WQ0005763_2003 Annual Report_20040802

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February 5, 2004
DENR/DWQ/Water Quality Section
Non -Discharge Compliance Unit
1617 Mail Service Unit
Raleigh NC 27699-1617
Gentlemen-,
intel) .y ti0p�
OONO mQ��anLe
Enclosed is the Annual Residuals Report for theTuckaseigee Water and Sewer Lime Stabilization
facility (permit #WQ0005763) for the period of January 1, 2003 - December 31, 2003.
Should you have any questions or if I can provide you any additional information, please don't
hPcitate to contact me-
Sincer ly,
Stan Bryson
Wastewater Plant Operations Superintendent
Tuckaseigee Water & Sewer Authority
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1246 West Main St. Sylva, NC 28779 o [phone] o Fax: [phone]

TABLE OF CONTENTS
.(I) REPORTING REQUIREMENTS/PERTINENT INFORMATION
(2) CERTIFICATION
APPENDIX
(a) 2003 sludge data
(b) 2003 distrubution and marketing summary
(c) 2003 laboratory analysis
(d) 2003 lime stabilization record of operation

ANNUAL SEWAGE SLUDGE REPORT
OF
TUCKASEIGEE WATER AND SEWER AUTHORITY
PLANT # 1-NPDES # NCO039578 (WQ0005763)
for the period of January 1, 2003-December 31, 2003
as required by
40 CFR, PART 503
STANDARDS FOR THE USE OR DISPOSAL OF SEWAGE SLUDGE

Y
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
PARAMETER MAXIMUM
Arsenic
<0.87 mg/kg
Cadmium
0.78 mg/kg
Chromium
5.4 mg/kg
Copper
59.0 mg/kg
Lead
5.5 mg/kg
Mercury
0.33 mg/kg
Molybdenum
2.1 mg/kg .
Nickel
3.1 mg/kg
Selenium
<0.3 9 mg/kg
Zinc
120 mg/kg
PART H - PATHOGEN REDUCTION (40 CFR 503 321
X Class A
Class B
PART III - 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 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 6th day of February , 2004.
Stan Bryson, Wastewa r Superintendent

MAR-7-2003 14:35 FROM:
TO:998296319089 P:3/4
ANNUAL PA.TITOGEN AND VECTOR ATTRACTION REDUCTION FORM..
Facili Name: �E'icJ�Y- / W.Permit Number.
WWTP,Naime: NPDLS ,Number: N-C nn s9.5
Monitoring Period: From _ l . To I a
Pathogen Reduction (40 CFR 503.32) - Please indicate level achieved and alternative performed:
MISS A:
Alternative 1Lj
Alternative 2 7-7
Alternative 3 U
Alternative 40 Alternative 5
Alternative 6 ❑
If applicable to alternative performed (Class A only) indicate "Process to Further Reduce :Pathogens":
Compost ��) Heat Drying El
Heat Treatment ❑
Thennophilic L]
Bola Ray ❑
Gamma Rayrl T
Pasteurization
Class B,
Alternative ILi
Ahernat:ive 2 L,;
Ah"native 3 Fl
Zf applicable to alternative performed (Class B only) indicate "Process to Significantly Reduce Pathogens":
Lime Ste+biliration
Aix Drying ❑ composting Li Aerobic Digestion ❑
Anaerobic Digestion❑
Tf applicable to alternative erfaruted (Class A, or Clair B) complete the following monitoring data:
'
Parameter
`
Level in
Pathogen .Density
um cr of
Exoee-
dances
Ercqucncy
of
Analysis
Sample
Type
u. y ict .
tech-
ni ue
Minimu
Geo. Me<3n
aximu
Units'
Fecal Coliform
2 x 1.O ORMe $th
power.WIPN perq
gram of total
solids or 2 x 10 to
the Sth powcr
Cl 7 U per ram of:
I
1000 mp11 per
ram of total solidt(,
weight) -
0
yt f
I Af
yh �r
Q
�7'�ADCj(dry
Salmonella Uoctcn,a
(in liou of fcc&1
coliform)
3 MPN per tl
Erams total solid
(dry weislit)
Vector Attraction Redaction (40 Cfi`R 503.33) - Please 'indicate option performed:
[Option 1. ❑ 10ption2 LJ loption 3 1 1 Option 4 L__l jqption S ❑
IOption 6 JK IOption 7 ❑ I aptian S ❑ 10ption 9 ❑ !Option 10 LJ 1
INo vector attraction reduction options were performed ❑
CERTIFICATION STA.TFi1UNT (please check the appropriate statement)
111.certify, under penalty of law, that the pathogen requirements in 40 CFR. 503.32 and the vector
attraction reduction requirement in 40 C YR 503.33 have been met."
...l "I certify, under penalty of law. that the pathogen requirements in 40 CFR. 503.32 and the vector
att:rnetion 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
sysl:em designed to ensure that qualified personnel properly g:a.ther and evaluate the information
used to determine that the pathogen and vector attraction reduction requirements have.bcen met. I
am aware. that there are significant penalties for false certification including fine and imprisonment."
C�C�1Yl�c��
Prcparcr arne and T'' (type or print)'
Signature. of Preparer
Land Applicr Name and Title (if applicable)(type or print)
�V -
l7 .tic Signatum of Land A,pplier (if applicable)
Pate
tr
Author Daryl D. Merritt. DENR FORM RF (7,2002)

ANNUAL DISTRIBUTION AMID IiARKETING! Sl cE D POS CERI IFICAfiI0i�1 AND 5UhL�1ARY FORtii
PEANUT 3FACILIffY INAME: -
P>3o;ula: �.�s R31� {:CHJNTY� a� �o� oP1EI��TOR:
FACILITY TYPE (please check one):. � Surface DispHal (complete PartA. (Soarce(s) and " . esidual IV Volume only) and. Part C)
Distribution and Marketing (complete Parts A, S, and C)
__ .�._ _� . -e. � 1 ,, v�....9 !J vpe --I No Na if Nn skin Darts A. B. C and certify farm below
was the faculty in operataon uutwg sue PaSWI tiM M..7.,.... ,.q-
Part A*:
Volume (dry lows)
Sources(s) (include NI'DES 9 if Adiooeudmentl
Llionth applicable) Residual Injy0dvet Out
Bulking Agg nt
Part 13*:
Recipi
Information
Names)
a (dam
tuns}
Intended use(s)
January
February —
March
April
Achy
June
July
August
Sept -ember.
Qcto6er
_
November
December
Totals: annual (dry tons):
A men enRa) use
Bu 'Rng Agent(s) u5 :
h eek box if additional shcet(s)
ate attached
ro
0
w
41
M
;u
O
* If more space than given is required, pie attacb addriicanal infirm:ition
Part C:
Facility was compliant during calendar year with all conditions of the permit (including but not limited to items 1-3 below) issued by the
Division of `Pater Quality. � Yes No If No, please provide a written description why the facility was not camptiant. o
1. All, monitoring was done in accordance with the peior it 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 oir, in thte case of deviation, prior authorization was received from tha Division of Water ro
v
Quality,
3. No contravention of Ground Water .Quality Standards occurred at a�monitoring well.
m
"I certify, hider penalty of law, that the above information is, to the best of my knowledge and belief, true, accurate and complete. I am aware
that Ikere are K ifican.t penalties for submitting false i formaitaln, including the possibility of fines and imprisonment for knowing violations."
�~ b
aSignalpre of Pettse Date Signature of Preparer** Date
(if different-imm Permittee) "Preparer is defined in 40 CFR Part 503.9(r) r,
i
Author Daryl D. M mitt DENR FORM DMSOF Vt2002)

2003
Annual Residual Sampling Summary Form
Attach 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: 1) Pace Analytical
Facility Name:Tuckaseigee Water and Sewer Auth. 2) N.C. Dept. of Ag.
NPDES # or 3)
WQ # : NC 0039578 4)
5)
WWTP Name:TWSA Plant # 1
Sample
Date
MMM
M.
T
Molybdenum
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."
Signature of repa r
:!
-)—/, 6 - - /_0
D e
(TWSA Version)
DENR FORM RSSF (7/2002)

Appendix A
2003 SLUDGE DATA

1
APPENDIX A
2003 SLUDGE DATA
TWSA PLANT # 1 (1.5 mgd)
NPDES # NCO039578
SLUDGE TO DIGESTOR.................................................................6,587,400 gallons
total lb s..................................................................... 424,988 lb s
total tons.......................................................................212.49 tons
total metric tons............................................................192.73 metric tons
TWSA PLANT # 2 (.5 mgd)
NPDES # NCO020214
SLUDGE HAULED TO PLANT # 1....................................................... 183,254 gallons
total tons........................................................................ 20.52 tons
total metric tons.............................................................18.6 metric tons
TWSA PLANT # 3 (.1 mgd)
NPDES # NCO063321
SLUDGE HAULED TO PLANT # 1......................................................... 186,540 gallons
totaltons............................................................................ 11.77 tons
total metric tons..............................................................10.67 metric tons
A portion of the sludge that was generated at the Tuckaseigee Water and Sewer Authority during
2003 was hauled by a private contractor to a designated landfill.
Landfill: Macon County Landfill
1448 Lakeside Drive
Franklin NC 28734
A total of 466.74 wet tons were hauled to the landfill during 2003. This does not reflect
residuals that are currently stored onsite.
Copies of haul tickets can be provided if needed.

Appendix B
2003 Distribution
Marketing Summary

APPENDIX B
TWSA PLANT # I
ANNUAL DISTRIBUTION AND MARKETING SUMMARY
2003
PART A
VOLUME IN DRY TONS
MONTH
ADMENDMENT/
RESIDUAL
PRODUCT
BULKING AGENT IN
IN
OUT
January
0
0
0
February
5.05
3.37
8.42
March
4.57
2.6
7.17
April
35.97
22.12
58.09
May
11.49
9.79
21.28
June
11.36
7.79
19.15
- Jul
- 0
0
-0
August
15.17
9.12
24.29
September
24.49
18.77
43.26
October
21.31
14.12
35.43
November
28.8
18.2
47
December
16.961
12
28.96
Annual Dry Tons
175.171
117.88
293.05

APPENDIX B
TWSA PLANT # 1
ANNUAL DISTRIBUTION AND MARKETING SUMMARY
2003
PART B
RECIPIENT INFORMATION
DATE
NAMES
VOLUME wet tons
INTENDED USE
1/9
Chester Sorrells (Waynesville)
27pasture/hay
fields
1/10
Wilbur Passmore S Iva
3.5pasture/hay
fields
1/11
Chester Sorrells (Waynesville)
9
Commercial Hauler
1/13
lChester Sorrells (Waynesville)
9
Commercial Hauler
1/13
Tom Kelley(Webster)
9pasture/hay
fields
1/24
Tom Kelley(Webster)
27pasture/hay
fields
2/18
Verlin B son Cullowhee
6
garden
3/27
Chester Sorrells (Waynesville)
27
Commercial Hauler
3/28
Chester Sorrells (Waynesville)
27
Commercial Hauler
3/31
Philip Ste hens Cullowhee
45pasture/hay
fields
4/2
Chester Sorrells (Waynesville)
18
Commercial Hauler
4/3
Chester Sorrells (Waynesville)
9
Commercial Hauler
4/3
IMark Bell S Iva
9pasture/hay
fields
4/24
lChester Sorrells (Waynesville)
9
Commercial Hauler
5/30
lChester Sorrells (Waynesville)
24
Commercial Hauler
6/10
Chester Sorrells (Waynesville)
21
Commercial Hauler
7/25
Chester Sorrells (Waynesville)
45
Commercial Hauler
8/14
Chester Sorrells (Waynesville)
63
Commercial Hauler
8/28,Andy
Caldwell a nesville
35
Commercial Hauler
9/6
Andy Caldwell (Waynesville)
21
Commercial Hauler
9/7
Andy Caldwell (Waynesville)
35
Commercial Hauler
9/9
Andy Caldwell (Waynesville)
21
Commercial Hauler
9/10
Andy Caldwell a nesville
21
Commercial Hauler
9/19,Bryan
Bum arner hittier
252pasture/hay
fields
10/6
Chester Sorrells (Waynesville)
45
Commercial Hauler
10/7
Chester Sorrells (Waynesville)
45
Commercial Hauler
10/8
Chester Sorrells (Waynesville)
27
Commercial Hauler
10/31
Chester Sorrells (Waynesville)
27
Commercial Hauler
12/31
Phil Wood S Iva
0.5
garden
Total
j 817.5

Appendix C
2003
Laboratory Analysis

,�raceAnalyfical °
www. pacelahs. cam
Solid results are reported on a dry weghi basis
Lab Sample No: 931503155
Client Sample ID: TWSA LIME RESIDUAL:,"
Parameters ' Results Units Report Limit Analyzed By CAS No. Rual RegLmt
Microbiology
Fecal Coliform MPN So_Tid ' Method: SM 922113/E
Coliform, Fecal ND
Metals
Pace Analytical Services, Inc.
2225 Riverside Drive
Asheville, NC 28804
Phone: [phone]
Fax. [phone]
Lab Project Number: 9337455
Client Project ID: TWSA LIME RESIDUAL
Project Sample Number: 9337455-001 Date Collected: 03/12/03 09:20
Matrix: Soil Date Received: 03/12/03 11:00
03/13/03
Metals, ICP'�trace-level
Prep/Method:
EPA 3050
/ EPA 6010
Aluminum'
6200
mg/kg
2200
03/24/03
Arsenic
ND
mg/kg
0.87
03/24/03
-Cadmium
0.78
mg/kg
0.087
03/24/03
Calcium
220000
mg/kg
870
03/24/03
Chromium
5.4
mg/kg
0.43
03/24/03
Copper
59.
mg/kg
0.43
03/24/03
Lead
5.5
mg/kg
0.87
03/24/03
Magnesium
2400
mg/kg
870
03/24/03
Molybdenum
2.1
mg/kg
0.43
03/24/03
Nickel
3.1
mg/kg
0.43 .
03/24/03
Potassium
1900
mg/kg
43.
03/24/03
! ilium
300
mg/kg
22.
03/24/03
zinc
120
mg/kg
1.7
03/24/03
Date Digested
03/19/03
03/19/03
Selenium, AAS Furnace
Prep/Method:
EPA 3050
/ EPA 7740
Selenium
ND
mg/kg
0.39
03/24/03
Date Digested
03/19/03
03/19/03
Wet Chemistry
Percent Moisture Method: % Moisture
Percent Moisture 51.4 %
Total Percent Solids Method: EPA 160.3
Percent Solids 49.0 %
Ammonia, Soil Method: EPA 350.3
Nitrogen, Ammonia 285. mg/kg
Total Kjeldahl Nitrogen, Soil
Nitrogen, Kjeldahl, Total
Date: 03/31/03
Laboratory Certification IN
NC Wastewater 40
NC Drinking Water 37712
Method: EPA 351.2
13700 mg/kg
ACL
EWS 7429-90-5
EWS 7440-38-2
EWS 7440-43-9
EWS 7440-70-2
EWS 7440-47-3
EWS 7440-50-8
EWS 7439-92-1
EWS 7439-95-4
EWS 7439-98-7
EWS 7440-02-0
EWS 7440-09-7
EWS 7440-23-5
EWS 7440-66-6
EWS 7782-49-2
03/18/03 WCB
-03/18/03 WCB
13.6 03/25/03
9.35 03/27/03
ALA 7727-37-9
ALA
REPORT OF LABORATORY ANALYSIS
This report shall not be reproduced, except in full,
without the written consent of Pace Analytical Services, Inc.
tNrGCpq
p ' �..w\cam
u /0t.
Page: 1 of 3
Laboratory Certification IN
TN Drinking Water 02980
SC Environmental 99030

Lab Project Number: 9337455
Pace Analytical Services, Inc.
2225 Riverside Drive
Asheville, NC 28804
Phone: [phone]
FaX [phone]
Client Project ID: TWSA LIME RESIDUAL
ab Sample No: 931503155
Project Sample Number: 9337455-001 Date Collected: 03/12/03 09:20
lient Sample ID: TWSA LIME RESIDUAL;:;:`='``
Matrix:Soil Date Received: 03/12/03 11:00
3ramete
rs =Res_ ul_ t
Units Report Limit Analyzed By CAS— Qual RegLmt
Jitrogen, Nitrate plus NitrMethod: EPA 353.2
Nitrate -Nitrite (as N) ND
mg/kg 6.2 03/26/03 ALA 7727-37-9
'itrogen, Nitrite, S.oi-7'a Method: EPA 354.1
Nitrite as N
ND mg/kg 2.5 03/26/03 ALA
]ant Avail.abl"e Nitrogen Method:
Vitrogenl 4100
mg/kg 1.0 03/31/03 ALA 7727-37-9
Date: 03/31/03
Page: 2 of 3
bOratoN Certification IDs P"EP®RY ®F IABUORAT®RY J�41if�]AL SI� ry Certificati_ on IDS
Wastewater 40 ey Labo�ato
Drinking Water 37712 This report shall not be reproduced, except in full, TN Drinking Water 02980
without the written consent of Pace Analytical Services, Inc. SC Environmental 99030
4W0 � g07y

aweAnalyficaf
/ rvt�itis: pacelsbs�om
fj
Solid results are reported on a dry weight basis
Pace Analytical Services, Inc.
9800 Kincey Avenue, Suile 100
Hunlersville, NC 28078
Phone: [phone]
Far 704.875.9091
Lab Project Number: 9242266
Client Project ID: Tuckaseigee W & S 9337455
Lab Sample No: 931503155
Project Sample
Number: 9242266-001
Date Collected: 03/12/03 09:20
Client Sample ID: TWSA LIME RESIDUAL
Matrix: Soil
Date Received: 03/12/03 11:00
Parameters
Results
Units Report Limit
DE Analyzed
By CAS No. Qual Re4Lmt
Metals
Mercury, CVAAS, in Soil
Method: EPA
7471
Mercury
0.33
mg/kg 0.0083
2.1 03/26/03
LBG 7439-97-6
Wet Chemistry
Percent Moisture
Method: % Moisture
Percent Moisture
49.3
%
1.0 03/13/03 21:09
CDE
Phosphorus, Total, Soil
Method: EPA
365.1 Modified
Phosphorus .
440
mg/kg 20.
19.7 03/21/03
HEH 7723-14-0
Date: 03/26/03
NG Wastewater
fication lDs REPORT OF LABORATORY ANALYSIS Laboratory Water
90
NC Wastewater 12 KY Drinking Water 90090
NC Drinking Water 37706 This report shall not be reproduced, except in full, VA Drinking Water 213
Sc 99006 without the written consent of Pace Analytical Services, Inc. FL NELAP E87627
Page: 1 of 6

lLeAna'lytical
www. pacelabs. coin
,id/results are reported on a dry we
Lab Sample No: 931443147
Client Sample ID: TWSA LIME RESI
Fecal Coliform MPN Soli
Coliform, Fecal
Wet Chemi stryn'
Percent Moisturez
Percent -Moisture
Date: 01/13/03
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: 9335577 Fax.[phone]
Client Project ID: TWSA LIME RESIDUAL
is
Project Sample Number: 9335577-001 Date Collected: 01/02/03 09:10
lALr' Matrix: Soil Date Received: 01/02/03 11:02
^'Y Results Units Report Limit Analyzed By CAS No_ Qual RegLmt
Method: SM 9221B/E
ND O1/08/03 ACL
Method: % Moisture
47.9 X
O1/09/03 DEJ
REPORT OF 'LABORATORY ANALYSIS
This report shall not be reproduced, except in full,
without the written consent of Pace Analytical Services, Inc.
CC AD
N 0
Page: 1 of 2
Laboratory Certification IDs
TN Drinking Water 02980
SC Environmental 99030

Pace Analytical Services, Inc.
2225 Riverside Drive
Asheville, NC 28804
Phone: [phone]
Lab Project Number: 9336647 Fax. [phone]
Client Project ID: TWSA LIME RESIDUAL
Lab Sample No: 931476592 Project Sample Number: 9336647-001 Date Collected: 02/11/03 09:00
Client Sample ID: TWSA LIME RESIDUAL::'' Matrix: Soil Date Received: 02/11/03 13:07
Parameters Results Units Report Limit Analyzed By CAS No
Microbiology "
Fecal Coliform MPN Sol.Method: SM 9221B/E
Coliform, Fecal ND 02/11/03 ACL
Wet Chemist V';
Percent Mois ue Method: X Moisture
PercentMoisture 48.3 X 02/18/03 WCB
Date: 02/21/03
i
Laboratory Certification IDs REPORT OF LABORATORY ANALYSIS
NC Wastewater 40 This report shall not be reproduced, except in full,
NC Drinking Water 37712
FL NELAP E87648 without the written consent of Pace Analytical Services, Inc.
N ♦CC00
Qual RegLmt
Page: 1 of 2
Laboratory Certification IN
TN Drinking Water 02980
SC Environmental. 99030

�IkeAnalyfica
l °
www. pacelahs. com
Solid results are reported on a dry weinh asis
Lab Sample No: 931480412
Client Sample ID: TWSA LIME
Parameters
Microbiology
Fecal Coliform MPN Solid.
Col iform, Fecal
Wet Chemist -"
Percent Moisture
Percent;:Moisture
Date: 02/21/03
r
Laboratory Certification IN
NC Wastewater 40
NC Drinking Water 37712
FL NELAP E87648
Pace Analytical Services, Inc.
2225 Riverside Drive
Asheville, NC 28804
Phone: [phone]
Fax.[phone]
Lab Project Number: 9336752
Client Project ID: COMPOST 2/14
Project Sample Number: 9336752-001 Date Collected: 02/14/U3 IU:UU
11AL'. Matrix: Soil Date Received: 02/14/03 11:08
Results Units Report Limit Analyzed By CAS No. Qua] RegLmt
Method: SM 9221B/E
ND 02/14/03 ACL
Method: % Moisture
48.7 %
02/18/03 WCB
REPORT OF LABORATORY ANALYSIS
This report shall not be reproduced, except in full,
without the written consent of Pace Analytical Services, Inc.
0_t'colR
Page: 1 of 2
Laboratory Certification IDs
TN Drinking Water 02980
SC Environmental 99030

f
Solid results are reported on a dry weigfit.basis
Pace Analytical Services, Inc.
2225 Riverside Drive
Asheville, NC 28804
Phone: [phone]
Fax: [phone]
Lab Project Number: 9337913
Client Project ID: TWSA LIME RESIDUAL
Lab Sample No: 931517650 Project Sample Number: 9337913=001 Date Collected: 03/27/03 08:50
Client Sample ID: TWSA LIME RESIDUAL•.;` Matrix: Soil Date Received: 03/27/03 10:52
Parameters Results Units Report Limit Analyzed By CAS No. Qual RegLmt
Microbiology
Fecal Coliform MPN Solid x` Method: SM,9221B/E
Coliform, Fecal '" ND 03/27/03 ACL
Wet Chemistry.``
Percent MO. Satire
Percent' 16isture
Date: 04/07/03
Laboratory Certification IDs
NC Wastewater 40
NC Drinking Water 37712
Method: % Moisture
49.0 %
04/01/03 WCB
REPORT OF LABORATORY ANALYSIS
This report shall not be reproduced, except in full,
without the written consent of Pace Analytical Services, Inc.
�i'c"
C 07
9
u c i'_
Page: 1 of 2
Laboratory Certification IN
TN Drinking Water 02980
SC Environmental 99030

_IaAnalyfical °
un,mi naralahc rnm
f
Solid results are reported on a dry
sis
Pace Analylical Services, Inc_
2225 Riverside Drive
Asheville, NC 28804
Phone: [phone]
Fax: [phone]
Lab Project Number: 9338238
Client Project'ID: LIME RESIDUAL
:,.r
Lab Sample No: 931529887 ..µs;,; Project Sample Number: 9338238-001 Date Collected: 04/08/03 :00
Client Sample ID: TWSA LIME RESlIUAL Matrix: Soil Date Received: 04/08/03 13:59
Microbiology
Fecal Coliform MPN
Coliform, Fecal
Wet Chemistry'`
Percent t t;sure
I•: , Percent -"Moisture
Date: 04/18/03
Laborato1y Certification IDs
NC Wastewater 40
NC Drinking Water 37712
FL NELAP E87648
Results Units Report Limit Analyzed By CAS No. Qual RegLmt
Method: SM 9221B/E
ND 04/09/03 ACL
Method: % Moisture
48.3 %
04/09/03 WCB
REPORT OF LABORATORY ANALYSIS
This report shall not be reproduced, except in full,
without the written consent of Pace Analytical Services, Inc.
i ACCOR
w
Page: 1 of 2
Laboratory Certification IDs
TN Drinking Water 02980
SC Environmental 99030

':3;=" •-_;;
Pace Analytical Services, Inc.
2225vilver Drive
aceAnal
Asheville, NCC 28804
a �C��o
Phone:[phone]
www.pacelabs.cnm;,;: ='
Fax: [phone]
Lab Project Number: 9339278
Client Project ID: TWSA LIME RESIDUAL
Solid results are reported on a dry weiigFjtbasis
Lab Sample No: 931562565 Project Sample Number: 9339278-001 Date Collected: 05/13/03 09:50
,lient Sample ID: TWSA LIME RESIDUALa Matrix: Soil ' Date Received: 05/13/03 12:57
Microbiology
Fecal Coliform MPN Sol
Coliform, Fecal
Wet Chemistry.,,
Percent MO1S 6t e'
Percent/ Moisture
Date: 05/27/03
Results Units Report Limit Analyzed By CAS No. Qual RegLmt
Method: SM 92216/E
ND 05/14/03 ACL
Mathrrl_ Moisture ;
0 ' 05/21/03 WCB
Laboratory Certification IN 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.
FL NELAP E87648
N AC .09D
�Wr�e�ac
Page: I of 2
Laboratory Certification IDs
TN Drinking Water 02980
SC Environmental 99030

ace Analytical °
. - www.pacelahs.com,
,rid results are reported on a dry wei
is
Pace Analytical Services, Inc.
2225 Riverside Drive
Asheville, NC 28804
Phone: [phone]
Fax: [phone]
Lab Project Number: 9339454
Client Project ID: LIME RESIDUAL
Lab Sample No:
931567457 ";. ` ;' Project Sample
Number: 9339454-001
Date Collected: 05/16/03 11:44
"lient Sample ID:
TWSA LIME RESIDUAL.v'
Matrix: Soil
Date Received: 05/16/03 13:41
Parameters
Results Units Report Limit
Analyzed By
CAS No. Qual RegLmt
Microbiology
Fecal Coliform MPN
Solid w Method: SM 9221B/E
Coliform, Fecal
ND
05/16/03 ACL
Wet Chemists,-j%''
�-- -�
Percent M^ S±Lyre
MethrJd: � Moisture
isture 0 % 05/21/03 WCB
1 � t
Date: 05/27/03
Laboratory Certification IDs
NC Wastewater 40
NC Drinking Water 37712
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.
O•,•qy
� n'dic
Page: I of 2
Laboratory Certification IDs
TN Drinking Water 02980
SC Environmental 99030

ace Analytical
www.pacelabs.com
Solid results are reported on a.dry"w`eight basis
�y
Lab Sample No: 923049282
Client Sample ID: TWSA LIME
Parameters f r`
Microbiology
Fecal Col iform .MPtJSol id
Mn.M�
Coliform, FeF
Wet Cheri�stry
Peril At. Moisture
.r;{Percent Moisture
Date: 06/23/03
P
Laboratory Certification IN
NC Wastewater 40
NC Drinking Water 37712
Pace Analytical Services, Inc,
2225 Riverside Drive
Asheville, NC 28804
Phone: [phone]
Fax: [phone]
Lab Project Number: 9245616
Client Project ID: TWSA LIME RESIDUAL
Project Sample Number: 9245616-001 Date Collected: 06/12/03 08:00
DUAL Matrix: Soil Date Received: 06/12/03 15:00
Results Units Report Limit Analyzed By CAS No. 0ual RegLmt
Method: SM 9221B/E
ND 1 06/13/03 ACL
iiethod: % Moisture
48.4 %
0.6/17/03 09:42 KLH1
REPORT OF LABORATORY ANALYSIS
This report shall not be reproduced, except in full,
without the written consent of Pace Analytical Services, Inc.
M ACCpRO
s
Oy �� f
Vro ��\
Page: 1 of 5
Laboratory Certification IDs
TN Drinking Water 02980
SC Environmental 99030

dceAllai�/�ical °
J`
www.pacelabs.com w
Solid results are reported on a dry'�w0""ght basis
Lab Sample No: 923168405
Client Sample ID: TWSA LIMI f-
Parameters
Microbiology =
Fecal Coliform MP4'2 id
Coliform. Fecal
Wet C emstry
Percent Moisture
Percent Moisture
Date: 08/06/03
Laboratory Certification IDs
NC Wastewater 40
NC Drinking Water 37712
FL NELAP E87648
Pace Analytical Services, Inc.
2225 Riverside Drive
Asheville, NC 28804
Phone. [phone]
Fax: [phone]
Lab Project Number: 9247717
Client Project ID: LIME RESIDUAL
Project Sample Number: 9247717-001 Date Collected: 07/22/03 09:30
DUAL Matrix: Soil Date Received: 07/22/03 13:30
Results Units Report Limit Analyzed By CAS No. Qual RegLmt
Method: SM 9221B/E
ND 07/23/03 ACL
Method: Z Moisture
44.8 %
07/23/03 10:18 KDH
REPORT OF LABORATORY ANALYSIS
This report shall not be reproduced, except in full,
without the written consent of Pace Analytical Services, Inc.
, ACCpq
p D
Page: I of 5
Laboratory Certification IDs
TN Drinking Water 02980
SC Environmental 99030

ace Analytical"
www.pacolahs.com
Solid results are reported on a dry -:Weight basis
Lab Project Number: 9248894
Client Project ID: COMPOST
Pace Analytical Services, Inc.
2225 Riverside Drive
Asheville, NC 28804
Phone: [phone]
Fax: [phone]
Lab Sample No: 923235535 Project Sample Number: 9248894-001 Date Coliectea: uu/ic/ua u7:au
Matrix: Soil Date Received: 08/12/03 14:30
Client Sample ID: TWSA LIME:RESIDUAL
Parameters Results Units Report Limit Analyzed By CAS No. ual Reg
Microbiology
Fecal Coliform MPK Solid Method: SM 9221B/E
Coli form, Fecal'':;: NO 08/12/03 ACL
::
Wet Chemistry
Percent.oisture Method: X Moisture
.R-rcent Moisture 50.1 X 08/13/03 KDH
Page: 1 of 5
Date: 08/25/03
REPORT OF LABORATORY ANALYSIS
Asheville Certification IDs This report shall not be reproduced, except in full, Charlotte Certification IDs
NC Wastewater 40 without the written consent of Pace Analytical Services, Inc. NC Wastewater 12
NC Drinking Water 37712 0..^Cc,, 9 NC Drinking Water 37706
Sc 99006
SC Environmental 99030 FL NELAP E87627
CQ7rAA in MCI AD c �.. a _

Pace Analytical Services, Inc.
2225 Riverside Drive
ace Anal�ical � ,; � Asheville, NC 28804
Phone: [phone]
www.pacelabs.com Fax: [phone]
Lab Project Number: 9249156
r Client Project ID: TWSA LIME RESIDUAL
Solid results are reported on a dry;.-.we'ght basis
Lab Sample No: 923250336 Project Sample Number: 9249156-001 Date Collected: 08/15/03 09:30
Client Sample ID: TWSA LIME.:RESIDUAL Matrix: Soil Date Received: 08/15/03 11:53
Parameters Results Units Report Limit Analyzed By AS No. ual RegLmt
Microbiology
Fecal Coliform MP14 Solid Method: SM 9221B/E
Coliform, Fecal..<.,"' ND 08/15/03 ACL
Wet Chemistry
Percent'Moisture Method: % Moisture
Percent Moisture 50.6 % 08/20/03 14:35 WRC
Date: 08/25/03
Asheville Certification IDS
NC Wastewater
40
NC Drinking Water
37712
SC Environmental
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.
H nt�pg0
°nelk
Page: 1 of 5
Charlotte Certification IDs
NC Wastewater 12
NC Drinking Water 37706
SC 99006
FL NELAP E87627

Analytical
www.pacelabs.com
esults are reported on a dry weight basis
Pace Analytical Services, Inc.
2225 Riverside Drive
Asheville, NC 28804
Phone: [phone]
Fax [phone]
Lab Project Number: 9251346
Client Project ID: TWSA LIME RESIDUAL
Sample No: 923373286
...
Project Sample Number: 9251346 001
Date Collected: 09/25/03 09:00
ient Sample ID: TWSA LIME,
RESIDUAL
Matrix: Soil
Date Received: 09/25/03 12:05
Parameters
Results Units
Resort Limit Analyzed By
CAS No. Qual RegLmt
Microbiology
Fecal Coliform MPN'Solid
Method: SM 9221B/E
Coliform, Fecal
ND
09/25/03 ACL
Wet Chemistry
Percent Moisture
Method: X Moisture
Percent Moisture
52.4 %
09/26/03 12:40 WRC
Total Percent Solids
Percent Solids
Date: 10/08/03
yr
Asheville Certification IDs
NC Wastewater 40
NC Drinking Water 37712
SC Environmental 99030
Method: EPA 160.3
47.6 %
09/30/03 WRC
REPORT OF LABORATORY ANALYSIS
This report shall not be reproduced, except in full,
without the written consent of Pace Analytical Services, Inc.
\N AC�OgD
,nj'i '
Page: 1 of 6
Charlotte Certification IN
NC Wastewater 12
NC Drinking Water 37706
SC 99006
n Alrl nn C07C07

lci Analytical °
www.pacelabs.com
Pace Analytical Services, Inc.
2225 Riverside Drive
Asheville, NC 28804
Phone: [phone]
Fax: [phone]
Lab Project Number: 9251988
Client Project ID: TWSA LIME RESIDUAL
Solid results are reported on a dry weight basis
Lab Sample No: 923408835 Project Sample Number: 9251988-001 Date Collected: 10/07/03 09:00
Client Sample ID: TWSA LIME .,RESIDUAL Matrix: Soil Date Received: 10/07/03 13:24
Parameters
Results Units
Report Limit Analyzed
By CAS No. Qua] RegLmt
Microbiology
Fecal Coliform MFN,Splid
Method: SM 9221B/E
Coliform, Fecal"
ND
10/08/03
ACL
Wet Chemistry
Percen-tA'oisture
Method: % Moisture
-Percent Moisture
52.8 %
10/08/03
09:03 WRC
:. Total Percent Solids
Method: EPA 160.3
Percent Solids
47.2 X
10/09/03
WRC
Date: 10/15/03
Asheville Certification IDs
NC Wastewater
40
NC Drinking Water
37712
SC Environmental
ri niri An
99030
r0-7ce0
REPORT OF LABORATORY ANALYSIS
This report shall not be reproduced, except in full,
without the written consent of Pace Analytical Services, Inc.
iACtpga
Ep ,9 C
Page: 1 of 6
Charlotte Certification IDs
NC Wastewater 12
NC Drinking Water 37706
SC 99006
FI NFI AP P97627

0
I
Solid results are reported on a
Lab Sample No: 923546345
Client Sample ID: TWSA LIME
r»
Parameters
Microbiology
Fecal Coliform MP.N Solid
Coliform, FecaT;,
' 4
<«i""
Wet Chem` � iiry
Periy-roisture
.„Percent Moisture
Total Percent Solids
Percent Solids
Date: 12/01/03
Laboratory Certification IDs
NC Wastewater 40
NC Drinking Water 37712
FL NELAP E87648
Pace Analytical Services, Inc.
2225 Riverside Drive
Asheville, NC 28804
Phone: [phone]
Fax. [phone]
Lab Project Number: 9254320
Client Project ID: LIME RESIDUAL
basis
Project Sample
Number: 9254320-001
Date Collected: 11l18/03 lU:UU
UAL
Matrix: Soil
Date Received: 11/18/03 15:06
Results
Units Report Limit
Analyzed By
CAS No: Qua] RegLmt
Method: SM
9221B/E
ND
11/18/03 MMG
Method: % Moisture
49.9 %
Method: EPA 160.3
46.9 %
11/19/03 15:02 SWB
11/25/03 KHJ
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 6
Laboratory Certification IDs
TN Drinking Water 02980
SC Environmental 99030

T �alYtical
N° p
www.pacelabs.com
Solid results are reported on a d,,,:, ght basis
Lab Sample No: 923563696
Client Sample ID:.TWSA LIME.
Parameters #'
Microbiology :7
Fecal Col i form MPN�'t ".1d
Coliform,
Wet Chemistry
Perceni^`Moisture
Percent Moisture
Total Percent Solids
Percent Solids
Date: 12/02/03
Laboratory Certification IDs
NC Wastewater 40
NC Drinking Water 37712
FL NELAP E87648
Pace Analytical Services, Inc.
2225 Riverside Drive
Asheville, NC 28804
Phone: [phone]
Fax: [phone]
Lab Project Number: 9254647
Client Project ID: LIME RESIDUAL
Project Sample Number: 9254647-001 Date Collected: 11/21/03 10:00
iOAL Matrix: Soil Date Received: 11/21/03 13:52
Results Units Report Limit Analyzed By CAS No. Qual RegLmt
Method: SM 9221B/E
ND 11/21/03 MMG
Method: X Moisture
54.2 %
Method: EPA 160.3
50.3 %
12/01/03 13:05 KDF
11/25/03 KHJ
REPORT OF LABORATORY ANALYSIS
This report shall not be reproduced, except in full,
without the written consent of Pace Analytical Services, Inc.
:K RGC-pq
O/
Page: 1 of 6
Laboratory Certification IDs
TN Drinking Water 02980
SC Environmental 99030

aceAnalytical °
www.pacelabs.com
Solid results are reported on a dry weight basis
Pace Analytical Services, Inc.
9800 Kincey Avenue, Suite 100
Huntersville, NC 28078
Phone: [phone]
Fax: [phone]
Lab Project Number: 9255126
Client Project ID: LIME RESIDUAL
Lab Sample No: 923593628 Project Sample Number: 9255126-001 Date Collected: 12/03/03 09:10
Client Sample ID: TWSA LIME RESIDUAL Matrix: Soil Date Received: 12/03/03 15:02
Parameters Results Units Report Limit Analyzed By CAS No. Qual RegLmt
Microbiology
Fecal Coliform MPN.Solid Method: SM 9221BIE
Coliform, Fecal NO 12/03/03 MMG
Wet Chemistry
Percent Moisture
Percent Moisture
Total Percent Solids
Percent Solids
Date: 12/10/03
Asheville Certification IDs
NC Wastewater 40
NC Drinking Water 37712
SC Environmental 99030
Method: ro Moisture
45.6 1/
Method: EPA 160.3
55.8 x
12/08/03 11:01 DDA
12/06/03 KHJ
REPORT OF LABORATORY ANALYSIS
This report shall not be reproduced, except in full,
without the written consent of Pace Analytical Services, Inc.
N ACCORa'
Page: 1 of 6
Charlotte Certification IDs
NC Wastewater
12
NC Drinking Water
37706
SC
99006
[I MEJ AD
CQ7997

Appendix D
2003
Lime Stabilization
Record of Operation

TWSA LIME STABILIZATION
DAILY RECORD
W
DATE J
START STOP TOTAL
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
B
SLUDGE FEED % SOLIDS /� PRESS , °% SOLIDS
LIME/SLUDGE RATIO 1 51, TOTAL PRODUCTION, DRY TONS �. l
jeu
PATHOGEN REDUCTION
TFAAPP:PATI IPF nF
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
It) 50
IQLL
L)
p-aCo
ISO
ir
DRY TON
.J.
VECTOR ATTRACTION REDUCTION
TIME OPERATOR
INITIAL PH
2 HRS.
22 HRS. �.
............................................................................................................................................................................................
OPERATIONAL
BELT PRESS SPEED, % `
POLYMER PUMP SPEED, % -30
>'LUDGE PUMP SPEED, % 5.5 GPM
LIME FEED .AUGER, %. LBS/HRy ��
MIXER SPEED, % / o
POLYMER USAGE
TYPE USED C
TANKS MIXED
LITERS/TANK ( O
IF v
I�

TWSA LIME STABILIZATION
DAILY RECORD
DATE
START STOP TOTAL -
RUNTIME, HRS lie,
DRY TON
SLUDGE FEED, GAL O 7
LIME FEED, LBS .973
07
SLUDGE FEED °h SOLIDS
PRESS. °% SOLIDS
LIME/SLUDGE RATIO I' TOTAL PRODUCTION, DRY TONS o
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
r�nnDG[7eT1 IRF of
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
a5 I
to -1170
TIME OPERATOR
INI'I IAL PH
(� 1� 2 HRS.
22 HRS.
..........I ......... ........ ................. :............. ................................ I.........................................................
OPERATIONAL POLYMER USAGE
BELT PRESS SPEED, % �. 1 PE USED 3 6L C
POLYMER PUMP SPEED, % J TANKS MIXED
,LUDGE PUMP SPEED, % GPM 3 '
LIME FEED AUGER, %_ LBS/HR
MIXER SPEED, %
JLITERS/TANK_
3Clz ° = q• � -
c C�- % G�

RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDS
LIMEISLUDGE RATIO
TWSA LIME STABILIZATION
DAILY RECORD
DATE ✓ L
PRESS, % SOLIDS
TOTAL PRODUCTION, DRY TONS
PATHOGEN REDUCTION
Tl=hA0C:DATl IRi= nF
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
IQ��`� I�
q I �►
I s�' ,
�� I
43,
3< .
o�
DRY TON
VECTOR ATTRACTION REDUCTION
TIME oar_' j?7 OPERATOR
INITIAL PH
.O6 2HRS_
22 HRS_
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, % T�
SLUDGE PUMP SPEED, %j) GPM �
LIME FEED AUGER, % N 3 LBS/HR 4� t
...........................................
POLYMER USAGE
YPE USED _ o
ANKS MIXED y
JLITERS/TANK__(12
MIXER SPEED, %

TWSA LIME STABILIZATION
DAILY RECORD �J
DATE C o '
START STOP TOTAL'
.RUN.TIME, HRS 0-0
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOUD3 f
LIME/SLUDGE RATIO a
lei Peo c-ke 9 n 4
PATHOGEN REDUCTION
r�nnoG[�eTl IRF nF
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
q-z6s.—
PRESS, % SOLIDS
TOTAL PRODUCTION, DRY TONS m ✓
DRY TON
w
VECTOR ATTRACTION REDUCTION
03 1y.C? .
TIME OPERATOR
3- INITIAL PH
163
'7J 2 HRS.
�J r 22 HRS__ d.
OPERATIONAL
BELT PRESS SPEED, % 33
POLYMER PUMP SPEED, % 3-5
,LUDGE PUMP SPEED, % 12 GPM
LIME FEED AUGER, % a3 LBS/HR
MIXER SPEED, / o 0 !973
POLYMER USAGE
YPE USEDJ5_2 Q_
ANKS MIXED l

( TWSA LIME STABILIZATION
DAILY RECORD 2
DATEho
�J
START STOP TOTAL
RUNTIME, HRS a ,' DRY TON
SLUDGE FEED, GAL
�0d.10,
a�
LIME FEED, LBS
SLUDGE FEED % SOLIDS '
LIME/SLUDGE RATIO • �/
04
PATHOGEN
REDUCTION
TEMPERATURE
of
INTO
TIME VVESSEL
OUT OF
VESSEL
OPERATOR
3' 1315-
l io
, sj- t o I
I
l W�l
PRESS, % SOLIDS
[����
TOTAL PRODUCTION, DRY TONS
VECTOR ATTRACTION IZ EDUCTION
:03 3,)) = , or 76
TIME OPERATOR
it'd L� _
17
1
.17
(p( r 2 HRS. %
!L_ 22 HRS-
...................................
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, % 1
W5 3
SLUDGE PUMP SPEED, % GPM
o 1,4 1-j LBSiHR X
LIME FEED AUGER, /o
MIXER SPEED. % CDO C1 Lfn G

RUN TIME, HRS
"�4j,)�
Ti AS
TWSA LIME STABILIZATION lie 1')
DAILY RECORD
%
DATE
START STOP TOTAL
:30 z/o !
DRY TON
SLUDGE FEED, GAL
3
LIME FEED, LBS
SLUDGE FEED % SOLIDS
PRESS. %SOLIDS
TOTAL PRODUCTION, DRY TONS F-2. R 1
LIME/SLUDGE RATIO c
PATHOGEN REDUCTION
TEMPERATURE OF
VECTOR ATTRAC ION REDUCTION
TIME
,�,�-./oar /a-�
OPERATOR
' aV
PH //
J
INITIAL
1a 5
2 HRS. .
I_eT
HRS_
22
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, % ` l�
SLUDGE PUMP SPEED, % r GPM
LIME FEED AUGER, % 15 _LBS/HR
MIXER SPEED, % %
POLYMER USAGE
TYPE USED U-'Z C-
TANKS MIXED lLI
�LITERS,'TANK VWQ
(Qy E ���� 'Wok

t
TWSA LIME STABILIZATION
DAILY RECORD n
DATE
START STOP TOTAL
.RUN TIME, HRS c) I
DRY TON
SLUDGE FEED, GAL �oOF.
o
LIME FEED, LBS. F7-
SLUDGE FEED % SOLIDS PRESS. °%SOLIDS
LIME/SLUDGE RATIO �� 1- TOTAL PRODUCTION, DRY TO
PA-THOGEN REDUCTION
-r=nnpFRATI JRF of
INTO
TIME VESSEL
OUT OF
VESSEL
OPERATOR
e'o
..................
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, %
.LUDGE PUMP SPEED, % GPM
LIME FEED AUGER, % t419 _LBS/HR
MIXER SPEED, %
VECTOR ATTRACTIQN REDUCTION
TIME ��(�_`��=r>-S� OPERATOR
c�J - INITIAL PH—
r03 (as.-
30
r Jar .11 4 '`
2 HRS"
22 HRS. I ��
.........................................................................................
POLYMER USAGE
PE USED 33 a C-
TANKS MIXED
LITERS/TANK
iibe. = ib,t- '�14
Rh; y bbs

TWSA LIME STABILIZATION
DAILY RECORD
DATE 14
START STOP TOTAL
RUN TIME, HRS V'
DRY TON
SLUDGE FEED, GAL "" 11
LIME FEED, LBS I �J�
[::::::::::=
SLUDGE FEED 0/6SOLIDS � � � PRESS , % SOLIDS
LIME/SLUDGE RATIO
® TOTAL PRODUCTION, DRY TONS�-
PATHOGEN
REDUCTION
VECTOR ATTRACTION REDUCTION
TIME
TEMPERATURE
INTO
VESSEL
of
OUT OF
VESSEL
OPERATOR
�o3Cs -/��)
,c3k�u` a'1 ;
TIME 1� ,i55-
OPERATOR
A•15 �
I �� I
1�(� I
� I
`77
�•J� ItVI11ALPi-i
ego
:.��
L
—3 2 HRS. %t
% c�
3 c�36 22 FIRS: � �^
711
1�
...............................................:............. .....................
................... 1-1 ..............................................................
OPERATIONAL
BELT PRESS SPEED, % J
POLYMER PUMP SPEED, % L
,LUDGE PUMP SPEED, % GPM
LIME FEED AUGER, % "Z LBSiHR
MIXER SPEED, % r�
POLYMER
USAGE
TYPE USED �
TANKS MIXED
[LITERS/TANK
--- I I Q 3 1

TWSA LIME STABILIZATION
DAILY RECORD
DATES O
START STOP TOTAL
RUN TIME, HRS f `�
DRY TON
SLUDGE FEED, GAL I
6d6
LIME FEED, LBS
PRESS, % SOLIDS
SOLIDS °
[:::::��
SLUDGE FEED %
TONS 6
LIME/SLUDGE RATIO a 0 TOTAL PRODUCTION, DRY
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TEMPERATURE of
OUT OF .
INTO TIME
`�G�
OPERATOR
TIME VESSEL VESSEL OPERATOR
! 1 ✓ V� f "' U lV I �
INITIAL PH
I
co
�s a
'r
.63=�3
1-7
22 HRS.
%T� 6,�
OPERATIONAL
POLYMER OSAGE
PE USED
BELT PRESS SPEED, %
POLYMER PUMP SPEED, % `
TANKS MIXED
,LUDGE PUMP SPEED, % GPM
LIME FEED AUGER, % LSS/HR
LITERS/TANK
MIXER SPEED, % ��
, r, 0 y? / 61c

RUN-TIME, HRS
SLUDGE FEED, GAL
TWSA LIME STABILIZATION
DAILY RECORD/
DATE
START STOP TOTAL DRY TON
LIME FEED, LBS I �03
[:::::::��
SLUDGE FEED 0/6 SOLID S
e (c PRESS. % SOLIDS
LIME/SLUDGE RATIO •O TOTAL PRODUCTION, DRY TONS °.
vn ed I ,e 41��q
'
PATHOGEN
REDUCTION
TEMPERATURE
of
INTO
TIME VESSEL
OUT OF
VESSEL
OPERATOR
I
ISM' ,
Z ,
VECTOR ATTRACTION REDUCTION
:v3(5"7) • r -t 1
TIME !�•(��, i7/- ld�� OPERATOR
INI T iAL PHa- �.
dl�� 2 HRS. •�.
............................................
OPERATIONAL
30
BELT PRESS SPEED, %
POLYMER PUMP SPEED, %Ld
,LUDGE PUMP SPEED, % 5n GPM 5I- V D
LIME FEED AUGER, % '� LBS/NR%
MIXER SPEED, % . /do
22 HRS. a ►�
,03
03 <,e.0 ,17g
POLYMER USAGE
TYPE USED : �C_
TANKS MIXED
LITERS/TANK Lf"9
d5-Px9= ilb,s

TWSA LIME STABILIZATION
DAILY RECORD
DATE
do
START
STOP,! -36
TOTAL
I ` L4
RUNTIME, HRS
DRY TON
SLUDGE FEED, GAL
D
LIME FEED, LBS
SLUDGE FEED % SOLIDS e
PRESS. % SOLIDS [:::::::
+ TOTAL PRODUCTION, DRY TONS
LIME/SLUDGE RATIO
--r�wv'd a5
PATHOGEN REDUCTION
VECTOR ATTRACTION REDUCTION
TEMPERATURE of
.03
INTO OUT OF
TIME VESSEL VESSEL OPERATOR
TIME
1p
!�
OPERATOR
-7 l
8' I ° I `'. � I �� 1
r !!,,
to
&
INITIAL PH l�
a:3 z.�
�� 1
2 HRS_ ,
--��
Ja .o
z..
o� 4
&' kO
/r��if
22 HRS_ 0
!
�Loq 7
� vo
OPERATIONAL
BELT PRESS SPEED, % 3
POLYMER PUMP SPEED, % 0-5
LUDGE PUMP SPEED,
GPM
LIME FEED AUGER, % 0 LBS/HR �5 a
MIXER SPEED, % 100.
POLYMER USAGE
TYPE USED, �3 a C,
TANKS MIXED
S/TANK
= I14,3 1105

,2 o. a B- Tow s, 4v
TWSA LIME STABILIZATION
DAILY RECORD
DATE I ®` b
START STOP TOTAL
0
RUNTIME, HRS Ek -DRY TON
SLUDGE FEED, GAL
-7 9'7&0
LIME FEED, LBS
SLUDGE FEED % SOLID PRESS, % SOLIDS[
TOTAL PRODUCTION, DRY TONS
LIME/SLUDGE RATIO
e4
-eq c k e
PATHOGEN REDUCTION
VECTOR ATTRACTION REDUCTION
TEMPERATURE of
'.OPERATOR'
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR_
TIME
nr)
)&oo
I 1 ��7
I
54
C-ij
!N!Ti AL PH Av
10 r\
2 HRS.`
A
, '06
Al
'M HRS_
—1
IS 22
103 ) i
k_
............. ................. ............. .................................. ... ............ ...................................................
OPERATIONAL
20
BELT PRESS SPEED, %
POLYMER PUMP SPEED, % -
.LUDG EPuMPSPEED,—GPM
LIME FEED AUGER, %_ _LBSlHR___VL3_1_
MIXER SPEED, %= It) 0
POLYMER OSAGE
TYPE USED,
_
TANKS MIXED It
[LITERS/TANK
&tb :7- ) � "D, rlL
V5,9 1105

/ 4-D d
TWSA LIME STABILIZATION
DAILY RECORD f
DATE
START STOP TOTAL
RUN.TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
�. PRESS. % SOLIDS
SLUDGE FEED %SGLiCS � Q'
[:::::����
LIMElSLUDGE RATIO i TOTAL PRODUCTION, DRY TONS v o164
PATHOGEN REDUCTION
TEMPERATURE of
DRY TON
q,. g
VECTOR ATTRACTION REDUCTION
TIME �.�, d 6 = ��1
a{
OPERATOR
-�� iNiTiAL PH�
l�3611,- �(?
2 HRS_- �
i,
22 HRS.
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, % GPM / 0//(
LIME FEED AUGER, % d LBS/HR
POLYMER USAGE
TYPE USED�� oC
TANKS MIXED
�LITERSITANK 6
MIXER SPEED, % % n 0-

TWSA LIME STABILIZATION
DAILY RECORD
DATE
START STOP TOTAL
RUIN.TIME, HRS o op DRY DRY TON
SLUDGE FEED, GAL
LIME FEED, LBS
PRESS, °h SOLIDS
[����
SLUDGE FEED % SOLIDS
®� TOTAL PRODUCTION, DRY TONS
LIME/SLUDGE RATIO c
PATHOGEN REDUCTION
TEMPERATURE of
INTO OUT OF
TIME VESSEL VESSEL OPERATOR
�g3
r
6'6aI 14�3
VECTOR ATTRACTION REDUCTION
3 �.S- '�2. • ��
c
TIME
t
l�J INITIAL PH I(�"
,63i�s=�1�.
=�
2 HRS. t.5
�
-
22 HR ,
.... .....
OPERATIONAL
b
BELT PRESS SPEED, %
POLYMER PUMP SPEED, % `� 6
o � GPM
->LUDGE PUMP SPEED, /o
LIME FEED AUGER, % � _LBS/HR �-
M1XFR SPEED, % / i!� V
OPERATOR
POLYMER USAGE
TYPE USED S3
TANKS MIXED
LITERS/T
p= I-ct .
'71a/ l�

TWSA LIME STABILIZATION
DAILY RECORD
DATE
START STOP TOTAL
.RUN TIME, HRS DRY TON
. . SLUDGE FEED, GAL
LIME FEED, LE3S
SLUDGE FEED'% SOLID PRESS, % SOLIDS
TOTAL PRODUCTION, DRY TONS
LIME/SLUDGE RATIO
55
A R vve� Te VI,,
vcv
PATHOGEN REDUCTION VECTOR ATTRACT ON REDUCTION
I. TEMPERATURE of 6-7),
INTO OUT OF OPERATOR
VE
SSEL
L TIME -7X
TIME VESSEL VESSEL OPERATOR
Fi,M =E 00 Ao'
2130 iNiTiAL
PH
ql, o Icy
,
.......................... I .................... ...............................
POLYMER USAGE
TYPE USED
TANKS MIXED
LITERS/TANK Le ------- J
1p,9 x "i (119lyk
�
laA.%r P
o 2 HRS-
22 HRS.
..
................ . ....................................... ............. -- .. ........... ..................... I .................................
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, % 4o GPM ld
')
LIME FEED AUGER, % LBS/HR
MIXER SPEED, % / ) if�

r
TWSA LIME STABILIZATION
DAILY RECORD
DATE .. /(G1 o 3
START STOP TOTAL
RUNTIME, HRS ` v `-' ` - °"'
'DRY TON
SLUDGE FEED, GAL
:5.��
LIME FEED, LBS
[����
SLUDGE FEED 0/6 SOLIDS ° PRESS. % SOLIDS
e TOTAL PRODUCTION, DRY TONS
LIME/SLUDGE RATIO /
(red �c'ac�.e:N� %�'-�""� zn vi:::]
��
01 �J
PATHOGEN REDUCTION
TEMPERATURE of
INTO OUT OF
TIME VESSEL VESSEL op
Id,,3,5 dCo
1.3 14 J
33
T
cf)
VECTOR ATTRACTION REDUCTION
.. t}3 C.s'�= o �Y
TIME / J OPERATOR
l!�(��•°OdY� !�
�ta INITIAL PH lx'IQ
.................... .
................................. 11 ........ , .................. ­1 ...................
OPERATIONAL
BELT PRESS SPEED, % :3 0
POLYMER PUMP SPEED, %_ 60
SLUDGE PUMP SPEED, % go GPM 3 5, �
LIME FEED AUGER, %. LBS/HRS
MIXER SPEED, % f/ d
2�HRS_
3 = 7
03( 7) .veld %
22 HRS_ X-
POLYMER USAGE '�-
YPE USED 1331a Q- p p
ANKS MIXED .
_ITERS/TANK '
30 3.'7 9
� / / No

JAW
TWSA LIME STABILIZATION
DAILY RECORD
DATE
START STOP TOTAL
RUN TIME, HRS 0 v v `— DRY TON
SLUDGE FEED, GAL
LIME FEED, LBS
I PRESS, % SOLIDS
[:::����
SLUDGE FEED 01, SOLIDS u
LIME/SLUDGE RATIO
m .6� TOTAL PRODUCTION, DRY TONS 1
C
PA-THOGEN REDUCTION
TEMPERATURE of
INTO
OUT OF
TIME
VESSEL
VESSEL OPERATO
�; a-
, l ��
, I.s� ,
1 jooa
F-If�1�'�r"��
r
VECTOR ATTRACTION REDUCTION
` 03 2f �� 3 = W?
TIME f , Qg% z A.� OPERATOR
31 INITi'AL PH I1 �
2 HRS. 'a
s�� x +'. 1,, =�.
22 HRS_
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, % GPM
LIME FEED AUGER, % r 1 LBS/HR g
MIXER SPEED, % 1 e7 O%
'POLYMER USAGE
PE USED slM,__—_
TANKS MIXED
,LITERS/TANK lY
§-)/`S 78-� f `f., atQ °� K
inQ- IL,

TWSA LIME STABILIZATION
DAILY RECORD `
DATE
START STOP TOTAL
RUN TIME, HRS DRY TON
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLID ` PRESS. °6 SOLIDS
LIME/SLUDGE RATIO ' TOTAL PRODUCTION, DRY TONS
PATHOGEN REDUCTION VECTOR ATTRACTION R DUCTION
TURE of
TEMPERA
INTO OUT OF a�� 9 ` OPERATOR
TIME VESSEL VESSEL OPERATOR TIME i •1 S -� ��,�{-�
INITU?.LPH ,�A
,3 2 HRS. _ ,, O
�3� ���. � � ,�(a.�=a�•��—fig
"1Cof 22 HRSI"
.........................................
OPERATIONAL POLYMER USAGE
SPEED % �cJ
BELT PRESS PE USED
MIXED
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, % GPM
44-
� � � �ir s
LIME FEED AUGER, %. 'LBS/HR
MIXER SPEED, % !�" 3?&� T

'
,
TVV3ALIME STABILIZATION
. DAILYRECORD
` DATE �
START STOP TOTAL
RIUN.TIME, HIRS -DRY TON
SLUDGE FEED, GAL 31,100
LIME FEED, LBS
PRESS SOLIDSF__
SLUDGE FEED % SOLID
LIME/SLUDGE* RATIO F7== TOTAL PRODUCTION, DRY TONS
'
`
' VECTOR REDUCTION
PATHOGEN QEDDCTDJ0 , ,,..^`,...~.,
rcixo=puT—
mFoF �
INTO OUT OF
TIME VESSEL VESSEL OPERATOR_
,
TIMEOPERATOR
�
� INITIAL PH
`
2HRS.
�
�
22HRS.
'---'-----'-----_-----_'-_
--'---_—'_--_.`------'----'-----_---_--------��--'--'`--_' . .
OPERATIONAL
POLYMER USAGE
TYPE USEDBELT PRESS SPEED, %
�
TANKS MIXED
POLYMER PUMP SPEED, %
�LUDGEPUMP SPEED, % GP
LBS/HR_ LITERS/TAN
LIME FEED AUGER, �F ';o y
MIXER SPEED, %

TWSA LIME STABILIZATION
DAILY RECORD
DATE
START STOP TOTAL
C'o®
RUNTIME, HRS 15' R
DRY TON
F
3�
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED °% SOLIDS u
PRESS, % SOLIDS [:::::��
TOTAL PRODUCTION, DRY TONS
LIMElSLUDGE RATIO
PATHOGEN REDUCTION
VECTOR ATTRACTION REDUCTION
-rlznnpT7-RATURE of
TIME OPERATOR
lNlTiAL PH
2 HRS.
22 HRS-
.............. : ---------
_.
OPERATIONAL
BELT PRESS SPEED,
POLYMER PUMP SPEED, % /
.SLUDGE PUMP SPEED, % -7� GPM
o/ LBS/HR
LIME FEED AUGER, o.
!� /. L 7� l
kAlYFR SPEED. % 4�J

I
TWSA LIME STABILIZATION
DAILY RECORD j
DATE
START STOP TOTAL
.RUN TIME, HRS ��6 I
D Y TON
SLUDGE FEED, GAL
LIME FEED, LBS
[::::::����
SLUDGE FEED % SOLIDS
o� PRESS, % SOLIDS
TOTAL PRODUCTION, DRY TONS
LIME/SLUDGE RATIO
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TEMPERATURE of
I TIME OPERATOR
INTO
TIME VESSEL
OUT OF
VESSEL
0PE}2ATOft
........................
O��PERATIONAL
BELT PRESS SPEED, % "! V
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, %_GPM
o/ LBS/HR
INITIAL PH
2 HRS.
22 HRS-
POLYMER USAGE
TYPE USED 13,3
TANKS MIXED
LIME FEED AUGER, o.
MIXER SPEED, % 15

TWSA LIME STABILIZATION
DAILY RECORD /
DATE I� `
START STOP TOTAL
RUNTIME, HRS ' D 'DRY TON
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLID 3 r. PRESS. %SOLIDS
LIME/SLUDGE RATIO
TOTAL PRODUCTION, DRY TONS
ev
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TEMPERATURE of
INTO OUT OF
TIME VESSEL VESSEL OPERATOR TIME
I 1 1 I I IfNI T IAL PH
2 HRS,
22 HRS_
f' OPERATIONAL
BELT PRESS SPEED, %"1
POLYMER PUMP SPEED % GPM � ��
SLUDGE PUMP SPEED, %
UGER 0/ LBS/HR
LIME FEED A °
MIXER SPEED, %
OPERATOR'

TWSA LIME STABILIZATION
DAILY RECORD Q,
DATE l
START STOP TOTAL
RUN TIME, HRS'�`� �• `e`� ��
SLUDGE FEED, GAL
LIME FEED, LBS J I
E:��SLUDGE FEED % SOLIDS d PRESS. °b SOLIDS
TOTAL PRODUCTION, DRY TONS °-
LIME/SLUDGE RATIO
Iv i dv�
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TEMPERATURE of
INTO OUT OF
TIME VESSEL VESSEL OPERATOR
..........
OPERATIONAL
BELT PRESS SPEED, % c 3s
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, % GPM
o/ LBS/HR
TIME OPERATOR
INITIAL PH
2 HRS.
22 HRS-
LIME FEED AUGER, o. _
q X �
MIXER SPEED, % /

TWSA LIME STABILIZATION
DAILY RECORD
DATE
START STOP TOTAL
RUNTIME, HRS f 0 u.7 I i I ��—+ � • � �-1 �
o DRY TON
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDS PRESS. °% SOLIDS
LIME/SLUDGE RATIO TOTAL PRODUCTION, DRY TONS
it 4cld ed
PATHOGEN REDUCTION
TFMPFRATURE of
—INTO—T—
OUT OF
TIME I VESSEL I VESSEL I OPERA
VECTOR ATTRACTION REDUCTION
TIME
1 N i T IAL PH
2 HRS.
22 HRS
OPERATIONAL
BELT PRESS SPEED, % r
POLYMER PUMP SPEED,
,LUDGE PUMP SPEED, % GPM
LIME FEED AUGER % LBS/HR
OPERATOR
POLYMER USAGE
TYPE USED C —
TANKS MIXED
S/TAN K
MIXER SPEED, %'��� /b��

TWSA LIME STABILIZATION,
DAILY RECORD
DATE
START STOP TOTAL
RUN TIME, HRS '�r Z� �® DRY TON
SLUDGE FEED, GAL
LIME FEED, LBS I I 1
m
SLUDGE FEEL? % SOLI
am �� PRESS, %. SOLIDS
LIME/SLUDGE RATIO TOTAL PRODUCTION, DRY TONS
t�� I
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TEMPERATURE of
INTO OUT OF
TIME VESSEL VESSEL OPERATOR
I 1 i I I
TIME OPERATOR
OPERATIONAL
25
BELT PRESS SPEED, %
POLYMER PUMP SPEED, % 4 L7
,LUDGE PUMP SPEED, % GPM 3
UGER °/ LBS/HR
INITIAL PH
2 HRS.
22 HRS_
POLYMER USAGE
TYPE USEDe—
TANKS MIXED
LIME FEED A °.
MIXER SPEED, % �� " /_

TWSA LIME STABILIZATION
DAILY RECORD DATE X/1610
START /STOP TOTAL
RUNTIME, HRS
DRY TON
SLUDGE FEED, GAL 7EF
LIME FEED, LBS
SLUDGE FEED % SOLIDS • PRESS , 9b SOLIDS
L!lVIE/SLUDGE RATIO TOTAL PRODUCTION, DRY TONS °
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TEMPERATURE of
INTO OUT OF OPERATOR
TIME VESSELI VESSEL OPERATOR TIME
INI'1 iAL PH
2 HRS.
22 HRS.
.....................................................................
.......... ................... ........................ ........................ ...................... ......... .............................. ............................................ ........
OPERATIONAL POLYMER USAGE
BELT PRESS SPEED, % PE USED
POLYMER PUMP SPEED, % ' G J TANKS MIXED
.LUDGE PUMP SPEED, % GPM 3 f -7
LIME FEED AUGER, % LBS/HR LITERS/TANK
MIXER SPEED, % X 9 A - " -7

t
TWSA LIME STABILIZATION
DAILY RECORD
DATE a
START STOP TOTAL
.RUN.TIME, FIRS I � l ' "v I r u -- I �•r� ,
/ DRY TON
SLUDGE FEED, GAL l`�
-----------------------
LIME .FEED, LBS
SLUDGE PEED %SOLIDS c. 1 . © D' PRESS , °6 SOLIDS
LIME/SLUDGE RATIO TOTAL PRODUCTION, DRY TONS
, j e.
'1 \o Wne_ '
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
rcnnoCDATI IRF nF
fNTO OUT OF
TIME VESSEL VESSEL I OPERATOR
TIME OPERATOR
INITIAL PH
2 HRS_
22 HRS_
.......................................................................................................................... .
OPERATIONAL POLYMER USAGE
BELT PRESS SPEED, % �0 PE USED��
POLYMER PUMP SPEED, % d � TANKS MIXED
lInL
SLUDGE PUMP SPEED, % N U GPM :3 0' Q�
LIME FEED AUGER, %. LBS/HR LITERS/TANK
95
q
MIXER SPEED, % 06>

t -
TWSA LIME STABILIZATION
DAILY RECORD/
DATE �/ . //G J
START STOP TOTAL
RUN TIME, HRS 1 J 0 1!Z f 6­2 °
DRY TON
SLUDGE FEED, GAL
LIME FEED, LBS L— I I I I
SLUDGE FEED °G SOLIDS to � �/� PRESS, % SOI IDS
LIME/SLUDGE RATIO TOTAL PRODUCTION, DRY TONS
Inlet reached temp @ �� / I i VIt
Outlet reached temp @
PATHOGEN REDUCTION
TEMPEKA I UKt Or
INTO I OUT OF
TIME I VESSEL VESSEL OPERATOR
m
VECTOR ATTRACTION REDUCTION
TIME
INITIAL PH
.....................................................................................................................................................................
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, % ' V�
SLUDGE PUMP SPEED, % , V GPM
LIME FEED AUGER, % LBS/HR
N�...R SPEED, %
2 HRS.
22 HRS.
OPERATOR
POLYMER USAGE
TYPE USED 33dC
TANKS MIXED
Revised 8/12/03
X C I 656,1-1 = �s

TWSA LIME STABILIZATION
DAILY RECORD %
DATE��/ `
START
STOP TOT
RUN TIME, HRS OF_
DRYTON
SLUDGE FEED, GAL D r
LIME FEED, LBS
� a
SLUDGE FEED °% SOLIDS o r PRESS, % SOLIDSI 1
LIME/SLUDGE RATIO TOTAL PRODUCTION, DRY TONS
Inlet reached temp @ '
Outlet reached temp @ ��
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
I LMHLRA I UKL Or
INTO OUT OF
TIME. VESSEL VESSEL JOPERATOR
TIME OPERATOR'
INITIAL PH
2 HRS.
22 HRS.
.......................................................................................................................................
7OPERATIONAL
BELT PRESS SPEED, %J 0
POLYMER PUMP SPEED, % G
SLUDGE PUMP SPEED, % , GPM `
LIME FEED AUGER, % LBS/HR
MIAER SPEED, %
POLYMER USAGE
TYPE USED .�
TANKS MIXED _ I
3��3XS�-- ` , 5-1 _YbL
Revised 8112/03

RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
TWSA LIME STABILIZATION
DAILY RECORD 2
DATE � / U3
START
TOT.
I c� I LT64() i I -IV-,�a I
SLUDGE FEED ;6 SO' —S v r �
LIME/SLUDGE RATIO
Inlet reached temp @
Outlet reached temp @
PATHOGEN REDUCTION
TFIIAPFRATI IRF nF
TIME.
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
10
q
l q jcli
. O
�1 r�
PRESS, % SCL0SI 1
TOTAL PRODUCTION, DRY TONS 1 112'. / 0
.......................................... ........... ......................
OPERATIONAL
BELT PRESS SPEED, % 3
VECTOR ATTRACTION REDUCTION
is . o� (—S.l : •� . /s-3
TIME
OPERATOR
INITIAL PH
2 HRS.
"� !d •fie I -,is ,
U 22 HRS. l a r
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, % q 7 GPM �s✓
LIME FEED AUGER, % LBS/HR D
Mi^ER SPEED, % 100
POLYMER USAGE
PE USED _ 23!aC
ANKS MIXED
LITERS/TANK
3y.&js6- = 9- 5) �
x 1 bsf t - 95. 59 ► l�s
Revised 8/12103

RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
TWSA LIME STABILIZATION
DAILY RECORD
DATE S1a1 d 3
START STOP TOTAL
DRY TON
SLUDGE FEED % SOLIDS
n
I ri4
LIME/SLUDGE RATIO
s ✓ d
Inlet reached temp @
`°
Outlet reached temp @
d
PATHOGEN REDUCTION
TFnAPI=PATI IRF nF
TIME.-
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
I • , is
1 � o
���
��
11:1
J q3
��a
co.
c)3
0
BELT PRESS SPEED, %
POLYMER PUMP SPEED, %
PRESS, % SOLIDSI I
TOTAL PRODUCTION, DRY TONS
OPERATIONAL
3S
SLUDGE PUMP SPEED, % qz_
LIME FEED AUGER, % 1
! "^E.R SPEED, %
VECTOR ATTRACTION REDUCTION
3 (as —
3
TIME 1 �- 6
f�•�� • . _
OPERATOR
�3)D INITIALPH
v343)
2HRS.
J L 3 i)yL - `:
22 HRS.
GPM "6 q
LBS/HR P
POLYMER USAGE
TYPE USED :33 D-Q,
TANKS MIXED
C3V5,116- = 9- 5/
� 4IbAj = C� 5-9
Revised 8/12103

TWSA LIME STABILIZATION
DAILY RECORD %
DATE
START STOP TOTAL
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDS I / i I
LIME/SLUDGE RATIO a
Inlet reached temp @ �-
j
Outlet reached temp (p
PATHOGEN REDUCTION
TFMPERATURE of
TIME,
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
eo
qy
Mk
BELT PRESS SPEED, %
PRESS, k SOLIDSI I
TOTAL PRODUCTION, DRY TONS
OPERATIONAL
30
POLYMER PUMP SPEED, % 3
SLUDGE PUMP SPEED, % GPM S
LIME FEED AUGER, % W LBS/HR
IviinCR SPEED, % - 0 D
DRY TON
VECTOR ATTRACTION REDUCTION
AG-.6�C�� tea)
TIME OPERATOR
!)L
r7 INITIAL PH-
.uiK4A)
o'b -.vs�)
T / / � 7 2 HRS 71 .7
' { 22 HRS.
POLYMER USAGE
TYPE USED
TANKS MIXED
AN
Revised 8/12103

RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
TWSA LIME STABILIZATION
DAILY RECORD
DATE
START STOP TOTAL
/19 3 0 1 y:140 07. d- �
SLUDGE FEED % SOLIDS 1 �� • Li
LIME/SLUDGE RATIO
Inlet reached temp @ D
Outlet reached temp @
PATHOGEN REDUCTION
TI=h/IPFPATI IRF nF
TIME.
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
qi�
6.
43
PRESS , °A SOLIDS, �
TOTAL PRODUCTION, DRY TONS
OPERATIONAL
DRY TON
VECTOR ATTRACTION REDUCTION
�L
TIME 5 <y = .; ) (05
OPERATOR
.� -y INITIAL PH
1� �)_<- '� 9.ci
j 03 'f 4,q .14�
41, so 2 HRS.
_
13-? 4, is% =
22 HRS.
BELT PRESS SPEED, % 20
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, % GPM
LIME FEED AUGER, %4_0�_ LBS/HR
NI...cR SPEED, %�
POLYMER USAGE
TYPE USED v
TANKS MIXED J
101 O,"/15J = I- 0aQ-
tk =
_ITERS/TANK
, i7. / - -I - LA
Revised 8/12103

TWSA LIME STABILIZATION
DAILY RECORD
DATE
START
RUN TIME, HRS 0-0
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED %SOLIDS I I Q I
LIME/SLUDGE RATIO FaTlf
Inlet reached temp @ •e-3
Outlet reached temp @ �
PATHOGEN REDUCTION
TGneDr:PATI IRF nF
TIME.
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
l6Y
-��
an9
ate:
/y
STOP TOTAL
g2x6o
PRE , °% SOLIDSI i
TOTAL PSIODUCTION, DRY TONS o (—V
160
�—/EIJT103 ATT CTIO REDUC
TIME
�/
`�� INITIAL PH
a s 2 HRS.
-0- ;D3Ca
22 HRS.
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, %_ GPM
LIME FEED AUGER, %� LBS/HR
Ni,..C-R SPEED, 1 ba
DRY TON
TION
OPERATOR
171
POLYMER USAGE
TYPE USED oZ Chi
TANKS MIXED
AN
-3V3,-73'5-:- q-5 'Q' y 11�9
(�5®& M-5
Revised 8112103

TWSA LIME STABILIZATION
DAILY RECORD
DATE
5
V
START STOP TOTAL
RUN TIME, HRS q - 4 � r "f � D ►y,
DRY TON
SLUDGE FEED, GAL
LIME FEED, LBS F d © ° 4
SLUDGE FEED % SOLIDS PRESS, % SOUD`F I
LIME/SLUDGE RATIO TOTAL PRODUCTION, DRY TONS ' ! z ` 51
Inlet reached temp
Outlet reached temp @
PATHOGEN REDUCTION
TFIIAPFRATI IRF nF
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
—TIME.
9a
le5
o
i
�` �s•-
`a6 f
1 ��
OPERATIONAL
VECTOR ATTRACTION REDUCTION
TIME f� " ��'� OPERATOR
6 Q INITIAL PH A-
is 2 HRS.
s&3X.3= : ovQ .
22 HRS.
dl- ov ;
BELT PRESS SPEED, % 3 v
POLYMER PUMP SPEED, % 3
SLUDGE PUMP SPEED, % GPM
LIME FEED AUGER, % O LBS/HR �� U
MIAER SPEED, % _T!7
I POLYMER USAGE I
USED 3 3 �
TANKS MIXED Tier 1
1 •6 lbs
Revised 8112/03

TWSA LIME STABILIZATION
DAILY RECORD �7 r 2
DATE F � P-7 '3
START
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDS f v J i
LIME/SLUDGE RATIO °
inlet reached temp @
Outlet reached temp @
PATHOGEN REDUCTION
TGnrt1D1=RATI IRF nF
TIME.
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
1 3
r,30
1
L
d .
a- Li
�B-d
TOT,
PRESS , % SOLIDS1
TOTAL PRODUCTION, DRY TONS '
VECTOR ATTRACTION REDUCTION
TIME .c3(,k) `66 6 OPERATOR-
/),.4-•OeZ -t
INITIAL PH
'r� a3 ('r-a5%s) - -a � c)o y
dd 2 HRS.
o3
Lil`&O 22 HRS. ��-
r. OPERATIONAL
BELT PRESS SPEED, % S 3
POLYMER PUMP SPEED, % � ��'
SLUDGE.PUMP SPEED, % GPM
LIME FEED AUGER, % o LBS/HR
Mint=R SPEED, %
POLYMER2 USAGE
TYPE USED JJ a C—
ANKS MIXED
LITERS/TANK
Revised 8112103

RUN TIME, HRS
SLUDGE FEED, GAL
TWSA LIME STABILIZATION
DAILY RECORD
DATE
START
STOP TOT
V.00 1 Iv qs- I II -X h"L, I
LIME FEED, LBS
SLUDGE FEED % SOLIDS PRESS, % SOLIDS
LIME/SLUDGE RATIO at TOTAL PRODUCTION, DRY TONS ° O
Inlet reached temp @ 1J � 3 D
o
Outlet reached temp @
PATHOGEN REDUCTION
TPn/IPFRATI IRE nF
TIME.
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
01;1S
194
1�Rq
eO
o� �?
q
BELT PRESS SPEED, %
OPERATIONAL
33
VECTOR ATTRACTION REDUCTION
. d3( l )
TIME
o�3� l�/7
OPERATOR -
INITIAL PH
a3C_a.r)=1
-��
2 HRS.
`
22 HRS.
POLYMER PUMP SPEED, % 3 (42
SLUDGE PUMP SPEED, % r�® GPM_
LIME FEED AUGER, % yr LBS/HR
Mi^ER SPEED, % / f)D
POLYMER USAGE I
TYPE USED _3, a
TANKS MIXED
Revised 8/12103

RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
TWSA LIME STABILIZATION
DAILY RECORD
DATE
START STOP TOTAL
= " 5-
DRY TON
SLUDGE ICEED % SOLIDS I
LIME/SLUDGE RATIO 1
Inlet reached temp
Outlet reached temp @ b
PATHOGEN REDUCTION
TI=RfiPFRATI IRF nF
TIME,
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
PRESS % SOLIDS1
TOTAL PRODUCTION, DRY TONS 1
VECTOR ATTRACTION REDUCTION
TIME / ` oEld_ `
OPERATOR
3 S 6) INITIAL PH
,S',S'O 2 HRS.
171
z —4-
ld-� -;ca =1�.
s�
22 HRS.
.....................................................................................................................
7 OPERATIONAL
BELT PRESS SPEED, % c�
POLYMER PUMP SPEED, % 35
SLUDGE PUMP SPEED, % 10 GPM CQ 0
LIME FEED AUGER, % 3 LBS/HR
Mi..ER SPEED, %
POLYMER USAGE
TYPE USED��
TANKS MIXED
ANK
a� e (p Ib__5
Revised 8112103

TWSA LIME STABILIZATION
DAILY RECORD
DATE/aa
START STOP TOTAL
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDS
LIME/SLUDGE RATIO
Inlet reached temp
.Outlet reached temp @ U
PATHOGEN REDUCTION
TFI1IPFRATI IRF nF
TIME.
INTO
VES/./S}E�L
OUT OF
VESSEL
OPERA/1/T`'OR
�V V
�4
DRY TON
PRESS, io SOLIDS! 1
TOTAL PRODUCTION, DRY TONS p
c> "tC
4-0
VECTOR ATTRACTION REDUCTION
TIME 1�' • s`� OPERATOR
r fie
INITIAL PH
2 HRS.
1.3
,3`4'�\ 22 HRS. `1"aea
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, % _ GPM g o
LIME FEED AUGER, % LBS/HR -� ` 1
NII,.ER SPEED, % j D®
I POLYMER USAGE
TYPE USED _ -
TANKS MIXED
LITERS/TAN
93 cp� n
Revised 8/12/03

RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
TWSA LIME STABILIZATION
DAILY RECORD
DATE jt5J S 103
START STOP TOTAL
-00 1 �fsS- 11.. IZI
/ a
SLUDGE FEED % SOLIDS I � I
LIME/SLUDGE RATIO S
Inlet reached temp @ v
Outlet reached temp @
PATHOGEN REDUCTION
-rGnnr)PPATI IRF nF
TIME.
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
16-9
co
Co
)q5
BELT PRESS SPEED, %
PRESS , Po SVLIDSI 1
TOTAL PRODUCTION, DRY TONS l(J
OPERATIONAL
33
L
93 .J3
DRY TON
VECTOR ATTRACTION REDUCTION
TIME %o�.� /�� 'OPERATOR
INITIAL PH 1Wj — 4Z4—
5'r,.o 2 HRS. _ L
igi
22 HRS. _
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, % GPM E . d
LII`AE FEED AUGER, % 30 LBS/HR 09
MIXER SPEED, % / O 0
POLYMER USAGE
TYPE USED .,33 oZ C—
TANKS MIXED I
ANK
36/3
Revised 8112103

t'
TWSA LIME STABILIZATION
DAILY RECORD
DATE Z12A2/21 3
START STOP TOTAL
RUN TIME, HRS 9 ` DO
:1
SLUDGE FEED, GAL L 0
LIME FEED, LBS
SLUDGE FEED %SOLIDS i `j PRESS, % SOLiDS1 i
LIME/SLUDGE RATIO i J TOTAL PRODUCTION, DRY TONS I v
Inlet reached temp @ m L 3
Outlet reached temp @ • �.7
PATHOGEN REDUCTION
TFRAPFRATI IRF nF
TIME
INTO
IVESSEL
OUT OF
VESSEL
OPERATOR
313d
OPERATIONAL
DRY TON
-3
VECTOR ATTRACTION REDUCTION
TIME a_t— , l6 , �� ���
OPERATOR
�U INITIAL PH
//
A
2 HRS.
� 11c)
22 HRS.
BELT PRESS SPEED, % 0
POLYMER PUMP SPEED, % `7 o
SLUDGE PUMP SPEED, % 60 GPM &9, -70
LIPAE FEED AUGER, % J �)' LBS/HR 00
MmER SPEED, %
POLYMER USAGE
TYPE USED 33 -2 C—
TANKS MIXED
1r.i?kX
9V. q %fv -s
Revised 8112103

d
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
TWSA LIME STABILIZATION
DAILY RECORD
DATE 49 / 0 3
START STOP TOTAL
DRY TON
SLUDGE FEED % SOLIDS (. ✓ �/ 1
LIME/SLUDGE RATIO F. v
Inlet reached temp @ n � p�
Outlet reached temp @ I j .0 1, 19 !
PATHOGEN REDUCTION
TFnrtPFRATI IRF nF
TIME.
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
19
PRESS, % SOLIDSI
TOTAL PRODUCTION, DRY TONS /, D
VECTOR ATTRACTION REDUCTION
147
TIME /yT l�a�3 OPERATOR
- � L INITIAL PH 1 �� (
-o3 Cam_ 1 q7
10 2 HRS.
22 HRS. 6
OPERATIONAL
BELT PRESS SPEED, % 3 O
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, % 0 GPM
LIME FEED AUGER, % 3,5 LBS/HR
Mi^ER SPEED, % I 0 0
POLYMER USAGE
TYPE USED e-
TANKS MIXED 0
_ITERS/TANK
jf,Q r. -5
Revised 8112f03

RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
TWSA LIME STABILIZATION
DAILY RECORD
DATE© P / d 13
IV
START STOP TOTAL
0 5 `� ! 1f S—
SLUDGE FEED °% SOLIDS
LIME/SLUDGE RATIO
Inlet reached temp
Outlet reached temp
PATHOGEN REDUCTION
TGnAPFPATI IRF nF
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
ncy
19-2
/ '�3
e 10
/q4
CIO
23 k.
67
�o 0
DRY TON
PRESS , °% SOLIDSI 1
TOTAL PRODUCTION, DRY TONS F­&,!t?3�
VECTOR ATTRACTION REDUCTION
03
TIME ��,� o ��� ^ /X' OPERATOR -
INITIAL PH
-7 /E g__ i)- 3�
2 HRS. l 5�
Vri XO 22 HRS. A -
OPERATIONAL -
BELT PRESS SPEED, % o
POLYMER PUMP SPEED, %�
SLUDGE PUMP SPEED, % GPM I
LIP"E FEED AUGER, % l LBS/HR .�
MIXER SPEED, %
POLYMER USAGE
TYPE USED JJ a C
TANKS MIXED
AN
Revised 8112103

TWSA LIME STABILIZATION
DAILY RECORD
START
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
DATE lal b
SLUDGE FEED % SOLIDS 1 I
LIME/SLUDGE RATIO
Inlet reached temp
r
Outlet reached temp @
PATHOGEN REDUCTION
TG=RMDPPATI IRF nF
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
31
0,01
/ "
60
64
f 7�
�R
o I
�7
-�29.
LI
STOP TOTAL
PRESS, % SOLIDS 1
TOTAL PRODUCTION, DRY TONS
VECTOR ATTRACTION REDUCTION
,JsC�S— Ic.�j=Yy=.r3�
TIME J� , �,� , �?�- ; �� OPERATOR
�.)O INITIAL PH IA-•Y
h--
;?.r - i/i
7-3
f
2 HRS. fh�.S-
ro3 C- wo) = 6-==' it
!o�s= o -41�
2"
-
22 HRS. _kV�
OPERATIONAL
BELT PRESS SPEED, % 56
POLYMER PUMP SPEED, % q6
SLUDGE PUMP SPEED, % '"1 o GPM q-: L
Lly' FEED AUGER, % LBS/HR 700
MIXER SPEED, % J a
POLYMER USAGE
TYPE USED C,
TANKS MIXED
_ITERS/TA
� �y
Revised 8/12/03

4, r
TWSA LIME STABILIZATION
DAILY RECORD
DATE
START
RUN TIME, HRS I O
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDS I I I
LIME/SLUDGE RATIO
Inlet reached temp
Outlet reached temp @ ,
PATHOGEN REDUCTION
TFhrtPI=PATl IRF nF
TIME
INTO
VESSEL
OUT OF
VESSEL
.
OPERATOR
,113�
BELT PRESS SPEED, %
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, %
TOTAL
DRY TON
PRESS, A.SOLIL" ij 1
TOTAL PRODUCTION, DRY TONS
OPERATIONAL
GPM
LWE FEED AUGER, % LBS/HR
MI7,ER SPEED, %
VECTOR ATTRACTION REDUCTION
TIME
j -- `�� l�-
OPERATOR-
INITIAL
PH
2 HRS.
22 HRS.`
POLYMER USAGE
TYPE USED 02 e—
TANKS MIXED
LITERSITANK
iy;3 �y j
Revised 8/12/03

TWSA LIME STABILIZATION
DAILY RECORD /
DATE �� I 1,5-3
START STOP TOTAL
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDS
LIME/SLUDGE RATIO d
Inlet reached temp @ I I c�
Outlet reached temp @ p.
PATHOGEN REDUCTION
TFnAPFRATI IRF nF
TIME. I
INTO
VESSEL_
OUT OF
OPERATOR
VESSEL
qo
c�
17
Ar-
Wo
1 q3
h oly
P
BELT PRESS SPEED, %
POLYMER PUMP SPEED, %
PRESS, % SOLIDS! ,
TOTAL PRODUCTION; DRY TONS
OPERATIONAL
3Y
33
VECTOR ATTRACTION REDUCTION
TIME 1� S�
OPERATOR
-j® INITIAL PH
2 HRS. j
Alf
_
22 HRS.
SLUDGE PUMP SPEED, % 5'o GPM Jr'qi 1-3
LIME FEED AUGER, % - /—l LBS/HR q,5—&
N u,r__R SPEED, % / d O
POLYMER USAGE
TYPE USED
TANKS MIXED
LITERS/TAN
Remised 8112103

RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
TWSA LIME STABILIZATION
DAILY RECORD]
DATE
START STOP TOTAL
DRY TON
a W, 1 3.34 1
SLUDGE FEED 0' SOLIDS
LIME/SLUDGE RATIO
Inlet reached temp @
Outlet reached temp
PATHOGEN REDUCTION
TFfiAPFRATI IRF nF
TIME.
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
&0
�O
00
BELT PRESS SPEED, %
PRESS., % SOLIDS, ,
TOTAL PRODUCTION, DRY TOMS
OPERATIONAL
25
VECTOR ATTRACTION REDUCTION
3Cas-14.k)= �5— -�7'
TIME /�� -- 17y� I�� L/ a6 OPERATOR
INITIAL PH
J rDs� 2 HRS. —�
22 HRS.�l�
POLYMER PUMP SPEED, % 33
SLUDGE PUMP SPEED, % GPMd
-LIME FEED AUGER, % LBS/HR
M1,.ER SPEED, %
POLYMER USAGE
TYPE USED 3 3 .2)
TANKS MIXED
AN
Y5 o 16 3
Revised 8112J03

RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
TWSA LIME STABILIZATION
DAILY RECORD
DATE'
START
STOP TOTAL
DRY TON
I n I /-/I.X00 I 1 1�3.S� J
SLUDGE FEED °% SOLIDS
LIME/SLUDGE RATIO �✓ �^
Inlet reached temp @ o v
Outlet,reached temp @ D�
PATHOGEN REDUCTION
TFhfiDP ATI IPF= nF
TIME.
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
l� :bo
0-0
- 7`:3�,
S�
BELT PRESS SPEED, %
PRESS, °% SOLIDS
TOTAL PRODUCTION, DRY TONS
OPERATIONAL
3-5
VECTOR ATTRACTION REDUCTION
TIME 1�+-� J'�r� S� OPERATOR-
=Vd INITIAL PH / -- _
12.E.
3 2 HRS.
22 HRS.
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, % GPM a�
LIME FEED AUGER, % r1 LBS/HR
M"[:ER SPEED, % 00
POLYMER USAGE
TYPE USED
TANKS MIXED
TERS/TAN
Revised 8112f03

z •.
TWSA LIME STABILIZATION
DAILY RECORD
DATE % l
START STOP TOOT/ALL
RUN TIME, HRS y / r �✓
SLUDGE FEED, GAL t d
LIME FEED, LBS
SLUDGE FEED % SOLIDS
LIME/SLUDGE RATIO ,� OA
Inlet reached temp
Outlet reached temp @
PATHOGEN REDUCTION
-rGNA1DF=PATI IRF nF
TIME,
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
10
f
10
kl
BELT PRESS SPEED, %
PRESS, ;n SOLIDSI i
TOTAL PRODUCTION, DRY TONS /
OPERATIONAL
'35
DRY TON
g
VECTOR ATTRACTION REDUCTION
TIME �� �j -, /41_7' OPERATOR -.
INITIAL PH A'
rD3l l Z7)
11 )LO 1 �-, 3g .
2 HRS.
!$�195- �r _
5S 22 HRS.
POLYMER PUMP'SPEED, % 3
SLUDGE PUMP SPEED, % GPM
LIME FEED AUGER, % LBS/HR �J
MI,.ER SPEED, % 0 Q
POLYMER USAGE
TYPE USED 33)�
TANKS MIXED ! ��
LITERS/TANK (D
Revised 8/12/03

TWSA LIME STABILIZATION
DAILY RECORD
DATE ! l ' mac' z o)
START STOP TOTAL
RUN TIME, HRS �L� •',� �'�
DRY TON
SLUDGE FEED, GAL I C% 1 a3 h&0 1 1 J.
LIME FEED, LBS 15-1 : S
SLUDGE FEED % SOLIDS PRESS, % SOLIDSI
LIME/SLUDGE RATIO �r TOTAL PRODUCTION, DRY TONS a
Inlet reached temp
Outlet reached temp @3
PATHOGEN REDUCTION
TFMPFRATURF nF
TIME.
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
1=33
qq
60
fo33
Uq
1q8'
Co
3 f,.3
ZO 6
Ar
BELT PRESS SPEED, %
OPERATIONAL
30
POLYMER PUMP SPEED, % J
VECTOR ATTRACTION REDUCTION
TIME
OPERATOR
S qS-
INITIAL PH
/_
/ . �Cti/^J
,o3
W/
HR
.03o-s-
�5
22 HRS. 12,4
SLUDGE PUMP SPEED, % % 6 GPM
LIME FEED AUGER, % T7 LBS/HR
Mii.cR SPEED, % lob
POLYMER USAGE
TYPE USED 3,3 a- L-
FANKS MIXED f 1
_ITERS/TANK
Revised 8/12/03

?,a
RUN TIME, HRS
SLUDGE FEED, GAL
TWSA LIME STABILIZATION
DAILY RECORD /
DATE , ���/ D�
p r,ess v 4s
START STOP TOTAL
T 4 q- , 1 ­2 To _T_ i o,. o
DRY TON
LIME FEED, LBS
SLUDGE FEED % SOLIDS
+
PRESS, % SOLiDS�
LIME/SLUDGE RATIO
TOTAL PRODUCTION, DRY TONS
L
Inlet reached temp
Outlet reached temp @
PATHOGEN REDUCTION
TFMPFRATURF_ of
TIME.
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
l�l?
qq
/q'5�
6io
3' 17
/q7
tIN
I A/
�oc
1
BELT PRESS SPEED, %
OPERATIONAL
30
VECTOR ATTRACTION REDUCTION
•a3
TIME ����-� %�3'L"�117 OPERATOR-
3 -L INITIAL PH
2 HRS.
;v3( )'o 0)
�o2-S = r IS=/�•3S
3722HRS.
POLYMER PUMP SPEED, % 3
SLUDGE PUMP SPEED, % -712 GPM 3 1
LIME FEED AUGER, %
Mv.cR SPEED, % / Gb
IS-0
LBS/HR / SD
POLYMER USAGE
TYPE USED 3 3c� e'
TANKS MIXED
Revised 8YI2103

TWSA LIME STABILIZATION
DAILY RECORD ,
DATE �ZZ L,2 o / 01* 3
START
RUN TIME, HRS
F I -
SLUDGE FEED, GAL
LIME .FEED, LBS
SLUDGE FEED 0' SOLIDS A.
p
LIME/SLUDGE RATIO E ll2
Inlet reached temp
Outlet reached temp @ . T I
PATHOGEN REDUCTION
TFMPFRATURF of
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
6D
STOP
2
TOTAL
B
w QIS s� p L�11 � ;wp to
PRESS, ONL SOLIDS, ,
TOTAL PRODUCTION, DRY TONS
DRY TON
It lei pi(N-
VECTOR ATTRACTION REDUCTION
�a36S'-1�1�
TIME (A� 7 ij�73% OPERATOR
INITIAL PH
A �e
2 HRS. /71
Ir?d 22 HRS.
OPERATIONAL
BELT PRESS SPEED, % �?5
POLYMER PUMP SPEED, % Z
SLUDGE PUMP SPEED, % 7 0 GPM
LIME FEED AUGER, %� LBS/HR
�vt,.cR SPEED, % boo
POLYMER USAGE
TYPE USED ,3v7 -2- C
TANKS MIXED
ANK
�5 1 bs
Revised 8112103

TWSA LIME STABILIZATION
DAILY RECORD/
DATE/®1
START STOP TOTAL
RUN TIME, HRS
DRY TON
SLUDGE FEED, GAL od--F
e
LIME FEED, LBS 3,43
SLUDGE FEED % SvLiDS I PRESS, % SOLIDS,
—T
LIME/SLUDGE RATIO o TOTAL PRODUCTION, DRY TONS m
Inlet reached temp
Outlet reached temp @
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TFMPFRATHRF of l -,) j) :y � _ J y%
TIME.
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
Ar
s: �3 .
I -6 o
g'
IK"
Io, d' ` ��
TIME
1 -
OPERATOR
INITIAL PH
A�
f 6
�-
2 HRS.
/
4 _')_I1= Ja. s�7
22 HRS.
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, % O GPM b ��
LIME FEED AUGER, % 5. o LBS/HR (90
M,,.cR SPEED, % D�
POLYMER USAGE
TYPE USED 3� 0-
TANKS MIXED tw
Revised 8112/03

i a
1
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
TWSA LIME STABILIZATION
DAILY RECORD
DATE`
� /rllJfi ��' �"�,� /fit.✓+✓
START STOP TOTAL
am
g.
SLUDGE FEED % SOLIDS
LIME/SLUDGE RATIO `
Inlet reached temp @ U d
Outlet reached temp @ �E3
PATHOGEN REDUCTION
TGnnPPPAT1 IRF nF
TIME.
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
CIO
3, a-3
i
)
Ar
L
PRESS , % SOLIDSI
TOTAL PRODUCTION, DRY TONS
OPERATIONAL
BELT PRESS SPEED, %_
POLYMER PUMP SPEED, % 3 -
DRY TON
e
VECTOR ATTRACTION REDUCTION
TIME /� 19J- = I� �d $ OPERATOR
Ici— INITIAL PH
S 2 HRS.
03 (X6 s- / a/G
1� 4 — ./00'
%S 22 HRS.
SLUDGE PUMP SPEED, % D GPM --� J , "I
LIME FEED AUGER, % `"1 LBS/HR �S_
Ml,..ZR SPEED, % / OC
. POLYMER USAGE
FYPE USED -3 3 C_
TANKS MIXED
AN
Revised 8112103

RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
TWSA LIME STABILIZATION
DAILY RECORD
In
DATE L% -Z
START STOP TOTAL
DRY TON
SLUDGE FEED % SO..—S
LIME/SLUDGE RATIO
, C
Inlet reached temp @
�'
Outlet reached temp @
'
PATHOGEN REDUCTION
TFMPFRATURF of
TIME
INTO
VESSEL
OUT OF
OPERATOR
VESSEL
1 d��
L�o
A03
e0
3�6�-
101
S' bra
187
�,00
BELT PRESS SPEED, %
M ✓ i
PRESS , /o SOLIDS
TOTAL PRODUCTION, DRY TONS
OPERATIONAL
�Llg
VECTOR ATTRACTION REDUCTION
TIME la -� -�- OPERATOR
INITIAL PH /4-
:--I3 =. �►�
c5 = /® 2 HRS. %a
L
I� 22 HRS. _% '
POLYMER PUMP SPEED, % 3 l
SLUDGE PUMP SPEED, % -7-3 GPM �� b
LIME FEED AUGER, % 3 �7 LBS/HR / 1
M.,.c.R SPEED, % 160
0
POLYMER USAGE
TYPE USED -33 Z C_
TANKS MIXED 144-111
TERS/TAN
Revised 8112103

M `k
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
TWSA LIME STABILIZATION
DAILY RECORD
DATE / 0
START STOP TOTAL
DRY TON
SLUDGE FEED .% SOLIDS / D
LIME/SLUDGE RATIO n
Inlet reached temp
Outlet reached temp @
PATHOGEN REDUCTION
r�nnoCDeTl (RF nF
TIME
INTO
VESSEL
OUT OF.
VESSEL
OPERATOR
a o�
N,�
0
00.
,570
"Zo
PRESS, °% SOLIDS i
TOTAL PRODUCTION, DRY TONS
OPERATIONAL
BELT PRESS SPEED,
POLYMER PUMP SPEED % 3 5
VECTOR ATTRACTION REDUCTION
o3 (-;L5. - if,
TIME �,� -, /�� = I OPERATOR
INITIAL PH
JLaS
2 HRS.
22 HRS.
SLUDGE PUMP SPEED, % GPM 5�` 7
LIhAE FEED AUGER, % LBS/HR �
MiAER SPEED, % D d
POLYMER USAGE
TYPE USED��
TANKS MIXED
ANK
Revised 8112103