,913
mg/
Ammonia -Nitrogen
55.
120
218
29.2
106
kg
Nitrate -Nitrite
260
11
15.6
<11.8
71.7
Plant Available N
2,700
2,000
5010
2,570
3,070
Total Phosphorous
230
2030
4,080
2890
2307.5
Fecal Coliform
<39
<38
<20
<37
<20
<20
<20
<20
0
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."
Icq L 0 JWSA Version)
Ignature of Preparer Date DENR FORM RSSF (7/2002)
367, /(a-/

L___
Analytical Results FEB 2 6 Zoos
Pace Analytical -Asheville For: 92136580
2225 Riverside Drive
Asheville NC 28804
Entered 1/24/2007
Reported: ' 2/2/2007
Sample Remark
Sample ID Parameter Cust ID Result Units Method Date Analyzed Analyst
070124-2 % Solids 927927400 50.9 % SM2540B 1/24/07 CL
070124-2 Fecal Coliform MTF 927927400 <39 MPN/g SM92210E 1/24/07 CL
Respectfully submitted,
Dena Myers
NC Cert #440,
NCDW Cert #37755,
EPA NCO0909
f:J
P.O. Box 228 • Statesville, North Carolina 28687. 704/872/4697

_;A
.:
3ceAnalytical °
www.pacelahs.com
Solid results are reported on a dry weight basis
Lab Sample No: 928002625
Client Sample ID: TWSA LIME RESIDUAL
Pace Analytical Services, Inc.
9800 Kincey Avenue, Suite 100
Huntersville, NC 28078
Phone: [phone]
Fax: [phone]
Pace Analytical Services, Inc.
2225 Riverside Drive
Asheville, NC 28804
Phone: [phone]
FaX [phone]
Lab Project Number: 92137955
Client Project ID: TWSA LIME RESIDUAL -ANNUAL
Project Sample Number: 92137955-001 Date Collected: 02/13/07 09:00
Matrix: Soil Date Received: 02/13/07 13:31
Parameters
Results
Units
Report Limit
Analyzed
By
CAS No. ual RegLmt
Metals
Metals, Trace ICP
Prep/Method: EPA 3050 /
EPA 6010
Aluminum
10000
mg/kg
20.
02/24/07
20:53
SHB
7429-90-5
Arsenic
1.2
mg/kg
0.98
02/24/07
20:53
SHB
7440-38-2
Cadmium
0.80
mg/kg
0.20
02/24/07
20:53
SHB
7440-43-9
Calcium
280000
mg/kg
20.
02/24/07
20:53
SHB
7440.70-2
Chromium
9.1
mg/kg
0.98
02/24/07
20:53
SHB
7440-47-3
,Copper
63.
mg/kg
0.98
02/24/07
20:53
SHB
7440-50-8
Lead
11.
mg/kg
0.98
02/24/07
20:53
SHB
7439.92-1
Magnesium
4800
mg/kg
20.
02/24/07
20:53
SHB
7439.95-4
Molybdenum
ND
mg/kg
0.98
02/24/07
20:53
SHB
7439-98-7
Nickel
5.9
mg/kg
0.98
02/24/07
20:53
SHB
7440-02 0.
Potassium
2000
mg/kg
200
02/24/07
20:53
SHB
7440-09-7
Selenium
ND
mg/kg
2.0
02/24/07
20:53
SHB
7782.49-2
Sodium
'360
mg/kg
200
02/24/07
20:53
SHB
7440-23-5
Zinc
240
mg/kg
2.0
02/24/07
20:53
SHB
7440-66-6
Date Digested
62/15/07 13:00
02/15/07
13:00
Mercury. CVAAS, in Soil
Mercury
Method: EPA 7471
0..25 mg/kg 0.079 02/14/07 12:50 ALV 7439.97-6
Wet Chemistry
Percent Moisture Method: i Moisture
Percent Moisture 49.0
Nitrogen, Ammonia Method: EPA 350.1 Modified
Nitrogen, Ammonia 55. mg/kg 20.
Total Kjeldahl Nitrogen, Soil Method: EPA 351.2
Nitrogen, Kjeldahl, Total 18100 mg/kg 200
Nitrogen, Nitrate plus Nitrite Method: EPA 353.2 Modified
Nitrate as N 230 mg/kg 16.
Nitrate -Nitrite (as N) 260 mg/kg 16.
Phosphorus, Total, Soil Method: EPA 365.2
Phosphorus 230. mg/kg 12.2
Date: 02/28/07
Asheville Certification IDs
NC Wastewater 40
'1C Drinking Water 37712
Sc 99030
FL NELAP E87648
02/15/07 09:07 TNM
02/15/07 13:15 JMW 7727-37-9
02/28/07 20:05 JMW
02/27/07 14:28 EWS
02/27/07 14:28 EWS 7727-37-9
02/28/67 13:19 WWB 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.
�� N AC CCRp9
�lnehc
Page: 1 of 5
Charlotte Certification IDs
NC Wastewater .12
NC Drinking Water 37706
SC 99006
FL NELAP E87627

Pace Analytical Services, Inc. Pace Analytical Services, Inc.
_�. 9800 Kincey Avenue, Suite 100 2225 Riverside Drive
Huntersville, NC 28078 Asheville, NC 28804
f aceA�alytical o Phone: [phone] Phone: [phone]
Fax [phone] FaX [phone]
ff www.pacclabs.com `
Lab Project Number: 92137955
;..,. Client Project ID: TWSA LIME RESIDUAL -ANNUAL
Lab Sample No: 928002625 Project Sample Number: 92137955-001 Date Collected: 02/13/07 09:00
Client Sample ID: TWSA LIME RESIDUAL Matrix: Soil Date Received: 02/13/07 13:31
Parameters Results Units Report Limit An By CAS No. Qual RegLmt
pH Method: EPA 9045
pH 11.7 units 02/22/07 16:00 MDK
Plant Available Nitrogen Method:'
Nitrogen 2700 mg/kg 1.0 02/28/07 SHB 7727-37-9
Date: 02/28/07
f
Asheville_ Certification IDs
NC Wastewater 40
NC Drinking Water 37712
SC 99030
FL NELAP E87648
REPORT OF LABORATORY ANALYSIS
This report shall not be reproduced, except in full,
without the written consent of Pace Analytical Services, Inc.
0 �N AC�pRo
W; F
ne acl
Page: 2 of 5
Charlotte Certification IDs
NC Wastewater 12
NC Drinking Water 37706
SC 99006
FL NELAP E87627

LA
11:bbHM Statesville HnaI!jtjcaj 704-878-2787
Analytical Results
X
Pace Analytical -Asheville For: 92137955
2225 Riverside Drive
Asheville NC 28804
Entered 2114/2007
Reported: Z16/2007
Sample Remark
ID Parameter Cust ID
070214-2 % Solids 928002625
0.70214-2 Fecal COlifbrrn.VM 928002625
Respectfully submitted,
-Yl<)
C , -z--a Myers
NC Cert #440,
4CDW Cert #37755,
EPA NCO0909
Result Units Method Date Analyzed Anawst
...........
52.5 % SM2540B 2114107 MD
<38-1 M.PN/9 SM92210E 2114/07 MD
P - I
P.O. Box 228 0 Statesville, North Carolina 28687 a 70"72/4697

J
Pace Analytical For: .92139651 ,.,..._.
9800 Kincey Avenue, Sui
Huntersville NC 28078
Entered 3/8/2007 r All
Reported: 3/12/2007
Sample Remark
Sample ID Parameter Clust ID Result Units Method Date Analyzed Analyst
01038-8 % Solids 928098210 49.0 % SM2540B 3/8/07 MD
07038-8 Fecal Coliform MTF 928098210 <20 MPN/g SM92210E 3/8/07 MD
Respectfully submitted,
Dena Myers
NC. Cert #440;
NCDW Cert #37755,
EPA NCO0909
P.O. Box 228 • Statesville, North Carolina 28687. 704/872/4697

' E
Analytical Results
Pace Analytical -Asheville For: 92142957
2225 Riverside Drive
Asheville NC 28804
Entered 4/25/2007
Reported: . 4/27/2007
Sample Remark
Sample ID Parameter Cust ID Result Units Method Date Analyzed Analyst
070425-12 % Solids 928292762
070425-12 Fecal Coliform MTF 928292762
Respectfully submitted,
Dena Myers
NC Cert #440,
NCDW Cert #37755,
EPA NCO0909
53.8 % SM2540B 4/25/07 CL
<37 MPN/g SM92210E 4/25/07 CL
P.O. Box 228 9 Statesville, North Carolina 28687. 704/872/4697

c
Q,; tk?y' a r�
3xVJ'�
ace Analytical
r www.pacelabs.com.
"Solid results are reported on a dry�we
Lab Sample No: 928381185
Client Sample ID: TWSA LIME
Metals
Metals, Trace ICP17'. V
Aluminum
Arsenic
Cadmium= �'z'!""
Calcium
Ckiromi um
Copper
Lead
Magnesium
Molybdenum
Nickel
Potassium
Selenium
Sodium
Zinc
Date Digested
Mercury, CVAAS, in Soil
Mercury
Wet Chemistry
Percent Moisture
Percent Moisture
Total Percent Solids
Percent Solids
Nitrogen, Ammonia
Nitrogen, Ammonia
basis
Pace Analytical Services, Inc.
9800 KinceyAvenue, Suite 100
Huntersville, NC 28078
Phone: [phone]
Fax, 704.875.9091
Pace Analytical'Services, Inc.
2225 Riverside Drive
Asheville, NC 28804
Phone: [phone]
Fax., 828.252.4618
Lab Project Number: 92144523
Client Project ID: TWSA LIME RESIDUAL 5/15
Project Sample Number: 92144523-001 Date Collected: 05/15/07 09:20'
Matrix: Soil Date Received: 05/15/07 14:22
Results Units Report Limit Analyzed By CAS No. Qual RegLmt
Prep/Method: EPA 3050 / EPA 6010
3200
mg/kg
9.4
ND
mg/kg
0.47
0.20
mg/kg
0.094
200000
mg/kg
940
2.9
mg/kg
0.47
38.
mg/kg
0.47
7.0
mg/kg
0.47
1300
mg/kg
9.4
1.1
mg/kg
0.47
1.6
mg/kg
0.47'
1500
mg/kg
94.
1.4
mg/kg
0.94
250
mg/kg
94.
140
mg/kg
0.94
05/18/07 11:45
05/23/07 03:32 EWS 7429-90-5
05/23/07 03:32 EWS 7440-38-2
05/23/07 03:32 EWS 7440-43-9
05/23/07 03:32 EWS 7440-70-2
05/23/07 03:32 EWS 7440-47.3
05/23/07 03:32 EWS 7440-50-8
05/23/07 03:32 EWS 7439-92-1
05/23/07 03:32 EWS 7439-95-4
05/23/07 03:32 EWS 7439-98-7
05/23/07 03:32 EWS 7440-0270
05/23/07 03:32 EWS 7440-09-7
05/23/07 03:32 EWS 7782-49-2
05/23/07 03:32 EWS 7440-23.5
05/23/07 03:32 EWS 7440-66-6
05/18/07 11:45
Method: EPA 7471
0.059 mg/kg 0.0051 05/16/07 13:11 ALV 7439-97-6
Method: � Moisture
6.8 %
Method: EPA 160.3
93.2 %
Method: EPA 350.1 Modified
120 mg/kg
Total Kjeldahl Nitrogen, Soil Method: EPA 351.2
Nitrogen, Kjeldahl, Total 6500 mg/kg
05/18/07 09:26 KDF.
05/18/07 OF
9.4 05/22/07 17:34 SAJ 7727-37-9
840 05/24/07 18:00 SAJ
Nitrogen, Nitrate plus Nitrite Method: EPA 353.2.Modified
Nitrate as N ND mg/kg 11
Nitrate -Nitrite (as N) ND mg/kg 11
Date: 05/31/07
05/23/07 13:57 JMW
05/23/07 13:57 JMW 7727-37-9
Asheville Certification IDs REPORT OF LABORATORY ANALYSIS
NC Wastewater 40 NC Drinking Water 37712 This report shall not be reproduced, except in full,
SC 99030 without the written consent of Pace Analytical Services, Inc.
FL NELAP E87648
e[ac=
Page: 1 of 3
Charlotte Certification IDs
NC Wastewater 12
NC Drinking Water 37706
SC 99006
FL NELAP E87627

ceAnalytical@
Lab Sample No: 928381185
Client Sample ID: TWSA LIME
Plant Available Nitrogen
Nitrogen
Date: 05/31/07
Asheville Certification IDs
NC Wastewater 40
NC Drinking Water 37712
Sc 99030
FL NELAP E87648
Pace Analytical Services, Inc. Pace Analytical Services, Inc.
9800 Kincey Avenue, Suite 100 2225 Riverside Drive
Huntersville, NC 28078 Asheville, NC 28804
Phone: [phone] Phone: [phone]
Fax: [phone] Fax: [phone]
Lab Project Number: 92144523
Client Project ID: TWSA LIME RESIDUAL 5/15
w Project.Sample Number: 92144523-001 Date Collected: 05/15/07 09:20
IlJ4C Matrix: Soil Date Received: 05/15/07 14:22'
Results Units Report Limit , Analyzed By CAS No. Qual RegLmt
Method: EPA 365.2
2030 mg/kg 105. 05/22/07 10:56 DMN 7723-14-0
Method: EPA 9045 -
12.3 units 05/19/07 13:00 MJR1
Method: SM 4500-0O2 D
6500 mg/kg 43. 05/29/07 SHB -7727-37-9
Method:
2000 mg/kg 1.0 05/29/07 SHB 7727-37-9
a
REPORT OF LABORATORY ANALYSIS
This report shall not be reproduced, except in full,
without the written consent of Pace Analytical Services, Inc.
\N ACC°
A
�G ac_
Page: 2 of 3
Charlotte Certification IDs
NC Wastewater
12
NC Drinking Water
37706
SC
99006
FL NELAP
E87627

Analytical Results
W
Pace Analytical -Asheville .For: 92144523
2225 Riverside Drive
Asheville NC 28804
Entered, 5/16/2007
Reported: 5/21/2007
Sample Remark
Sample ID, Parameter Cutt ID. Result Units Method Date Analyzed Analyst
070516-4 % Solids 928381'185 45.2 % SM2540B 5/16/07 IVID
070516-4 Fecal Coliform IVITF 928381185 ..<20 MPN/g SM92210E 5/16/07 IVID
Respecffully submitted,
Dena Myers
NC Cert. #440,
NtDW Cert #37755,
EPA NC00909
P.O. Box 228 • Statesville, North Carolina 28687. 704/872/4697

k R
Luc Pace Analytical Services, Inc.
3 ® 2225 Riverside Dr.
�Ycat
Asheville, NC 28804
pacelabs:com;
[phone]
s. ANALYTICAL RESULTS
Project: TWSA Lime Residual
Pace Project No.: 921961
Pace Analytical Services, Inc.
9800 Kincey Ave. Suite 100
Huntersville, NC 28078
[phone]
Sample: TWSA LIME RESIDUAL Lab ID: 921961001 Collected: 08/21/07 09:00
Solid results reported on dry weight basis
Parameters Results Units Report Limit DF
Received: 08/21/07 13:03 Matrix: Solid
Prepared Analyzed CAS No. Qual
6010 MET ICP
Analytical Method: EPA 6010 Preparation Method: EPA 3050
Aluminum
5570 mg/kg
13.7
1
08/29/0.7 22:30
08/31/07 18:47
7429-90-5
Arsenic
ND mg/kg
0.68
1
08/29/07 22:30
08/31/07 18:47
7440-38-2
Cadmium
0.24 mg/kg
0.14
1
08/29/07 22:30
08/31/07 18:47
7440-43-9
Calcium
256000 mg/kg
13.7
1
08/29/07 22:30
08/31/07 18:47
7440-70-2
Chromium
5.2 mg/kg
0.68
1
08/29/07 22:30
08/31/07 18:47
7440-47-3
Copper
66.6 mg/kg
0.68
1
08/29/07 22:30
08/31/07 18:47
7440-50-8
Lead
6.2 mg/kg
0.68
1
08/29/07 22:30
08/31/07 18:47
7439-92-1
Magnesium
2060 mg/kg
13.7
1
08/29/07 22:30
08/31/07 18:47
7439-95-4
Molybdenum
2.5 mg/kg
0.68
1
08/29/0122:30
08/31/07 18:47
7439-98-7
Nickel
3.0 mg/kg
0.68
1
08/29/07 22:30
08/31/07 18:47
7440-02-0
Potassium
2210 mg/kg
685
1
08/29/07 22:30
68/31/0718:47
7440-09-7
Selenium
2.9 mg/kg
1.4
1
08/29/07 22:30
08/31/07 18:47
7782-49-2
Sodium
ND mg/kg.
685
1
08/29/07 22:30
08/31/07 18:47
7440-23-5
Zinc
222 mg/kg
0.68
1
08/29/07 22:30
08/31/07 18:47
7440-66-6
7471 Mercury
Analytical Method: EPA 7471 Preparation Method: EPA 7471
Mercury
0.091 mg/kg
0.0068
1 .
08/29/0714:18
08/29/0716:43
7439-97-6
-11
i ent Moisture
Analytical_ Method: ASTM D2974-87
Percent Moisture
27.0 %
0.10
1
08/23/07 10:50
9045 pH Soil
Analytical Method: EPA 9045
pH at 25 Degrees C
12.4 Std. Units
0.10
1
08/30/07 02:00
Plant Available Nitrogen
Analytical Method: 40CFR PART 503
Plant Available Nitrogen
5010 mg/kg
1.0
1
09/10/07 14:38
Total Nitrogen Calculation
Analytical Method: 40CFR PART 503
Nitrogen
16500 mg/kg
40.0
1
09/10/0714:21
7727-37-9
350.1 Ammonia
Analytical Method: EPA 350.1
Nitrogen, Ammonia
218 mg/kg
14.0
1
09/03/0712:19
7764-41-7
351.2 Total Kjeldahl Nitrogen
Analytical Method: EPA 351.2
Nitrogen, Kjeldahl, Total
16500 mg/kg
1400
50
09/09/07 15:10
7727-37-9
353.2 Nitrogen, NO2/NO3
Analytical Method: EPA 353.2
Nitrogen, Nitrate
15.6 mg/kg
12.0
1
08/30/07 21:18
Nitrogen, NO2 plus NO3
15.6 mg/kg
12.0
1
08/30/07 21:18
mate: 09/13/2607 06:15 PM REPORT OF LABORATORY ANALYSIS
This report shall not be reproduced, except in full,
without the written consent of Pace Analytical Services, Inc..
%% ♦c C09
Page 5 of 15

t
Analytical Results
Pace Analytical -Asheville For:. 921961
2225 Riverside Drive
Asheville NC 28804
Entered 8/22/2007
Reported. 8/28/2007
Sample Remark
Sample ID Parameter Cu'st ID
Result Units Method Date Analyzed Analyst
070822-3 % Solids 921961001
55.0 %` SM2540B 8/22/07 MD
070822-3 Fecal Coliform MTF 921961001
<20 , MPN/9 :SM92210E` . 8/22/07 MD
Respectfully submitted,
-ena Myers
NC Cert #440,
NCDW Cert #37755,
EPA NC00909,
P.O. Box 228 Statesville, North Carolina 28687. 7041872/4697

Analytical Results
Pace Analytical Asheville For: 924510
2225 Riverside Drive
Asheville NC 28804
Entered 9/27/2007
Reported: 10/10/2007
Semple Remark
'ample ID Parameter Cust IQ Result Units Method Date Analyzed Analyst
)70927-2 % Solids 924510001 59.5 % SM2540B 9127/07 MD
070927-2 Feral Coliform MTF 924510001 <20 / MON/g SM92210E 9/27107 MD
Respectfully submitted,
Dena Myers
NC Cert #440,,
NCDW Cert #37756,
EPA NC00909
P.O. Box 228 + Statesville, North Carolina 28687. 704/87214697
T•A rn17_01 n_LI"11 Ton Tn aToI1u AT T TnGan P'1C 1.1 UOC!C /nn7 0T 13n

e
Pace Analytical Services, Inc.
2225 Riverside Dr.
Asheville, NC 28804
ANALYTICAL RESULTS
=t: TWSA Lime Residual
Project No.: 927665
[phone]
Pace Analytical Services, Inc.
9800 Kincey Ave. Suite 100
Huntersville, NC 28078
[phone]
••r•� �••••� --�Iu L-
Lao tu: yL7ti65001
Collected: 11/1310710:15
Received: 11/13/07 12:37 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
Arsenic
3730 mg/kg
11.8
1
11/18/67 22:30
11/20/07 03:05
7429-90-5
Cadmium
ND mg/kg
0.59
1
11/18/07 22:30
11/20/07 03:05
7440-38-2
Calcium
0.18 mg/kg
0.12
1
11/18/07 22:30
11/20/07 03:05
7440-43-9
Chromium
242000 mg/kg
1180
100
11/18/07 22:30
11/20/07 16:56
7440-70-2
Lead
3.1 mg/kg
0.59
1
11/18/07 22:30
11/20/07 03:05
7440-47-3
Magnesium
3.6 mg/kg
0.59
1
11/18/07 22:30
11/20/07 03:05
7439-92-1
Molybdenum
1550 mg/kg
11.8
1
11/18/07 22:30
11/20/07 03:05
7439-95-4
Nickel
2.7 mg/kg
0.59
1
11/18/07 22:30
11/20/07 03:05
7439-98-7
Potassium
1.9 mg/kg
0.59'
1
11/18/07 22:30
11/20/07 03:05
7440-02-0
Selenium
1370 mg/kg
592
1
11/1.8/07.22:30
11/20/07 03:05
7440-09-7
Sodium
1.9 mg/kg
1.2
1
11/18/07 22:30
11/20/07 03:05
7782-49-2
Zinc
ND mg/kg
592
1
11/1.8/07 22:30
11/20/07 03:05
7440-23-5
155 mg/kg.
1.2
1
11/18/07 22:30
11/20/07 03:65
7440-66-6
7471 Mercury
Analytical Method: EPA 7471 Preparation Method: EPA 7471
Mercury
0.019 mg/kg
0.0066 1 11/15/0715:16
11/19/0715:30 7439-97-6
ent Moisture
Analytical Method: ASTM D2974-87
Percent Moisture
15.5 %
0.10 1
11/15/07 09:22
9045 pH Soil
Analytical Method: EPA 9045
pH at 25 Degrees C
12.0 Std. Units -
0.10 1
.11/16/07 10:40
Plant Available Nitrogen
Analytical Method: 40CFR PART 503
Plant Available Nitrogen
2570 mg/kg
1.0 1
11/27/07 08:56
Total Nitrogen Calculation
Analytical Method: 40CFR.PART 503
Nitrogen
8550 mg/kg
40.0 1
11/26/0716:25 7727-37-9
350.1 Ammonia
Analytical Method: EPA 350.1
Nitrogen, Ammonia
29.2 mg/kg
11.6 1
11/16/07 12:39 7764-41-7
351.2 Total Kjeldahl Nitrogen
Analytical Method: EPA 351.2
Nitrogen, Kjeldahl, Total
8550 mg/kg
1160 50
11/15/07 00:49 7727-37-9 .
353.2 Nitrogen, NO2/NO3
Analytical Method: EPA 353.2
Nitrogen, NO2 plus NO3
ND mg/kg
11.8 1
11/16/07 11:19
Qual
Date: 11/29/2007 04:29 PM REPORT OF LABORATORY ANALYSIS Page 4 of 13
This report shall not be reproduced, except in full,
without the written consent of Pace Analytical Services, Inc..
�IJJ Y�Y.1�A.

Analytical Results
}
r rub ace Analytical Asheville
�2225 Riverside Drive
Asheville NC 28804
Entered 11/14/2007
Reported: . 11 /26/2007
Sample Remark
For: 927665
Sample ID Parameter Cust ID Result Units Method Date Analyzed Analyst
'071114-1 % Solids 927665001 54.4
071114-1 Fecal Coliform MTF 927665001 <20
Respectfully submitted,
uena Myers
NC Cert #440,
NCDW Cert #37755,
EPA NC00909
% SM2540B 11/14/07
MPN/g SM92210E 11/14/07
CL
CL
P.O. Box 228 • Statesville, North Carolina 28687 s 704/872/4697

Pace Analytical Services, Inc.
P 2225 Riverside Dr.
ANALYTICAL RESULTS
;t: TWSA Lime Residual
Project No.: 9211137
Asheville, NC 28804
[phone]
Pace Analytical Services, Inc.
9800 Kincey Ave. Suite 100
Huntersville, NC 28078
[phone]
ample: TWSA LIME
Lab ID: 9211137001
Collected: 12/27/07 09:00
Received: 01/08/08 15:40 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
6750 mg/kg
17.6
1
01/14/08 09:45
01/14/08 23:53
7429-90-5
Arsenic
0.94 mg/kg
0.88
1
01/14/08 09:45
01/14/08 23:53
7440-38-2
Cadmium
0.47 mg/kg
0.18
1
01/14/08 09:45
01/14/08 23:53
7440-43-9
Calcium
413000 mg/kg'
1760
100
01/14/08 09:45
01/15/0817:19
7440-70-2
Chromium
12.9 mg/kg
0.88
1
01/14/08 09:45
01/14/08 23:53
7440-47-3
Copper
66.3 mg/kg
0.88
1
01/14/08 09:45
01/14/08 23:53
7440-50-8
Lead
4.2 mg/kg
0.88
1
01/14/08 09:45
01/14/08 23:53
7439-92-1
Magnesium
2800 mg/kg
17.6
1
01/14/08 09:45
01/14/08 23:53
7439-95-4
Molybdenum
2.8 mg/kg
0.88
1
01/14/08 09:45
01/14/08 23:53
7439-98-7
Nickel
17.8 mg/kg
0.88
1
01/14/08 09:45
01/14/08 23:53
7440-02-0
Potassium
4360 mg/kg
879
1
01/14/08 09:45
01/14/08 23:53
7440-09-7
Selenium
ND mg/kg
1.8
1
01/14/08 09:45
01/14/08 23:53
7782-49-2
Sodium
ND mg/kg
879
1
01/14/08 09:45
01/14/08 23:53
7440-23-5
Zinc
226 mg/kg
1.8
1
01/14/08 09:45
01/14/08 23:53
7440-66-6
Percent Moisture Analytical Method: ASTM D2974-87
Percent Moisture 52.6 % 0.10' 1 01/16/08 12:41
.1 Phosphorus, Total Analytical Method: EPA 365.1
Phosphorus 4086 mg/kg 211 50 ' 01/15/08 21:53 7723-14-0
Qual
Sample: TWSA LIME 'Lab ID: 9211137002 Collected: 12/31/07 09:40 Received: 01/08/08 15:40 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
Arsenic
Cadmium
Calcium
Chromium
Copper
Lead
Magnesium
Molybdenum
Nickel
Potassium
Selenium
Sodium
Zinc
Percent Moisture
Percent Moisture
Ct`e: 01/16/2008 01:52 PM
6420 mg/kg
ND mg/kg
0.40 mg/kg
452000 mg/kg
4.8 mg/kg
63.3 mg/kg
4.5 mg/kg
2780 mg/kg
2.4 mg/kg
4.1 mg/kg
2880 mg/kg
2.5 mg/kg
ND mg/kg
219 mg/kg
Analytical Method: ASTM D2974-87
51.5 %
19.5
1
01/14/08 09:45.
01/15/08 00:06
7429-90-5
0.97
1
01/14/08 09:45
01/15/08 00:06
7440-38-2
0.19
1
01/14/08 09:45
01/15/08 00:06
744043-9
1950
100
01/14/08 09:45
01/15/08 17:22
7440-70-2
0.97
1
01/14/08 09:45
01115/08.00:06
7440-47-3
d.97
1
01/14/08 09:45
01/15/08 00:06
7440-50-8
0.97
1
01/14/08 09:45
01/15/08 00:06
7439-92-1
19.5
1
01/14/08 09:45
01/15/08 00:06
7439-95-4
0.97
1
01/14/08 09:45
01/15/08 00:06
7439-98-7
0.97
1
01/14/08 09:45
01/15/08 00:06
7440-02-0
973
1
01/14/08 09:45
01/15/08 00:06
7440-09-7
1.9
1
01/14/08 09:45
01/15/08 00:06
7782-49-2
973
1
01/14/08 09:45
01/15/08 00:06
7440-23-5
1.9
" 1
01/14/08 09:45
01/15/08 00:06
7440-66-6
0.10 1
REPORT OF LABORATORY ANALYSIS
This report shall not be reproduced, except in full,
without the written consent of Pace Analytical Services, Inc..
01 /16/08 12:42
Page 4 of 10

Pace Analytical Services, Inc.
Pace Analytical Services, Inc.
Ii,CZ! ®
2225 Riverside Dr.
9800 Kincey Ave. Suite 100
z pacelabs:com:,
Asheville, NC 28804
Huntersville, NC 28078
,d
[phone]
[phone]
ANALYTICAL RESULTS
ect: TWSA Lime Residual
'�r ace Project No.: 9211137
Sample. TWSA LIME Lab ID: 9211137002 Collected: 12/31/07 09:40
Received: 01/08/08 15:40
Matrix: Solid
Resuits reported on a "dry-weighf"basis
Parameters Results Units Report Limit DF
Prepared Analyzed
CAS No. Qual
365.1 Phosphorus, Total Analytical Method: EPA 365.1
Phosphorus 2890 mg/kg 186 45
01/15/0818:43 7723-14-0
Date: 01/16/2008 01:52 PM
REPORT OF LABORATORY ANALYSIS
This report shall not be reproduced, except in full,
without the written consent of Pace Analytical. Services, Inc..
Page 5 of 10

Appendix D
2007
Lime Stabilization
Record of
Operation

TWSA RESJRUAL
MONTHLY OPERE IN TOTALS
--
Press Run Time Sludge Hauled to Landfill
Janua 2007
SLUDGE FEED
LIME FEED
Po l mer Usa
lb
a
$/Da -
hrs $Ida Wet Ton Ti
ing Fee
DATE % Solids
Gallons D
Ton
Ibs D Ton $/Da
24.40
$749.58
1
2
$0.00
76.1
$114.15
12.5 $225.00 47.66 $1,464.1
.3 1.5
54,000
3.38
0
4
5
6
7
8
9
0 $0.00
76.1
$114.15
12.0 $216.00
9.5 $171:00
10 1.5
51,300
3.21
0 $0.00
57.1
$85.65
42.21
$1,295.08
11 1.4
27,300
1.59
12
13
25.67
$787.61
14
15
22.51
$689.58
16
17
$0.00
76.1
$114.15
9.6 $172.80
18 1.4
35,420
2.07
p
19
20
21
22
23
$0.00
76.1
$114.15
11.0 $198.00 24.00
$734.80
24 1.6
41,054
2.74
0
24.31
$744.29
25
26
27
28
9
29
0 $0.00
38.0
$57.00
9.5 $171.00
8.7 $156.60
1.8
34,500
2.59
0 $0 00
57.1
$85.65
31 1.5
34,600
2.16
65.2
$97.84
10.4 $187.20
daily
av 1.5
39 739
2.53
0 0 p
72.8 $1,310.40 210.76
$6,465.07
monthly
1 278.174
17.73
0.0 0.00 $0.00
456.E
$684.90
total
9 loads hauled to landfill @ $450/load=
$4,050•00
# of days
press was run
7
Total Residual Cost for the month =
$1
# of days lime
was added
_ 0

T\8/SALIME STABILIZATION
DAILY RECORD �
` -
' ) �
DATE
START STOP TOTAL
RUNTIME, FIRS
SLUDGE FEED, GAL
LIME FEED, LBS
�
PRESS, �
[::::::=
sLuooaFsEomaouoa � . -----
�
^ PRODUCTION, DRY
uM�acuooE�T|o TOTAL `
Inlet reached temp @
�
Outlet reached temp @PATHOGEN
VECTOR K�E0U I CTION
REDUCTION�"~^^^~~-''—'
'
�
OPERATORTIME
`
INITIAL PH ----_-____
' .
' 2HRG.
�
. .
� 22HR8.
-_-_---_�_ �
'.
------'-'----'_--_--_'_-----_------^.'------_----..
�
OPERATIONAL
| '
` BELT PRESS SPEED.96 -
� pOLYMERPUMP SPEED, 96
� SLUDGE PUMP SPEED, 96 r
-
\ | [ -� )cE � AUGER.
- --��
\
` K8D{ERSPEED, %
. '.
\ '
Revised mxoon ^
POLYMER USAGE
TYPE USED 11 114q63
TANKS MIXED
| o����� »tk' km�^«�
)L~~

RUN TIME, HRS.
SLUDGE FEED, GAL
LIME FEED, LBS
TWSA LIME STABILIZATION
DAILY RECORD
DATE
-rAf
START STOP I'll- 7 1 Ili
Ic f
SLUDGE FEED% SOLIDS, E:T�= PRESS , % SOLIDS
LIME/SLUDGE RATIO. TOTAL PRODUCTION, DRY TONS
Inlet reached temp Q
Outlet reached temp @ F_7=
PATWnxcFKI* REDUCTION' VECTOR ATTRACTION REDUCTION
TEMPERATURE of
INTO OUT OF
)ME VESSEL VESSEL OPERATOR
TON
TIME OPERATOR
INITIAL, PH_
2 HRS..
22 HRS.
................................................................................................................................................................... .......................................................
POLYMER USAGE
OPERATIONAL
TYPE USED
BELT PRESS SPEED, %
POLYMER PUMP SPEED, % TAN . KS MIXED Wt-
SLUDGE PUMP SPEED, % GPM
I
Ll'�, -)FEED AUGER,% LBS/HR
LITERS/TANK i74
MIXER SPEED, % q61 t1as
Revised 8112103

TWSA LIME STABILIZATION
DAILY RECORD
ppJ
DATE
START STOP TOTAL.
F -7
RUN TIME, HRS!,00
SLUDGE FEED, GAL
LIME FEED, LB.&'
PRESS, % SOLIDS
SLUDGE FEED 1/o SOLIDS.
LIME/SLUDGE RATIO TOTAL PRODUCTION, DRY TONS
Inlet reached temp @
Outlet reached temp @
-VECTOR ATTRACTION REDUCTION
TEMPERATURE of
I INTO I.OUTOF
TIME OPERATOR
INITIAL PH_
................................................ .......................................... ...........................................................................
OPERATIONAL
137,
BELT PRESS SPEED, %
POLYMER PUMP SPEED,
SLUDGE PUMP SPEED, % _'Z 77 _GPM__!�(1_
LI,JFEED AUGER, % LBS/HR_
MIXER SPEED, %
Revised 8112103
2 HRS.
22 HRS.
.......................................... :­ -----
POLYMER USAGE
TYPE USED
TANKS MIXED ILL-
FERS/TANK
5-rl,.! ib-.s

TWSA LIME STABILIZATION
DAILY RECORD
1 DATE 5
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
START STOP TOTAL Y "`
9!n-s I `7400
SLUDGE FEED % SOLIDS `
LIME/SLUDGE RATIO
Inlet reached temp @
Outlet reached temp @
PATHOGEN REDUCTION
tmt tKA I uKr- ur
INTO I OUT OF
!ME
PRESS, % SOLIDS
[::::::=
TOTAL PRODUCTION, DRY TONS [:::::=
VECTOR ATTRACTION REDUCTION
TIME
INITIAL PH
2 HRS.
22 HRS.
..................................................................................................................................................
OPERATIONAL
Lj
BELT PRESS SPEED, %
POLYMER PUMP SPEED, % G�O
SLUDGE PUMP SPEED, % S_�GPM
Lh FEED AUGER, % LBS/HR
MIXER SPEED, %
Revised 8/12103
OPERATOR
POLYMER USAGE
TYPE USED
r
TANKS MIXED
�611 �Vd S

TWSA LIME STABILIZATION
DAILYRECORD,
DATE,��©
START
RUN TIME, HRS
SLUDGE FEED, GAL
DRY TON
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
TCIIBDFDATI IRF nF
_
)ME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
TIME
I
....................................................................................................................................................................
OPERATIONAL
BELT PRESS SPEED,
t �O
POLYMER PUMP SPEED, % !
SLUDGE PUMP SPEED, % 2,5 % GPM
Lh )FEED AUGER, % LBS/HR
MIXER SPEED, %
INITIAL PH
2 HRS.
22 HRS.
OPERATOR
POLYMER USAQGEp,
TYPE USED u �J /� a
TANKS MIXED [
ILITERS/TANK '4+
%A tb.5
Revised 8/12/03
4

TWSA LIME STABILIZATION
DAILY RECORD
DATE 1130167
START STOP TOTAL
T Cl
RUN TIME, HRS
DRY TON
SLUDGE FEED, GAL 500
LIME FEED, LBS
SLUDGE FEED % SOLIDS PRESS, SOLIDSr
LIME/SLUDGE RATIO TOTAL PRODUCTION, DRY TONS
-inlet reached temp @
Outlet reached temp @
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
...................
................................................ ................................................................... m ............................................................................... .......... .......................................
OPERATIONAL POLYMER USAGE
BELT . PRESS SPEED, % TYPE USED 14 q (o 13 -'1 <6 (60
POLYMER PUMP SPEED, % l TANKS MIXED
7
SLUDGE PUMP SPEED % GPM "7
)FEED AUGER, % LBS/HR 'LITERS/TANK
MIXER SPEED, %: --77—
Revised 8/12/03

TWSA LIME STABILIZATION
DAILY RECORD
DATE
.START STOP TOTAL
RUN TIME, HRS `s Fa►-,
DRY TON
SLUDGE FEED, GAL C)
d
LIME FEED, LBS
SLUDGE FEED % SOLIDS P PRESS, % SOLIDS
LIME/SLUDGE RATIO TOTAL PRODUCTION, DRY TONS
Inlet reached temp @
Outlet reached temp @
0nrunrr9=nl RGnI ICTI0hI VECTOR ATTRACTION REDUCTION
_ TEMPERA] UKt Or
INTO OUT OF
'1ME I VESSELI VESSEL
TIME
INITIAL PH
2 HRS.
22 HRS. .
................... :............................................................................................................................................................
I OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, % 3
SLUDGE PUMP SPEED, %) _GPM V
I L(' )FEED AUGER, % LBS/HR .
MIXER SPEED, %
I
Revised 8/12103
I
OPERATOR
POLYMER USAGE
TYPE USED q ` (94 Q
TANKS MIXED I

February 2007
r
DATE
% Solids wGallons
D Ton
Ibs_
Dry Ton
1
"
2
3
4
5
6
7
1.2
37,100.
1.86
0
8
1.4
40,777
2.38
0
9
1.9
48,337
3.83
.0
10
11
12
13
14
15
2.2
50,800
4.66
0
16
17
18
19
20
21
22
23
24
25
26
27
28
0.99
40,0181
1.651
0
TWSA RESIDUAL
MONTHLY OPERL )N TOTALS v
LIME FEED Polymer Usage Press Run Time Sludge Hauled to Landfill
Itmo., �hc S/Dav hrs $%day Wet Ton ` Ti in Fee
00
76.1
$114.15
8.7
$156.60
00
76.1
$114.15
11.0
$198.00
00
95.1
$142.65
11.5.
$207.00
76.1 $114.15 11.8
76.1 $114,15 1
23.83
22.95
24.14
20
�a
3EE31
- daily L _
ail 1.5 43 406 2.87 0 ERR 0 79.9 $11`9.85 10.8 $194.40
monthly
total 217,032 14.37 0.0 0.00 1 $0.00 399.5 $599.25 54.0 T$972.00 70.92 $2 173.02
3 loads hauled to landfill @ $450/load $1,350.00
# of days press was run 5
# of days lime was added 0
Total Residual Cost for the month $5,094.27

TWSA LIME STABILIZATION
DAILY RECORD
DATE
I a
START STOP IUIAL
RUN TIME, HIRS r /0 -7!'S-0 I �
DRY TON
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDS PRESS, % SOLIDSI
LIME/SLUDGE RATIO . TOTAL PRODUCTION, DRY TONS
Inlet reached temp Q
Outlet reached temp @
PATHOGEN REDUCTION VECTOR, ATTRACTION REDUCTION
TPhfiPF:PATI IPF nF
IME
INTO
VESSEL-
OUT OF
VESSEL
OPERATOR
TIME. OPERATOR
INITIAL PH
............................................................................................. : ....................................................................
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, % 3 GPM
Ll' ;FEED AUGER, % LBS/HR.'
MIXER SPEED, %
Revised 8/12/03
.2 HRS.
. POLYMER USAGE
TYPE USED q2bL4B4?1(D
TANKS MIXED lilt

TWSA LIME STABILIZATION
DAILY RECORD
DATE
START STOP TOTAL
RUN TIME, HRS
DRY
TfO�N
SLUDGE FEED, GAL'10
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
TEMPEKA I UKt Or
INTO OUT OF
'ME VESSEL VESSEL oP
TIME OPERATOR.
2 OPERATIONAL
3
BELT PRESS SPEED, %
G
POLYMER PUMP.SPEED, %
SLUDGE PUMP SPEED, % qd QL 0 GPM 91
LI' -EED AUGER, % LBS/HR
MIXER SPEED,
I
Revised 8/12103
POLYMER USAGE
TYPE USED 43 08 -f- �
TANKS MIXED
I ITFRS/TANK 4 �t

TWSA LIME STABILIZATION
DAILY RECORD (�
DATE l
START STOP (TOTAL
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDS r
LIME/SLUDGE RATIO
Inlet reached -temp.@
Outlet reached temp @
PATHOGEN REDUCTION
TEMPERA I UKt Or
INTO OUT OF
VESSEL VESSEL 1 O
IT3'i0IZI
PRESS, % SOLIDS
TOTAL.PRODUCTION, DRY TONS
VECTOR ATTRACTION REDUCTION
TIME
INITIAL PH
2 HRS.
22 HRS.
............................................................................................................................................................................
OPERATIONAL
BELT PRESS SPEED, % 351/0
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, % d b GPM ' 5 G
Ll' j EED AUGER, % LBS/HR
MIXER SPEED, %
i
Revised 8112103
OPERATOR
POLY''MrrE��R USAGE
TYPE USED '7V�8f66
TANKS MIXED
qI
9160 Iv✓�

TWSA LIME STABILIZATION
DAILY RECORD.
DATE er
START STOP TOTAL
RUN TIME, HIRS 0 '3 L" 1 0
SLUDGE FEED, GAL
LIME FEED, LEIS
SLUDGE FEED % SOLIDS PRESS, % SOLIDSI
LIME/SLUDGE RATIO TOTAL PRODUCTION, DRY TONS
Inlet 'reach . ed temp @
-Outlet reached temp @
mcni it—rifw
"TEMIJEKA I IJKL Ot-
INTO OUT OF
LME_ VESSEL VESSEL o
VECTOR Um ATTRACTION
TIME OPERATOR
INITIAL PH
2 HRS.
22 HRS.
......................................................................................................................... ..................................................
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, %
L
SLUDGE PUMP SPEED, % GPM_
LI'_ FEED AUGER,% LBS/HR
L. MIXER SPEED, %
Revised 8/12103.
POLYMER USAGE
TYPE USED Y�4A406_15
TANKS MIXED I 111
76

TWSA LIME STABILIZATION
DAILY RECORD
DATE
START STOP TOTAL
n
RUN TIME, HRS , ! • t♦'►r
DRY TON
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDS 0199
PRESS, °% SOLIDS
LIME/SLUDGE RATIO TOTAL PRODUCTION, DRY TONS
Inlet reached temp @
Outlet reached temp @
PATI-IC7GEN REDUCTION VECTOR ATTRACTION REDUCTION
1 tMNtKA I UKt Of
INTO OUT OF
'"IME I VESSEL VESSEL
TIME
INITIAL PH
2 HRS.
22 HRS.
..........................................................................................................................................................................................
OPE/RATIONAL
BELT PRESS SPEED, %y`
POLYMER PUMP SPEED, % q
6 O
SLUDGE PUMP SPEED, % 3b �` O GPM � 1
LI° FEED AUGER, % LBS/HR
I
MIXER SPEED, %
OPERATOR
POLYMER USAGE
TYPE USED L34' 4-� I
TANKS MIXED 4
y6.i 165
Revised 8112103

T1NSA RESRUAL
MONTHLY OPERF. N TOTALS
# of days press was run 8
# of days lime was added $
1 loads hauled to landfill @ $450/load= $450.00
Total Residual Cost for the month = $9,006.36

TWSA LIME STABILIZATION
DAILY RECORD
DATE �6
START STOP TOTAL
RUN TIME, HRS Too r''L. �• 5 V\rs
DRY TON
T9SLUDGE FEED, GAL �7"U 1 �� �� >t �Dd 35,a'•-7 D
LIME FEED, LBS
SLUDGE FEED % SOLIDS 6 PRESS, % SOLIDS
LIME/SLUDGE RATIO o i TOTAL PRODUCTION, DRY TONS
Inlet reached temp @ c L
Outlet reached temp @
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TFMPFRATI IRF nF
-
)ME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
101
►9.I
-I93
to:09
i 84
188
'L
:00 PM
o go
189
1,9c0
cen
TIME `fi�% j„ OPERATOR
%� • rr rn��j ``�C
INITIAL PH
!� 1a�N$- .198
I2 HRS.
�'• 30 Qrh 22 HRS.
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, % "lD
SLUDGE PUMP SPEED, % GPM �Ob • ��
LI. _ FEED AUGER, '% LBS/HR
MIXER SPEED, %
Revised 8/12/03
POLYMER USAGE
TYPE USED'
TANKS MIXED

RUN TIME, HIRS
SLUDGE FEED, GAL
LIME FEED, LBS
TWSA LIME STABILIZATION
DAILY RECORD
DATE 3z*k /6
START STOP - TOTAL
',3� 1 r1: 00--
SLUDGE FEED % SOLIDS Z, PRESS, % SOLIDSI
LIME/SLUDGE RATIO /j- TOTAL PRODUCTION, DRY TONS
Inlet reached temp Q o
Outlet reached temp @
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
Tr:RAPPIPATI IPP- ni='
WE
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
75
1
&0
d:aIg
Z)
-cz
coo
1171,11
-3-6
(P'4'30
19 l
190'
TIME
I A3-.151
INITIAL. PH
2HRS-.
22 HRS.
P' . ............ ... tl* .................................................................... ...................................
..........
MID OF OPERATIONAL
I. plum
BELT PRESS SPEED, % Ao
1 -.0
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, % At) GPM (PS-52
LC,_ )FEED AUGER, % 55 LBS/HR-L17-�
MIXER SPEED, %
Revised 8112/03
1101E
OPERATOR
ri
U
USAG
TYPE USED "-0160-1416C'
TANKS MIXED
AN

RUN TIME, HRS
SLUDGE FEED, GAL
TWSA LIME STABILIZATION
DAILY RECORD .
DATE ;�fl �J .
START STOP TOTAL
mo `7 k,/5 71
LIME FEED, LBS I V 11-1 jU w1 I
SLUDGE FEED % SOLIDS 1 PRESS, % SOLIDS
LIME/SLUDGE RATIO a y TOTAL PRODUCTION, DRY TONS a
qtn
Inlet reached temp @
Outlet reached temp @
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TDIIADFRATI IPP nF
_ JME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
5,145
TT
C�
T Co 0
L112-�
ab q
� : it 0.............................. :.......
OPERATIONAL
BELT PRESS SPEED,-% T
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, % 30 GPM %oC , 34
Llla.>FEED AUGER, % 93 LBS/HR i i 336
MIXER SPEED, %
TIME OPERATOR
�g'A-ead`
d INITIAL PH_12" x--
2 HRS. I I%
22 HRS.
POLYMER USAGE
TYPE USED
TANKS MIXED
�r
18112103,

TWSA LIME STABILIZATION
DAILY RECORD
DATE�7
pSTART STOP TOTAL
RUN TIME, HRS
DRY TON.
SLUDGE FEED, GAL 1 SK `t U Sr I I ry TJ I
LIME FEED, LBS o • 3
SLUDGE FEED °% SOLIDS PRESS, e% SOLIDS
LIME/SLUDGE RATIO cZ DL1 TOTAL PRODUCTION, DRY TONS c 6
Inlet reached temp @ .
Outlet reached temp @
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TEMPERATURE nF
.TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
Jig
/0,-S3
a
A03
C .
1 -
C9
Ao [
E
:3
®�
o
.
�.Qo
Aori
'a03
Lm
TIME OPERATOR
a r INITIAL PH
AW
2 HRS. . LfQ C, i
22 HRS.
OPERATIONAL
BELT PRESS SPEED, % �� �l0
POLYMER PUMP SPEED, % 3S� o/O
SLUDGE PUMP SPEED, % 35 ©O GPM /a
I LIME FEED AUGER, % q �Gt� LBS/HR
Mh-_._R SPEED, %
Revised 8112103
POLYMER USAGE
TYPE USED�P'���
TANKS MIXED
LITERSlTANK -

TWSA LIME STABILIZATION
DAILY RECORD
DATE /1 C.T 1
START STOP TOTAL.
RUN TIME, HRS
DRY TON
SLUDGE FEED, GAL 3 S 0 3 S
LIME FEED; LBS rS
SLUDGE FEED %SOLIDS ! • PRESS , °%.SOLIDS
LIME/SLUDGE RATIO ® I TOTAL PRODUCTION, DRY TONS
Inlet reached temp @
Outlet reached temp @:
PATHOGEN REDUCTION _ VECTOR ATTRACTION REDUCTION
TFIIAPFRATIJRF: nF
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
l�
C
E1JD erf RU
10 1
TIME I4q OPERATOR
ia. a
2,67'° INITIAL PH TL
o, .b 2 HRS. I go 0'-F
r
OPPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, % :30 04
SLUDGE PUMP SPEED, % � GPM
- c/
LIME FEED AUGER, % W 6D LBS%HR S°2
Mh-_ _ A SPEED,
Revised BMW
22 HRS.
POLYMER USAGE
PE USED
TANKS MIXED

TWSA LIME STABILIZATION
DAILY RECORD
...DATE �� ® LD
START STOP
RUN TIME, HRS
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 @
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TFMPFRATURF nF
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
CLAJ
C� AF
TON
TIME OPERATOR
LA INITIAL PH I'R e 6 b v
r 2 HRS. , 04
ra,5?7.69(p
a: r7 2ZHRS. l 2, w 7 w�
.1 ` 00.......:. ` ...®............. xb..1................... t.n................... •...........................................
.EN
OPERATIONAL
BELT PRESS SPEED, % 5 a
POLYMER PUMP SPEED, %�
SLUDGE PUMP SPEED, % 3b GPM 5 g / 3
LIME FEED AUGER, % LBS/HR 1666
ML __;2 SPEED, %
POLYMER USAGE
TYPE USED���
TANKS MIXED
TERS/TANK�
Revised 8112103

TWSA LIME STABILIZATION
DAILY RECORD
n
DATE
I Zo
START STOP TOTAL
OF
INTO
OUT
TON
TIME OPERATOR
a124.
INITIALPH
.o'15..
3 : 5 / 2 HRS.-9.3
°m I 22 HRS. , '
OPERATIONAL
BELT PRESS SPEED, % I %S Ala
POLYMER PUMP SPEED, % 36%
SLUDGE PUMP SPEED, % 30��a GPM
I LIME FEED AUGER, % 1p 60 LBS/HR ad
MI:: =� SPEED, %
Revised 8112103
i
i.,
Lam_
POLYMER USAGE
PE USED ����- �� loD
TANKS MIXED
LITERS/TANK

TWSA LIME STABILIZATION
DAILY RECORD
START STOP TOTAL
RUN TIME, HRS �C7 c Py"\
SLUDGE FEED, GAL
LIME FEED; LBS
SLUDGE FEED .% SOLIDS . PRESS , % SOLIDS
LIME/SLUDGE RATIO TOTAL PRODUCTION, DRY TONS fi
,
Inlet reached temp @ _ w
Outlet reached temp @
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TEMPERATURE of
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
�'vI
aol
ao
I qa
ao8
)108 :
ems,
/a05
�rf
V7,
�1n'1
TIME OPERATOR
U.55-o St
INITIAL PH l .
2 HRS. -Ia, 36 '
01 22 HRS. 1r"1
P...........:%CJh..................: ............................................
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED,
SLUDGE PUMP SPEED, % caC L t/� GPM'
I LIME FEED AUGER, %B! LBS/HR I
MI:-._R pt'r-mu"p/co
I
Revised 811y03
I
PE USEDt&kj %1 UT D.
TANKS MIXED _Lm1

TWSA RESIRUAL
MONTHLY OPERA N TOTALS
0
LIME FEED
Polymer Usage
Press Run Time
MUI
# of days press was run 8
? loads hauled to landfill @ $450/load= $0.00
# of days lime was added 8 Total Residual Cost for the month = $6,451.01

TWSA LIME STABILIZATION
DAILY RECORD
DATE i/sz
START STOP
RUN TIME, HRS A3CD. I 7,...o o
SLUDGE FEED, GAL (i
LIME FEED, LBS
SLUDGE FEED % SOLIDS PRESS, % SOLIDS1
LIME/SLUDGE RATIO TOTAL PRODUCTION, DRY TONS
Inlet reached temp @
Outlet reached temp*.@
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TFIVIPFRATHRF `nl=
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
%3a
®9
v
MY
/q6'
m
�s
en
q -6D.
ao "
3
ail
Cw--,
to, 30
91 D
'Zkon
..........
TON
TIME
OPERATOR
15
INITIAL PH mow
Q.
2 HRS.
�
22 HRS.
OPERATIONAL
BELT PRESS SPEED, % 36
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, % GPM
LIME FEED AUGER, LBS/H
M'i. SPEED, %
POLYMER USAGE
TYPE USED 4F S;14 3
TANKS MIXED
1LITERS/TANK '4v4'
Rewised 8112103

TWSA LIME STABILIZATION
DAILY RECORD
DATE b
RUN TIME, HRS -
SLUDGE FEED, GAL
DRY TON
LIME FEED, LBS "I c
SLUDGE FEED % SOLIDS Y PRESS, % SOLIDS
LIME/SLUDGE RATIO s b TOTAL PRODUCTION, DRY TONS '
o
Inlet reached temp @ v
Outlet reached temp @ .
PATHOGEN REDUCTION VECTOR ATTRACTION' REDUCTION
TEMPERATURE of
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
`D
/
C
q `jbe,
1'7q
I I�
�
6D
fad
to q-,
Ck,
TIME
OPERATOR
INITIAL PH
`a e 07
2 HRS..
� yh 22 HRS..
[ -
OPERATIONAL
BELT PRESS SPEED, %� ©�D
POLYMER PUMP SPEED, % �� �( O
SLUDGE PUMP SPEED, % `, �l� GPM
LIME FEED AUGER, % S I a, LBS/HR l
SPEED, %
POLYMER USAGE
TYPE USED
TANKS MIXED
1AQ' I b 5
Revised 8112103
r
r

TWSA LIME STABILIZATION
DAILY RECORD j
DATE/ 1
START STOP TOTAL
RUNTIME, HRS . , () '�� d -oa
dd DRY TON
SLUDGE FEED, GAL
LIME FEED; LBS 1 ��� �• ls2 tJ'�
SLUDGE FEED °% SOLIDS PRESS , e% SOLIDS
LIME/SLUDGE RATIO -U TOTAL PRODUCTION, DRY TONS ° U
a
Inlet reached temp @
Outlet reached temp @ 4
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TEMPERATURE �nF
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
:°
d�
.14
lP 4
]Ve
(o'+
a.00 1.
d10-3
END OF,/vy
/
p+^
TIME OPERATOR
Ia.rd�-,a3�►
INITIAL PH i a. 497 vtn
�l .
2 HRS.
..............................
:.........................................................
:.....................................................
........................
OPERATIONAL
BELT PRESS SPEED,
POLYMER PUMP SPEED, % 30,
j SLUD. GE PUMP SPEED, % � a GPM 1�0, 35
'LIME FEED AUGER, % I Gd LBS/HR I Q
( MI, ;'z SPEED, % t)d
Revised 8112103
f
POLYMER USAGE
TYPE USED . 0 (o�&4 '
TANKS MIXED
LITERS/TANK
,57- -Z I b,5

TWSA LIME STABILIZATION
DAILY RECORD
DATE.
START STOP TOTAL
3E.
RUN TIME, HRS /0(a)
R. e.
cy"
DRY TON
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDS Lo q PRESS, . % SOLIDSF
LIME/SLUDGE RATIO
TOTAL PRODUCTION, DRY TONS
IDSInlet reached temp @
Outlet reached temp.@D
'PATHOGEN. REDUCTION VECTOR ATTRACTION REDUCTION
TF=UPI=PATI IPF=
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
ML-
5:,20
116
f"
0,0
-i"
1 jo,
TIME 159 OPERATOR
INITIAL Pl-i�l�
-2 Hks,. fvkn
as - f\ I Ao Z-3 4 5'
Id,
22 HRS..
................................................................................................................................................................
............. .................... ........
m 0
OPERATIONAL POLYMER USAGE
BELT PRESS SPEED, % TYPE USED �QCdv5jLi
POLYMER PUMP' SPEED, % TANKS MIXED
• SLUDGE PUMP SPEED, % 0 GP
'LIME FEED AUGER; LBS/HR ILITE R [TAN K

TWSA LIME STABILIZATION'_
DAILY RECORD
DATE
START 1111111. STOP TOTAL
RUN TIME, HRS ca�
�-7 DRY TON
SLUDGE FEED, GAL ` [ 117
LIME FEED, LBS
SLUDGE FEED % SOLIDS PRESS % SOLIDS p
LIME/SLUDGE RATIO EEIV= TOTAL PRODUCTION, DRY TONs
Inlet reached temp @ ®(�
Outlet reached temp
PATHOGEN REDUCTION.-
TEMPERATURE of VECTOR ATTRACTION REDUCTION
-INTO OUT. OF i... =J : -�► O ':3
TIME VESSEL VESSEL OPERATOR
TIME 5 % 'G 6 � OPERATOR
`INITIAL PH
%q /e& ,. tam- (aas-as)x.o3
qD ZHRS. ®.� ..
3 _�ao43-4aS�- l.© 9,03
i AL-f 22 HRS.
4qi.4
1f6 (9�
rv,
.............................
OPERATIONAL
/ POLYff
MER USAGE
MELT PRESS SPEED, % �(b .
PE USED C�
HOLYMER PUMP SPEED, % B`p
LUDGE PUMP SPEED, % 6
ANKS MIXED I
(S �� GPM ." ,
-ME FEED AUGER, % bt`� LBS/HR O $- LITERS/TANK
.
..I: ,ti SPEED, %
' ised SM2103

TWSA LIME STABILIZATION
DAILY RECORD
DATE
START STOPTOTAL
RUN TIME, HRS T-7
;a,v
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED °% SOLIDS
LIME/SLUDGE RATIO
Inlet reached temp @
c
Outlet reached temp @ `-
PATHOGEN REDUCTION
TEMPERATURE 'oF
INTO. I OUT OF
N
PRESS , _�% SOLIDS
TOTAL PRODUCTION, DRY TONS
VECTOR ATTRACTION REDUCTION
TIME OPERATOR
'A AG-0,T Al) x, 03,
3Q INITIAL PH
`I 30 2 HRS. :
22 HRS.
OPERATIONAL
'BELT PRESS SPEED', %- �' �7
POLYMER PUMP SPEED, % -3 D
SLUDGE PUMP SPEED, % (i GPM , -"-Z
LIME FEED AUGER, %_ ® LBS/HR f�
mi, ;SPEED, %
- vised 8/12103
TYPE USED0 Z
TANKS.MIXED

J.
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
TWSA LIME STABILIZATION
DAILY RECORD
DATE #
51AKI STOP TOTAL
F-ge -0
SLUDGE FEED % SOLIDS PRESS, % SOLIDSI
LIME/SLUDGE RATIO TOTAL PRODUCTION, DRY TONS
Inlet reached temp Q
Outlet reached temp @ q Q'U d�
PATHOGEN REDUCTION VECTOR ATTRACTI
ON REDUCTION
TEMPERATURE 'nF
TIME
INTO
VESSEL
OUT OF
VESSEL
,
OPERATOR
91
a03
is?
����
19 a--
g
e .),
5: rg-
q(S
..........................................................................................
OPERATIONAL
BELT PRESS SPEED, % q'o
POLYMER. PUMP SPEED, 4D
SLUDGE, PUMP. SPEED, % GP
LIME FEED AUGER, % LBS/HR
MI, SPEED, %
levised 8112J03
TON
TIME
OPERATOR
o INITIAL PH. 12-53
cag--AIA-2 A �.63
2 HRS.
.6 WL
22 HRS. 12.4
POLYMER USAGE
YPE USED
ANKS MIXED
1LITERS/TANK
I 19Z)

At te �-
olu's.
TWSA LIME STABILIZATION
DAILY. RECORD
DATE - d
START STOP TOTAL
RUN TIME, HRS 0-0 4m, per+ 13 firs
n DRY TON
SLUDGE FEED, GAL 5 f , L
LIME FEED'$ LBS O
SLUDGE FEED 64 SOLIDS PRESS ; °% SOLIDS
LIME/SLUDGE RATIO TOTAL PRODUCTION, DRY TONS
Inlet reached temp @
Outlet reached temp @ .14
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TEMPERATURE of
TIME
INTO . .
VESSEL
'OUT OF'
VESSEL
OPERATOR
, �
118
5
S
Ig8
l9
&n
TIME
5...2.SX.03 =.07SSOPERATOR
X-,.30
INITIALPH'
33.
2 HRS. VIZ. so* C Y,..
03
(.3 •
22 HRS. .
;s gooa� q. .,.-....,....................:..............................................................................................................................................:.........
O!��TIONAL .
BELT PRESS SPEED,
POLYMER PUMP SPEED, t>
SLUDGE PUMP SPEED, %% GPM . 7 o3
LIME FEED AUGER, % b LBS/HR q 1
MI SPEED. % 0
Revised 8/12J03
TYPE USEDR�t
TANKS MIXED JW
LITERS/TANK

TWSA RES'RUAL
MONTHLY OPERA N TOTALS
2007
SLUDGE
FEED
LIME FEED
Pol mer
Usage
Press
Run Time
Slud a Hauled
to Landfill
DATE
% Solids
Gallons
Dry
Ton
Ibs
D Ton
$/Da
Ibs
$/Da
hrs
$/da
Wet Ton
Tipping Fee
PMa
1
1.8
37,928
2.84
9536
4.77
$560.34
76.1
$114.15
10.0
$180.00
2
1.4
35,710
2.08
6278
3.14
$368.90
57.1
$85.65
10.0
$180.00
3
4
5
6
7
1.3
43,322
2.35
9043
4.52
$531.37
57.1
$85.65
10.7
$192.60
8
1.5
34,895
2.18
8233
4.12
$483.77
76.1
$114.15
10.6
$190.80
9
1.3
31,275
1.69
4990
2.50
$293.21
57.1
$85.65
7.0
$126.00
10
11
12
13
14
1.2
54,030
2.70
9641
4.82
$566.51
76.1
$114.15
11.0
$198.00
15
1.5
35,436
2.21
10192
5.10
$598.88
57.1
$85.65
9.8
$176.40
16
17
18
19
20
21
22
1.7
38,769
2.75
7300
3.65
$428.95
38.0
$57.00
9.2
$165.60
23
24
25
26
27
28
29
1.1
38,769
1.78
8199
4.10
$481.77
57.1
$85.65
9.3
$167.40
30
1.5
30,528
1.91
7125
3.56
$418.67
57.1
$85.65
8.0
$144.00
31
daily
av
1.4
38,066
2.25
8,054
4
473
60.9
$91.34
9.6
$172.08
monthly
total
380,662
22.50
80537.0
40.27
$4,732.35
608.9
$913.35
95.6
$1720.80
0.00
$0.00
# of days press was run 10
# of days lime was added 10
? loads hauled to landfill @ $450/load= $0.00
Total -Residual Cost for the month = $7,366.50

e�-o irnLQ--
TWSA LIME STABILIZATION
DAILY RECORD
DATE ,:5- "
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED °% SOLIDS c
LIMEISLUDGE RATIO
Inlet reached temp @ , c�
Outlet reached temp @
PATHOGEN REDUCTION
INTO I OUT
is's
d'oo
140
A6a/gg
Co
5 ` So
doh
00
PRESS, °% SOLIDS
TOTAL PRODUCTION, DRY TONS
OPERATIONAL
BELT PRESS SPEED, % 3
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, % GPM
LIME FEED AUGER, %_ `-f LBS/HR
nAj, 2 SPEED, % UD
TO
TO
VECTOR ATTRACTION REDUCTION
TIME ,��°®3-e�)r�
iaa 3:7 ,bi OPERATOR
`< _ ' INITIAL PH
pr� 22 2 HRi S,_12 3
Ay
22 HRS.
YPE USED -' I
ANKS MIXED
_ITERS/TANK
&, 1
wised 8112103

RUN TIME, HRS-
SLUDGE FEED, GAL
LIME FEED; LBS
TWSA LIME STABILIZATION
DAILY RECORD
DATE
�1HKI STOP TOTAL
L�W- o o
SLUDGE FEED % SOLIDS c+ PRESS , °% SOLIDS
LIME/SLUDGE RATIO TOTAL PRODUCTION, DRY TONS
Inlet reached temp @ .
Outlet reached temp @
PATHOGEN REDUCTION
TEMPERATURE :oF
VECTOR.ATTRACTI.ON REDUCTION
TIME'
INTO..
VESSEL•
OUT -OF•
VESSEL
OPERATOR
TIME .6PERAI"OR
{vJ
` 4 INITIAL PH
_
fNa
• 2 HRS.
4
.f
1 rig
d 22 HRS. ^ .�+4 �
................................................................................................................................
OPERATIONAL
BELT PRESS SPEED, % r?�
POLYMER PUMP .SPEED,
SLUDGE PUMP SPEED, GPM
% �.
_
z_d_3
LIME FEED AUGER, %_ SC LBS/HR
mi. ._,�.SPEED, % rG%V
evised 8112103
POLYMER USAGE
TYPE USED
TANKS MIXED
LITERS/TANK

l�lr Ilp ,
I TWSA LIME STABILIZATION
DAILY RECORD
DATE "'7,ID
START STOP,
TOTAL
RUN TIME, HRS
S.,
fZ a S
SLUDGE FEED, GAL
Q'� a.a
DRY TON
.
LIME FEED, LBS
r'
�1
Q 3 .
SLUDGE FEED °%SOLIDS PRESS, % SOLIDS
LIME/SLUDGE RATIO
" , TOTAL PRODUCTION, DRY TONS
~ . ,
Inlet rgached temp @
Outlet reached temp
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TEMPERATURE of `
INTO
OUT OF.--
a$ aI. S= 3:5*k 03 0105
TIME .,.
VESSEL
VESSEL•
OPERATOR
, TIME
L.-5 -, dS OPERATOR
-� 0
INITIAL PH. Aa,LA 3; F-Yy'1
a. AD,
: pi''.
2 HRS. la.5s-.Los
,a. ��
1. -r7
�
22 HRS.
v
•
...:.................................................. ................................... ..................... _.................. :............... ................ ................................
OPERATIONAL
.:..:..._:..................... ....... ................. .......................
POLYMER USAGE
2.
BELT PRESS SPEED, % J
TYPE USED" 1�clgs 711 '
POLYMER PUMP SPEED, %O
TANKS MIXED
._... JGE PUMP SPEED, % GPM
LIME FEED AUGER; %a LBS/HR (
LITERS/TANK
MIXER SPEED, % V.
7p �► S

1
TWSA LIME STABILIZATION
DAILY RECORD'
-DATEl
START_ STOP. TOTAL
RUN TIME, HRS
DRY TON
SLUDGE FEED, GAL
q
q. t .
LIME FEED, LBS
SLUDGE FEED °%SOLIDS
'PRESS , °h SOLIDS
LIME/SLUDGE RATIO
TOTAL PRODUCTION, DRY TONS
Inlet reached temp @
Outlet: temp`@
„
reached.
PATHOGEN REDUCTION VECTOR ATTRACTION. REDUCTION a
I . TEMPERATURE of . v?:A, 9l & o;
TIME
INTO
I VESSEL
.OUT OF
VESSEL
OPERATOR
TIME �� `� .�: E� OPERATOR
h
y INITIAL PH' ... _ia b _�
HRS.ly
zmt
6
12,`E3..o33
3. 30 22 HRS.: la", 39 • ��M
010 0
L: 9. q,
OPERATIONAL. POLYMER.USAGE
BELT PRESS SPEED,
?
% J� 7�S
TYPE USED /4 o f %&
POLYMER PUMP.SPEED, % /0
TANKS MIXED
1 bGE PUMP SPEED,
%o 35 5 - GPM
LIME FEED AUGER; %° !O LBS/HR
LITERS/TANK
MIXERSPEED, %

TWSA LIME STABILIZATION
DAILY RECORD ,.
DATE
START
.-STOR
TOTAL
RUN TIME, HRS
a
(1
�• c
DRY TON
SLUDGE FEED, GAL
.67
E`7-a
LIME FEED, LBS
SLUDGE' FEED % SOLIDS
PRESS, %SOLIDS
LIME/SLUDGE RATIO
TOTAL -PRODUCTION,
DRY TONS f �/
Inlet peached temp
.
Outlet reached; temp @
PATHOGEN REDUCTION
VECTOR ATTRACTION REDUCTION
'TEMPERATURE of .
TIME
:INTO
VESSEL
OUT OF
VESSEL
OPERATOR
TIME"
.
a.4 5. oayOPERATOR
INITIALPH:: vv`
6
aS_ 23.1t 13 ,03,;033
12r3$ 'o33
11 11%
LA
3 I- 6,
[.(o3
L jq, 1:
' S l
22 HRS.:. a, o
6 0.
a�OyPERATIONAL !6
BELT PRESS SPEED, % X5
POLYMER PUMP SPEED, % )A D
SGE PUMP SPEED, % l!3' GPM q a
LIME FEED AUGER, %° LBS/HR 3 3
MIXER SPEED, % �O 1

STAR
RUN TIME; HRS
SLUDGE FEED, GAL-
TWSA.LiME.STABILIZATION
DAILY RECORD
DATE. =C
F -STOP, TOTAL
1Tdo
DRY TON
7E�
LIME FEED, LBS I .. - . 11. .� e ;� I
SLUDGE FEED % SOLIDS PRESS ,% LIDJ
So
LIME/SLUDGE RATIO TOTAL PRODUCTION; DRY TONS
lnl6t mached tem p'@
Outlet:reached.temp @
PATHOGEN REDUCTION. VECTOR ATTRACTION REDUCTION
TEMPERATURE oF,
TIME'
..INTO ­
VESSEL
OUT OF -
VESSEL'
OPERATOR
q,
13
a5- 24.3 0.1 X, 03 = .,021:
TIME
-OPERATOR
a 30
INITIAL PH^�1`� f"'
0, 9,� y.. 0,7=. o,oG
.4i 30.
2 HRS... LLA,
a (),5rl
t; Ail
'22HRS. '
OPERATIONAL
BELT PRESS SPEED POLYMER PUMP SPEED, % Tl
6GE PUMP SPEED, GPM
LIME FEED AUGER, LBS/HR
MIXER SPEED, '%
........ . ...... ................. .............................. .........
POLYMER USAGE-
YPE USED
ANKS MIXED

VA
RUN TIME, HRS - -
TWSA LIME STABILIZATION
DAILY RECORD
DATE.—S
START STOP TOTAL
SLUDGE FEED, GAL O 3543(
Al z-; 0
LIME FEED, LBS I o
SLUDGE FEED % SOLIDS PRESS, % SOLIDS
LIME/SLUDGE RATIO 7�. TOTAL 'P RODUCTION, DRY TONS
InlefclA reacheemp (g 019.
Outlet reached. temp @
11 9,01
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TF=UP;=PATI lPr=-rfr=
�-TIME
INTO
vESSEL:
-OUTOF-
VESSEL
-OPERATOR.
810.
0— -A
5 -.34N
loc
be -v
POLYMER USAGE
TYPE USED
TANKS MIXED
veto.
1. U-0 =0'0'3�1)
TIME 639-% OPERATOR
: INITIAL PH -m
2 HRS. 1q. 50
(_95 -23Ai I,t1J.X,o3.
CIA, -._65+=-
22 HRS.'
OPERATIONAL
BELT PRESS SPEED, "./.
POLYMER PUMP SPEED, %
DGE PUMP SPEED, % 12 -GPM_f (el
LIME FEED AUGER, %_L�114. LBS/HR-_q3
MIXER SPEED, % -In
!�7

a
TWSA LIME STABILIZATION
DAILY RECORD
DATE a ;. D .
START STOP TOTAL
RUN TIME, HRS ��� ` , • 0 d .•. ,o%C %.. , V. `
DRY TON
SLUDGE FEED, GAL
LIME FEED, LBS &5
SLUDGE FEED% SOLIDS s+ PRESS % SOLIDS
LIME/SLUDGE RATIO.. TOTAL PRODUCTION, DRY. TONS
Inlet reached temp @ I J.)a L?
Outlet reached temp
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TEMPERATURE of
.I,S--)S S— 5"ic-o3
TIME I
INTO . .
- VESSEL
OUT OF -
VESSEL
I OPERATOR
3
�a5
1. N
1.-
8 oo
\ rlaawi t Of a,5)
TIME. \ - 1 OPERATOR
` INITIAL PH 50 .
ks-OL4,8.=.0.9. Xro3 e.OQlbj
Oa, S� -. 006 a,.50)
q. ► 55 2 HRS. 4 a .50i
51 I©� Cam- d3Q5:= 1r5X:-03- ®4s)
-
4 -. 0
22 HRS.
OPERATIONAL
-66
BELT PRESS SPEED;
POLYMER PUMP SPEED,
bGE PUMP SPEED, '% GPM S
LIME FEED AUGER, % LBS/HR
POLYMER USAGE
TYPE.USED
TANKS MIXED
too,.
MIXER. SPEED, %° : �J� 1�

A?
RUN TIME, HRS
SLUDGE FEED, GAL
TWSA LIME STABILIZATION
DAILY.RECORD I
DATE n�
START STOP- OTAL 9, 3 L
c
D
LIME FEED, LBS . L ({J 1 —6 ;1 !7 1
SLUDGE FEED SO(
s a PRESS % SOLIDS
- .
LIME/SLUDGE RATIO TOTAL PRODUCTION, DRY TONS l! v
.Inlet reached temp @
Outlet reached temp @ v
PATHOGEN REDUCTION VECTOR ATTRACTION, REDUCTION
_ "TFMPFRATURF nF .. .
TIME-
INTO
VESSEL
OUT OF'-
VESSEL
OPERATOR
3" Ill
1,q3
� F
Elk
F
Too.
147
TIMEj;, �rd� '�-, p = ta,04 . OPERATOR -
INITIAL PH - (y
p� 02.)
2 HRS, _ &A
96 22 HRS.
.................. :......................................... ...................................................... ................
.............................
OPERATIONAL
BELT PRESS SPEED, %D
POLYMER PUMP SPEED, %
9
DGE PUMP SPEED, % . ® GPM
LIME FEED AUGER, % LBS/HR
MIXER SPEED, % 70

[L zi(4P
Q3'a-wk-i
SLUDGE FEED, GAL
ICJ I
Jam✓
I
I / �` C 1
I
LIME FEED, LBS
SLUDGE FEED %SOLIDS
PRESS , °k'SOLIDS
'
TOTAL PRODUCTION; DRY TONS
LIME/SLUDGE RATIO
Inlet reached temp @
Outlet reached temp @
a.
PATHOGEN. REDUCTION
VECTOR,ATTRACTION.REDUCTION
( }: TEMPERATURE.oF
TIME
INTO
VESSEL
OUT OF=
VESSEL
..
OPERATOR
3-��
5,. I4
TIME . C[a ���t ;O9(o = I�•GI�'
OPERATOR
INITIAL PH ,
40
5 r ©5 ..
t
63
ID%S .. 22 HRS.' "
........................... _................................................................ :......"........._..............._...............................................................
OPERATIONAL
BELT PRESS SPEED,
POLYMER PUMP :SPEED, % .
k. -)GE PUMP 'SPEED, % -GPM--
LIME FEED AUGER, % LBS/HR
MIXER SPEED, '% "
TYPE USED 4 6'/&
TANKS MIXED
LITERS/TANK N

TWSA RESID-JAL
MONTHLY OPERA ')\I TOTALS
June 2007
LIME FEED
Pol mer Usa a
Press Run Time Slud a Hauled o Lancitill
SLUDGE FEED
DATE % Solids Gallons D
Ton
Ibs D Ton
$/Da
Ibs
$/Da
hrs $/da Wet Ton Ti
ing Fee
1
2
3
4
5 2 51,952
4.33
0
$0.00
76.1
$114.15
12.0 $216.00
6 1.9 37,000
2.93
0
$0.00
38.0
$57.00
6.0 $108.00
7
25.55
$788.24
8
9
10
11
12
13
14
15
16
17
18
19 1.6 41,645
2.78
0
$0.00
95.1
$142.65
10.5 $189.00
20
27.26
$841.16
21
22
23
24
25 2.3 31,929
3.06
5960 2.98
$350.21
76.1
$114.15
8.0 $144.00
26
27
28
29
30
31
2
3.27
1490 2.98
9
91 $164.25daily
ail 2.0
monthly
total 162 526
13.09
5960.0 2.98
$350.21
285.3
$427.95
36.5 $657.00 52.81
$1 629.
2 loads hauled to landfill @ $450/load=
$900.00
# of days press was run
4
Total Residual Cost for the month =
$3,964.56
# of days lime was added
1

i
TWSA LIME STABILIZATION
DAILY RECORD
DATE .
START ...
STOP:. TOTAL
RUN TIME; HRS
3-6
DRY TON
SLUDGE"FEED GAL.
u
.LIME FEED, LBS
SLUDGE FEED % SOLIDS"
e.
PRESS, % SOLIDS `
LIME/SLUDGE RATIO
------------
TOTAL'PRODUCTION, DRY TONS
Inlet reached temp @:
Outlet reached temp @
PATHOGEN REDUCTION
VECTOR ATTRACTIMI R;=ni Ir_Tlnni
OPERATIONAL
BELT PRESS SPEED,
POLYMER PUMP SPEED, %.
��b,GE PUMP SPEED, % " "-GPM
LIME FEED AUGER, % L'BS/HR
POLYMER USAGE
TYPE USED VI
TANKS MIXED -
LITERSITANK
MIXER SPEED, %J00 5

TWSA LIME STABILIZATION
DAILY RECORD
DATE
START STOP TOTAL
RUN TIME, HRS-
go
DRY
SLUDGE FEED, GAL
0
CD
LIME FEED, LBS
SLUDGE FEED % SOLIDS
c
PRESS. % SOLIDS
LIME/SLUDGE RATIO
TOTAL PRODUCTION, DRY TONS
Inlet reached temp@
Outlet reached temp @
PATHOGEN
REDUCTION
VECTOR ATTRACTION REDUCTION
TEMPERATURE of
.ME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
TIME
INITIAL PH
2 HRS.
22 HRS.
...................... .................................................................................................................................................. :.....................
OPERATIONAL
BELT PRESS SPEED, %�
POLYMER PUMP SPEED, % l b
SLUDGE PUMP SPEED, % GPM
UmE FEED AUGER, % LBS/HR
MIXER SPEED, %° 1
Revised 8112103
TON
OPERATOR
POLYMER USAGE
TYPE USED
TANKS MIXED
ILITERS/TANK �,� -1.
T5-,� I�-)5

TWSA LIME STABILIZATION.
DAILY RECORD
DATE �7
START STOP' TC)TAI
RUN TIME, HRS I 11, 60
DRY TON
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDS PRESS, % SOLIDSI
LIME/SLUDGE RATIO TOTAL PRODUCTION DRY TONS
Inlet reached temp @
C—
Outlet reached temp @ N
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TFIVIPFRATI IPF= nP
TIME
INTO
VESSEL
OUT OF
VESSE
OPERATOR
) -)
-L
y
q_3
7
TIME �PERATOR
C 19v I-. 136"=- Q, (4ys-
INITIAL PH
t9, -7 -, 141 = 12, S59
19 2HRS.
13 iroo 3 =, 0 q
31(qq 22 HRS.
........................ ............................................................................ .............................................
...........................
OPERATIONAL
' ELT PRESS SPEED % 0 %
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, % GPM'
I.IftAF FEED AUGER, LBS/HR'
MIXER SPEED, % D6Ap
evised 8/12/03
POLYMER USAGE
TYPE USED, Z�S7&1014( F11b)
TANKS MIXED-.11 It

ti
July 2007'
TW,�A ktSlbuAL
MONTHLY OPERP. N TOTALS
'• .•-
•e -• e •
�■�®tee
®��®�■��—
# of days press was run 7
# of days lime was added 5
Total dry ton of sludge ? loads hauled to landfill @ $450/load
treated with lime
this month 10.9 Total Residual Cost for the month -$5,366.01

TWSA LIME STABILIZATION
DAILY RECORD
DATE
START STOP TOTAI
RUN TIME, HRS 1 I 0 k f5
DRY TON
SLUDGE FEED, GAL
LIME FEED, LBS
(�
SLUDGE FEED % SOLIDS
< ✓
LIME/SLUDGE RATIO
- z 2z,
Inlet reached temp @
o�
Outlet reached temp
PATHOGEN REDUCTION,
TFMPFRATI IRF nF
AME
INTO
VESSEL
OUT OF
VESSEL..
OPERATOR
%J
6.
CAD
e'
TO
cap
r
v
5
ac9�2
1 ° 7
64-1
,PRESS, %.SOLIDS
TOTAL PRODUCTION, DRY TONS o
VECTOR.ATTRACTION REDUCTION
TIME CAS-aF�$�3e�;r<a3-�O9uo/OPERATOR
(l0,q(^; o9lo=
e INITIAL PH : 11-3
C5(5-X. 'to3AY.63.=, W)
s0 2 HRS.
3 s 22 HRS.. L
OPERATIONAL
BELT PRESS SPEEDf, % t, o
POLYMER PUMP SPEED, % 2
SLUDGE PUMP SPEED, % 3 GPM 61, 03
L'im m FEED AUGER, % O- LBS/HR .
MIXER SPEED, % I_O
POLYMER USAGE
TYPE USED Lft
TANKS MIXED
quo c 11o'-s
Revised 8l12/03

•�ME,
INTO :.
VESSEL
OUT OF
VESSEL
OPERATOR
(20
cN©
TIME . CaS(Ja�= �{,Sx,O3 • ►3s�. OPERATOR
a.J s
6 INITIAL PH' ,
2 HRS.,.
22 HRS.
OPERATIONAL
BELT PRESS SPEED, % v
POLYMER PUMP SPEED, %. J°
SLUDGE PUMP SPEED; %. � � GPM
b } 5e LBS/HR :
Lh.,c FEED AUGER, .% L-5 '

TWSA LIME STABILIZATION
DAILY RECORD
DATE
START STOP TOTAL
RUN TIME, HRS '7roo
DRY
SLUDGE FEED, GAL.
LIME FEED, LBS I 1 -3 IWO, 1 -5- 6 j I
, I
SLUDGE FEED % SOLIDS PRESSWSOLIDS
LIMEJSLUDGE RATIO' TOTAL PRODUCTION, DRY TONS •
Inlet reached temp @
Outlet reached temp @
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
7P:KAPF=PAT1 10= -=
JME
INTO
VESSEL.
OUT OF
VESSEL
OPERATOR
0-0
.P
A/
3 14
zoo-
7e? Iq
a06
go q
G.-I
- C-wv
q1t I q
-.
TIME 0-7 T- 12.�t19 OPERATOR
50: INITIAL PH
(12'.77 I'L.16 I>
2 HRS. 'L, 7..
22 HRS. 9'9—!3
............. ................................... ........................................... ..............................
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED,
SLUDGE "PUMP SPEED, %
GPM
bmci FEED AUGER, % SO q&- -LBS/H
MIXER SPEED, %,_. 60
POLYMER USAGE
TYPE USE D
TANKS MIXED
41
Revised 8112103

TWSA LIME STABILIZATION
DAILY RECORD �.
DATE ` hip— �3 4 /-®
START STOP TOTAL
RUN TIME, HRS
DRY TON
SLUDGE FEED, GAL
LIME FEED, LBS
-------------
SLUDGE FEED % SOLIDS PRESS , %.SOLIDS
LIMEISLUDGE RATIO 1 TOTAL PRODUCTION, DRY TONS
Inlet reached_,temp @ Z
Outlet reached temp @
W
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TFMPFRATI IRF nF
`
l �ME
1NT`O
VESSEL
OUT OF
VESSEL
OPERATOR
e3
c
k
(20
EAd
ao
U
TIME Z,$'-�ZO.�-�=� 7C �b3 = V i55 OPERATOR
9v'L9S-= a i35 = .t't 1*57
�9-79.ip tl INZ.,
INITIAL PH �
2 HRS. 12. 2. t
S - 2I.S._ 3.sx .e3 - a I oS
.
S 7 22 HRS.2. 1
.............. .............................................................................................. .................... :.......................... ........................
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, %
SLUDGE PUMP'SPEED, % 40 GPM
- 2
L _if FEED•AUGER, %_� LBS/HR J
.MIXER SPEED, % ` U
Revised 8/12103.
POLYMER USAGE
4O TYPE USED 446 V4166
TANKS MIXED
4-
q- I.-
1��.

TWSA LIME STABILIZATION
DAILY RECORD
.DATE b�
STOP
RUN TIME, HRS
DRY TON
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDS
LIME/SLUDGE RATIO �
Inlet reached temp @
Outlet reached temp @
PATHOGEN REDUCTION
TFMPF:PATI IRF: nF %
)ME.
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
,ps8
c), o 9
1q.5
xrfi
A60
oil
ACA
JOS-
E an,
PRESS, WSOLIDSI —1
TOTAL PRODUCTION, DRY TONS
VECTOR ATTRACTION REDUCTION
TIME IME
ilmq� OPERATOR
INITIAL PH-Q, 5
11.7 r -4
2 HRS. 1g,
22 HRS. 10'1'q
............ kq--10--r7 ........... ................................................................
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED,% GPM
1
Li,.,--') FEED AUGER. % LBS/HR
MIXER SPEED, % (00".
I POLYMER USAGE----]
YPE USED4a6#jk4i
ANKS MIXED
TERS/TAN
Revised 8/12/03

TWSA LIME STABILIZATION
DAILY RECORD
DATE
START STOP TOTAL
RUN TIME, HRS 01.0c)—
SLUDGE FEED, GAL
LIME FEED, LBS
I'SLUDGE FEED% SOLIDS PRE -SS., %.SOLIDS
LIME/SLUDGE RATIO TOTAL PRODUCTION, DRY TONS
Inlet reached temp @ ffi
Outlet reached temp @
PATHOGEN 'REDUCTION VECTOR ATTRACTION REDUCTION
TEMPLKA I IJKt Ot-
INTO OUT OF
)ME VESSEL VESSEL OPERATOR
............................. .......................................................................... .............................................................
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, % 4 5
SLUDGE PUMP SPEED, % 4.5. GPM
FEED AUGER, % LBS/H,R
MIXER SPEED, %
Revised 8/12103
POLYMER USAGE
'TYPE USED
TA . NKS MIXED'H
[LITERS/TANK

��0
TWSA LIME STABILIZATION
DAILY RECORD
� DATE
START
RUN TIME, HRS
DRY TON
SLUDGE FEED, GAL
LIME FEED, LBS .
SLUDGE FEED % SOLIDS PRESS, %.SOLIDS
LIME/SLUDGE RATIO TOTAL PRODUCTION, DRY TONS C� 1
Inlet reached temp @
Outlet reached temp @
PATHOGEN REDUCTION
TEMPERATURE of
1ME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
VECTOR ATTRACTION REDUCTION
TIME OPERATOR
INITIAL PH
2 HRS.
22 HRS.
OPERATIONAL
BELT PRESS SPEED, % . d�®
POLYMER PUMP SPEED, % 46 %
SLUDGE PUMP SPEED, %J �/� GPM 63
I �
Lip c FEED AUGER, % LBS/HR ✓U
MIXER SPEED, % l06
POLYMER USAGE
TYPE USED�Ca'�
TANKS MIXED I
TERSFF
Revised 8/12103

..7
TW5-A RE5ID-YAL.
MONTHLY OPERA N TOTALS
August 2007
•
# of days press was run 5 Total dry ton of sludge L�� �d to landfill @ $450/load= $900.00
treated with lime ,- ��� �'Gpe 1
# of days lime was added 2 this month _ �� � ko.1jW �- ,dual Cost for the month = $5,168.13

RUN TIME, HRS
TWSA LIME' STABILIZATION
DAILY RECORD
DATE'
START STOP TOTAL
DRY
.SLUDGE FEED,. GAL
I
r:!)1911U
LIME FEED, LBS'
SLUDGE FEED % SOLIDS
PRESS, WSOLIDSI
LIME/SLUDGE RATIO
TOTAL PRODUCTION,
PTION, DRY TONS
=7
Inlet reached tbmp,@
'Ji .
Outlet reached temp @
30 4,
PATHOGEN REDUCTION.
VECTOR ATTRACTION. REDUCTION
TEMPERATURE oF
INTO,
VESSEL
OUT OF
VESSEL*
OPERATOR -
ID: 30,./g
io,z.
o26s
0
Ai
jqq
6'm
TIME
-K, (3 3 =. .117
J 1-7 r 1:2 i283
OPERATOR
INITIAL -PH
13S
75,
0ta,
0 6 03
Igo
22 1_2,3.q
.............................. ............................................. I ................. ............. ............. ............ .......
OPERATIONAL
BELT PRESS SPEED,
POLYMER PUMP SPEED,
SLUDGE PUMP SPEED, % GPM
�FEED 'AUGER,% L5S/HR--
V_
MIXER SPEED, %
Revised 8/12103
POLYMER USAGE
TYPE 'USED :
TANKS MIXED
ILITERSITANK

RUN TIME, HRS
DRY TON
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDS
PRESS %,SOLIDSI'
I
LIME/SLUDGE RATIO
TOTAL PRODUCTION, DRY TOM
Inlet reached temp @
Outlet reached temp
PATHOGEN REDUCTION
VECTOR ATTRACTION REDUCTION
TEMPERATURE-oF
)ME
INTO
VESSEL'
OUT OF
VESSEL
OPERATOR
G
lsqs�
A
31
o107
M
go 4o
Uo
0,3 d7j.
TIME
tot - OPERATOR
INITIAL PH
95 ZIA,
r)
2 HRs-, --
96 -,263 = 4.7 K, 03=-,)ql
1 -4 1 t.2. L4 61
22 HRS.
. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. . ..
. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . ... . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . ... . . . . . . . . . . . . .
OPERATIONAL POLYMER USAGE,
.BELT PRESS SPEED, OX 350/6 TYPE USED
POLYMER PUMP SPEED, oo 14016-. TANKS MIXED
qq
SLUDGE PUMP SPEED, %- 00% GPM . 3)
LI.-I:,FEED AUGER, %-qLBS/HR
S LITERS/TANK

C OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED,
SLUDGE PUMP SPEED, % J jJ GPM �� • 0
Lk... FEED AUGER, %., LBS/HR

31
TWSA LIME STABILIZATION
DAILY RECORD
DATE
START
RUN TIME, HRS
TOTAL
DRY TON
SLUDGE FEED, GAL
a
nl
LIME FEED, LBS
SLUDGE FEED % SOLIDS
/
PRESS, %.SOLIDS
LIME/SLUDGE RATIO
TOTAL PRODUCTION, DRY TONS
•�
Inlet reached temp @
Outlet reached temp @
PATHOGEN REDUCTION
TEMPERATURE of
)ME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
VECTOR ATTRACTION REDUCTION
TIME OPERATOR
INITIAL PH
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, % GPM �/� . I
L. J FEED AUGER, % IV !/'[ LBS/HR
MIXER SPEED, % 100
2 HRS.
22 HRS.
POLYMER USAGE
TYPE USED 14'R 4-4
TANKS MIXED
Revised 8112/03

TWoA Rr-SlrjuAL
MONTHLY OPERf �)N TOTALS
September 2007
��M
• ' @
# of days press was run 6 Total dry ton of sludge
treated with lime this month
# of days lime was added 2 this month
1 loads hauled to landfill @ $450/load= $450.00
4.5 Total Residual Cost for the month = $3,916.05

If
RUN TIME, HRS
SLUDGE FEED, GAL
TWSA LIME STABILIZATION
DAILY RECORD
DATE.
START STOP TOTAL
DRY
LIME FEED, LBS
SLUDGE FEED % SOLIDS o / PRESS , °,;SOLIDS
F7.
LIME/SLUDGE RATIO / TOTAL PRODUCTION, DRY TONS n
Inlet reached temp @ y
-Outlet reached temp @. '
PATHOGEN REDUCTION VECTOR ATTRA_ CTION REDUCTION .
TEMPERATURE of
TIME.
INTO
VESSEL
OUT OF.,
VESSEL
OPERATOR
C
3; �I
188
Z03
7,11,
alo
10rf
�rn
END
TIME
�5• ��•4= •x •os= •7.0
OPERATOR
3�.
INITIAL PH
w1
r2.b`- ..1!77= i,2.SV3
% 30'
2 HRS. • .
7 - 07
22.HRS.
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, %' [/ D
l (DGE PUMP SPEED, % T D �D GPM
LIME FEED AUGER, % .5D /D LBS/HR
MIXER SPEED, % D
POLYMER -USAGE
TYPE USED
TANKS MIXED
7hd�Ibs
Revised 8112103

TWSA LIME STABILIZATION
DAILY RECORD I %.
DATE.
START STOP TOTAL
RUN TIME, HRS �' ; tin
DRY TON
SLUDGE FEED, GAL ,
LIME FEED, LBS
SLUDGE FEED °% SOLIDS 1,9 PRESS, °%,:SOLIDS .
4
-LIME/SLUDGE RATIO 4 TOTAL PRODUCTION, DRY TONS . .
Inlet reached temp @ =
,Outlet reached temp @
PATHOGEN REDUCTION ,VECTOR ATTRACTION REDUCTION
TEMPERATURE of
..TIME-
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
fN
ao
0,60
eoo
0: oa
'7�0a
181
963
"fm
TIME. 15 al.� = 3,y X.o3=',IOa. -OPERATOR
ia,Ss-.:loz � ra,�yg
66.. INITIAL PHA{
.2 HRS.
22 HRS.
OPERATIONAL
BELT PRESS SPEED, % yo /D
POLYMER PUMP SPEED, % JS
S'L .GE PUMP SPEED, % S /0 GPM 3
LIME FEED AUGER, %° LBS/HR I O
MIXER SPEED, % f!
Revised 8112/03 ..
POLYMER USAGE
TYPE USED �R64 1 D
TANKS MIXED

OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, % D
SLUDGE PUMP SPEED, % D GPM _
LIME FEED AUGER, % LBS/HR

TWSA LIME STABILIZATION
DAILY.'REECORp
DATE r 1 l all
gSTART'. STOP TOTAL
RUN TIME, HRS fJ' d S (p.1w I1(s
DRY TON
SLUDGE FEED, .GAL - 9A 18(0 I•
LIME FEED, LBS
SLUDGE FEED % SOLIDS �' � PRESS %:;SOLIDS
LIME/SLUDGE RATIO' TOTAL PRODUCTION, DRY TONS /
Inletreached temp
.Outlet reached temp @
PATHOGEN REDUCTION VECTORATTRACTION REDUCTION
TFMPFRATI IRF nF
e. OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, % yD D
SLUDGE PUMP SPEED., % ' � S !a ` GPM S�
LIME FEED AUGER, % LBS/HR
MrXER SPEED, %
Revised 8/12103 -
POLYMER USAGE
TYPE USED
TANKS MIXED
LITERS/TANK' V

UrtKA i IUNAL, POLYMER'USAGE
BELT PRESS SPEED,- % "t
TYPE -USED..'
POLYMER PUMP SPEED, % TANKS MIXED
f
)DGE PUMP SPEED, % GPM �D �` J
LIME FEED AUGER, % LBS/HR LITERS/TANK`
MIXER SPEED,
:Revised8112103 - -

TWSA KESPIYAL
MONTHLY OPERA` N TOTALS
Ortnher 2nn7
OEM
fflONFRE M.
Imo=
®®
®■��—®����
# of days press was run 7
# of days lime was added 0
Total dry ton of sludge
treated with lime this month
this month 0.0
4 loads hauled to landfill @ $450/load= $1,800.00
Total Residual Cost for the month = $6,818.34

TWSA LIME STABILIZATION
DAILY RECORD
DATE __Ld // b 0
START/ STOP TOTAL
RUN TIME, HRS c Oil �p ; ate I krs
DRY
SLUDGE FEED, GAL qt), 100
LIME FEED, LBS
SLUDGE FEED % SOLIDS PRESS, WSOLIDS
LIME/SLUDGE RATIO TOTAL PRODUCTION, DRY TONS
Inlet reached tem.p.@
Outlet reached temp @
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION -
22 HRS.
OPERATIONAL
BELT PRESS SPEED, % C /D
POLYMER PUMP SPEED, %
!�-' JJDGE PUMP SPEED, % ' !I GPM
I
LIME FEED AUGER, % LBS/HR
MIXER SPEED, % ob
.Revised 8/12/03
POLYMER USAGE
TYPE USEDLD��
TANKS MIXED
ILITERS/TAN'K ij 0
� 33 Ib�

OPERATIONAL .
BELT PRESS SPEED, %
POLYMER PUMP SPEED, % SRO /D
P"JDGE. PUWSPEED, % 3O <D GPM. 55,53
LIME FEED AUGER,.%° �� LBS/HR
MIXER SPEED,. % VLZ
.Revised 8/i=3 - - -

START,.
..STOP TOTAL
RUN TIME, HRS.
_ I n� 00
+ -
DRY TON
SLUDGE FEED, GAL
1.
LIME FEED, LBS
SLUDGE FEED % SOLIDS
PRESS ,"0,6,$OLIDS
LIME/SLUDGE RATIO
TOTAL PRODUCTION, DRY TONS .
-------------------
Inlet reached temp,@
-Outlet reached temp @.
PATHOGEN REDUCTION
VECTOR 'ATTRACTION REDUCTION
OPERATIONAL POLYMER USAGE
BELT PRESS SPEED, % l 0 TYPE USED 31100
POLYMER PUMP SPEED, % 0, /0 TANKS=MIXED
F' �.IDGEPUMP SPEED, % I Ja�d GPM.
l
LIME FEED AUGER, % IV (- � LBS/HR LITERS/TANK
MIXER SPEED, % (� L (o s
.Revised 8/ 12/03 - - -

START STOPTOTAL
RUN TIME, HRS (7: on
SLUDGE FEED, GAL DRY
LIME FEED, LBS
SLUDGE FEED % SOLIDS PRESS, WSOLIDS[����
LIME/SLUDGE RATIO" TOTAL?RODUCTI'
ON, DRY TONS
inlet reached ternp @
-Outlet -reached temp @
PATHOGEN REDUCTION
VECTOR ATTRACTION REDUCTION -
TEMPERATURE OF..
INTO OUT OF.
TIME VESSEL VESSEL . _OPERATOR TIME OPERATOR
0
INITIAL PH
2 HRS.
22, HRS.
.......................................................................... : ..............
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, %
P'IJDGE PUMP SPEED, % GPM
LIME FEED AUGER, % LBS/HR
MIXER SPEED, %
,Revised 8/12/03
POLYM.,E�Z USAGE
TYPE USED
TANKS MIXED
LITERS/TANK

.............. ........................... ...................................................... ........................................... ............................... .......... ..................................... ..... ..... ............ . ....
OPERATIONAL POLYMER 'USAGE
BELT PRESS SPEED, % .4b
TYPE USED -C5?1�(
POLYMER PUMP SPEED, % -M IXE TANKS Da,
S' lJDGE PUMP SPEED, % GPM.,
`LIM'E'FEED AUGER, % LBS/HR. ILITERS/TANK
MIXER SPEED, % 5
Revised.8112/03

TWSA LIME STABILIZATION
DAILY RECORD
DATE 6 Z7.
START STOP TOTAL
RUN TIME, HRS
• DRY T(
SLUDGE FEED, GAL ,j
LIME FEED, LBS
SLUDGE FEED % SOLIDS PRESS , %..SOLIDS
LIME/SLUDGE RATIO TOTAL PRODUCTION, DRY TONS
Inlet reached tetn,p @
Outlet reached temp ig
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
I CMt t:KA I UKC OI- .
INTO OUT OF -
(ESSEL' VESSEL
TIME OPERATOR
OPERATIONAL POLYMER USAGE
BELT PRESS SPEED, %._ 4 TYPE USED
POLYMER PUMP SPEED, % 6.5 TANKS MIXED
Si IJDGE PUMP SPEED, % F-E D GPM
LIME FEED AUGER, % LBS/HR LITERS/TANK
MIXER SPEED, % QQ Y Q
Revised 8M2/03

TWSA LIME STABILIZATION
DAILY RECORD
DATE
RUN TIME, HRS
DRY
SLUDGE FEED, GAL
'
LIME FEED, LBS
SLUDGE FEED %SOLIDS
PRESS , °%.SOLIDS
LIMEISLUDGE RATIO
TOTAL PRODUCTION, DRY TONS
Inlet reached temp @
Outlet reached'teinp @
PATHOGEN REDUCTION
.VECTOR ATTRACTION REDUCTION
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, %
c' iJDGE PUMP SPEED, % GPM
LIME. FEED AUGER, % LBS/HR .
MIXER SPEED, %
Revised 8/12103
POLYMER
RRiUSAGE
PE USED
TANKS MIXED
5-7 1 f��

TWSA RE5,Jd,UAL
MONTHLY OPEW )N TOTALS
November 2007
Press Run Time
# of days press was run 8 Total dry ton of sludge
treated with lime this month
# of days lime was added 8 this month 16.7
2 loads hauled to landfill @ $450/load= $900.00
Total Residual Cost for the month = $8,853.49

TWSA LIME STABILIZATION
DAILY RECORD
DATE
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDS
LIME/SLUDGE RATIO
Inlet reached temp @ h �.
•Outlet reached temp @ .
PATHOGEN REDUCTION
,- TEMPERATURE:oF.
I
.. TIME
INTO
VESSEL
OUT OF -
VESSEL
-'
OPERATOR
CZ
lo-83
/ G 0
�.o
El;./ .
a Oa
• PRESS, °h;SOLIDS
TOTAL.PRODUCTION, DRY TONS 15.03
' ,VECTOR ATTRACTION •REDUCTION
]LITERs/-rANK4v-�
TIME a5-17.3=7,Z.�;:03 =.23.1
OPERATOR
INITIAL PH 1. .:: 33
• 1�V�. 2HRS: •� •
�tM
22 HRS.
..................................................................................................................................................
OPERATIONAL POLYMER USAGE
BELT PRESS SPEED, % `a TYPE USED 6 . � I
POLYMER PUMP SPEED, % �J . TANKS MIXED
�FUDGE PUMP SPEED,
LIME FEED AUGER, % % . L • LBS/HR SD
MIXER SPEED, %
.Revised 612/03 - - -

TWSA LIME STABILIZATION
_ 4( DAILY RECORD
7
D
3 37 '7
14
STA STOP TOTAL
RUN TIME,HRS 9
DRY TON
SLUDGE FEED, GAL
LIME FEED, LBS rir?s 9 . ...... T7
SLUDGE FEED % SOLIDS PRESS, 0/..SOLIDS
LIME/SLUDGE RATIO ti TOTAL PR0DU6TI6-N,-bRY,T, ONS­
Inlet reached temp @ - -
Outlet -reached temp @
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TEMPERATURE of
TIME
INTO
VESSEL'
OUT OF
VESSEL
OPERATOR
140
-J/9 S
A /,5,5--
Cl)
c) 6H,
5;[Q
boo
.116
TIME
-
INITIAL PH 80
AS = I'?.O.=- 4.01(43 114)
2 HRS.
22 HRS.
.............. ............ ........................................................................ ................... ..................... : ..............................................................
OPERATIONAL POLYMER USAGE
BELT PRESS SPEED, % JO 6 TYPE USED �60
POLYMER PUMP SPEED, % &5 Ai TANKS'MIXED
-ho
P''JDGE PUMP SPEED, % fJbl d GPM
J,
L _. IME FEED AUGER, % LB8/HR- LITERSf1-ANK3
MIXER SPEED, % o
lb's.
-Revised 8f12J03

s+evrt
L4 4� f1b
RUN TIME, HIRS
SLUDGE FEED, GAL
TW.SA LIME STABILIZATION
DAILY RECORD
DATE �Z
START STOP TOTAL
II
DRY
LIME FEED, LBS C), o co
SLUDGE FEED % SOLIDS PRESS %-SOLIDS1.
LIME/SLUDGE RATIO 4q/1_ TOTAL P . RODUCTION, . 'DRY TONS D.
Inlet reached ternpg
-Outlet reached temp @
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TEMPERATURE oF
_7:TIME
INTO-
-VESSEL
OUT OF
VESSEL
OPERATOR
15S
�;
1 "31
I CS�
�
&421
0 0
/q3-
On
TIME OPERATOR
INITIAL PH
Tj
2 HIRS.
22.HRS. 12- 5
............................................................................................................................................ ........................
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED,' %
P' 1JD . GE PUMP SPEED, % _3 D GPM)42)
LIME FEED AUGER, 61. LB8/HR f (W7
MIXER SPEED, %
POLYMER USAGE
TYPE USED 42 6W3
TANKS MIXED
RS/T,
.Revised 8112/03

TWSA LIME STABILIZATION
j
DAILY RECORD "
J
DATE
START
STOP TOTAL
RUN TIME, HRS
v �d
" 06
DRY TON
SLUDGE FEED, GAL.
122
O�
.�
LIME FEED, LBS
SLUDGE FEED %SOLIDS
�.�
PRESS , °,6l.SOLIDS
LIME/SLUDGE RATIO
. 0A
TOTAL PRODUCTION, DRY TONS
Inlet reached temp @
(�
Outlet reached temp
PATHOGEN. REDUCTION
VECTOR ATTRACTION REDUCTION`
TEMPERATURE of
TIME
INTO
VESSEL'
OUT OF .
VESSEL
OPERATOR]
91
0_6
Ao
qa
TIME
25' 17.5= 7-S 1'03 ; �,ZS'
OPERATOR
r7;06'
INITIAL PH 11.11.
2 HRS 3
fa.�•1-, oL37-.lot, 2a3
OO
22 HRS. J a', g.C)
.
OPERATIONAL
BELT PRESS SPEED, % f 6p
POLYMER PUMP SPEED, % 0 `
P ' JDGE PUMP SPEED, % D GPM J S)Z
LIME FEED -AUGER, % -! J LBS/HR ��
MIXER SPEED, %
.: .Revised 8112J03 - -
POLYMERUSAGE
TYPE USEDL q.
TANKS. MIXED
LITERS/TANK

TWSA LIME STABILIZATION
j DAILY RECORD
DATE
START STOP TOTAI
RUN TIME, HRS
`''� -
G % 00
DRY TON
SLUDGE FEED, GAL
(,� 191
d
S I O
LIME FEED, LBS -
SLUDGE FEED % SOLIDS
�. " ��
PRESS,
WSOLIDS
LIME/SLUDGE RATIO
.�
TOTAL PRODUCTION, DRY TONS
Inlet reached temp @
• J .
-Outlet reached temp @
PATHOGEN
REDUCTION
VECTOR ATTRACTION REDUCTION
TEMPERATUREoF
t
,TIME
INTO
VESSEL'
OUT OF
VESSEL
OPERATOR
C0
k(IF ­-0
02� 0 D
`
�1� J.
5:55
aoo
l 1g:
6
oa
boo
l q g
�
TIME
'o�oZX.03=.OPERATOR
W.95 ..216=12...33Y
TOO
INITIAL PH
.,
25 - 17.5 z15'x: 03 = •aaS
2 HRS. 1� yvL_
l2.53 ,. a4G =12;a $y
l�
22 HRS.
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, % gShcb
I GE PUMP SPEED, % S aGa GPM SI�
LIME FEED'AUGER, % 4. T % LBS/HR �O
MIXER SPEED, %
.Revised 8112/03 -
POLYMER`USAGE TYPE USED { \
(q, 0
TANKS MIXED

TWSA LIME STABILIZATION
DAILY -RECORD ,
DATE
START
STOP TOTAL
RUN TIME, HRS
"
-] ..O S
SLUDGE FEED,
DRY TON
GAL'
7 7
LIME FEED; LB5
SLUDGE FEED % SOLIDS
PRESS , °k:SOLIDS
LIME/SLUDGE RATIO
i
TOTAL PRODUCTION, DRY TONS.
Inlet reached temp.@
�e
-Outlef reached temp @
�>
PATHOGEN REDUCTION
VECTOR ATTRACTION 'REDUCTION
TEMPERATURE oF'
TIME
INTO
VESSEL'
OUT OF
. VESSEL
OPERATOR
n
`off
117
day
L'0,157
. l OO
/97
F�oS
170
IT
i�
TIME
o2$-,17.Sr=` 7.ot X.03 =, al(� .
OPERATOR
7`' 3.0
INITIAL PH
rl-ego?
;ZS-2o.g=�i.aX.o3=�ra�-
12�41-.I24= l2cSSq
!. JD
.22 HRS.
OPERATIONAL
BELT PRESS SPEED,, % 56�6
POLYMER PUMP SPEED, %
J DGE PUMP SPEED, 4lO GPM J�•:C13
'LIME FEED AUGER, % � �O LBS/HR-jat) .
POLYMER USAGE
TYPE USED -' 0
TANKS MIXED
LITERS/TANK -i3
MIXER SPEED, % l �-CJ L?f' I �7� . b S,
... .Revised 8112(03

TIME'
INTO
'VESSEL_
OUT OF.
VESSEL
OPERATOR
'Alk
l
'C-J9
dab
le
19.E
6"
'7:.0o
c qT
?S-11.3=S-14n?.171
TIME.
&2,fod -:;(7l=1�..4�aq OPERATOR
730
INITIAL PH �,43
c 2,G6�,
q.
30.2
HRS'
30
i2.5-T 19l=la,�310
!T 30
V 22 HRS. l o�
OPERATIONAL
BELT PRESS SPEED, % Q
POLYMER PUMP SPEED, %�6
F'' 'JDGE` PUMP SPEED, % GPM_
LIME FEED AUGER,'% ^[ 1�(4 LBS/HR�
POLYMER USAGE .
TYPE USED'
TANKS MIXED 1
ILITE RS/TA'NK -6
MIXER SPEED, % _-O O. ®`�r7-p
.Revised 8112/03

TWSA LIME STABILIZATION
1.
DAILY.RECORD
DATE _ %I3
START.
STOP TOTAL
RUN TIME, HRS
.,
7`-O
DRY TON
SLUDGE FEED, GAL
3a,30 '
LIME FEED, LBS
SLUDGE FEED. % SOLIDS
rQ
PRESS , °,,.:SOLIDS
LIME/SLUDGE RATIO'
[ig '
TOTAL PRODUCTION, DRY TONS
Inlet reached temp @
°.
Outlet reached temp @-
b.
PATHOGEN_ REDUCTION .
VECTOR ATTRACTION REDUCTION,
TEMPERATURE oF,
TIME
INTO .
VESSEL
OUT -OF,
VESSEL
.
OPERATOR
693
TIME oiS-oZC�K��(ib )(�03=,,(,3'$ OPERATOR
�13d INITIAL PH �,,L�+-►';
r 30 2'HRS.13
t +J� Clwii
ZZ i n o f
`d ® 22 HRS. c r ) 4-�j
OPERATIONAL
BELT PRESS SPEED, o°
POLYMER PUMP .SPEED; % LI D
WbE PUMP SPEED', %° 3C7 GPM
LIME'FEED'AUGER, % , 56 tilts LBS/HR
POLYMER USAGE
TYPE USED
TANKS MIXED
LITERS/TANK cg Y, i
MIXER SPEED, %
..ReOsed.6/12/03 ,

TVvQA Rr-SIDUAL
MONTHLY OPERA. )N TOTALS
December 2007
SLUDGE FEED
# of days press was run 8
# of days lime was added 8
Total dry ton of sludge 1 loads hauled to landfill @ $450/load= $450.00
treated with lime this month
this month 21.5 Total Residual Cost for the month = $8,427.56,

TWSA LIME STABILIZATION
j
DAILY RECORD
2
DATE 3
START,.
STOP. TOTAL.
RUN TIME, HRS
/
rCj i (5 .
SLUDGE FEED, GAL.:
. DRY TON
J d,34 6
LL
55 1
a,
LIME FEED, LBS
`6 R3
1
SLUDGE FEED % SOLIDS
CQ ri
PRESS. %:SOLIDS
LIME7SLUDGE RATIO
•,-
TOTAL PRODUCTION, DRY TONS
Inlet reached tern.P @
.Outlet reached temp @'
PATHOGEN REDUCTION
- .VECTOR ATTRACTIONREDUCTION-
TEMPERATUREoF.
TIME
INTO
VESSEL,
OUT OF.
VESSEL
OPERATOR
ea
r1_oqjj
TIME a5- q,(,'=5'�iX•B3 :rL OPERATOR
17, bb .: INITIAL.PH
197o'l-2.V3
q; o 0 2 HRS.- 12, s"
� s
22 HRS. '. s
.:..................................... .......
"v+ stivf rl = &wm (a &,*j OPERATIONAL
BELT PRESS .SPEED, % �p d Gl0
POLYMER PUMP SPEED,
IDGE'PUMP SPEED, % 3011l6 GPM.
LIME FEED 'AUGER, %. 53°/6 LBS/HR
POLYMER USAGE
,TYPE USE64Vo16y 9 1bb
TANKS MIXED y
LITERS/TANK
MIXER SPEED, %
_Revised 6112103

TWSA LIME STABILIZATION
1 DAILY RECORD J
'DATE
START STOP TOTAL
RUN TIME, HRS�.
o � d
SLUDGE FEED, GAL I n r7 Ll '] Z
LIME FEED, LBS
SLUDGE FEED %SOLIDS o PRESS, °G.SOLIDS[��
LIME/SLUDGE RATIO V TOTAL PRODUCTION, DRY TONS
Inlet reached ter -pp @� -
Outlet reached temp @ r
PATHOGEN REDUCTION ,VECTOR ATTRACTION REDUCTION
TEMPERATURE oF_
TIME
INTO
:VESSEL`
OUT OF.
VESSEL
OPERATOR
vfO
1 W
d- a
`
! 7�
5 r 417
{ (a
TIME.5 OPERATOR
19,*Z-<1q,4= j;Z;�r�
INITIAL PH ��' �.
A, ,61K[03=.Ig7
ta, r�c-r=1 ,y73
30 2'-HRS: a , `7_
aS:.aeTz Cc3a- , 0411
/136 22 HRS. la,
............................
. ............................................................ : ..............................................................
OPERATIONAL - POLYMER 'USAGE I
BELT PRESS SPEED, %
_505-
POLYMER PUMP SPEED, %
1DGE PUMP SPEED, % GpM. a,
l c�Jp2
LIME FEED'AUGER, %_ LBS/HR V' 6
MIXER SPEED, % 1 00 �O
Revised 8112/03
JTYPE USED 1L �
TANKS M IXlfD
133
15

TWSA LIME STABILIZATION
DAILY RECORD
DATE
START
STOP., - TOTAL
RUN TIME, HRS -
..,
'7.1
dc1
DRY TON .
SLUDGE FEED; GAL
LIME FEED, LBS'.
SLUDGE -FEE I D %,SOLIDS
PRESS ; °� SOLIDS
,
LIME/SLUDGE RATIO
,I ° �
TOTAL PRODUCTION; YDRY TONS
Inlet reached.tem
Outlet reached temp
PATHOGEN -REDUCTION'
VECTOR -ATTRACTION REDUCTION
( I. TEMPERATURE OF
TIME
INTO.,
VESSEL:
OUT OF
VESSEL
'oPERATOR:
?TIMES; i9°-`�`'�;15P�
OPERATOR .
INITIALPH
SS-o 1g7z &I Y03
3 22 HRS.
J
d
ChA
OPERATIONAL
BELT PRESS SPEED.;'
POLYMER PUMP SPEED, %.
DGE. PUMP SPEED, % GPM `
LIME FEED AUGER, % LBS/HR
MIXER.SPEED, %

TWSA LIME STABILIZATION
DAILY RECORD
DATE
START
RUN TIME, HRS* - I .
SLUDGE FEED, GAL
LIME FEED', LBS
SLUDGE FEED % SOLIDS
LIME/SLUDGE RATIO
Inlet reached temp Q
r-4 to
Outlet reached temp @
PATHOGEN REDUCTION
TEMPERATURE of
INTO -
I OUT OF
id.
m
o 2" I ns
OPERATIONAL
BELT PRESS SPEED, % 5�6
POLYMER PUMP SPEED, %
STOP TOT
7'
PRESS, % SOLIDS
[—
TOTAL PRODUCTION, DRY TONS
VECTOR ATTRACTION REDUCTION
p
I)e LJ
TIME
X. a 3 ,,,OPERATOR
INITIAL PH- IAwd5
=.5,2 X, 0,5
9, 35 2 HRS. J S-S
d U
7113!5
22 HRS.
SLUDGE PUMP SPEED, % '46 GPM '77 r/
LIME FEED AUGER, %-E� LBS/HR_LL-76
MIXER SPEED, %
tevised 8112/03
POLYMER USAGE
YPE USED
ANKS MIXEDWj
T51 I c�
q-4

TWSA LIME STABILIZATION
DAILY RECORD
DATE
START STOP TOTAL
RUN TIME, HRS
DF
SLUDGE FEED, GAL'
LIME FEED', LBS
SLUDGE FEED % SOLIDS C)
PRES % SOLIDS
LIME/SLUDGE RATIO TOTAL PRODUCTION, DRY TONS
Inlet reached temp Q
Outlet reached.temp @ 0
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TEMPERATURE 'OF
INTO'. I OUT OF I
e-10
36.
(9,60
0,1 03
............................................
I ...............................
TIME
2S - -40,a 03
i.qq 12,46fo OPERATOR
INITIAL PH
2 HRS.
22 HRS..
OPERATIONAL
BELT PRESS SPEED, % &0 VV
POLYMER PUMP SPEED, % -,-)0
SLUDGE PUMP SPEED, % GPM 502
,473
LIME FEED AUGER, 91.L6 %) LBs/HR_jjQ,'�
MIXER SPEED, % 00 OX0
Zevised 8/12103
PE USED
A,NKS MIXED
TEILIA_
LiT
RS/TANK
�7

TWSA LIME STABILIZATION
DAILY RECORD
DATE �� _ �;7'
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
TO
SLUDGE FEED % SOLIDS l PRESS , % SOLIDS
LIME/SLUDGE RATIO TOTAL PRODUCTION, DRY TONS A
Inlet reached temp @
cl
Outlet reached temp @ -
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TIME �S .a0,=`i,�Xrd3 =o l41 OPERATOR
/ INITIAL PH l a , 51
.12,7®-.141 12.55.E
' « 2 HRS.
ia.��-.i�Z.=la•55�
22 HRS: L vt , 5(p
OPERATIONAL
BELT PRESS SPEED, % B
POLYMER PUMP SPEED, % �6
SLUDGE PUMP SPEED, % lC3 GPM
LIME FEED AUGER, %i� t `/6 L13S/HR__LL3 r
,JIIXER SPEED,
ivised W12/03
ITYPE USED
TANKS MIXED
_1TERS/TANK

TWSA LIME STABILIZATION f
DAILY RECORD.
'DATE / r.%..;�• ..
,3�sA 6
START f STOP TOTAL k
RUN TIME, HRS 3.3
G
h DRY TON
SLUDGE FEED, GAL C�
n
LIME FEED, LBS l� ,
SLUDGE FEED % SOLIDS PRESS, °,b SOLIDS'
LIME/SLUDGE RATIO 1- TOTAL PRODUCTION,_ DRY TONS
r
Inlet reached temp @ ,•
Outlet reached temp @ - /
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TEMPERATURE `OF.
INTO . OUT OF
TIME VESSEL VESSEL OPERATOR • TIME
/2k OPERATOR
[158 ta.�lr- rah=ra.�a�
®INITIAL PH
o, ��. qv 1,1-1 ya
s� .�•J $
s T 2 HRS.
0 � ! _..
o
22 HRS.
OPERATIONAL POLYMER USAGE
BELT PRESS SPEED, % ld PE USEDG��-�
POLYMER, PUMP SPEED, %®/D ANKS MIXED
SLUDGE PUMP SPEED, `% : e GPM
LIME FEED AUGER, % e� . /% LBS/HR•/ / LITERS/TANK
ndIIXER SPEED, % l ���/p / �LJ ( (� •'
6vised 8/12103

TWSA LIME STABILIZATION
DAILY RECORD
DATE 1
a
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS .
SLUDGE FEED % SOLIDS
LIME/SLUDGE RATIO
!,;� 56.
�3,3/
Inlet reached temp..@ °
' r
Outlet reached temp @ (�
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TEMPERATURE OF
INTO OUT OF
TIME VESSEL VESSEL OPERATOR TIME %S - 2 a r = 4.1 X' ;p 3 =, (23. OPERATOR
;,4
/�.�� 12.3�
�` / S INITIAL PH /J
jq�:�Is -
r.
Oj,5. )
j,5+j_[ID
OPERATIONAL
BELT PRESS SPEED; %
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, .% GPM 2 . D '
LIME FEED AUGER, LBS/HR D ` —L ..
MIXER SPEED, %
wised 8/72103
lV
d �
22 HRS. Ll
TYPE'USED
TANKS MIXED