WQ0005763_2002 Annual Report_20030310

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Auth®raiy s
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March 10, 2003
DENR/DWQ/Water Quality Section
Non -Discharge Compliance Unit
1617 Mail Service Unit
Raleigh NC 27699-1617
Gentlemen;
9
Enclosed is the Annual Residuals Report for theTuckaseigee Water and Sewer Sludge/Compost
facility (permit #WQ0005763) for the period of January 1, 2002 - December 31, 2002.
An error on my part resulted in some monitoring required by the permit being inadvertently left
off the analysis request sheet when annual samples were sent to the lab. These parameters have
been noted on the Annual Residual Sampling Summary form. Samples have been taken from
residuals stored on the pad during 2002 and the analysis will be sent in as an amended report.
Should you have any questions or if I can provide you any additional information, please don't
hesitate to contact me.
Sincerely,
1
\._.. '
.Stan Bryson i
Wastewater Pla t Operations Superintendent
Tuckaseigee Water & Sewer Authority
Eric.
1246 West Main St. Sylva, NC 28779 • [phone] • Fax: [phone]

ANNUAL SEWAGE SLUDGE REPORT
OF
TUCKASEIGEE WATER AND SEWER AUTHORITY
PLANT # 1-NPDES # NCO039578 (WQ0005763)
for the period of January 1, 2002-December 31, 2002
as required by
40 CFR, PART 503
STANDARDS FOR THE USE OR DISPOSAL OF SEWAGE SLUDGE

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. # NC003 9578
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

TABLE OF CONTENTS
(1) REPORTING REQUIREMENTS/PERTINENT INFORMATION
(2) CERTIFICATION
APPENDIX
(a) 2002 sludge data
(b) 2002 distrubution and marketing summary
(c) 2002 laboratory analysis
(d) 2002 lime stabilization record of operation

.. ,
CERTIFICATION REQUIREMENTS
PART I -POLLUTANT CONCENTRATION
Arsenic
* * * mg/kg
Cadmium
0.28 mg/kg
Chromium
* * * mg/kg
Copper
84.4 mg/kg
Lead
2.1 mg/kg
Mercury
* * * mg/kg
Molybdenum
*** mg/kg
Nickel
2.9 mg/kg
Selenium
* * * mg/kg
Zinc
128 mg/kg
PART H - PATHOGEN REDUCTION (40 CFR 503.32)
X Class A Class B
PART III - VECTOR ATTRACTION (40 CFR 503,33)
Option 1 —Option 2 _ Option 3 —Option 4
Option 5 X Option 6 _ Option 7 _ Option 8
*** Parameter was inadvertently left off annual analysis. Analysis will be conducted and reported
as an amended report.

1
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 CFR, Part [503. 33(b)(6)]
has been met. I am aware that there are significant penalties for false certification including fine
and imprisonment."
Signed this 26th day of February , 2003.
C F,7
Stan Bryson, Wa. tewater Superintendent

MAR-7-2003 14:35 FROM:
T0:9692eG319©69 . P:3/4
ANNUAL P,A,TI-1OGEN AND VECTOR ATTRACTION REDUCTION TORM..
Facility Name:
WWTP Name:
Moni<tgring Pet
Permit Number:
NP>DES Number: Ale �j`��
Pathogen Reduction (40 CFR 503.32) - Please Indicate level achieved and alternative performed:
Class A:
Alternative I U--7
Alternative 2 ❑
Alternative 3 U
Aitemative 4
Alternative 5 -Alternative 6 ❑
If applicable to alternative performed (Class A only) indicate "Process to Further Reduce Pathogens'°:
Compost J_j Heat Drying El
Heat Treatment ❑
ThermopHic [j
13014li,ay ❑
GFunma Ray(]
Ya.steurization
Class ji:
Altemative lU
Alternative 2 ❑
Alternative 3 []
1<f applicable to alternative performed (Clasq B only) indicate "Process to Significantly Reduce Pathogens":
Lime Stabilization F]
Air Drying Composting LJ Aerobic Digestion Ll
Anaerobic vigestion❑
zf applicable to alternative erfolrmed (Class A or Class S) complete the following
monitoring data:
Parameter
Level in
Pathogen Density
um rot
EXcCC-
dct]Cp9
krCclucriPY
of
nal si9
Samples
TY)3e
a y .
Tech-
nip uE
N iruinu
Geo. Mean
aximu
Units
Fecal Coliform
Moto ie611
power.l✓ijN per
gram of total
solids or 2 x 10 to
the 66 power
CFU per gram of
1000 mpn per
gram of total solid
(dryweight)
<
C CN
�
P
��
S�
l'(lonA
of 1 Q�
Salmonella bacteria
(in lieu of feeFl
colifonn)
3 MPN per A
>;"M3 total solid
(dry weight)
Vector Attraction Reduction (40 CFR 503.33) - Please indicate option performed:
pption l ❑ Option2 }J Option 3 1.1 1 Option 10ption 5 ❑
Option. 6 W j0ption. 7 ❑ Option S ❑ (Option 9 ❑ Option 10 Lj
No vector attmetion mdu.etion options were performed ❑
CERTIFICATION STATEAUNT (plcaisc check the appropriate. statement)
(� "I certify, under penalty of law, that the pathogen requirements in 40 C1 R 503.32 and the vector
attraction reduction requirement in 40 C1<R 503.33 have been met."
-1: certify, under penalty of law. that the pathogen requirements in 40 CF.R 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 determiaRtion 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."
prepareryame a d Title ( e or print) Land Applier Name and Title (if applicable)(type or print)
Signature of Preparer
Signature of .Land A.pplier (if applicable)
Author Daryl 13. Merritt
Date
DENR FORM RF (W2002)

ANNUAL RESIDUAL SAAIPLLXCY ,SUMMARY F0%NT
�
Attaeb this form to the corresponding Annual Report
Please note that your permit away contain
additional parameters to be analyzed than those required t
e summarized on this fo
ru
Permit Number: D
Laboratory: I}
_/VC—
Facility Name: eA.
_ 2)
IMES N or
3)
Gl
m
4)
WWTP Name-. 1 yj
.A—v-.sae >n,.4-
Sample of
_�_��
1�I certify, under penalty of lsw, 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 submitfed. I am aware that there are
significant penalties far submitting false information, including the possibility of fines and imprisoameai for knowingviolations."
Signature of Preparer Da
,ems'3'P )e' . 4f C;i1q �I S'r -,>
Auftr Daryl D. Mt n-M
Ckh
DENR FORM RSSF (712002)
A
.h

r
ANNUAL DISTRIB(MON AND ALUWETINGI SURFACE DISPOSAL C;ERTIFICA.TION
.3FACELffY NAINI& ems' U)
PHONE: s-tea / COUNTY: �Ksep�OPERATOR:
V .FORNI
FACILITY TYPE (please check one): �1 Surface Disposal (complete Part A (lioarce(s) and "Resid.uaftn" Volume only) and Part C)
�( Distribution and Marketing (complete Parts A, A and C)
Wits the facility in operation during the past calendar year? ;''Yes :1 No No If No :skip parts A, B, C and certify form below
Part A*. •
Part B*:
Mouth
(include NPDES # if
applicable)
applicable)
Volume (dry ions)
Recipient Information
AdrinexzdmentJ
Bulking Agent
Residual In-
Product Out
Name(s)
Volume (dry
Intended use(s)
Jannary
v
February.
March
_
April
May
June
`
July
—
August _
V
September.
October
_
November
--
December
Totals:
Annual (dry tons):
ArMen
MnTs use
Bu ngAgent(s)
use :
* If mop, space than given is required, please attach additional information shoet(s). Lq/Check box if additional sheet(s) are attached
Part C: ''���
Facility was compliant daring calendar year 2 t�,wjth all con.tlitions of the permit (including but not limited to items 1-3 below) issued fry the
Division of Water Quality, u Yes No If No, please provide a written description why the facility was not compliant.
1..A.]I 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 aperation and maintenance requireinents were compiled with or, in the case of a deviation, prior authorization was received from the Division of Water
Quality,
3. No contravention of Ground dater Quality Standards occurred at armonitoHng well.
"I certify, uider penalty of law, that the above information is, to the hest of my kuowWg�e and belief, true, accurate and complete. I am aware
that kere are Kignifimnt penalties for sebmltti7-/.qoa'�
se informaiion, inciu.ding the possibility of fines and imprisonment for knowing violations."
�_ -
Signature of Pexmittee ate Signature of PrepareO* Date
g
(if different from Perm.ittee) "P.repa-rer is defined in 40 CFR Part 503.9(r)
Author Daryl D. hien-itt DENR FORM DMSDF (T207)

APPENDIX A
2002 SLUDGE DATA
TWSA PLANT # 1 (1.5 mgd)
NPDES # NCO039578
SLUDGE TO DIGESTOR.................................................................6,240,750
gallons
total lbs.:..................................................................
268, 9341bs
total tons.......................................................................134.47
tons
total metric tons
............................................................121.96 metric tons
TWSA PLANT # 2 (.5 mgd) .
NPDES # NCO020214
SLUDGE HAULED TO PLANT # 1....................................................... 228,101 gallons
total tons........................................................................ 15.65 tons
total metric tons.............................................................14.19 metric tons
TWSA PLANT # 3 (.1 mgd)
NPDES # NCO063321
SLUDGE HAULED TO PLANT # 1......................................................... 223,579 gallons
totaltons............................................................................ 22.54 tons
total metric tons..............................................................20.44 metric tons
A portion of the sludge that was generated at the Tuckaseigee Water and Sewer Authority during
2002 was hauled by a private contractor to a designated landfill.
Landfill: Macon County Landfill
1448 Lakeside Drive
Franklin NC 28734
A total of 178.7 wet tons were hauled to the landfill during 2002. This does not reflect residuals
that are currently stored onsite.
Copies of haul tickets can be provided if needed.

APPENDIX B
TWSA PLANT # 1
ANNUAL DISTRIBUTION AND MARKETING SUMMARY
2002
PART A
VOLUME IN DRY TONS
MONTH
ADIVIENDMENT/
ULKING AGENT I
RESIDUAL
IN
PRODUCT
OUT
January_23.78
14.54
38.32
Februay
17.33
8.64
25.97
March
32.83
16.85
49.68
April
14.05
10.15
24.2
May
18.58
15.15
33.73
June
19.7
11.79
31.49
July
12.77
7.83
20.6
August
16.23
10.73
26.96
September
0
October
0
November
0
December,
0
Annual Dry Tonsl
155.27
95.69-1
250.95

APPENDIX B
TWSA PLANT # 1
ANNUAL DISTRIBUTION AND MARKETING SUMMARY
2002
PART B
RECIPIENT INFORMATION
DATE
NAMES
VOLUME wet tons
INTENDED USE
1/16/02
Philip Stephens Cullowhee
60
Pasture
1/17/02
Philip Stephens Cullowhee
15
Pasture
1/18/02
Mark Bell Franklin
28
Hayfield
2/14/02
IVerlin Bryson Cullowhee
1.5
Garden
2/19/02
IChester Sorrells (Waynesville)
18
Commercial Hauler
2/23/02
Chester Sorrells (Waynesville)
36
Commercial Hauler
2/25/02
Chester Sorrells (Waynesville)
36
Commercial Hauler
Ij/ /v
.,, „02
f + Corr ll /1 / vn. . ill.%
.,hes�er����e„s �tia �,. vs„„
3z
C'nmm.r�i�l I--la�wlcr
...,,,,,,,ercial
3/5/02
Forn Kelley (Webster)
20
Pasture
3/7/02
Dee Mull Cullowhee
6
Pasture
3/8/02
Chester Sorrells (Waynesville)
9
Commercial Hauler
3/11/02
Dee Mull Cullowhee
9
Pasture
4/4/02
Chester Sorrells (Waynesville)
15
Commercial Hauler
4/5/02
Chester Sorrells (Waynesville)
15
Commercial Hauler
4/6/02
Chester Sorrells (Waynesville)
18
Commercial Hauler
4/15/02
IChester Sorrells (Waynesville)
9
Commercial Hauler
4/20/02
Chester Sorrells (Waynesville)
9
Commercial Hauler
4/30/02
Chester Sorrells (Waynesville)
27
Commercial Hauler
5/9/02
Chester Sorrells (Waynesville)
9
Commercial Hauler
5/11/02
Tim Crowe S Iva
15
Pasture
6/10/02
Chester Sorrells (Waynesville)
7
Commercial Hauler
6/11/02
IChester Sorrells (Waynesville)
56
Icommercial Hauler
6/12/02
Chester Sorrells (Waynesville)
36
Commercial Hauler
6/13/02
Chester Sorrells a nesville
14
Commercial Hauler
6/17/02
Tim Crowe S Iva
5
Pasture
Total
1
505.5

laceA'nalyticafm
www.pacelabs.com
i
ckaseigee Water 8 Sewer Auth
• as
Box 1051 ' r
Iva, NC 28779
tn: Mr. Stan Bryson ;r
one: [phone] c`
lid results are reported on a dry weight basis
Pace Analytical Services, Inc.
54 Ravenscroff Drive
Asheville, NC 28801
Phone. [phone]
Fax,- 828254-4618
Lab Project Number: 9326504
Client Project ID: TWSA LIME RESIDUAL
:b Sample,,No" 931106793
Project Sample
Number: 9326504-001
Date Collected: 01/22/02 11:40
ient•S-Wle ID: TWSA LIME
RESIDUAL
Matrix: Soil
Date Received: 01/22/02 13:00
,
r'ameters
Results Units
Report Limit Analyzed
GAS No. Ftnote Reg Limit
A Chemistry
,ercent Moisture
Method: X Moisture
Percent Moisture
49.0 %
01/22/02
AAB
ecal Col iform MPN Solid
Prep/Method: SM 9221B/E
/ SM 9221B/E
Col iform. Fecal
ND
2 01/23/02
KAS
Date: OIJ31102
Laboratory Certification IDs REPORT OF LABORATORY ANALYSIS
NC Wastewater 40 This report shall not be reproduced, except in full,
NC Drinking Water 37712 without the written consent of Pace Analytical Services, Inc_
ACCON
04/ `•\D1'
Page: 1
Laboratory Certification IDs
TN Drinking Water 02980
SC Environmental 99030

�Analytical�'
www pacelahs_com
s
q
,ee Water & Sewer Auth rN.
1051
,a, NC 28779
Pace Analytical services, Inc.
54 Ravenscroft Drive
Asheville, NC 28801
Phone: [phone]
Fax.* 828.254.4618
Lab Project Number: 9327027
Client Project ID: TWSA LIME RESIDUAL `
ttn: Mr_ Stan Bryson
hone: [phone]
x �
Aid results are reported
on a dry weight basis
ib Sample No 'r.931
mple
ient.SaLIME
ID: TWSA LLIME
RESIDUAL
Project Sample Number: 9327027-001
Date Collected: 02/12/02 08:45
1 >'
Matrix: Soil
Date Received: 02/12/02 11:40
rameters
'-t Chemistry�—
Results Units
Report Limit
� Analyzed
CAS
No. _ Ftnote Reg Limit
ercent Moisture
Method: % Moisture
'ercent Moisture
49.0
02/19/02 JDA
!cal Coliform MPN Solid
Prep/Method: SM 9221B/E
/ SM 9221B/E
:oliform, Fecal
ND
2 021I2102 JGJ
Date: 02/28/02
ioratory Cert"rficati IINWastewater 40 REPORT OF LABORATORY ANALYSIS
Drinking Water 37712 This reportshall not be reproduced, except in full,
without the written consent of Pace Analytical Services, Inc.
'Y 'CCpq,
O' {, ``'c
Page: 1
Laboratory Certification IDS
TN Drinking Water 02980 )
SC Environmental 99030

ice Analytical
wwcs! pacelabs.cam
Pace Analytical Services, Inc.
54 Ravenscroft Drive
Asheville, NC 28801
Phone: [phone]
Fax. 828,254.4618
.seigee Water & Sewer Auth *X; Lab Project Number: 9327105
aox 1051 = Client Project ID: TWSA LIME RESIDUAL
yl va, NC 28779
Attn: Mr. Stan Bryson r�;K `
Phone: [phone]-r
Solid results are .reported on a dry weight basis
Lab Sample ,Nd:- - 931129142 Project Sample Number:. 9327105-001 Date Collected: 02/15/02 09:00
Client Sample ID: TWSA LIME RESIDUAL Matrix: Soil Date Received: 02/15/02 16:01
_NV
.P,ar`•ameters Results Units Report Limit Analyzed CAS No. Ftnote Reg Limit
Wet Chemistry
Percent Moisture Method: X Moisture
Percent Moisture 47-4 '% 02/19/02" JDA
Fecal Coliform MPN Solid Prep/Method: SM 9221B/E / SM 9221B/E
Coliform. Fecal ND 2 02/15/02 JGJ
Date: 02/26/02
Laboratory Certification 1Ds REPORT OF LABORATORY ANALYSIS
NC Wastewater 40 This report shall not be reproduced, except in full,
NC Drinking Water 37712 without the written consent of Pace Analytical Services, Inc.
M I[COA
Page: I
Laboratory Certification IDs
TN Drinking Water 02980
SC Environmental 99030

aceAnalyticalm
www.pacelabs.com
r '
fuckaseigee-Water & Sewer Auth
PO Box 1051y
Sylva. NC 28779
Pace Analytical Services, Inc.
54.Ravenscroft Drive
Asheville, NC 28801 .
Phone. [phone]
Fax. [phone]
Lab Project Number: 9328342
Client Project ID: TWSA LIME RESIDUAL
Attn: Mr. Stan Bryson
Phone: [phone]
Solid results are.,:reported on a
dry weight basis
Lab Sample_ o 931177828
Project Sample
Number: 9328342-001
Date Collected: 04/04/02 08:00
Client Sample ID: TWSA LIME RESIDUAL 4/4
Matrix: Soil.
Date Received: 04/04/02 11:21
Parameters
Results- Units
Report Limit
Analyzed
by
CAS No. Ftnote Reg Limit
Wet Chemistry
Percent Moisture
Method: X Moisture
Percent Moisture
51.1 X
04/12/02
MPS
Fecal Coliform MPN Solid
Prep/Method: SM 9221B/E
/ SM 9221B/E
Coliform, Fecal
ND
2
04/04/02
JGJ
0
Date: 04/17/02
Page: 1
i. -5aboratory Certification 1Ds Laboratory Certification IDs
REPORT OF LABORATORY ANALYSIS TN Drinking NC Wastewater 40 This report shall not be reproduced, except in full, g Water 02980
NC Drinking Water 37712 _
without the written consent of Pace Analytical Services, Inc. SC Environmental 99030.
\F A[[p

ace Analytical "'
www. pacelabs. com
t
I
Tuckase.igee Water & Sewer Auth
1246 West Main Street
Sylva, NC 28779
Attn: Mr. Stan Bryson
Phone: [phone]
Solid results are reported on a dry weight basis
Pace Analytical Services, Inc.
2225 Riverside Drive
Asheville, NC 28804
Phone: [phone]
rax. 828.252.4618
Lab Project Number: 9329140
Client Project ID: LIME RESIDUAL
Lab Sample_Nn;:' 932208771 Project Sample Number: 9329140-001 Date Collected: 05/07/02 09:20
Client Sample ID: TWSA LIME RESIDUAL Matrix: Soil Date Received: 05/07/02 11:49
Parameters Results Units Report Limit Analyzed by CAS No- Ftnote Reg Limit
Wet Chemistry
Percent Moisture Method: X Moisture
Percent Moisture 50.7 X 05/07/02 AAB
Fecal Coliform MPN Solid Prep/Method: SM 9221B/E / SM 9221B/E
Coliform, Fecal ND 2 05/07/02 KAS
Date: 05/15/02
Laboratory Certification IDs REPORT OF LABORATORY ANALYSIS
NC Wastewater 40 This report shall not be reproduced, except i❑ full,
NC Drinking Water 37712 without the written consent of Pace Analytical Services, inc.
N •CC�go
Page. 1
Laboratory Certification IDs
TN Drinking Water 02980
SC Environmental 99030

Pace Analytical Services, Inc.
54 Ravenscroft Drive
Asheville, NC 28801
Phone: [phone]
Fax: [phone]
Lab Project Number:'9329239
Client Project ID: Lime Residual
Attn: Mr. Stan Bryson �.
Phone: [phone]
Solid results are.:r`eported on a dry weight basis
Lab Sample `931212617
Project Sample
Number: 9329239
001
Date Collected: 05/10/02 01:23
_N6,;
Client Samp`Te ID: TWSA LIME
RESIDUAL
Matrix: Soil
Date Received: 05/10/02 15:10
Pa =tern
Results Units Report Limit
Analyzed
by
CAS No. Ftnote Reg Limit
-Wet Chemistry
Percent Moisiture
Method: X Moisture
Percent Moisture
50.6 X
05/15/02
AAB
Fecal Coliform MPN Solid
Prep/Method: SM 9221B/E / SM 9221B/E
Col iform, Fecal
ND 2
05/11/02
KAS
Date: 05/22/02
Caboratory Certification IDS
NC Wastewater 40
NC Drinking Water 37712
REPORT OF LABORATORY ANALYSIS
This report shall not be reproduced, except in full,
without the written consent of Pace Analytical Services, Inc.
M ACLp
en�r,f
Page: 1
Laboratory Certification IDS
TN Drinking Water 02980
SC Environmental 99030

i
.�laceAnalyicaf"
www.pacelabs.com {
,,lid results are reported on a dry weight basis
Pace Analytical Services, Inc.
54 Ravenscroft Drive
Asheville, NC 28801
Phone. [phone]
Lab Project Number: 9330392 Fax:[phone]
Client Project ID: LIME RESIDUAL
_ab Sample No: 931258131 Y' Project Sample Number: 9330392-001 Date Collected: 06/27/02 08:40
:lient Sample ID: TWSA LIME RESIDUAL Matrix: Soil Date Received: 06/27/02 10:44
'arameters y •r' Results Units Report Limit Analyzed by CAS No. Qual RegLmt
Fecal Col i form MPN Solid„" :,' . Method: SM 922113/E
Col iform, Fecal ND 2 06/27/02 ACL
Jet Chemistry
Percent Moistu€ Method: i.Moisture
Percent Moisture 51.3 % 07/01/02 EWS
Hate: 07/11/02
Laboratory Certification IDs REPORT OF LABORATORY ANALYSIS
NC Wastewater 40 This report shall not be reproduced, except in full,
NC Drinking Water 37712 without the written consent of Pace Analytical Services, Inc.
x 4CCOA
Page: 1
Laboratory Certification IDs
TN Drinking Water 02980
SC Environmental 99030

z Analytical °
www. pacelabs.com
cs are reported on a dry weight; fi'a'sis
Pace Analytical Services, Inc.
2225 Riverside Drive
Asheville, NC 28604
Phone. [phone]
Lab Project Number: 9331962 Fax.[phone]
Client Project 1D: TWSA LIME RESIDUAL
,le No: 931315527 Project Sample Number: 9331962-001 Date Collected: 08/20/02 05:30
Sample ID: TWSA LIME RESIDUAL`..` Matrix: Soil Date Received: 08/20/02 07:35
arameters Results Units Report Limit Analyzed By CAS No. Qual RegLmt
Fecal Coliform MPN Solid >>% Method: SM 9221B/E
Coliform, Fecal ND 2 08/20/D2 ACL
Jet Chemistry.
Percent Moisture`:; Method: % Moisture
Percent Mpi.9r'e 45.9 X 08/26/02 ALA
Date: 08/29/02
LaboratoryCertification IDs REPORT OF LABORATORY ANALYSIS
NC Wastewater 40 This report shall not be reproduced, except in full,
NC Drinking Water 37712
without the written consent of Pace Analytical Services, Inc.
t
Page: 1
Laboratory Certification IDs
TN Drinking Water 02980
SC Environmental 99030

Pace Analytical Services, Inc.
2225 Riverside Drive
Asheville, NC 28804
Phone. 828,254.7176
Lab Project Number: 9333289
Fax.- 828.959 4618
Client Project ID_ LIME RESIDUA
;suits are reported on a dry weigjV basis
;,^L^
Sample No: 931362594 Project Sample Number.: 9333289-001 Date Collected: 10/08/02 08:40
lent Sample ID: TWSA LIME RESIDUAL' Matrix: Soil Date Received: 10/08/02 14:27
Parameters Results Units Report Limit Analyzed By CAS No. Qual RegLmt
Fecal Coliform MPN Solid; :"' Method: SM 9221B/E
Col iform, Fecal ND 10/09/02 ACL
Wet Chemistry,,:.:°;
Percent Moislur" Method: % Moisture
Percent Moisture 48.8 % 10/10/02 WCB
Date: 10/17/02
Laboratory Certification IN
NC Wastewater 40
NC Drinking Water 37712
REPORT OF LABORATORY ANALYSIS
This report shall not be reproduced, except in full,
without the written consent of Pace Analytical Services, Inc.
� ACLOq
C
1
Page: I of 2
Laboratory Certification IDs
TN Drinking Water 02980
SC Environmental 99030

1 ace Analytical..
www. pacelabs. cam
Solid results are reported on a dry weig}'Ia'sis
Pace Analytical Services, Inc.
54 Ravenscro(t Drive
Asheville, NC 28801
Phone. [phone]
Lab Project Number: 9334232 Fax.[phone]
Client Project ID: LIME RESIDUAL
Lab Sample No: 931396303 = Project Sample Number: 9334232-001 Date Collected: 11/12/02 09:00
Client Sample ID: TWSA LIME RESIDUAL.,"v'R� Matrix: Soil Date Received: 11/12/02 12:34
Parameters 'Results Units Report Limit Analyzed By CAS No. Qual RegLmt
Fecal Coliform MPN Solid*_!5='y- Method: SM 9221B/E
Coliform, Fecal w ND 11/12/02 ACL
Wet Chemistry„ _
Percent Moisture' Method: X Moisture
Percent Moisture 47.2 X 11/15/02 WCB
Date: 11/21/02
�c
-dboratory Certification IDs
NC Wastewater 40
NC Drinking Water 37712
REPORT OF LABORATORY ANALYSIS
This reportshall not be reproduced, except in full,
without the written consent of Pace Analytical Services, Inc.
M ILCp
IF
ti O�^\O r
,.r:£
N
Page: 1 of 2
;i
i
i
Laboratory Certification IN
TN Drinking Water 02980
SC Environmental 99030

Lab Sample No: 931401947
Client Sample ID: TWSA LIME
Parameters
Fecal Coliform MPN Solid
Coliform. Fecal
Wet Chemi stry x`tl<t
Percent Moistur:."'
Percent Moisture
Comment : SHELF H
08:55
Date: 11/27/02
Laboratory Certification IDs
NC Wastewater 40
NC Drinking Water 37712
Pace Analytical Services, Inc,
2225 Riverside Drive
Asheville, NC 28804
Phone. [phone]
Lab Project Number: 9334377 F2x 828.252-4618
Client Project ID: LIME RESIDUAL
::•
Project Sample
Number: 9334377-001
Date Collected: 11/15/02 0855
JDl1AL 2"'
Matrix: Soil
Date Received: 11/15/02 13:20
Results Units
Report Limit
Analyzed By
CAS No- Qual RegLmt
Method: SM 9221B/E
ND
11/15/02 ACL
Method: X Moisture
48.3 %
11/25/02 WCB
REPORT OF LABORATORY ANALYSIS
This report shall not be reproduced, except in full,
without the written consent of Pace Analytical Services, Inc -
Page: 1 of 2
i
Laboratory Certification IDs
TN Drinking Water 02980
SC Environmental 99030

TWSA LIME STABILIZATION
DAILY RECORD
DATE //� 7
START STOP TOTAL
RUN TIME, HRS 1
U iJ c� ~�S k �v�-
SLUDGE FEED, GAL
DRY TON
LIME FEED, LBS
SLUDGE FEED % SOLIDS b PRESS , °h SOLIDS
LIME/SLUDGE RATIO. o TOTAL PRODUCTION, DRY TONS
o
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
-rc:enflcnATl IPP: nF
TIME
INTO.
VESSEL
OUT OF
VESSEL
OPEf2A70R
s 3 0
o
/
AF
TIME OPERATOR
I is �i l V�11V1!lam /T
ID 2HRS.
22 HRS-
.......................... I ... .......... .............--..................:............................................... .
OPERATIONAL
BELT PRESS SPEED,,,
POLYMER PUMP SPEED, %
L UDGE PUMP SPEED, % ____GPM 71
LIME FEED AUGER, %-LBS/HR
MIXER SPEED, % I/�t)
POLYMER USAGE
TYPE USED ��✓�
TANKS MIXED
►1

r) f-L3
TWSA LIME STABILIZATION
DAILY RECORD
DATE
START STOP TOTAL
RUN TIME, HRS ► I i ' "
SLUDGE FEED, GAL/ 3 O
LIME FEED, LBS
SLUDGE FEED °h SOLIDS PRESS. %' SOLIDS
LIME/SLUDGE RATIO
TOTAL PRODUCTION, DRY TONS
� s , `n
PA-THOGEN REDUCTION
TcnnDt=DOT1 IPF nF
TIME
INTO.
VESSEL
OUT OF
VESSEL
OPERATOR
f
l k
/0-
Ar
DRY TON
VECTOR ATTRACTION REDUCTION
TIME OPERATOR
>�i Lip T;�, ��, ►l �I ��
y 2 HRS.
y =L�-- 22 HRS- c�
................. ............. ............. I ................................. ............................................ . .
. ..................
OPERATIONAL
BELT PRESS SPEED, 4�
POLYMER PUMP SPEED, % 1
LUDGE PUMP SPEED, % 5- GPM 1, , f�
LIME FEED AUGER, %LBS/HR
MIXER SPEED, % 1 6 b
POLYMER USAGE
.TYPE PE (USED �v
TANKS MIXED
(LITERS/TANK

RUN TIME, HRS
SLUDGE FEED, GAL
TWSA LIME STABILIZATION
DAILY RECORD /
DATE
START STOP TOTAL -
ego p-n-
I ID �A6-�
LIME FEED, LBSF. 7
SLUDGE FEED °% SOLIDS s PRESS, °% SOLID
-LIME/SLUDGE RATIO e / TOTAL PRODUCTION, DRY TONS
I le R C'-� C�1E a rt'
PATHOGEN REDUCTION
T>=nnpFRnTI IRF nF
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
IF %f-,
Ace
iG,G+
�12
DIS
71f
DRY TON
VECTOR ATTRACTION REDUCTION
TIME OPERATOR
WITI
......� . O; j
/ 2 HRS.
........................................................... ................ .......... ....................... ....................... ...................
OPERATIONAL
BELT PRESS SPEED, o�
POLYMER PUMP SPEED, %
LUDGE PUMP SPEED, % GPM
LIME FEED AUGER, % 3 LBS/HR
MIXER SPEED, % ! 6n
22 HRS.
POLYMER USAGE
TYPE USED
TANKS MIXED
RS/TANK

TWSA LIME STABILIZATION
DAILY RECORD
DATE � I q
START STOP t jTOTAL
RUN TIME, HRS
�J -DRY TON
SLUDGE FEED, GAL ` 6
LIME FEED, LBS
SLUDGE FEED % SOLIDS PRESS. - SOLIDS
LIME/SLUDGE RATIO / 1 TOTAL PRODUCTION, DRY TONS
Tn
►�`� ) e'� e Q can. C) 3
PATHOGEN REDUCTION
TFMPFRATURF of
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
11� 43
lR�
6
17a
VECTOR ATTRACTION REDUCTION
TIME-t
11.I IT1 A 1 Pt /
2 HRS. /
�f = 22 HRS.
c. OPERATIONAL
BELT PRESS SPEED, o/ `
POLYMER PUMP SPEED, %
_UDGE PUMP SPEED, % GPM !;
LIME FEED AUGER, %. _� LBS/HR
MIXER SPEED, % _�/ %)(�
OPERTOR
A/__
41--n
POLYMER USAGE
TYPF USED
i
TANKS MIXED
�LITERS/TANK_ '_�_ I

TWSA LIME STABILIZATION
DAILY RECORD
DATE 11-3b IDQ"
SC�"� SY� �v TOTAL
TART C
RUN TIME, HRS r L v
DRY TON
SLUDGE FEED, GAL G� '
LIME FEED, LBS
SLUDGE FEED % SOLIDS ° PRESS . % SOLIDS
LIMEISLUDGE RATIO EZ TOTAL PRODUCTION, DRY TONS ?71
It`d ) Lei G?0,cV
PA-FHOGEN REDUCTION
T> hAPPPATI IRF of
TIME
INTO.
VESSEL
OUT OF
VESSEL
OPERAnTOR
eo-
y
aQc%
j g
e-0
Lj
00
JAc
VECTOR ATTRACTION REDUCTION
TIME OPERATOR
I'd IT! AI P;; „�.._ ..
.............. .....
OPERATIONAL
IJ LL t LVV .-✓,
POLYMER PUMP SPEED, % J
'-UDGE PUMP SPEED,
GPM .�
LIME FEED AUGER, % 3 � LBS/HR
MIXER SPEED, 1 fl (--)
2 HRS.
22 HRS. l
POLYMER USAGE
TYPE I ICEII - / C_
TANKS MIXED 1 .
LITERS/TAN

TWSA LIME STABILIZATION
DAILY RECORD
DATET
START STOP TOTAL
e p 0 "3
—� -
RUNTIME, HRS DRY TON
ly
7 ` l
SLUDGE FEED, GAL ,� �e) `
LIME FEED, LBS
�,
t ���PRESS. % SOLIDS
SLUDGE FEED %SOLIDS !
[::::::::�=
LIME/SLUDGE RATIO % TOTAL PRODUCTION, DRY TONSjv
F
PATHOGEN REDUCTION
-r�nnoCOATI IRF nF
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
1 k
N/0
VECTOR ATTRACTION REDUCTION
TIME OPERATOR
..................... ............................ :..................................
OPERATIONAL
BELT PRESS SPEED,
POLYMER PUMP SPEED, %
LUDGE PUMP SPEED, % -J GPM �: J
LIME FEED AUGER, %.22T`i LBS/HR
MIXER SPEED, % ! 12 (2
2 HRS.
22 HRS"
POLYMER USAGE
PE USED
TANKS MIXED NJ
LITERS/TANK

TWSA LIME STABILIZATION
DAILY RECORD
DATE Q
START STOP TOTAL
RUNTIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
DRY TON
SLUDGE FEED % SOLIDS �1�' PRESS. °6 SOLIDS
F7�
LIME/SLUDGE RATIO f l F--
TOTAL PRODUCTION, DRY TONS =,6�9
PATHOGEN REDUCTION
T�ner�conTl Il7G nF
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
If
SO
LAZI
VECTOR ATTRACTION REDUCTION
TIME
OPERATIONAL
I -Dr PRESS SPEED, % S 0
POLYMER PUMP SPEED, %
LUDGE PUMP SPEED, % - ! GPM &t9
LIME FEED AUGER, %- t(i LBS/HR
MIXER SPEED, % / 0 0
2 HRS- 1- D
22 HRS.
OPERATOR
................
POLYMER USAGE
TYPE I iSEn (i
TANKS MIXED 1�6U 14
ILITERSfTANK

TWSA LIME STABILIZATION
DAILY RECORD
DATE
START STOP TOTAL
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDS t PRESS, °b SOLIDS
LIME/SLUDGE RATIO 3 TOTAL PRODUCTION, DRY TONS
PATHOGEN REDUCTION
T1=nAQFRATI IRF nF
TIME
INTO.
VESSEL
OUT OF
VESSEL
OPERATOR
1 % ;4-' L.
1 ! V 1 �' 1
� `� :J 1
• cam/ v �
�V �
`
�` `q3
DRY TON
VECTOR ATTRACTION REDUCTION
TIME OPERATOR
-2HRS.
-% 22 HRS-
.............. ................... ..........................................................................................................................
OPERATIONAL
BELT PRESS SPEED, -?
POLYMER PUMP SPEED,
LUDGE PUMP SPEED, % GPM
LIME FEED AUGER, % 3 CT LBS/HR
1
POLYMER USAGE
TYPE USED 3 3 �, �
I
TANKS MIXED f 1
LITERSITANK
MIXER SPEED, % /e'In

RUNTIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
TWSA LIME STABILIZATION
DAILY RECORD
DATE
START STOP TOTAL
-DRY TON
-F
- T =3(P:=
SLUDGE FEED °,fi SOLIDS ® PRESS , 6 SOLIDS
TOTAL PRODUCTION, DRY T
LIME/SLUDGE RATIO ONS
PATHOGEN REDUCTION
-rr:neflGC?4T1 1PF nP
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
&-30
,�
N
%3
'2-•ool
VECTOR ATTRACTION REDUCTION
TIME OPERATOR
2 HRS.
oJ( 22 HRS*-
............. ..... .............................. ........ ......... ..................... r ..........
...................................... .............................. ........ ......
OPERATIONAL
BELT PRESS SPEED,
POLYMER PUMP SPEED, %
LUDGE PUMP SPEED, % GPM JJ
LBSIHR
LIME FEED AUGER, % 7
MIXER SPEED, % IT D
POLYMER USAGE
TYPE :,'SED J c
TANKS MIXED
ILITERS/TANK

TWSA LIME STABILIZATION
DAILY RECORD
DATE -2
QSTART STOP TOTAL
RUN TIME, HRS `� 3`�
. 'DRY TON
SLUDGE FEED, GAL
LIME FEED, LBS I
[::::::::�=
SLUDGE FEED % SOLIDS PRESS. % SOLIDS
LIME/SLUDGE RATIO 1 r TOTAL PRODUCTION, DRY TONS
cc� ct
PATHOGEN REDUCTION
rcneo[=DATl IPP nE
INTO.
OUT OF
TIME
VESSEL
VESSEL
OPERATOR
I � ;' ? 1
f
i a G ILC�i�
i
)39
5! d.
VECTOR ATTRACTION REDUCTION
TIME OPERATOR
................... .......................... :......................................
OPERATIONAL
BELT PRESS SPED,
POLYMER PUMP SPEED, %
LUDGE PUMP SPEED,
GPM y
LIME FEED AUGER, %. LBS/HR Q
MIXER SPEED, %
2 HRS.
22 HRS_
POLYMER USAGE
TYPE USED
TANKS MIXED
LITERS/TANK

TWSA LIME STABILIZATION
DAILY RECORD
DATE
START
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LEIS
STOP
TOTAL
SLUDGE FEED %SOLIDS l r / PRESS. % SOLIDS f
LIME/SLUDGE RATIO
a TOTAL PRODUCTION, DRY TONS /
ilD
Ve-
PA-THOGEN REDUCTION
r rnnnco ATl l0f= nP
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
1 �� '� � �
' I U 1 1
� f✓ 1
� psi 1
144-
Cd
DRY TON
VECTOR ATTRACTION REDUCTION
TIME
0�
........................... ....................................................................................
OPERATIONAL
BELT PRESS Sr EED,
POLYMER PUMP SPEED, %
LUDGE PUMP SPEED, % GPM -
LIME FEED AUGER, % LBS/HR
MIXER SPEED, % ]
2 HRS.
22 HRS-
OPERATOR
f
POLYMER USAGE
TYPE USED
TANKS MIXED I
STANK

TWSA LIME STABILIZATION
DAILY RECORD
DATE
START
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
STOP
SLUDGE FEED % SOLIDS / PRESS , °h SOLIDS
LIME/SLUDGE RATIO TOTAL PRODUCTION, DRY TONS
PATHOGEN REDUCTION
Tr_nnrCl--)ATI IRG nF
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR.
j M i
/ � i
1 ,V- i
"7 y� I
°.zl
t
lit
r
OTAL
aZ 3, -d Nsy��'�„�
&A)
DRY TON
VECTOR ATTRACTION REDUCTION
TIME
OPERATOR
r'1
l �y
In I1TIAi Du
11 V 1 I IIlL 1
! V—
r-
2 HRS.
OPERATIONAL
BELT PRESS SPEED, %°
POLYMER PUMP SPEED, % 7?
LUDGE PUMP SPEED, % 146 GPM q6
S)u
UGER °/ 16 LBS/HR
LIME FEED A , °
MIXER SPEED, % =t Itc� J�
22 HRS. ' �V

TWSA LIME STABILIZATION
DAILY RECORD
DATE
START STOP .TOTAL
foqgf EI
RUN TIME, HRS DRY TON
SLUDGE FEED, GAL �� a
LIME FEED, LBS
SLUDGE FEED % SOLIDS = PRESS. °b SOLIDS
LIME/SLUDGE RATIO O TOTAL PRODUCTION, DRY TONS
PATHOGEN REDUCTION
TGAAPFRATL )RE OF
!NTO.
TIME VESSEL
OUT OF
VESSEL
OPERATOR
'f o
/e7
/7
VECTOR ATTRACTION REDUCTION
TIME
S - Yv InliTid,i PF-i i J
'ram
2 HRS_
22 HRS- j '�-
...................................
OPERATIONAL
BELT PRESS SPEED, 0/1=� J5
POLYMER PUMP SPEED,
_UDGE PUMP SPEED, % —GPM-- G �'
LIME FEED AUGER, %.,6-1 LBS/HR To q
MIXER SPEED, % On
OPERATOR
!r ;
POLYMER USAGE
TANKS MIXED1141,
J5'

RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
TWSA LIME STABILIZATION
DAILY RECORD
DATE�� / a
START STOP TOTAL
DRY TON
/
PRESS. % SOLIDS
SLUDGE FEED % SOLIDS IICI •
a TOTAL PRODUCTION, DRY TO /
LIMEJSLUDGE RATIO CQ
jo
PA►HOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TEMPERATURE of
INTO. OUT OF OPERATOR
TIME VESSEL VESSEL OPERATOR TIME
!"ITIA
�'
L PH F c�—
J 2 HRS. /
l
;.� 1dam 22 HRS. th
................................ ..............:.........
.................................................................................. ...................
OPERATIONAL
8EL T PRESS SPEED, °/V
POLYMER PUMP SPEED, %
_UDGE PUMP SPEED, % 1, GPM
LIME FEED AUGER, L Sj LBS/HR
MIXER SPEED, % 106
POLYMER USAGE
I T PE USED L%J
TANKS MIXED
ANK - -5

RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
TVVSA LIME STABILIZATION
DAILY RECORD
DATE
START STOP TOTAL
3 5-1 Z/Q 6,
SLUDGE FEED % SOLIDS PRESS. % SOLIDS
LIMEISLUDGE RATIO 1 TOTAL PRODUCTION, DRY TONS
PATHOGEN REDUCTION
Tr_nncoATl IQP nF
TIME
I
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
DRY TON
ali
VECTOR ATTRACTION REDUCTION
TIME OPERATOR
INITIAL PH
!�.
2 HRS_
0 22 HRS_.
................................................................................... ................ .
OPERATIONAL
c� PR C EED °%
BEL1 rREJS .�P�Lv, iu r
POLYMER pumP SPEED, % V
LUDGE PUMP SPEED, % GPM 1 U
LIME FEED AUGER, % 3 - LBS/HR
MIXER SPEED, % /
POLYMER USAGE
TYPE USED '
!TANKS MIXED I
RS/TAN
;A��L-4

RUN TIME, FIRS
SLUDGE FEED, GAL
LIME FEED, LBS
TWSA LIME STABILIZATION
DAILY RECORD
DATE l//z A �
START STOP TOTAL
D . I
DRY TON
(� 77
zip - c ,
SLUDGE FEED 0/6 SOLIDS �. "- PRESS , % SOLIDS
LIME/SLUDGE RATIO F Sl TOTAL PRODUCTION, DRY TONS
PA 1A
PA-THOGEN REDUCTION
r r-n nncfDATl IRG nF
TIME
INTO.
'VESSEL
OUT OF
VESSEL
OPERATOR
telun
-.
-7�r
.q
VECTOR ATTRACTION REDUCTION
TIME
?� 2 HRS.
22 HRS.
/ �4
......................................................................................................
OPERATIONAL
mm PRESS SPEED,
POLYMER PUMP SPEED, % J
LUDGE PUMP SPEED. % GPM
LIME FEED AUGER, %
LBS/HR J
MIXER SPEED, %
OPERATOR
1�7-
POLYMER USAGE
I 1 iE USLSJ �
TANKS MIXED
�L-ITERS[TANK \-5- --]

TWSA LIME STABILIZATION
DAILY RECORD
�jE
DATE
START
RUN TIME, HRS
SLUDGE FEED, GAL
STOP TOTAL
DRY TON
LIME FEED, LBS
SLUDGE FEED % SOLIDS . PRESS. % SOLIDS
• TOTAL PRODUCTION, DRY TONS
LIMEISLUDGE RATIO
Eq cV,-ed -T.-c
PATHOGEN REDUCTION
TTA AiI CO ATI 10I= nF
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
_
/ 1
�q
!�
��jv
.......................................... ...... : .. . ........................
OPERATIONAL'
BELT PRE -SS SPEED, 04,
7
POLYMER PUMP SPEED, % s�
LUDGE PUMP SPEED, % 66 GPM \15
LIME FEED AUGER, %y LBS/HR
MIXER SPEED, %
VECTOR ATTRACTION REDUCTION
TIME OPERATOR
IMITIAL PH
2 HRS.
-1� 22 HRS-
POLYMER USAGE
TYPE USED
TANKS MIXED' F 1

TWSA LIME STABILIZATION
DAILY RECORD
DATE
START
RUN TIME, HRS
STOP . TOTAL
SLUDGE FEED, GAL `�
LIME FEED, LBS
SLUDGE FEED % SOLIDS { / PRESS , °b SOLIDS
LIMEISLUDGE RATIO ° TOTAL PRODUCTION, DRY TONS
PATHOGEN REDUCTION
renerDCt7oTl IRF nF
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
I ;I; VI
4�
Ixq
-`
1
l�
............. ....................... ........ ...... .................... ................................
OPERATIONAL
BELT DP>_vC CPFED
POLYMER PUMP SPEED,
LUDGE PUMP SPEED, % GPM
LIME FEED AUGER, % LBS/HR
MIXER SPEED, % % o
DRY TON
VECTOR ATTRACTION REDUCTION
TIME OPERATOR
y:dc INITIAL PH rX • / [� �1/ %
2 HRS. A�—
J �. 22 HRS. A-
POLYMER USAGE
TYPE USED 9_ 1
TANKS MIXED ,
ANK

TWSA LIME STABILIZATION
DAILY RECORD p�
DATE 31-2
START STOP TOTAL
RUN TIME, HRS f - �77'
DRY/TON
SLUDGE FEED, GAL ' ! 1 oo `7
LIME FEED, LBS
SLUDGE FEED % SOLIDS + PRESS. °h SOLIDS
LIMJSLUDGE RATIO / E TOTAL PRODUCTION, DRY TONS /
i
cl\-E
PATHOGEN REDUCTION
TFMPFRATURF of
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
-_5
I J�
C-0
17V
VECTOR ATTRACTION REDUCTION
TIME
INITIAL PH %
yy1
2 HRS.
...... ...............................
OPERATIONAL
PEERATIONAL
BELT PRESS SPEED,
POLYMER PUMP SPEED, % J
LUDGE PUMP SPEED, % GPM
7
LIME FEED AUGER, %. LBS/HR
MIXER SPEED. % t�
22 HRS. A2
OPERATOR
POLYMER USAGE
'TYPE USED `�� �
l ]
TANKS MIXED
LITERS/TANK

TWSA LIME STABILIZATION
DAELY RECORD
%
DATE /_r! /' / 0
START STOP TOTAL
RUN TIME, HRS ` DRY TON
SLUDGE FEED, GAL
LIME FEED, LBS
SOLIDS
[:::::::=
SLUDGE FEED °%n ' PRESS, °o SOLIDS
LiMEISLUDGE RA -CIO
D�t
TOTAL PRODUCTION, DRY TONS �c
PATHOGEN REDUCTION
TEMPERATURE of
INTO
OUT OF
TIME
VESSEL
VESSEL
OPERATOR
o ;
X 4
i L' j
ow
IqD-
190
N-7
VECTOR ATTRACTION REDUCTION
TIME OPERATOR
,N %--I
q10 2 HRS.
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, % GPM �/ /
o LBS/HR
�6
LIME FEED AUGER, /o.
MIXER SPEED, %
22 HRS.
POLYMER USAGE
TANKS MIXED
�LITERS/TANK --5'

TWSA LIME STABILIZATION
DAILY RECORD I
DATE
START STOP TOTAL
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED., LBS U
F—­=:�1
SLUDGE FEED % SOLIDS �r
PRESS. °6 SOLIDS
l TOTAL PRODUCTION, DRY TONS
LIME/SLUDGE RATIO
�K�fet.� . P-(-0— q
PATHOGEN REDUCTION
TEMPERATURE of
DRY TON
VECTOR ATTRACTION REDUCTION
TIME OPERATOR
rii-� 11 -7)
11TlAI
.............. ............ ...................... :..........................................
OPERATIONAL
BELT P KCjj SPEED, o
POLYMER PUMP SPEED,
SLUDGE PUMP SPEED, %
GPM
i LBS/HR b
LIME FEED AUGER, %.
MIXER SPEED, % p ��
22 HRS.
............... ............. ...........:...........:..................................................
POLYMER USAGE
11 1 PF-, USED - ?-2 �-
TANKS MIXED
RS/TANK

TWSA LIME STABILIZATION
DAILY RECORD l
DATE `7 /� / U Al
START STOP TOTAL
.RUN TIME, HRS Sb
1
DRY TON
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDS / PRESS, %. SOLIDS
LiMESLUDGE RATIO '~ JTOTAL PRODUCTION, DRY TONS
PATHOGEN REDUCTION
TFNPPFRATIIRF of
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
ct ` ,,)-
VECTOR ATTRACTION REDUCTION
TIME - OPERATOR
T.
C 2 HRS. 7C
OPERATIONAL
POLYMER PUMP SPEED,
,LUDGE PUMP SPEED, % GPM
LIME FEED AUGER, %. —S LBS/HR `
22 HRS.
POLYMER USAGE
.. e PF i_icF-n J
TANKS MIXED
LITERS/TANK
MIXER SPEED. % %�

TWSA LIME STABILIZATION
DAILY PP:
DATE
T ,T gTC)P TOTAL
RUNTIME, FIRS
SLUDGE FEED, GAL
LIME FEED, LBS
F��
SLUDGE FEED % SOLIDS ' PRESS. °b SOLIDS
TOTAL PRODUCTION, DRY TONS �
UmF_JSLUDGE RATIO
A -c' "o
T f
PATHOGEN
REDUCTION
TEMPERATURE
of
INTO.
OUT OF
TIME VESSEL
VESSEL
OPERATOF
� 1,3E
VECTOR ATTRACTION REDUCTION
TIME
/ 7 :!gITI4_L PH
max. •-� � _ . � I
2 HRS. r r
j. 22 HRS.
.................................................:.........I.....................
OPERATIONAL
D
BELT PR1
ESS SPEED,
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, % GPM (D
LIME FEED AUGER, %. LBS/HR #
OPERATOR
POLYMER USAGE
TYPE USED G
TANKS MIXED f
MIXER SPEED, % ��

vt� W Itt/yt
RUNTIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
PRESS % SOLIDS
SLUDGE FEED °% SOLIDS e
.
TOTAL PRODUCTION, DRY TONS
LIME/SLUDGE RATIO
Lf
TWSA LIME STABILIZATION
DAILY RECORD
DATE
START
I D S�
STOP
i ; .
TOTAL
TON
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TEMPERATURE of
INTO OUT OF TIME OPERATOR
TIME VESSEL VESSEL OPERATOR
I i ' I ( f �-�1 1 it r'�. I �i_ _fY„ i!"fl T i _L PLI i_ - /
2HRS.
Elf
22 HRS.
.....................:.:............
OPERATIONAL POLYMER USAGE
W (TYPE USED`
BELT PRESS SPEED, olo
TANKS MIXED
POLYMER PUMP SPEED, %
,LUDGE PUMP SPEED, % 0 GPM S< <
LIME FEED AUGER, /
J � LITERS/TANK LBS/HR
MIXER SPEED, %

TWSA LIME STABILIZATION
DAi't Y RECORD
DATE 0
START
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
STOP .. .
TOTAL
SLUDGE FEED °h SOLIDS. / PRESS , °%SOLIDS
LIME/SLUDGE RATIO F7:=i, � TOTAL PRODUCTION, DRY TONS �l
PATHOGEN REDUCTION
r�nnoGC7�Tl IPF of
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
J `4
as—
VECTOR ATTRACTION REDUCTION
TIME
OPERATOR
y _ yfj
/Gv
I[VI I IF1L P1-I
'
2 HRS.
22 HRS.
..................... ....................... ....... I ............................................
OPERATION
o>=LI PRESS SPEED, °o
POLYMER PUMP SPEED, %
,LODGE PUMP SPEED, % C'
LIME FEED AUGER, %
MIXER SPEED, % l AO
9ER USAGE -
i

RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
TWSA LIME STABILIZATION
DAILY RECORD
DATE
START STOP TOTAL
ov DRY TON
SLUDGE FEED 0,6 SOLIDS
LIMEJSLUDGE RATIO ,� I
Ln I ��qe�►e� -Temp ��-
PATHOGEN REDUCTION
TEMPERATURE OF
PRESS , °6 SOLIDS
[::::��
TOTAL PRODUCTION, DRY TONS �J
VECTOR ATTRACTION REDUCTION
TIME, OPERATOR
2 HRS.—hy
22 HRS.
I- ............... .......................... 1-1 ......................... ........ ......... .................. I .... ............................................. .............. .......
....................................
................... I........
OPERATIONAL POLYMER USAGE
�0 TANKS MIXED
PE USED ,
n
BELL PRESS SrEEv,
°�
POLYMER PUMP SPEED-Z-- ,
SLUDGE PUMP SPEED, % GPM
6- L 7L
LIME FEED AUGER,
LBS/HR LITERS/TANK
MIXER SPEED, % _ I�

RUNTIME, HRS
SLUDGE FEED, GAL
TWSA LIME STABILIZATION
DAILY RECORD
DATE
START STOP TOTAL
DRY TON
LIME FEED, LBS v
[�����
SLUDGE FEED °h SOLIDS PRESS , °h SOLIDS
a TOTAL PRODUCTION, DRY TONS -
LIME/SLUDGE RATIO r
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
-rrnnr�c�ATi IRG nF
OPERATOR
ii
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
i
I C- 6,3
°f,) q[
i n
/6'sa
Igo
[ sq
e-o
f a g
e-io
'sag/
19�'
o
....................... ..............
%OPERATIONAL
�'I A
RG_i_T DRESS DEED '
POLYMER PUMP SPEED, % v
LUDGE PUMP SPEED, % 3 GPM
LIME FEED AUGER, %LBS/HR
MIXER SPEED, % �_ (h-)_
TIME
6� 8 IAIITIAI 0 �G�O
2 HRS.a 7�
ar
POLYMER USAGE
TYPE USED,
TANKS MIXED
IUTERS/TANK o

TWSA LIME STABILIZATION
DAILY RECORD
START STOP TOTAL
RUN TIME, HRS'
DRY�TON
SLUDGE FEED, GAL Cb
LIME FEED, LBS
F ____J
SLUDGE FEED % SOLIDS Eji:=
PRESS. °b SOLIDS
LIME/SLUDGE RATIO (i TOTAL PRODUCTION, DRY TONS
r�.
ec(
i���j.�.
�-��;��� -per
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TEMPERATURE of
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
nip
I v�!/ I
(�IL
I C� C i
. -
f J t
'co
t �i
TIME
^' i - `'_
<� r
2 HRS_
..........................:.................... :...... ................
.... ................ ...... .... ....................
OPERATIONAL
DELPRESS SPEED, °/-
POLYMER PUMP SPEED,
%
LUDGE PUMP SPEED, % GPM
LIME FEED AUGER, % �LBS/HR
a
MIXER SPEED, %
22 HRS. l
OPERATOR
POLYMER USAGE
TYPE USED �c_
TANKS MIXED
RS/TANK

TWSA LIME STABILIZATION
DAILY RECORD
DATE
START STOP TOTAL
r
RUN TIME, HRS DRY TON
SLUDGE FEED, GAL I /Arm-
�F'
LIME FEED, LBS
SLUDGE FEED % SOLIDS v PRESS. °6 SOLIDS
LIME/SLUDGE RATIO t TOTAL PRODUCTION, DRY TONS
PATHOGEN REDUCTION
-r r_nenCOATI IQP: nF
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
JJ:119b1:
qo
Eo.
m I
........................................................................... .............
]OPERATIONAL
BELT PRESS SPEED °/ / J
POLYMER PUMP SPEED, %
LUDGE PUMP SPEED, % U GPM
LIME FEED AUGER, %
MIXER SPEED, % _I P3J
VECTOR ATTRACTION REDUCTION
TIIjM��E
OPERATOR
r ; 2 HRS. / )l, 1-7/
22 HRS_
POLYMER USAGE
TYPE USED -23 ZC-'-
TANKS MIXED if
S/TAN K

TWSA LIME STABILIZATION
DAILY RECORD
DATE
START STOP TOTAL
RUN TIME, HRS ! CY - TZ
DRY TON
SLUDGE FEED, GAL
LIME FEED. LBS
L� o
SLUDGE FEED % SOLIDS 1 PRESS. °% SOLIDS
LIME/SLUDGE RATIO y TOTAL PRODUCTION, DRY TONS y
ri lei- kesz-�TL'�' i
0 Ile
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
-rt=nnQFRATI IRF nF
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
4b
1 �
� i
RaPf
1 ��
/:r�
TIME
OPERATOR
( gA
y
a !
INI T iAi PH
A7
f �
1
2 HRS.
17
22 HRS. <
�OPERATIONAL
RFI T PRESS SPFFfI
POLYMER PUMP SPEED, %
LUDGE PUMP SPEED, % GPM
LIME FEED AUGER, %. '),,C) LBS/HR V
MIXER SPEED, % /
........................
POLYMER USAGE
TANKS MIXED
SWANK

TWSA LIME STABILIZATION
DAILY RECORD
DATE le -
START STOP TOTAL
RUNTIME, HRS `
DRY TON
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED %SOLIDSF 3 PRESS . °� SOLIDS
LIMEISLUDGE RATIO
♦ TOTAL PRODUCTION, DRY TONS F—A" S
nip `r is �: 5
�t t� ex-keih� g
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
Tz::AiDGRnTI IRF nF
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
1
.r
t--tJ
TIME
f\I[TIA_I ED14 1 i
2 HRS. / �0
22 HRS.
............................. ................. . ...............
OPERATIONAL
r� -r PRESS Jc Pi-�'-'EED, % 1
BCL I t-R�-
POLYMER PUMP SPEED, %�
,LUDGE PUMP SPEED, % GPM r !J I
LIME FEED AUGER, %. �� LBS/HR [�
t
MIXER SPEED, %
OPERATOR
.......................................... . .................
POLYMER USAGE
YPE USED `--
ANKS MIXED
SIT

TWSA LIME STABILIZATION
DAILY RECORD.
DATE
START STOP TOTAL
RUNTIME, HRS F DRYTON
SLUDGE FEEE), GAL
o
LIME FEED, LBS
S PRESS. % SOLIDS[::::::::::�=
SLUDGE FEED 0/- :SOLID
LIME/SLUDGE RAT
IO TOTAL PRODUCTION, DRY TONS
24
PATHOGEN REDUCTION
IPF OF
TIME
INTO
[VES=SEL
OUT OF
VESSEL
OPERATOR
0,3
q- 0
VECTOR ATTRACTION REDUCTION
TIME OPERATOR
-7
!t.JITIAL PH
2,HRS.
22 HRS.
. .............................. ...... ....................... ....... ......... ... ..........................................................................................
OPERATIONAL
SPEED, %-
POLYMER PUMP SPEED, %
;LUDG E PUMP SPEED, % 0 GPM
LIME FEED AUGER, %�M -LBSIHR
MIXER SPEED, % / CL5
POLYMER USAGE
TYPE USELE),
TANKS MIXED
ANK

TWSA LIME STABILIZATION
DA!LY RECORD
DATE -,2� 0
START
.RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
STOP TOTAL
SLUDGE FEED °6 [::::::::��
SOLIDS PRESS. % SOLIDS
LIME/SLUDGE RATIO TOTAL PRODUCTION, DRY TONS I
PATHOGEN REDUCTION
-rcnnoCooTl IRF nF
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
8.115D
18
1
p;sa
! q
1
NJ
oz
DRY TON
VECTOR ATTRACTION REDUCTION
TIME!
'HRS.
1
22 HRS.
............ ........................ .............. :............................ ............. .............. ..........
OPERATIONAL
POLYMER PUMP SPEED, % o
"LUDGE PUMP SPEED, % GPM
LIME FEED AUGER, % LBS/HR o
MIXER SPEED, % /� U
OPERATOR
A
��_
d�r
POLYMER USAGE
! i F-E ijSE i
TANKS MIXED I
�LITERS/TANK

RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
TWSA LIME STABILIZATION
DAILY RECORD
DATE
START STOP TOTAL
abq
SLUDGE FEED °!o SOLIDS t PRESS , °b SOLIDS
TOTAL PRODUCTION, DRY TONS
LIME/SLUDGE RATIO o `
PATHOGEN REDUCTION
rrnnnc�ATl IDf= A
INTO.
VESSELESSEL
UT OFTIME
F
OPERATOR
OPERATIONAL
BELT PRESS SPEED
Liv,
POLYMER PUMP SPEED, % chi
.LUDGE PUMP SPEED,. %l/ GPM S
LIME FEED AUGER, % LBS/HR
MIXER SPEED, % i0o
DRY TON
VECTOR ATTRACTION REDUCTION
TIME /11)
IlTinpw nil
.I .
l 2 HRS.
22 HRS. / L-7f_
OPERATOR
�W, 1
\s}al
E�-
POLYMER USAGE
TYPE PE VSED
,TANKS MIXED
S/TAN K

TVVSA LIME STABILIZATION
DAILY RECORD
DATE
START STOP TOTAL
RUNTIME, HRS 1
DRY TON
SLUDGE FEED, GAL 3 Q�
LIME FEED, LBS C "' / I
SLUDGE FEED 0/- SOUlDS i PRESS. °% SOLIDS
::::�
LIME/SLUDGE RATIO /� l I TOTAL PRODUCTION, DRY TONS '
PATHOGEN REDUCTION
rr nnocooTl IPP: nF
TIME
INTO
VESSEL
OUT OF
OPERATOR
I iv-U�i
i1i I
VESSEL
1
r+N I
'g�
J
Ar
VECTOR ATTRACTION REDUCTION
TIME OPERATOR
IAIITI AI PLI
2 HRS._
L 22 HRS. /Z
.................
.......................... ..... .................................. .....................
........................ ...........
OPERATIONAL
occ r ooccc c�ccn o%
VLL t t I \t_JJ VI LI_V, � ��-
POLYMER PUMP SPEED, %
,LUDGE PUMP SPEED, % GPM
LIME FEED AUGER, % C), LBS/HR
MIXER SPEED, %
POLYMER USAGE
PIT/ rE USED
TANKS MIXED ,
R S/TAN K

TVVSALIME STABILIZATION
DAILY RECORDDATE
S TART
RUN TIME, HRS
SLUDGE FEED, GAL,
LIME FEED, LBS
3T0P TOTAL
PRESS. SOLIDSE:��
SLUDGE FEED SOLID
TOTAL PRODUCTION, DRY TONS
PATHOGLNREDUCTION
TBNPERATUREoF
RATTRACTDN8EDVCTION
'
..OPERATOR
'
`
|N|TIALPH
- 22HR3.
,
f^
�
—.�---------------~'----���_—'
--- �---'-------�----`��--�_--'
N�L '
(}PEPA�lO
BEIJ PRESS SPEED%.%
POLYMER PUMP SPEED, ^& .
LUDGEPUMP SPEED, % G
PM
LBS/UK�EFEE[)AU(�EK. .'
MIXER SPEED.%
........... .................. ...... .................. ........... ..........
POLYMER UjSAGjE::7q
�TANKS MIXED

TVVSA LIME STABILIZATION
DAILY RECORD
DATE '1 I7 0 ��--
START
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
STOP TOTAL
l51
SLUDGE FEED 9/6 SOLIDS
PRESS. °% SOLIDS
E::::==
LiMUSLUDGE RA 710
u I TOTAL PRODUCTION, DRY TONS
J�FT
PATHOGEN REDUCTION
rcenrDr-OAT1 IRF nF
TIME
INTO
VESSEL
OUT OF
VESSEL
oPERA..TnnOR
I 1' C-. t.f 1
I
.................................. ... ......................
OPERATIONAL
BELT ri T PRESS SPEED, °%
DRY TON
VECTOR ATTRACTION REDUCTION
TIME OPERATOR
(� 2 HRS. &
u` �G 22 HRS. A, 66
6
POLYMiER PUMP SPEED, % * 3
,LUDGE PUMP SPEED, % Eo GPM 1 6-
LIME FEED AUGER, % - LBS/HR 6 D
MIXER SPEED, % / d
POLYMER USAGE
IVPF 1 I-,EfI
TANKS MIXED 1
ANK

TWSA LIME STABILIZATION
DAILY RECORD j
DATE 7/ p� �/
—�
START
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
STOP TOTAL
SLUDGE FEED % SOLIDS t PRESS.' SOLIDS
LIMEJSLUDGE RATIO t TOTAL PRODUCTION, DRY TONS
N44W_
PATHOGEN REDUCTION
-rcnAflCDOTI IRG ,P
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
]I /. /l
✓Jib
�/ �:
It
A7
DRY TON
VECTOR ATTRACTION REDUCTION
TIME OPERATOR
rf �� 2 HRS.
�� bd 22HRS_
OPERATIONAL
BELT PRESS SPEED, %
4
POLYMER PUMP SPEED, % 5
;LUDGE PUMP SPEED, % GPM v V
LIME FEED AUGER, %. LBS/HR 0
MIXER SPEED, %
POLYMER USAGE
T'E "."S. ED
I � r yI/---
TANKS MIXED
SITAN

TWSA LIME STABILIZATION.
DAILY RECORD
DATE ,7
START
RUN TIME, HRS
SLUDGE FEED, GAL
STOP TOTAL
DRY TON
LIME FEED, LBS v
SLUDGE FEED °.6 SOLIDS o PRESS. %' SOLIDS
:::�
LIME/SLUDGE RA-f10 TOTAL PRODUCTION, DRY TONS
eCPO
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
rcnnoCDnTI IRG nF
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
i
Ar
TIME
OPERATOR
2 HRS.
22 HRS.
........ ........................................ :........................................... ............ ...........................
OPERATIONAL
BELT t'KCJJ SrnE�Cv, �u
POLYMER PUMP SPEED, % -�
.LUDGE PUMP SPEED, % GPM
LIME FEED AUGER, %. LBS/HR
MIXER SPEED, % i
POLYMER USAGE
TYPE USED,
TANKS MIXED Ilk
ILITERS/TAN

4
TWSA LIME STABILIZATION
DAILY RECORD
DATE
START LSTOP TOTAL
RUN TIME, HRS / t 4 ks L\
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDS PRESS. °h SOLIDS
E:�:�
LIME/SLUDGE PNTIO / TOTAL PRODUCTION, DRY TONS rl
Fr
ed
PATHOGEN REDUCTION
rL-hADr:PLTI IPF nF
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR'
TIME
uT If L IKllTl A 1. OLJ /- /
f fJ --------''
OPERATIONAL
BCI T CPOCCC. CDCCI-1 t;�
LLl
POLYMER PUMP SPEED, %
LUDGE PUMP SPEED, % GPM
LIME FEED AUGER, %. 14LBS/HR�
MIXER SPEED, % .160
2 HRS. &
22 HRS.
DRY TON
VECTOR ATTRACTION REDUCTION
OPERATOR
POLYMER USAGE
^'PE USED ? "C
TANKS MIXED
S/TAN K

TWSA LIME STABILIZATION
DAILY RECORD
DATE
START
RUN TIME, FIRS
SLUDGE FEED, GAL'
STOP TOTAL
DRY TON
LIME FEED, LBS U I I -� 1 1 I `" •�
SLUDGE FEED % SOLIDS F-i , lJ PRESS. °v SOLIDS
LWJSLUDGE RATIO s TOTAL PRODUCTION, DRY TONS ' C •
PATHOGEN REDUCTION
-rr-:e/IDCROTI IRF nF
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
V)
I n1y I
iv
la 1 I
i
S-1 d�
VECTOR ATTRACTION REDUCTION
TIME OPERATOR
G
6 O 2 HRS.
OPERATIONAL
BELT PRESS SPEED
POLYMER PUMP SPEED, % o
`� Q "
LUDGE PUMP SPEED, % GPM -7q
Ll
LIME FEED AUGER,
LBS/HR L /
MIXER SPEED, %
22 HRS-
POLYMER ///� USAGE
I I PE USED 1 , /
TANKS MIXED
ANK

I
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
TWSA LIME STABILIZATION
DAILY RECORD
DATE a� D Z.
-START STOP TOTAL
DRY TON
O a
SLUDGE FEED % SOLIDS �� PRESS. °h SOLIDS
[::::==
LIME/SLUDGE RATIO TOTAL PRODUCTION, DRY TO a
Zn le,
PA-THOGEN REDUCTION
-r-=nnoCooTI IRF nF
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
kr
Sr
kr
VECTOR ATTRACTION REDUCTION
TIME OPERATOR
3(� 2 HRS.
i C1 22 HRS. ��(• ` /� —
........................................................................................................................................
OPERATIONAL
BELT PRESS SPEED "I
POLYMER PUMP SPEED, %
LUDGE PUMP SPEED, %
S GPM d
LIME FEED AUGER, %-
S-5 LBS/HR�s�
POLYMER USAGE
TYPE USED z�
TANKS MIXED
ILITERS/TANK
MIXER SPEED, % / 0 0

i
TWSA LIME STABILIZATION �
DAILY RECORD
1/-
DATE R
- I
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDS f � PRESS. °h SOLIDS
LIME/SLUDGE RATIO TOTAL PRODUCTION, DRY TONS
PATHOGEN REDUCTION
rrn nncr7>ATl IC7 f= nF
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
CU
o
'Pfir
DRY TON
VECTOR ATTRACTION REDUCTION
TIME
OPEJRATOR
w
II I I Ira r,I \'L)
HRS. '
2
"/ ! r� 22 HRS,
............................... ....... .......... :................................
OPERATIONAL
ri I
BELT PRESS SPEED,
POLYMER PUMP SPEED, % 35
SLUDGE PUMP SPEED, % 0 GPM D•
LIME FEED AUGER, %. LBS/HP. ' { S0
MIXER SPEED, %
'POLYMER USAGE
PF I IC F- ��
_ t � —J d'
TANKS MIXED
ANK

c � T
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
I
I
TWSA LIME STABILIZATION
DAILY RECORD
DATE
I
START STOP TOTAL
(/\G
c PRESS , °h SOLIDS
[:����
SLUDGE FEED °h SOLIDS r� G%
LIME/SLUDGE RATIO
TOTAL PRODUCTION, DRY TONS
PATHOGEN REDUCTION
-r�RmDPRATI IRF nF
INTO.
OUT OF
TIME
VESSEL
VESSEL
OPERATOR
/ r
AI /
VECTOR ATTRACTION REDUCTION
TIME
�S 2 HRS_; J�`- "'
p�_ J 22 HRS. �� .
OPERATIONAL
BELT PRESS SPEED, %
I
POLYMER PUMP SPEED, %
,LUDGE PUMP SPEED, % GPM
�j
LIME FEED AUGER, % _LBS/HR lS
MIXER SPEED, % / 00 j
4
OPERATOR
POLYMER USAGE
TYPE USED __ 7� � 7
TANKS MIXED )I 1
ANK

TVVSA LIME STABILIZATION
DAILY RECORD
DATEb
START STOP TOTAL
.RUN TIME, HRS j
DRY TON
SLUDGE FEED, GAL L/ 33 3 Oo +
LIME FEED, LBS
SLUDGE FEED %SOLIDS �O '01O PRESS . °6 SOLIDS
[::::::::::::=
LIME/SLUDGE RATIO TOTAL PRODUCTION, DRY TONS I J
Ln1 e a- 1��.�chec-�l 1e-r� y� �9:1
PATHOGEN REDUCTION
r c"oct:)oTI IRF nF
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
C: z�
PIS
9q
co
lo"t
-7 N�10
171
OPERATIONAL
r� 20
BELT PRESS rr
POLYMER PUMP SPEED, % (�
SLUDGE PUMP SPEED, % V GPM 7
LIME FEED AUGER, %_ LBS/HR
MIXER SPEED, % /J
VECTOR ATTRACTION REDUCTION
TIME OPERATOR
!
q .— 2 HRS. la
-6 0 22 HRS_, �; S /
POLYMER USAGE
c -rvp11c=n
1 1 L
TANKS MIXED

RUN TIME, HIRS
SLUDGE FEED, GAL
LIME FEED, LBS
PRESS. SOLIDS
FEED% SOLIDS
TOTAL PRODUCTION, DRY TONSL.
F.
LimE/SLUDGE RATIO
J.e
VECTOR ATTRACTION REDUCTION
PATHOGEN REDUCTION
TEMPERATURE 0
EM 1. ---1
TVVSA LIME STABILIZATION
DAILY RECORD
DATE
TOTAL
START STOP
L -1`3 ol'
D
DRY TON
TIME
ITIAl l')14 - _lS1
2 HRS. -' k C)
22 HRS-
OPERATOR
. . . ............. ......... . ............ ...... - ..... ................................................
............................
......................... . .................
..................... ............. ... ............
POLYMER USAGE
OPERATIONAL
[TYPE USED
BELL PRESS SPEED,
POLYMER PUMP SPEED, LANKS MIXED
�
p SPEED, % GPM
ILUDGE PUMP LITERSITANK
LIME FEED AUGER, % LBS/HR
MIXER SPEED, %

TWSA LIME STABILIZATION
DAILY RECORD
DATE ta
STO
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDS
Tn - TAL
TOTAL PRODUCTION, DRY TONS
s
LIMEISLUDGE RATIO Q
�49Qc
of e4c� �c� �2 ►v.,
VECTOR ATTRACTION REDUCTION
PATHOGEN REDUCTION
TEMPERATUREoF OPERATOR
INTO. OUT OF TIME
;:"
:J:VESSEL VESSEL OPERATOR
ITiAL 'Pu v
22 HRS. /
l
....................................................................................
..................................... ... POLYMER USAGE
OPERATIONAL
FPE USED .�� a
BELT S'-s- SPEi=D, ,
ANKS MIXED
POLYMER PUMP SPEED, %
LUDGE PUMP SPEED, % LITERS/TANK
LBS/HR
LIME FEED AUGER, %
MIXER SPEED,
100

NCDA Agronomic Division 4300 Reedy Creek Road Raleigh, NC 27607-6465 [phone] Report No: W08170 W
Grower: Tuckaseigee Water & Sewer Copies To:
PO Box 1051
Sylva, NC 28779
4/25/02
Sample Info.
Sample ID:
TWSALR
Waste Code:
Waste Analysis Reffort Farm: TWSA
Jackson County
Laboratory Results (parts per million unless otherwise noted)
N I P K Ca Mg
Total 169 3366 1107 244894 2739
IN -N
-NH4
S Fe
1107 3324
Mn Zn Cu B Mo CI C
163 128 84.4 10.0
MLS
-NO3
Na Ni Cd
Pb
A] Se Li pH
SS C:N
DM% CCE% ALE (tons)
Description:
OR-N
279 2.90 0.28
2.14
11.94
52.27 87.50 2.00
Municipal (Lime Stab.)
Urea
Recommendations:
Nutrients Available for First Crop
lbs/ton (wet basis)
Other Elements
Ibs/ton (wet basis)
Application Method
N PzO5
K20 Ca Mg S Fe
Mn
Zn Cu B . Mo CI
Na Ni
Cd Pb A] Se Li
Broadcast
0.05 4.8
1.1 153.6 1.7 0.69 2.1
0.10
0.08 0.05 0.01
0.29 T
T T
Soil Incorp
0.07 6.0
1.3 192.0 2.2 0.87 2.6
0.13
0.10 0.07 0.01
0.29 T
T T
The waste product has a high neutralizing value
and should only be applied at rates needed to increase soil pH to the desired range. The ALE indicates the amount of the waste required to equal the neutralizing value of
one ton of agricultural lime.