WQ0005763_2004 Annual Report_20050224

Tuckaseigee Water & Sewer Authority
Serving Jackson County
1246 West Main Street
Sylva, NC 28779
Ph. [phone]
Fax [phone]
�Q
January 27th, 2005
DENR/DWQ/Water Quality Section
Non -Discharge Compliance Unit
1617 Mail Service Unit
Raleigh NC 27699-1617
Gentlemen;
RECEIVED
FEB - 3 200
WATER QUALITY SECTION
Non -Discharge Conrknce Ent.
Enclosed is the Annual Residuals Report for theTuckaseigee Water and Sewer Lime Stabilization
facility (permit #WQ0005763) for the period of January 1, 2004 - December 31, 2004.
Should you have any questions or if I can provide you any additional information, please don't hesitate
to contact me.
Smcer y,
Stan Bryson
Wastewater Plant Operations Superintendent
Tuckaseigee Water & Sewer Authority
Enc.
D EE
FFEB 4 7C,33
WATER QUALITY SECTION
iHEVILLE REGIONAL OFFICE

a ir,
ANNUAL SEWAGE SLUDGE REPORT
OF
TUCKASEIGFE WATER AND SEWER AUTHORITY
PLANT # 1-NPDES # NCO039578 (WQ0005763)
for the period of January 1, 2004-December 31, 2004
as required by
40 CFR, PART 503
STANDARDS FOR THE USE OR DISPOSAL OF SEWAGE SLUDGE
FEB — 3 2005
WATER QUALITY SECTION
Non -Discharge Com;klce Ent.

A J(
TABLE OF CONTENTS
(1) REPORTING REQUIREMENTS/PERTINENT INFORMATION
(2) CERTIFICATION
APPENDIX
(a) 2004 sludge data
�n
(b) 2004 distrubution and marketing summary
(c) 2004 laboratory analysis
(d) 2004 lime stabilization record of operation
RECEIVED
FEB _ Z005
Non•Dischaml Cora

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

it I
CERTIFICATION REQUIREMENTS
PART I -POLLUTANT CONCENTRATIONS
PARAMETER _ MAXIMUM
Arsenic............................................:..........2.5 mg/kg
Cadmium...................................................1.2
mg/kg
Chromium..................................................80
mg/kg
Copper.....................................................150
mg/kg
Lead..........................................................9.6
mg/kg
Mercury....................................................1.9 mg/kg
Molybdenum.............................................2.6
mg/kg
Nickel........................................................7.0
mg/kg
Selenium.....................................................1.5 mg/kg
Zinc...........................................................400
mg/kg
PART H - PATHOGEN REDUCTION (40 CFR 503.321
X Class A Class B
PART III - VECTOR ATTRACTION (40 CFR 503.34
Option 1 _ Option 2 —Option 3 _ Option 4
Option 5 X Option 6 — Option 7 —Option 8

PART IV - CERTIFICATION
" I certify under penalty of law, that the Class A pathogen requirements in 40 CM 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 27th day of January , 2005.
Stan Bryson, Was water Superintendent
RECEIVE
FEB - 3 ZM"
WATER QUALITY SECTION
Non -Discharge Conolance Ed

ANNUAL DISTRI113t ION AND MARKETING/ SURFACE DISPOSAL CERTIFICATION AND 5UNDL4RP .FOILM
PERIifI' #: 411 -5 63ACILIrY ]+TAME:
PHONE -:gag- S,g(,, -9.3jk COUNTY: J0.C�K�,�,� OPERATOR:
FACILITY TYPE (please check one): 9,Surface Disposal (complete Part A (Soarce(s) and *Residual IV Volume only) and Part C)
IDistribution and Marketing (complete Parts A, B, and C)
Was the facility in operation daring the past calendar year? C✓lea ] No No If No skip parts A, B, C and certify farm below
Part A*:
Part B*:
Month
Sources(s) (include NPDES d if
applicable)
Volume (dry ions)
Recipient Information
Admendment/
Bulking Agent
Residual In
Product Out
Name(s)
Volume (dry"
tons)
Intended use(s)
January
February
March
April
May
I n
:r
c`
June
July
August
September
October
November
December
Totats:
.Annual (dry tons):
A
men ens use
u ngAgent(s)use
:
z=
w
d U
W
W
co
U
�cc
Q U
29
� o
3
-�l
N
0
i
W
* If more space than given is required, please attach additional information sbeet(s). ❑ Check box if additional sheet(s) are attached
Part C:
Facility was compliant during calendar yeas©]} with all conditions of the permit (including but nut limited to items 1-3 beiaw) issued by the
Division of Water Quality. Yes ❑ No If r49, please provide a written description why the facility was not compliant. -��+
1. All monitoring was done in accordance with the permit and reported for the year as required and three (3) copies of certified laboratory results are attached. W
2. All operation acid maintenance require-ments were compiled with oar, in the case of deviation, prior authorization was received from the Division of Water P
Quality, m
3. No contravention of Ground Water Quality Standards occurred at vmonitoring well. W
"I certify, wider penalty of law, that the above information is, to the best of my knowledge and belief, true, accurate and complete. I am aware
89
th t ere are . nifiean.t penalties for submitting false informaion, including the possibility of fines and imprisonment for knowing violations." Signature of Per . 'ee AD� Signature of Pregarer** Date
(if different -from Per itte-e) "Preparer is defined in 40 CFR Part SD3.9(r) -2
ru
Author Daryl D. Memtt DENR FORM DMSOF (7/ 002)

I'IHK- 14:.it> FROM:
T0:9882863190e9 . P:3/4
ANNUAL PATIROGEN AND VECTOR ATrRA. CTfOK REIDUCI' ON 1?ORK
Facilify Name: f �1C t.5ei c�roP 1I` RJR- XW P,,� � A. Permit Number: '00
WWTP Name: %�t� j NPDES dumber: U 003!78-
Monitoring Period: From 1 / i M .4 To t -n / �, ) ^ 11
Pathogen Reduction (40 CFR 503.32) - Please indicate level achieved and Alternative nerfnrmAde
Class A-
Aitemative 1 Lj
Alternative 2 ❑
Alternative 3 ALJ
Alternative 4❑
Altemative 5 LX
. Alternative 6 ❑
If applicable to alternative performed (Class A only) indicate "Process to Further Reduce Pathogens":
Compost LJ Heat Drying ❑ Heat Treatment ❑ Thermophilic L]
Bela Ray ❑
lumina RayF1
Pasteurization
Class B.-
Alternative 1LJ
I Alternative 2 L
Altcmativc 3 ❑
If applicable to alternative .performed (ClaN.a B only) indicate `Process to Significantly Reduce Pathogens":
Litne Stabilization [] Air Drying Composting LI Aerobic Digest9on (�
Anaerobic Vigestion❑ '
If applicable to $Itc... I erformed Class A, or Class B) complete the following monitoring data:
Parameter
Level in
Pathogen
Density
um cr o
Exece-
rcqucncy
of
Semple
112inimu
Geo. Mean
aximu
Units
rebth
dcnces
An�lvsis
Type
Tech-
ni ue '
2x10to
power.MPN per
swim of total
Fecal Colifarm
solids or 2 x 10to
the bth power
n I�
C�
Lk
�v1,
�y�j
��
6vl
CFU per gram of
�I
I DOD mpn per
smm of total solid
(dry weight)
Salmonella bacteria
3 MPH per 4
(in.licu of fecal
stems total solid
colifomt)
(dry weight)
Vector Attraction Reduction (40 CYR 503.33) - Please indicate option performed:
0ption t ❑ j0ption2 Lj 10ption 3 l _) Option 4 ❑ Option S ❑
Option 6 U.1 j0ption 7 a ion 8
Ft 0 laption 9 L-j (Option 10 Li I
No vector attraction reduction options were performed ❑
�..wAlil'lVtf lJ.Vl\ oi.ts,dr,rru.t� 1 tprcase cile" tits appropriate statement)
"I certify, under penalty of law, that the pathogen requirementA in 40 CFR 503.32 and the vector
attraction reduction requirement in 40 Cl!R 503.33 have been met"
i =7 "I certify, under penalty of law, that the pathogen requirements in 40 CPR 503.32 and the irector
attraction reduction requirement in 40 CFR 503.33 have not been met." (Please note if you cheek
this statement attach art explanation why you have not met one or both of the requirements.)
"This determination has been made under my direction and supen.ision 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 ara that t ere are_signili ut penalties for fags rtification including; fine and imprisonment."
�t)
1� V o
Prep r Natne and T ie (typeor La ['tipplicr Name and Title (if applicable)(type or print)
o1r1 ),
Signature of Prcparer Daln Signature of Land A.pplier (if applicable) Date
C
Author Daryl D. Merritt DENR FORM RF (7,12002)

Appendix
(a)
2004 Sludge Data

J
APPENDIX A
20J SLUDGE DATA
TWSA PLANT # 1 (1.5 mgd)
NPDES # NC0039578
SLUDGE TO DIGESTOR.................................................................7,098,130 gallons
totallbs..................................................................... 415, 0261b s
totaltons.......................................................................208 tons
total metric tons............................................................188.2 metric tons
TWSA PLANT # 2 (.5 mgd)
NPDES # NC0020214
J SLUDGE HAULED TO PLANT # 1...........
total tons .........................
total metric tons ..............
TWSA PLANT # 3 (.1 mgd)
NPDES # NCO063321
..............................................90,719 gallons
............................................... 9.35 tons
..............................................8.48 metric tons
SLUDGE HAULED TO PLANT # 1......................................................... 148,689 gallons
totaltons............................................................................ 11.62 tons
total metric tons..............................................................10.5 Dry metric tons

PROCESS SUMMARY SHEET
T
PLANT NAME TWSA #1
ANNUAL (2004)
J
FOR THE PERIOD OF
111104 THROUGH 12/31/04
A
PLANT FLOW,.mgd
0.810 daily avg
B
INFLUENT BOD, mg/I
146.8 daily avg
C
EFFLUENT SS, mg/I
23.9 daily avg
D
MLSS, mg/I
3317 daily avg
E
RSSS, mg/I
5891 daily avg
F
WAS RATE, mgd
0.01945 daily avg
G
AER. BASIN VOL., mg
0.468
H
CLARIFIER VOL, mg
0.1508
I
F/M RATIO
..........................................................
LB APPLIED/LB UNDER AERATION
J
MCRT
DAYS
ACTIVATED SLUDGE DATA
DATE
30 MIN
SETT.
SLUDGE
MLSS
m /I
MLVSS
m /I
EFF
FLOW
MGD
RSSS
m /I
ZSV
ft/hr
SVI
MCRT
da s
SLUDGE WASTING
gallons Ibs
JAN.
420
3850
2993
0.865
7129
4.2
108
14
654,000
38,816
FEB.
369
4660
3028
1.043
7490
3.9
91
22
324,000
20,795
MAR.
425
4026
3267
0.930
7325
4.6
104
12
721,000
44,779
APR.
316
3290
2598
0.943
6355
4.8
95
11
798,900
43,739
426
3783
2924
0.875
6433
4.3
112
17
546,000
30,906
JUN.
440
3878
2870
0.826
7408
4.4
111
16
524,730
35,149
JUL.
390
4300
3191
0.918
7569
4.6
90
15
727,500
45,070
AUG.
300
4175
2900
0.897
6720
4.9
72
14
804,300
45,563
SEP.
338
3909
2805
1.496
7190
4.5
86
16
411,000
24,343
OCT.
495
3518
2659
1.074
6040
3.5
139
14
638,250
32,890
NOV.
429
3616
2838
1.174
6602
4.1
118
13
657,450
37,924
DEC.
420
3439
2673
1.107
6211
3.3
121
23
291,000
15,052
AVG
318
3317
2482
0.810
5891
3.7
96
13
507009
MAX
495
4660
3267
1.496
7569
4.9
139
23
804300
45563
MIN
300
3290
2598
0.826
6040
3.3
72
11
291000
15052
Total Gallons
Daily Average
7,098,130
415,026 T
19,447
208 T
zuo i mai tons x .au t metric tonitngnsn ton=
188.2 Dry Metric Ton
)tal lbs.
)tal tons

2004
TWSA #2 SLUDGE PRODUCTION
MONTH
Gals Hauled.To
TWSA # 1
AVG
% SOLIDS
TOTAL
DRY TON
January
0.00
February
0.00
March
12,424
0.5
0.26
April
9,318
2.6
1.01
May­13,977
2.1
1.22
June
0.00
Julv
25,000
2.5
2.60
August
0.00
September
0.00
October
0.00
November
0.00
December
30 000
3.4
4.25
TOTAL 90,7191
9.35
TOTAL 9.35 X .907 metric ton/English Ton
= 8.48 Dry Metric Tons

2004
TWSA #3 SLUDGE PRODUCTION
MONTH
Gals Hauled To
TWSA # 1
AVG
% SOLIDS
TOTAL
DRY TON
January
4,370
1.7
0.31
February
8165
2.6
0.88
March
11788
2.1
1.03
April
15,410
1.4
0.90
May
19,138
1.4
1.12
June
22,770
1.9
1.76
Julv
26,394
1.8
1.96
August
7,821
1.9
0.61
September
8,798
2.2
0.81
October
0
0.0
0.00
November
24,035
2.3
2.25
December
0.00
TOTAL 148,689,
11.62
TOTAL 11.62 X .907 metric ton/English Ton
=10.54 Dry Metric Tons

Appendix
(b)
2004 Di'strubution
and
Marketing Summary

APPENDIX B
TWSA PLANT # I
ANNUAL DISTRIBUTION AND MARKETING SUMMARY
2004
VOLUVE IN DRY TONS
MONTH
ADNENDIVENT/
RESIDUAL
PRODUCT
BL LMNGAGENT IN
IN
CUT
Janu
22.22
17.04
39.26
Febuary
13.53
11.18
24.71
IVwch
38.51
29.05
67.56
�
43.2
41.32
84.52
11.56
11.12
22.68
June
11.49
14.65
26.14
Jul
19.78
23.33
43.11
ust
19.02
20.93
39.95
ember
2.66
1.98
4.64
Octobff
35.54
33.39
68.93
November
25.96
20.25
46.21
Deoen'Der
12.52
9.77
22.29
Annual
Dy
Ton
255.99
234.01
490.00

APPENDIX B
TWSA PLANT # 1
ANNUAL DISTRIBUTION AND MARKETING SUMMARY
2004
PART B
RECIPIENT INFORMATION
DATE
NAMES
LUME wet ton
INTENDED USE
3117
Steve Ledford Franklin NC
50
Pasture/ha fields
3/23
Chester Sorrells (Waynesville NC
32
Commercial Hauler
3/26
Chester Sorrells (Waynesville NC
45
Commercial Hauler
3/26
Verlin B son Cullowhee NC
2
Garden and Pasture
3/29
Chuck Bates Franklin NC
30
Pasture/ha fields
3/30
Jim Rhinehart Webster NC
24
Pasture/ha fields
4/1
Verlin B son Cullowhee NC
2
Garden and Pasture
4/2
Chuck Bates Franklin NC
12
Pasture/ha fields
4/6
Chuck Bates Franklin NC
12
Pasture/ha fields
4/10
jJim Rhinehart Webster NC
24
Pasture/ha fields
4/15
Jim Rhinehart Webster NC
1.2
Pasture/ha fields
4/19
Chester Sorrells (Waynesville NC
21
Commercial Hauler
4/21
Chester Sorrells (Waynesville NC
50
Commercial Hauler
4/22
Chester Sorrells (Waynesville NC
60
Commercial Hauler
4/22
Jim Rhinehart Webster NC
12
Pasture/ha fields
4/23
lChester Sorrells (Waynesville NC
75
Commercial Haule
4/24
Jim Rhinehart Webster NC
12
Pasture/ha fields
4/28
Jim Rhinehart Webster NC
7
Pasture/ha fields
4/28
Chester Sorrells (Waynesville NC
45
Commercial Hauler
4/29
Chester Sorrells (Waynesville NC
90
Commercial Hauler
4/29
Jim Rhinehart Webster NC
7
Pasture/hay fields
4130
Jim Rhinehart Webster NC
21
Pasture/ha fields
4/30
Chester Sorrells (Waynesville NC
10
Commercial Hauler
5/8
Jim Rhinehart Webster NC
7
Pasture/ha fields
5/12
Jim Rhinehart Webster NC
7
Pasture/ha fields
5/25
Jim Rhinehart Webster NC
7
Pasture/ha fields
10/1 lChester
Sorrells (Waynesville NC
21
Commercial Hauler
11/17
Chester Sorrells (Waynesville NC
28
Commercial Hauler
11/18
Chester Sorrells (Waynesville NC
34
Commercial Hauler
Total
759

Appendix
(C)
2004 Laboratory
Analysis Summary

2004
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 # orNC 0039578 3)
WQ # : WQ 0005763 4)
WWTP Name: TWSA Plant # 1 5)
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 o Prepar
a7 b�
Dat
(TWSA Version) DENR FORM RSSF (7/2002)

Appendix
(d)
2004 Lime Stabilization
Record
of
Operation

TWSA LIME STABILIZATION
DAILY RECORD
DATE l `
START __ i � � P� UP
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
--
SLUDGE FEED % SOLIDS
/p
LIME/SLUDGE RATIO
Inlet reached temp @
Outlet reached temp @
a :�
PATHOGEN REDUCTION
Tr• -��-
TIME
96
INTO
VESSEL
OUT OF
VESSEL
OPERAT(
�o/
lR
l0 t
0
Ale;
7
3
NAM"
PRESS, ",6 SOLIDS
E=:==j.'
TOTAL PRODUCTION, DRY TONS
c
VECTOR ATTRACTION REDUCTION
03 647—
TIME.
�IINITIAL PH
.d3 (aLr -«.
---_2.HRS.
22 HRS. .: L
..........................................
OPERATIONAL
:LT PRESS SPEED, %
LYMER PUMP SPEED, % 35'
1DGE PUMP SPEED, % j
GPM �97 1 r
F FEED AUGER, %
LBS/HR ��
ER SPEED, % 1 p
18/12/03
OPERATOR
mmm
.........................................: ......:......... ...............
POLYMER USAGE
YPE USED C.
ANKS MIXED
i 1 tKS/TANK D
W-3 )b5

RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDS
LIME/SLUDGE RATIO
Inlet reached temp @
Outlet reached temp @ r�
PATHOGEN REDUCTION
TEMPERATURE oF
TWSA LIME STABILIZATION
DAILY RECORD
DATE 93
START STOP
TOTAL
.............. I........................
�' 3 0(5
VECTOR ATTRACTION REDUCTION
TIME
TON
OPERATOR-
�`3 '�INtT1AL PH 4
1
=�� f 2 HRS.
`f � /22 HRS.
...........
OPERAI"IONAL . ............................
.LT PRESS SPEED, % POLYMER SAGE
)LYMER PUMP SPEED, % 3E TYPE USED �C
UDGE PUMP SPEED, % d ANKS MIXED
GPM Jro- Gf-3
4E FEED AUGER, % LBS/HR 6 0
ZER SPEED, % LITERS/TANK
W 8i12/03

/� J�d
TWSA LIME STABILIZATION
DAILY RECORD
r
DATE
START STOP TOTAL
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED °% SOLIDS
LIME/SLUDGE RATIO
p 2
Inlet reached temp @
,
Outlet reached temp @
o
PATHOGEN REDUCTION
PRESS' °,6 SOLIDS
[::::::=
TOTAL PRODUCTION, DRY TONS
•
DRY TON
O
VECTOR ATTRACTION REDUCTION
TIME � =t 3g� OPERATOR-
INITIAL PH.A!_i
`- 2-HRS.
�•8"x.o3 � . a�� .
`r 22 HRS.
OPERATIONAL
BELT PRESS SPEED, % 3 S
POLYMER PUMP SPEED, % 3 S
SLUDGE PUMP SPEED, % I GPM (,
►"" FEED AUGER, %__ LBS/HR f?
MIXER SPEED, % % (�
wised 8/12103
POLYMER USAGE
YPE USED Q_
•ANKS MIXED
FERSlTANK (�

TWSA LIME STABILIZATION
DAILY RVL---
DATE
START
RUN TIME, HRS E_Ti�'
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDS c: 0
LIMEISLUDGE RATIO �� q
Inlet reached temp @
Outlet reached temp @ ®�
PATHOGEN REDUCTION
TEMPERATURE OF
=13
OPERATIONAL
ELT PRESS SPEED, %
DLYMER PUMP SPEED, %
I
3
STOP TOTAL
PRESS , % SOLIDS
TOTAL PRODUCTION, DRY TONS D
E:3,
DRY TON
VECTOR ATTRACTION REDUCTION
TIME
OPERATOR
b ti_06— INITIAL PH
�-a .5'_ 2 HRS.
D
22 HRS.
_UDGE PUMP SPEED, % GPM tf 1.
FEED AUGER, % Gy LBS/HR Q
XER SPEED, % (7
-d 8/12/03
POLYMER USAGE
YPE USED
ANKS MIXED
` • f
/ 14"(14

TWSA LIME. STABILIZATION.
DAILY RECORD
DATE' lI rg A M 41
ClTAP -
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED °% SOLIDS
LIME/SLUDGE RATIO
Inlet reached temp
y.
Outlet reached temp @ . d_
PATHOGEN REDUCTION
TEMPERATURE OF
VECTOR -ATTRACTION REDUCTION
TIME �y� ;
OPERATOR-
3_0 INITIAL PH-
2- HRS.
=/'=
02
14
22 HRS...
OPERATIONAL
3ELT PRESS SPEED, %
'OLYMER PUMP SPEED, %
'LUDGE PUMP SPEED, % :JT_ GPM
FEED AUGER, % G
j LBS/HR o�
IIXER SPEED, %
vised 8/12103
................
POLYMER USAGE
YPE USED - c'
ANKS MIXED
ILITERS/TANK � h
5� � � lb

RUN TIME, HRS
SLUDGE FEED, GAL.
LIME FEED, LBS
TWSA LIME STABILIZATION
DAILY RECORD
DATE (�
START STOP TOTAL
TON
SLUDGE FEED % SOLIDS p
I PRESS, % SOLIDS
LIME/SLUDGE RATIO 1 TOTAL PRODUCTION, DRY TONS
Q
Inlet reached temp @ `
r
/J=l`) k+ eZJVLe a�
Outlet reached temp @
PATHOGEN REDUCTION . VECTOR ATTRACTION REDUCTION
TIME
OPERATOR
INITIAL PH
2 HRS. ��-
C64C
1 22 HRS._
OPERATIONAL
3ELT PRESS .SPEED, %
'OLYMER PUMP SPEED, % s
>LUDGE PUMP SPEED, % GPM
FEED AUGER,
IIXER SPEED, % / 6 0
wised 8/12/03
POLYMER USAGE
YPE USED
ANKS MIXED
AWL
2. q85

TWSA LIME STABILIZATION!
DAILY RECORD
j DATE _ 9-11 0 Lf
START STOP TOTAL
RUN TIME, HRS .
DRY TON
SLUDGE FEED, GAL (1� "�� L/no5 ,� fl\ <-)
LIME FEED, LBS
SLUDGE FEED °% SOLIDS o f PRESS, % SOLIDS
LIME/SLUDGE RATIO °CJ TOTAL PRODUCTION, DRY TONS EU=
Inlet reached temp @
Outlet reached temp @ e
PATHOGEN REDUCTION TEMPERATURE of VECTOR ATTRACTION. REDUCTION
INTO . OUT OF
TIME VESSEL VESSEL OPERATOR TIME
OPERATOR
3 -'10INITIAL PH
�10 2 HRS. /
22 HRS.
>9;
OPERATIONAL POLYMER USAGE .
BELT PRESS SPEED, %
FA
USED C
'OLYMER PUMP SPEED,
MIXED
SLUDGE PUMP SPEED, % GPM jFEED AUGER, %yILBS/HR /TANK 10
AIXER SPEED, %
evised 8/12103

a
RUN TIME, HRS
SLUDGE FEED, GAL
TVVSA LIME STABILIZATION
DAILY' RECORD
DATE' 1916 4,
START STOP 'TOTAL
DRY TON
LIME. FEED, LBS
-----------
SLUDGE FEED % SOLIDS s PRESS, % SOLIDS[
LIME/SLUDGE RATIO TOTAL PRODUC
TION, DRY TONS
c
Inlet reached temp @ Igo kf3
Outlef reached temp @
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
. TF=KfiP;=PATJ IP;=
-_WE *
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
21f 62 IQ�
( 0-40 1
"o
TIME
OPERATOR-
7-
INITIAL PH
2 HRS.
22 HRS.
. ............ : ............ I ................ i ............... I .......... ............... ................................................. ...............................
OPERATIONAL
�2 <7
BELT PRESS SPEED, %
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, % q GPM_
Lr'- FEED AUGER, LBS/HR
MIXER SPEED, % 106
Revised 8112103
................................................ : .............................
POLYMER 'USAGE
YPE USED C,
ANKS MIXED
.ITERSITAN"
q�- 9 [615

TWSA LIME STABILIZATION
DAILY RECORD
DATE___j
START STOP
TOTAL
RUN TIME,.HRS
SLUDGE FEED, GAL
LIME. FEED, LBS
TON
SLUDGE FEED % SOLIDS -PRESS., %SOLIDS
L I ]ME/SLUDGE RATIO TOTAL PRODUCTION, DRY TONS
Inlet reached temp
Outlet reached temp
PATHOGEN REDUCTION
VECTOR ATTRACTION
REDUCTION
ION
/61
TIME
#F.
OP
OPERATOR
INITIAL PH - �-
-��
2 HRS.
37
22 HRS.
.................................. : ........... I .................. : ...................................................................................................
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, % e7v
GPM ,
17 FEED AUGER, LB S/HR 13'
AfX_ER SPEED,%
!evised 8112103 1
............................................................. 7 ..........................
POLYMER USAGE
TYPE USED
TANKS MIXED
9.1 9 (0- . 1,03

TWSA LIME STABILIZATION
DAILY RECORD
DATE
START STOP TOTAL
RUN TIME, HRS
ISLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED °% SOLIDS PRESS , °% SOLIDS[::::����
LIME/SLUDGE RATIO TOTAL PRODUCTION, DRY TONS O e
Inlet reached temp
0
Outlet reached temp @
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TEMPERATURE of _ v INTO OUT -OF Poi
TIME VESSEL VESSEL oPERATOR TIME 1�'6 OPERATOR
C 7
? - ' INITIAL PH
1A.
• �-$'� 2 HRS.
r o3A�
22 HRS.
OPERATIONAL
BELT PRESS SPEED, % -
POLYMER PUMP SPEED, % .
SLUDGE PUMP SPEED, % - (� GPM oO
FEED AUGER, %° LBS/HR
AIXER SPEED, %
revised 8/12103
.--...................................................................
POLYMER USAGE
YPE USED 02
ANKS MIXED
LITERS/TANK
14d0'3

TWSA LIME STABILIZATION
DAILY RECORD
( DATE
START STOP TOTAL
s
RUN TIME, HRS �.'� f n AA
DRY TON
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED °% SOLIDS ® PRESS, °% SOLIDS
LIME/SLUDGE RATIO �m TOTAL PRODUCTION, DRY TONS
Inlet reached temp @
Outlet reached temp @
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TEMPERATURE of
TIME
4
INTO
VESSEL .
OUT OF
VESSEL
OPERATOR
I S�
1-�sco
ffi /
g
qq
Co
aq
1 qq
CD
Jet
TIME �a
OPERATOR
-` S. INITIAL PH 01
2 HRS.
22 HRS..'
.
OPERATIONAL
BELT PRESS SPEED, .% -' l 6'
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, % 0- GPM I•
I I- eC FF_FD AUGER.. % LBS/HR ..

I Ur JUIAL
'1RUN TIME, HRS 60
SLUDGE FEED, GAL
LIME, FEED, LBS V s
SLUDGE FEED % SOLIDS PRESS, % SOLIDS[
LIME/SLUDGE RATIO TOTAL PRODUCTION, DRY TONS 9& 0
Inlet reached. temp @ F7O 6 0 71
Outlet reached temp
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TEMPERATURE of`
TIME
',i�
INTO
VESSEL
OUT OF
'VESSEL
OPERATOR
r3 _5
��
61.
C
CIO
&62
'96A
CIO
3`0
I'K7
'I
`ace
j
i 7
TIME
OPERATOR-',
/0 -INITIAL PH*' S
Jk7— -
2* HRS
3! /0 22 HRS.
................ ................................................... ...... ................. ...... : ................................ ............................
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, % 146
SLUDGE PUMP S'PEED, % 0 GPM 73.
L FEED AUGER, % LB 'S/H
MIXER SPEED, %
Revised 8/12/03
POLYMER USAGE
TYPE USED
TANK S MIXED
ANK
9`�a�l� ohs

RUNTIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
TWSA LIME STABILIZATION '
DAILY RECORD
DATE
START STOP TOTAL
m
SLUDGE FEED °% SOLIDS. `: O
LIME/SLUDGE RATIO
Inlet reached temp @ o Q
Outlet reached temp @ °
PATHOGEN REDUCTION
TFI1If[�F{?eT� roc „�
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
f:
63
1 0
113
OPERATIONAL
BELT PRESS SPEED, % 30.
37,
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, % GPM �13
L j FEED AUGER, %_ . LBS/HR �a
MIXER SPEED, % I 0 0
PRESS ; °% SOLIDS
E:==
TOTAL PRODUCTION, DRY TONS
VECTOR ATTRACTION REDUCTION
TIME J .4W OPERATOR
i �J INITIAL PH_Z�ff �
2 HRS.
a�® 22 HRS.
Revised 8/12/03
POLYMER USAGE
PE USED
TANKS MIXED
LLITERSITANK

TWSA LIME STABILIZATION
DAILY RECORD
DATE
START STOP TOTAL
RUN TIME, HRS 9 a °
DRY TON
SLUDGE FEED, GAL Jo k q
LIME FEED, LBS ( .33
SLUDGE FEED °% SOLIDS PRESS, °% SOLIDS
LIME/SLUDGE RATIO TOTAL PRODUCTION, DRY TONS
Inlet reached temp a@ A
e �
Outlet reached temp @ . 69
PATHOGEN REDUCTION
TFMPFRATURF nF
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
&0
11�6
C
lCU
'I qs
C-10
VECTOR ATTRACTaN REDUCTION
iY\3
TIME �' y �- ®.� $jam = �a a 1' OPERATOR
INITIAL PH
2 HRS. Cp
%
22 HRS.
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, %'
SLUDGE PUMP SPEED, % GPM
U1" FEED AUGER, % _ LBS/HR
MIXER SPEED, % 1
Revised 8I12/03
POLYMER USAGE'
UC�SAGE `
TYPE USED,3,39 C
TANKS MIXED
ANK
/�1:9& /65

TWSA LIME STABILIZATION
DAILY RECORD
DATE CD'
START STOP TOTAL:
RUN TIME, HRS
DRY TON
SLUDGE FEED, GAL �. c
LIME FEED, LEIS
a"
SLUDGE FEED % SOLIDS PRESS , % SOLIDS
-------------
LIME/SLUDGE RATIO ' ® �' TOTAL PRODUCTION, DRY TONS C
Inlet reached temp @ aq
Outlet reached temp @ 7
PATHOGEN REDUCTION VECTOR TTRACTION REDUCTION
TEMPERATURE of
-TIME
7-7
INTO -
VESSEL'
OUT OF
VESSEL.
OPERATOR
C�%50
lq#
as
�a
.e3A( d3 .l is ; _ r"
TIME OPERATOR
:ad INITIAL PHIst
1� ►LP f�j
P
[� . � 2 HRS. .
)4 22 HRS. �ED
OPERATIONAL
BELT PRESS SPEED, % 3S
POLYMER PUMP SPEED, o° �SV
SLUDGE PUMP SPEED, % 0 GPM. c3
L!' FEED AUGER, % l LBS/HR� CP�%
MIXER SPEED, % /DD "
Revised 8112/03 -
POLYMER USAGE
TYPE USED
TANKS MIXED
LITERS/TANK
,5e r/ lb

i
RUN TIME, HRS
SLUDGE FEED, GAL
TWSA LIME STABILIZATION
DAILY RECORD d'
DATE c
START STOP TOTAL.
LIME FEED, LBS
SLUDGE FEED °% SOLIDS PRESS, °% SOLIDS
LIME/SLUDGE RATIO J-- TOTAL PRODUCTION, DRY TONS 5
Inlet reached temp @
F
Outlet reached temp
PATHOGEN REDUCTION , VECTOR ATTRACTION REDUCTION
TDneDPRATI P;= nF
.TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
60
a f, � ..
it
�I
ll
07
/�— U.
9 Q
-
V �o
/ 75'
TIME ��, —, /S-6 = �� - OPERATOR
`1P INITIAL PH
/d- 2 HRS/.
les—
Al
/O 22 HRS._
OPERATIONAL
BELT PRESS SPEED, '% 3
POLYMER PUMP SPEED, % `T
SLUDGE PUMP SPEED, % GPM L_r_
LI' FEED AUGER; %1 LBS/HR
MIXER SPEED, %
Revised 8/12/03
POLYMER USAGE
TYPE USED .?&;)
TANKS MIXED tM
ANK

TWSA LIME STABILIZATION all
DAILY RECORD'
DATE •/ /ho
START STOP TOTAL
RUN TIME, HRS '
DRY TON
SLUDGE FEED; GAL
LIME FEED, LBS J�.J
SLUDGE FEED °% SOLIDS �b PRESS, % SOLIDSE::::�
LIME/SLUDGE RATIO .. 4 D L TOTAL PRODUCTION, DRY TONS ® s
Inlet reached temp
Outlet reached temp @. 4
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TEMPERATURE of
TIME
INTO
VESSEL
OUT OF
VESSEL.
OPERATOR.
103L5
A
�.b
! .s-
1eq
Ar
TIME IS _ /,L y OPERATOR
'e�Ca INITIAL PH lig
15� 7) :s..,3 _ /,r
2 HRS.
3' 22 HRS. I Al
UHLRATIONAL
BELT PRESS SPEED, % 37
POLYMER_PUMP SPEED, %.
SLUDGE PUMP SPEED, % 9-5 GPM a t>
L)E FEED AUGER, % 50 LBS/HR '
MINCER SPEED, .% / p o
POLYMER USAGE
TYPE USED 33 -�, C_
ANKS MIXEDVAL

TWSA LIME -STABILIZATION S" q
DAILY RECORD
} DATE
START STOP TOTAL
RUN TIME, HRS.' �oZ> -7
DRY TON
SLUDGE FEED, GAL•�u, (�
LIME FEED, LBSga
SLUDGE FEED °% SOLIDS o PRESS, °% SOLIDS
LIME/SLUDGE RATIO a) TOTAL PRODUCTION, DRY TONS e
Inlet reached temp
Outlet reached temp @ i
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TEMPERATURE OF
TIME
INTO
VESSEL
OUT OF
VESSEL
oPERATOR
60
CIO
-7if,3f
l
ff
OPERATIONAL
BELT PRESS SPEED, '% s3
POLYMER PUMP SPEED,
SLUDGE PUMP SPEED, % 75' GPM '
LIME FEED AUGER, % LBS/HR
Owl
TIME /. =���6� OPERATOR
DES' INITIAL PH
Ica
1477
2 HRS.
r-.s '- a ya m
22 HRS.

TWSA LIME STABILIZATION
DAILY RECORD'
DATE
START STOP TOTAL
RUN-TIME, HRS
DRY TON
SLUDGE FEED, GAL
LIME. FEED, LBS
SLUDGE FEED .% SOLIDS t PRESS-,ObSOLIDS
I !m I
LIME/SLUDGE RATIO c TOTAL PRODUCTION, DRY TONS •
Inlet reached temp
Outlet reached temp @
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION'
TEMPERATURE of
TIME
-, Atp
INTO
:VESSEL
OUT OF
'VESSEL
OPERATOR
� �, �
Ise.
q4
A
1)0
3r
TIME OPERATOR
INITIAL PH '
2* HRS.
22 HRS.
1165
................ ..................... ......................... .............................................................. ........................ ................... ................. ....... ............................ .... .... ................ .......
OPERATIONAL POLYMER USAGE
BELT PRESS SPEED, % TYPE USED c2 C—
POLYMER PUMP SPEED, % J S ANKS M.IXEDmilift
SLUDGE PUMP SPEED, % GPM
Ll UIE FEED AUGER, % S LBS/HR LITERS/TANK

SLUDGE FEED, GAL. CJ Iwo 70—(-If I
LIME FEED, LBS
SLUDGE FEED % SOLIDS, d PRESS ,.% SOLIDS
LIME/SLUDGE RATIO, lei rl..r TOTAL PRODUCTION, DRY TONS 9.1.q oq
Inlet reached temp
Outlet reached temp
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TEMPERATURE of -)� = 7.7 -A I
--TIME
INTO
VESSEL
OUT OF
VESSEL
'OPERATOR
A
'17
-7 o19
fig/OPERATOR-
TIME
INITIAL PH. A-5
14
2 HRS.
z
22 HRS.
. ... . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .... . .. . . . . . .. . . . . . . .. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . ...... .......................................
OPERATIONAL
BELT PRESS SPEED,
POLYMER PUMP SPEED, % Z-7
SLUDGE PUMP SPEED, % GPM 7�lel/
LIME FEED AUGER, % LBS/H
MIXER SPEED, %
Revised 8112103
POLYMER USAGE
TYPE USED
TANKS MIXED 71.4J 11[:
LITERS/TANK

TWSA LIME STABILIZATION
DAILY RECORD'
DATE
START STOP TOTAL
RUN TIME, HRS " /.:'J ! O
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED °% SOLIDS PRESS, °% SOLIDS
LIME .SLUDGE RATIOTOTAL PRODUCTION, DRY TONS c
Inlet reached temp @ �'
GA`
Outlet reached temp
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TFi1rtPFRATI IF2F nF ,d ay
;TIME
INTO
VESSEL
OUT OF.
VESSEL
.
OPERATOR
/0'
g
0
60
4f'
.D �J � kLI
TIME i,� --r %� = ��°�
OPERATOR
'L )p INITIAL PH'
a 2 HRS.
d 03(cb - a)-3)
22 HRS.
Y t
:............. ................................ ....... .......... .............. ;...........................................................................
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP.. SPEED, % SO
SLUDGE PUMP SPEED, % _ 7 GPM -7
L1104E FEED AUGER, % LBS/HR f o�
7 �©
.MIXER SPEED,
Revised 8112/03
POLYMER USAGE
TYPE USED Q­
TANKS MIXED

TWSA LIME STABILIZATION
DAILY RECORD' G
�s `4e
DATE
START STOP TOTAL �s
RUN TIME, HRS I i F il 4
SLUDGE FEED, GAL
LIME FEED, LBS V
SLUDGE FEED °% SOLIDS • . PRESS , °% SOLIDS
,LIME/SLUDGE RATIO TOTAL PRODUCTION, DRY TONS
Inlet reached temp @ �=
Outlet reached temp
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
TFMPFPATI IPF of 7 A it jA '.4 — 17
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
P/A
1q
l qs...y�
'_07
TIME 1 �j��� Da"7 1 a 3 OPERATOR
c� S� INITIAL PH / d'
l�-,S � p p•� i= /�- j/
2 HRS.
22 HRS. JaCIO
OPERATIONAL'
BELT PRESS SPEED, %;, .-5"
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, % GPM=
LIME FEED AUGER, % '3 ol- LBS/HR
MC&ER SPEED, % �to
Revised 8112/03
POLYMER USAGE
TYPE USED
TANKS MIXED b .
ANK

TWSA LIME STABILIZATION
DAILY RECORD
r q
DATE
P 1 .
START. STOP TOTAL
RUN TIME, HRS DRY TON
SLUDGE FEED, GAL
Jf
LIME FEED, LBS b� f
SLUDGE FEED °% SOLIDS r__( PRESS , °% SOLIDS .
LIME/SLUDGE RATIO
TOTAL PRODUCTION, DRY TONS 4 4
inlet reached temp @ 1 A " o
Outlet reached temp
PATHOGEN REDUCTION VECTOR ATTRACTION REDUiCTaIOirN.
r=nno=DATI IRF nF n ® ` l r=J l� t 03 r 3q
TIME
INTO
VESSEL
-OUT OF
VESSEL
OPERATOR
J_L_�
TIME ja OPERATOR, -
INITIAL PH
40 2 HRS.. C
'o - J - sy,
22 HRS.
?? OPERATIONAL
BELT PRESS SPEED, % �7
POLYMER PUMP SPEED:, %�
SLUDGE PUMP SPEED, % GPM
LIME FEED AUGER, % `4 D LBS/HR
� C®�
MrxER SPEED,
Revised 8/12/03
POLYMER USAGE
TYPE USED
TANKS MIXED
1 13
Im
,:Y23ti�Y

TWSA LIME STABILIZATION
: DAILY RECORD
DATE
TT -sue _ J ����r>�► a°!� '
START STOP TOTAL
RUN TIME, HRS
SLUDGE FEED, GAL
DRY TON
LIME FEED, LBS
SLUDGE FEED % SOLIDS 6 PRESS, SOLIDS
LIME/SLUDGE RATIO TOTAL PRODUCTION, DRY TO
Inlet reached temp Q. F71+ !'�
Outlet reached temp @
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
rCRR:)CDATI fRF nF
li' 3 (I'T —
TIME
c f
INTO
.VESSEL
OUT OF
VESSEL
.OPERATOR
r.
TIME /�i.� ��7 ' "
OPERATOR-
i� INITIAL PH `f'
�� _r7• '7J % �f = r A
*0
2 HRS d
al y
�.� HRS..::
. 22
OPERATIONAL '
BELT PRESS SPEED, %
POLYMER PUMP SPEED, O/o
SLUDGE PUMP SPEED, % S GPM 2 e
LIME FEED AUGER, % LBS/HR
MIXER SPEED, %
Revised 8/12103
POLYMER USAGE
TYPE USED 33 0" C-
TANKS.MIXED
AN

TWSA LIME STABILIZATION
DAILY RECORD
DATE
START STOP TOTAL
RUNTIME, HRS
DRY TON
SLUDGE FEED, GAL 6, o�
-7
LIME FEED, LBS
SLUDGE FEED % SOLIDS =PRESS , % SOLIDSF
LIME/SLUDGE RATIO 0 TOTAL PRODUCTION, DRY TONS 110 U,
Inlet reached temp
Outlet reached temp @ _q
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION'
of I if r7 Of
,TEMPERATURE -, I
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
F;33
)23
rsci
E�
No
a®
Z3
AT
71a�
dle
•
TIME
OPERATOR -
INITIAL -PH'
0_9 As- tr) S� F 16s-
Ljr— 2 HRS.
Wa_
22 HRS.:.
-------------­- ............................................................
........... .................................. .............. ....... .................. .............................................
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED,.%
SLUDGE PUMP SPEED, % GP
.1 1 PL BE: c7c: =n A I lr'-F=P 0/,FS LBS/HR
POLYMER USAGE
TYPE USED , 33
TANKS MIXED

TWSA LIME STABILIZATION
DAILY RECORD
DATE
START STOP TOTAL
.RUN TIME, HRS If ' m 1. .1.
DRY TON
SLUDGE FEED, GqL-71
s�
LIME FEED, LBS
M
SLUDGE FEED % SOLIDS r PRESS , % SOLIDS
LIME/SLUDGE RATIp C 1 TOTAL PRODUCTION, DRY TONS qI /
Inlet reached temp
9173 3 •
Outlet reached temp @ •
PATHOGEN REDUCTION VECTOR ATTRACTION REDUCTION
rz= 0=0ATI Ipp nF
TIME
°ce%�
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
/ `
84
o -5 a"
TIME
�� ^~. /� = /�-3 9'3 OPERATOR
INITIAL PH
jal�?d
2 HRS_
22 HRS.
OPERATIONAL
BELT PRESS SPEED, % 3 '
POLYMER PUMP SPEED, %
SLUDGE. PUMP SPEED, % GPM (-
LIME FEED AUGER, % LBS/HR Fl /
MiAER SPEED, % Y
Revised 8112103
POLYMER USAGE
TYPE USED S ��
TANKS MIXED
LITERS/TANK

TWSA LIME STABILIZATION
DAILY RECORD
DATE -5—/ / / 1 a 4
Y, & 3
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDS
LIME/SLUDGE RATIO
Inlet reached temp @
Outlet reached temp @ 1 ! a. �7
PATHOGEN REDUCTION
TFIIAPFRATI IRF nF
I �11/1 I I I 1�101),
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
dip,
0
CIO
PRESS, % SOLIDS -
TOTAL PRODUCTION, DRY TONS
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, % 3 -7
VECTOR ATTRACTION REDUCTION
TIME / o�- �'-'� 01? = $%4 �3 OPERATOR
INITIAL PH l�
"4
C _ 2 HIRS.
` 22 HRS. 29�
SLUDGE PUMP SPEED, % GPM go • le —
LIME
1 FEED AUGER, % LBS/HR -Z
f1S. R SPEED, % 400
Revised 8/12/03
USAGE
rYPE USED 3�3
TANKS MIXED
10,5;?", - ;� /65

N
TWSA LIME STABILIZATION
DAILY RECORD
DATE
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDS o
LIME/SLUDGE RATIO
Inlet reached temp @ —(
Outlet reached temp @ 1 / r
PATHOGEN REDUCTION
TEMPERATURE of
1E
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
I ? o
/ 59
E
W;513
1914.
1,
c
a
�C
PRESS , % SOLIDS
TOTAL PRODUCTION, DRY TONS
s,
VECTOR ATTRACTION REDUCTION
TIME %�. �'� a�`s ' ��/ ��r OPERATOR
�. INITIAL -PH o�
03(as—;Lqj) —j?=,o�.f
2 HRS.
a� 22 HRS.
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, % % GPM
LI111" TEED AUGER, %LBS/HR 42
MIXER SPEED, % % do
I POLYMER USAGE I
rYPE USED 3
TANKS MIXED
AN
I1(,& L(o5
Revised 8112103

TWSA LIME STABILIZATION
DAILY RECORD
DATE
RUN TIME, HRS
TOTAL
2 ^� DRY�T/ON
p
SLUDGE FEED, GAL � 0 0 3 a
LIME FEED, LBS o 19,13 e V
D
SLUDGE FEED % SOLIDS �� O
LIME/SLUDGE RATIO
Inlet reached temp
Outlet reached temp @ I C1 "o 1-5
PATHOGEN REDUCTION
TFMPFRATI IRF nF
j 7E
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
B
�13
hr-
s-v-3
/e-7
/ i�
14K
•-_ �t •►I
BELT PRESS SPEED, %
POLYMER PUMP SPEED, % •jc-
PRESS, % SOLIDS
TOTAL PRODUCTION, DRY TONS q 57
VECTOR ATTRACTION REDUCTION
TIME ,��f os'! = i�.�/�� OPERATOR
INITIAL PH
/�' S" t-
2 HRS.
.63 -do,
a 22 HRS.
SLUDGE PUMP SPEED, of 0 GPM
LIAR -ED AUGER, % LBS/HR (/ ,
4
MIXER SPEED, % /60
I POLYMER USAGE I
YPE USED ,. 33 9 c--
ANKS MIXED
AN
(q\QQ 1bs
Revised 8/12/03

TWSA LIME STABILIZATION
DAILY RECORD
DATE
START
RUN TIME, HRS
SLUDGE FEED, GAL
STOP
LIME FEED, LBS
SLUDGE FEED % SOLIDS 1
LIME/SLUDGE RATIO
Inlet reached temp.@
Outlet reached temp
PATHOGEN REDUCTION
TFIUIPF=PATI IRF nF
r- jE
7-3
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
Ar
PRESS, % SOLIDS
TOTAL PRODUCTION, DRY TONS
. OPERATIONAL
BELT PRESS SPEED, % `1 6
POLYMER PUMP SPEED, % q
VECTOR ATTRACTION REDUCTION
� /�-r.�;--�� � . > _ •tea
TIME l cr" oal �'`mil OPERATOR
C>2i'?C:)
3 8� INITIAL P %
S,F,da�_ �,�:A, 7
3 2 HRS. a
4':'6 22 HRS. t. , 6 (1-LAO
wp pn_70 GPM SLUDGE p
Lll ,jtED AUGER, LBS/HR • d.^e�3 MIXER SPEED, % 0
I POLYMER USAGE I
E USED 13 -off' -
KS MIXED
%k,"
Revised 8/12/03

LT-rA
TWSA LIME STABILIZATION
" DAILY RECORD
DATE P/ r / 0 14
START STOP TOTAL
RUN TIME, HRS W - o -� !'N 'o
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDS
LIME/SLUDGE RATIO OU
a
Inlet reached temp 0
Outlet reached temp @ •�
PATHOGEN REDUCTION
--- TF.MPFRATURE of
( CIE
9 3 0
INTO
VE(S�'SEL
OUT OF
OPERATOR
9
VESSEL
eo—
d
s'35-.-
U-0
l�
PRESS, % SOLIDS
TOTAL PRODUCTION, DRY TONS -
............
��OPERATIONAL
BELT PRESS SPEED, % �T 3
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, % GPM
LIA. ..� EED AUGER, % ��. Z5 LBS/HR
MIXER SPEED, % ' o b
DRY TON
VECTOR ATTRACTION REDUCTION
TIME qt ay8 OPERATOR
a: 10 INITIAL PH
03 (.L-r of = 1 = t o3
a,S f a3.� lolRS3
2 HRS.
�la 22 HRS. I Z -s
POL
TYPE USED 3,5 G
TANKS MIXED
joa-a (b5
Revised 8/12103

TWSA LIME STABILIZATION
DAILY RECORD
DATE I� D
START STOP TOTAL
RUN TIME, HRS & e-3 - VX— '/, r1,5—
DRY
SLUDGE FEED, GAL ' Q )—o 0 � l
LIME FEED, LBS
SLUDGE FEED % SOLIDS . g PRESS , % SOLIDS
PATHOGEN REDUCTION J.,,. VECTOR ATTRACTION' REDUCTION
TFMPFRATI IRF nF,
IE
INTO
VESSEL
OUT OF:.,.;
VESSEL-
"OPERATOR
iSL?
c
it
95
19
:.
Zj
OPERATIONAL
IME
%v�.�' , ov' !` /oL �,s-� OPERATOR
y.
-
INITIAL PH
=
2 HRS.
22 HRS.
-�
BELT PRESS SPEED, % 3
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, % -70 }Gann
C& _ ,EED AUGER, LBS/HR
Y _
MIXER SPEED, %
Revised 8/12/03
POLYMER USAGE
PE USED 3 1
3
TANKS MIXED
LITERS/TANK

TWSA LIME STABILIZATION
DAILY RECORD
DATE (o 116 4
START
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDS
LIME/SLUDGE RATIO o 2,T1
Inlet reached temp @ I i i 3-0
Outlet reached temp @ ti
PATHOGEN REDUCTION
TFMPFRATI IRF nF
( SAE
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
C:
06
O
l
rim
)_03
a o 1
6 � `o . I
0`o
%Ld
STOP
DRY TON
PRESS, °,6 SOLIDS
TOTAL PRODUCTION, DRY TONS 1 3 o
VECTOR ATTRACTION R DUCTION
TIME %�-"T t • /�•Y�� OPERATOR
INITIAL PH�
2 HRS.'
3rs.� 22 HRS.
OPERATIONAL
BELT PRESS SPEED, % "S
POLYMER PUMP SPEED, % -6-,
SLUDGE PUMP SPEED ,% S -7 GPM gI,
j
Uk !EED AUGER, % 3 0 LBS/HR l7
MIXER SPEED, % 00
Revised 8/12103
POLYM
TYPE USED
TANKS MIXED

TWSA LIME STABILIZATION
DAILY RECORD
DATE
START STOP TOTAL
RUN TIME, HRS �` �� �� o � �._._ � /
SLUDGE FEED, GAL
LIME FEED, LBS 1 0
SLUDGE FEED % SOLIDS CJ a 1
LIME/SLUDGE RATIO
Inlet reached temp @
Outlet reached temp @
PATHOGEN REDUCTION
"LQ
-711
PRESS , % SOLIDS
E::::=
TOTAL PRODUCTION, DRY TONS .
VECTOR ATTRACTION REDUCTION
TIME ��, y o g . �1 y OPERATOR
`l® INITIAL PH
l;L- s,- t- . 10IF--- /d.dear
2 HRS. --
22 HRS.�s
....................................................................
OPERATIONAL r
ELT PRESS SPEED, % �{
OLYMER PUMP SPEED, % 5
_URGE PUMP SPEED %
P FEED AUGER, % 3 LBS/HR I
XER SPEED, % D
sed 8/12103
POLYMER I Igor=�
YPE USED ?3� t✓
ANKS MIXED
/#b J6s

TWSA LIME STABILIZATION
DAILY RECORD
DATE _ 7> Ica /D
ST
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDS I C(, 5
LIME/SLUDGE RATIO
Inlet reached temp @
Outlet reached temp @ I
q.P
PATHOGEN REDUCTION
TFMPF:PATI IPP: nF
IE
q-
INTO
VESSEL'
OUT OF
VESSEL
OPERATOR
D�
ao .
.��
10-7
kr 1
OPERATIONAL
BELT PRESS SPEED, %
PRESS, % SOLIDS
TOTAL PRODUCTION, DRY TONS b
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED, % GPM
LIN )EED AUGER, %- LBS/HR
MIXER SPEED, % _ 00
Revised 8112103
VECTOR ATTRACTION REDUCTION
TIME a 4 7�-- /4 e = IX.-S"42' OPERATOR
INITIAL PH �.
y
2 HRS.
1 _O 22 HRS.
I POLYMER USAGE I
TYPE USED ly o C-
TANKS MIXED
/ 1,!5-r g", tb 5

TWSA LIME STABILIZATION
DAILY RECORD
C
DATE®
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDS
TON
0 1 q:?, 7ed I I `,~'_ "-z'
d ao3 5-"oa
LIME/SLODGE RATIO I ,�
Inlet reached temp @ gz a 5
Outlet reached temp @ p�
PATHOGEN REDUCTION
TFMPFRATI IRF nF
1E
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
lb,tgO
A64
d,
/;Z;SD
oq
C20 to
C--,j
a
IDS
Co
-li
PRESS, % SOLIDS
TOTAL PRODUCTION, DRY TONS v
VECTOR ATTRACTION REDUCTION
Ir `� '_ � e" = .oFf,
f'f3 l2-s a- • q)
TIME %)_• y ,�.; ci Tq !-� /}" Vf f OPERATOR
�-''03 INITIAL PH
1103 Cu—, W. () = O
2 HRS. nd4
22 HRS.
.............................................. ........................................................................................................
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, % (QO
SLUDGE PUMP SPEED, % GP!l^ (¢
LIP. fEED'AUGER, % 3 I LBS/HR O Ib
MIXER SPEED, % J-06
Revised 8/12/03
POLYMER USAGE
TYPE USED �_ 3 Q C—'
TANKS MIXED
LITERS/TANK
f1-16,g'

TWSA LIME STABILIZATION
DAILY RECORD
M
l DATE rl LlfLo ' J`
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
START STOP TOTAL
s aD 1 -7j 1/,5-- 1 1 1..4
SLUDGE FEED % SOLIDS
LIME/SLUDGE RATIO
Inlet reached temp @
Outlet reached temp @
PATHOGEN REDUCTION
TFMPFRATI IRF nF
G lE
/:34tp
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
Q04?
ISO
eo
103).
/q3
Iq
Co
C-4
-713
OPERATIONAL
BELT PRESS SPEED, % 3 7
POLYMER PUMP SPEED, % FLO
TON
PRESS, % SOLIDS
TOTAL PRODUCTION, DRY TONS l 0 d
VECTOR ATTRACTION REDUCTION
�.�
TIME /�� �'�'� OPERATOR
3'1NITIAL PHA
2 HRS.
-1/0
' 22 HRS.
SLUDGE PUMP SPEED, % 0 GPM . -3
LIIY TEED AUGER, % LBS/HR
$6�-
MIXER SPEED, % / 6 0
Revised 8/12103
POL
YPE USED 23a
ANKS MIXED
AN
Ib6.lQ 1bs

TWSA LIME STABILIZATION
r
DAILY RECORD
DATE 4U
START
RUN TIME, HRS /®•.
SLUDGE FEED, GAL
LIME FEED, LBS
N
1 ,cam 1 3�1/ 1 1 1'aq I
SLUDGE FEED % SOLIDS
LIME/SLUDGE RATIO e_
Inlet reached temp @
Outlet reached temp @ �zI
PATHOGEN REDUCTION
TEMPERATURE of
IE
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
3
o
,
PRESS, % SOLIDS_
TOTAL PRODUCTION, DRY TONS Q3. 4 S
VECTOR ATTRACTION REDUCTION
TIME ��_r t Jp� _ /.L(°�' OPERATOR
INITIAL PH
2.HRS. %a"IfQ
3 yg 22 HRS. 1
OPERATIONAL
BELT PRESS SPEED, % k�
POLYMER PUMP SPEED, %y
SLUDGE DGE PUMP SPEED, % �V GPM 6 �1 7
LII TEED AUGER, % rJLJ LBS/HR J0
MIXER SPEED, % Ida
a
Revised W12/03
POLYMER USAGE
TYPE USED 3,39C
TANKS MIXED Ill. I -
ANK

RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
TWSA LIME STABILIZATION
DAILY.RECORD
DATE co L/
TART STOP TOTAL
:3D `7.'30 g ixx
TON
I 0 1 6393 1 &. I
SLUDGE FEED % SOLIDSe
LIME/SLUDGE RATIO O Z T,
Inlet reached temp @ -00
Outlet reached temp
PATHOGEN REDUCTION
TEMPERATURE nF
`1E .
D
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
%�
cp,©q
(9,01p
CD
PRESS, °% SOLIDS
AL PRODUCTION, DRY TONS
VECTOR ATTRACTION REDUCTION
TIME !� O 8� ` ' OPERATOR
Q) INITIAL PH
2 HRS. 1 �S
,o3 aoo3
c= 22 HRS.
...................................................... .......................................................................................................
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, % �1
SLUDGE PUMP SPEED, % 60 GPM ��I
LI%, _:r'EED AUGER, % LBS/HR
MIXER SPEED, % J DD
Revised 8112/03
POLYMER USAGE
TYPE USED 33 a C,
TANKS MIXED
'y7.6- i6-5

RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
TWSA LIME STABILIZATION
DAILY RECORD
DATE . Vh D 0 y
START STOP TOTAL
DRY TON
C2 , r?oo 0 Ej
SLUDGE FEED % SOLIDS O( «
LIME/SLUDGE RATIO I _
Inlet reached temp @ '
Outlet reached temp @
PATHOGEN REDUCTION
TEMPERATURE of
j 1E
INTO
.VESSEL
OUT OF
VESSEL
OPERATOR
"f,2
l9s-
BELT PRESS SPEED, %
OPERATIONAL
4
PRESS, % SOLIDS
TOTAL PRODUCTION, DRY TONS
VECTOR ATTRACTION REDUCTION
TIME /� S ,�.46f° /�-SF/�
OPERATOR
INITIAL'PH
s-f-°rf
2 HRS.
V30 22 HRS.
POLYMER PUMP SPEED, %
SLUDGE PUMP SPEED % GPM —7 Q
LI11i.., ."'EED AUGER, %_ 39 LBS/HR
MIXER SPEED, % 0 0
Revised 8112103
POLYMER USAGE
TYPE USED
TANKS MIXED
fi'Da•a (b5

TWSA LIME STABILIZATION
DAILY RECORD
DATE
START
RUN TIME, HRS
TOTAL
DRY TON
SLUDGE FEED, GAL L 0 I 33
LIME FEED, LBS 1 .0 1 /d, 7
SLUDGE FEED % SOLIDS �o
LIME/SLUDGE RATIO a D +—
Inlet reached temp @ I �� q
Outlet reached temp @
PATHOGEN REDUCTION
TFMPF_RATURF of
1E
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
107
io3
h--
PRESS, % SOLIDS_
TOTAL PRODUCTION, DRY TONS • 3 5r
VECTOR ATTRACTION REDUCTION
a315
TIME /J� �� �' _ 12"j"4'OPERATOR
OPERATIONAL
BELT PRESS SPEED, % 3 6
POLYMER PUMP SPEED, % f O
SLUDGE DGE PUMP SPEED, % T7 GPM - /iV ../O 9
Llk,__-TEED AUGER, % �lT— LBS/HR
MIXER SPEED, % 490
Revised 8/ 12/03
INITIAL PH j�-
f 03 C — 3� J1,3 = .03%
/�. S f' a. J-3,7
2 HRS.
22 HRS. ��•
L
TYPE USED 2- 9 C.
TANKS MIXED
f,o'9.;L,

TWSA LIME. STABILIZATION
DAILY RECORD
START
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDS
LIME/SLUDGE RATIO °
Inlet reached temp @ 9 ©(�
Outlet reached temp @ I o
PATHOGEN REDUCTION
TEMPERATURE of
E
C)���
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
jqlf
3% 3 11
h
v`•l33
�,
-19g,
U�
Ar
DATE -�a, -T-'�
AWN
PRESS, % SOLIDS
TOTAL PRODUCTION, DRY TONS 1 O ° 8
VECTOR ATTRACTION REDUCTION
. 03().f )S-3 ®, = .o 9
TIME /)--"/ f- ° 9' /,.q.,qOPERATOR
<� 3 d INITIAL PH16,77)
O 2 HRS.
30 22 HRS.
OPERATIONAL
BELT PRESS SPEED, % q 49
POLYMER PUMP SPEED, % ` C!
SLUDGE PUMP SPEED, % GPM
WIL NEED AUGER, LBS/HR
MIXER SPEED, % 0 0
Revised 8/12103
........................._........................................................
POLYMER USAGE
PE USED o�
TANKS MIXED

TWSA LIME STABILIZATION
DAILY RECORD
DATE _ % ,2- S)O e f
ART P ' - 1
RUN TIME, HRS
SLUDGE FEED, GAL
,LIME FEED, LBS 0
�r
3 '5-�e
TOTAL
SLUDGE FEED % SOLIDS LA
PRESS, °% SOLIDS[::::::::::=
LIME/SLUDGE RATIO EDV� TOTAL PRODUCTION, DRY TONS
Inlet reached temp @ —! „ l,,� ; a a
Outlet reached temp @ ; a g
PATHOGEN REDUCTION
VECTOR ATTRACTIONRfEDUCTION
I D3 ��s-- Z �_ = ( - . d�l�
TIME 1'�4 s- 5wg-
OPERATOR
- v J l./ INITIAL PH
1A "J" g,-g ' o 03 Cam— , of---�-
2 HRS: v� a
�0 22 HRS. A..
....................................................................................... ...................................................................................................................................................................................
OPERATIONAL POLYMER USAGE
3ELT PRESS SPEED, % _ (l
TYPE USED
'OLYMER PUMP SPEED, % 2 a
ANKS MIXED
;LUDGE PUMP SPEED, % J.--) GPM Lo0
Ilh 1EED AUGER, %_ .3 : LBS/HR I
LITERS/TANK
IIXER SPEED, % !� d
vised 8/12103
194(p f(o-5

DATE 0 Lt
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
TOT
Tr, 3D _ 1 i'3o I g 1,%4 1
SLUDGE FEED % SOLIDS / p PRESS, % SOLID
LIME/SLUDGE RATIO C OZ TOTAL PRODUCTION, DRY TONS
Inlet reached temp a /. -04?
Outlet reached temp @
PATHOGEN REDUCTION
TFMPFRATI IRF nF
JE .
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
ao
aotp
E�
koa
a'o(o
6td10
Id/
)'_o s
OPERATIONAL
VECTOR ATTRACTION REDUCTION
63 CAI-- 7
TIME ��, S� ` j)-' ykl OPERATOR
o� yd INITIAL PH �. S
o3(AS'- act) _ l 033
2 HRS.
22 HRS. �—
BELT PRESS SPEED, %
POLYMER PUMP SPEED, % H L
SLUDGE PUMP SPEED, % 60 GPM
LIA ..TEED AUGER, % —i LBS/HR (QU
MIXER SPEED, % / DO
Revised 8/12/03
POL
YPE USED 33 a C
ANKS MIXED
5�7.6 ib5

RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS.
TWSA LIME STABILIZATION
DAILY RECORD
DATE. ho /0 9
START STOP TOTAL
q I � of I 1 D.S. �
SLUDGE FEED % SOLIDS CPm I
LIME/SLUDGE RATIO
Inlet reached temp @ o •�
Outlet reached temp @
PATHOGEN REDUCTION
TFMPFRATLIRF nF
( E
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
/9+
lsg
fc �
aol
an y
co
BELT PRESS SPEED, %
OPERATIONAL
4
POLYMER PUMP SPEED, % 110
PRESS, °% SOLIDS
TOTAL PRODUCTION, DRY TONS
SLUDGE pi i!!4P SPEED, % 60 GPPA O
LIN, _ .,IEED AUGER, % 3 LBS/HR `Z
MIXER SPEED, % / O O
Revised 8/12/03
DRY TON
* o 5-
VECTOR ATTRACTION REDUCTION
TIME /x S'/1a6y /X-SW OPERATOR
INITIAL PH�
036�- U-'7)-- /.'7 = ,Ar/
2 HRS. I)L,6
ro3(Xr---)5'7)
&sy0%r0--r =& s�I
22 HRS.
POLYMER USAGE
TYPE USED ,33 �-
TANKS MIXED TW_
AN

TWSA LIME STABILIZATION
DAILY RECORD
a ff /
DATE ///
ST,
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS 1 .(:7)
SLUDGE FEED % SOLIDS t3n U(
LIME/SLUDGE RATIO a V 1
U=:1
Inlet reached temp @ s,6 q
Outlet reached temp @ I A3
PATHOGEN REDUCTION
TEMPERATURE of
( �1E
INTO
VESSEL
OUT OF
VESSELS
OPERATOR
OLO
),3
o` D,3
aD l
�,.J
sax3
mS
v7
S' 3 �.
10.3
Aca
Ar
71
Ad
PRESS, % SOLIDS_
TOTAL PRODUCTION, DRY TONS �r
DRY TON
WE
VECTOR ATTRACTION REDUCTION
TIME /J.�l 12"`rlrOPERATOR
INITIAL PH
r 0 3 (x,- — U�)=4,3 =
A,
P 46" 2 HRS. ?
JAW/ ff 03:7
22HRS. 0-6
OPERATIONAL
BELT PRESS SPEED; % 3
POLYMER PUMP SPEED, %�
SLUDGE pt mfip SPEED, 4! `7 GPM
1-I1�:`-.'EED AUGER, % LBS/HR q
MIXER SPEED, % 400
Revised 8/12/03
TYPE USED g C1
TANKS MIXED
AN

TWSA LIME STABILIZATION
DAILY RECORD
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
DATE`/D?
START Sy/TOP TOTAL
--T—i
}��jl�
FJ 9 r -7! //S— I f `
SLUDGE FEED % SOLIDS '
LIME/SLUDGE RATIO a
Inlet reached temp @ 9 ; ©(�
Outlet reached temp @ I q a ;71
PATHOGEN REDUCTION
TEMPERATURE of
1E
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
CID
(m`
C0
p.zo
jqq
SN 3 1
hr
Ar
DRY TON
PRESS, % SOLIDS
TOTAL PRODUCTION, DRY TONS 1 3.091
VECTOR ATTRACTION REDUCTION
/ 03� = S4= 3 _ ,0 9
TIME /)-'y /- c /' ' /, of OPERATOR
INITIAL PH_ /I- J' A—
U,77) I- ?_ ,off
O 2 HRS. %�--
ix,
�; 30 22 HRS.
OPERATIONAL
BELT PRESS SPEED, % 1149
POLYMER PUMP SPEED, % o SLUDGE PUMP SPEED, % y511, GPM 041
W rEED AUGER, % LBS/HR fLC
MIXER SPEED, % 10 Z)
Revised 8112103
POLYMER USAGE
PE USED '2302
TANKS MIXED
LITERS/TANK (67
jIC�•� I.�s

RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
TVVSA LIME STABILIZATION
DAILY RECORD
DATE 12S)04
STOP
ART TOTAL
e—
'SLUDGE FEED % SOLIDS =-Li= PRESS, % SOLIDS[::::
LIME/SLUDGE RATIO TOTAL PRODUCTION, DRY TONS Ed�
Inlet reached temp Q
Outlet reached temp
PATHOGEN REDUCTION
TEMPERATURE of
INTO OUT OF
'IE VESSEL VESSEL OPERATC
JL11v INITIAL PH—
/ oeg- o3 ag'o);= 3 r of
o 2 HRS.,
0
os j rf
22 HRS.
...........................................................................
OPERATIONAL POLYMER USAGE3ELT PRESS SPEED, %0���7 USED)OLYMER PUMP SPEED, %LIUDGE PUMP SPEED, % r_1 ANKS WED -------
PM 00
I
EED AUGER, LBS/HR_�2�
LITERS/TANK
IIXER SPEED, %
VECTOR ATTRACTION DUCTION
A3 C) q9�
TIME
OPERATOR
��-
TYPE
vised 8112103

i
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
TWSA LIME STABILIZATION
DAILY RECORD
DATE`}
START STOP TOTAL
o .s c
SLUDGE FEED % SOLIDS ,
LIME/SLUDGE RATIO t
Inlet reached temp @ I 1 a�j
Outlet reached temp @ I d, - I C)
PATHOGEN REDUAON
TFMPFRATI IRF nF
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
,et ;11)
/60
«s'
.C-D
PRESS, % SOLI
TOTAL PRODUCTION, DRY TONS
VECTOR ATTRACTION REDUCTION
os� =
TIME %a'u� �' OPERATOR��
INITIAL PH \
2 HRS.
�- 22 HRS.,,
................................................................... pc�.�,,,.......a6.p..-3.. v,�. ...............
OPERATIONAL
BELT PRESS SPEED, '%
POLYMER PUMP SPEED, % S© /
33I URGE PUMP SPEED. o/ rn(r)
_IME FEED AUGER, % S-5 LBS/HR
POLYMER USAGE
TYPE USED 48I&YR
TANKS MIXED
AN
MIXER SPEED, % Z a O ?--t,6 t,6 5

TWSA LIME STABILIZATION
DAILY RECORD
DATE /© 0
f/51A
START
RUN TIME, HRS I-?-. Do
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDS
LIME/SLUDGE RATIO 1
Inlet reached temp
Outlet reached temp @
PATHOGEN REDUCTION
TFIIAPFC?ATI IGC .,m
1 nE
Al 00
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
1� �
S;
en
)jo
�
OPERATIONAL
BELT PRESS SPEED, % - G
STOP TOTAL
® S?' A
PRESS, % SOLIDS
TOTAL PRODUCTION, DRY TONS ,
VECTOR ATTRACTION REDUCTION
=- = fa d
TIME OPERATOR
INITIAL PH_J�—S' i;r—:
'YO 2 HRS.
r 03 Cd..!
t tip .f -"d "i= /X•'S�o i
22 HRS.
POLYMER PUMP SPEED, %�
SLUDGE PUMP SPEED, % GPM /lJ 10
LIN ,'EED AUGER, %— LBS/HR e
MIXER SPEED, %
tevised 8112103
POL
YPE USED '"T
ANKS MIXED
,5'�79`t )h5

TWSA LIME STABILIZATION
DAILY RECORD
DATE r
START STOP TOTAL
RUN TIME, HRS '.�� "7►� �� a
SLUDGE FEED, GAL
LIME FEED, LBS I
SLUDGE FEED % SOLIDS
L- L)
. L I
LIME/SLUDGE RATIO
Inlet reached temp
Outlet reached temp p
e ! U
PATHOGEN
REDUCTION
TEMPERATURE OF
INTO
IE VESSEL
OUT OF
VESSEL
OPERATOR
/ q.
r
�Qj
M
P
171
11 *'e
OPERATIONAL
3ELT PRESS SPEED, % 4 3
'OLYMER PUMP SPEED, %
TON
16
PRESS, % SOLIDS
TOTAL PRODUCTION, DRY TONS o
VECTOR ATTRACTION REDUCTION
03
TIME %? �� �- ,�8'�/ =" I� r fi/6 OPERATOR
INITIAL PH i c
r l
2 HRS.
.
22 HRS. A7'�-
:' i iiDGE P %4P SPEED, % rpn4 / /
INS. 1EED AUGER, % �b LBS/HR / ®O
IIXER SPEED, %
vised 8/12/03
...........................................................................................................
POLYMERR USAGE
TYPE USED
TANKS MIXED N
I
1v31e' I'Vs

TWSA LIME STABILIZATION
DAILY RECORD
DATE 119111 m 4
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDSff .
LIME/SLUDGE RATIO f
Inlet reached temp @ EIK=o5
Outlet reached temp Ca `
PATHOGEN REDUCTION
TFIIAPI=PAT7 IOC „c:
YIE
I,, W
INTO
VESSEL
-7
OUT OF
VESSEL
A07
OPERATOR
�,Z6
_51G
iq
s
CzL5,0
�%I
TON
PRESS , % SOLIDS
TOTAL PRODUCTION, DRY TONS
VECTOR ATTRACTION REDUCTION
TIME 1,2 , (p 5 ,QRATOR
� oe INITIAL PH
d 2 HRS. 1 ,
22 HRS. f�..
OPERATIONAL
3ELT PRESS SPEED, %. d 5
'OLYMER PUMP SPEED, %
:L! DGE PUMP SPEED, % p .r
111. TEED AUGER, % Gj LBS/HR
MIXER SPEED, %
avised 8112/03
.................... :......................................... ..................
POLYMER USAGE
YPE USED
ANKS MIXED
)Da.,P_ Hos
_I
'I

TWSA LIME STABILIZATION
DAILY RECORD
f 1 / f �(�
DATE / D J/ a/ r L)T
START STOP TOTAL
RUN TIME, HRS : V b -7 j 7r�— >Q / a
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED °% SOLIDS
LIME/SLUDGE RATIO f i
Inlet reached temp @ I �1 •�
Outlet reached temp @
PATHOGEN REDUCTION
TFflAPFRGTI IPP nG
1E
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
60
E0
H 7
A/--
�7
,fA(
W
r
OPERATIONAL
BELT PRESS SPEED, %
DRY TON
PRESS, °% SOLIDS
TOTAL PRODUCTION, DRY TONS'
CI
VECTOR ATTRACTION REDUCTION
TIME OPERATOR
INITIAL PH-k
2 HRS.
i vJJ 22 HRS.
POLYMER PUMP SPEED, % 3-3
SLUDGE IDGE PUMP SPEED, °! 112 ® GPM _7 f
Llf NEED AUGER, %_ '7 & LBS/HR 7 _`
MIXER SPEED, % _ 106
Revised 8112103
L_ POLYMER USAGE
TYPE USED
TANKS MIXED
LITERS/TANK
106 6- C b5

TWSA LIME STABILIZATION
DAILY RECORD
DATE , / / n4
START
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDS
LIME/SLUDGE RATIO E==
Inlet reached temp
Outlet reached temp @ °
PATHOGEN REDUCTION
TEMPERATURE OF
INTO OUT OF
'lIE VESSEL VESSEL OPERATnR
tag
ws
t
OPERATIONAL
BELT PRESS SPEED, % 3
'OLYMER PUMP SPEED, % 3
STOP
AL
PRESS, % SOLIDS
TOTAL PRODUCTION, DRY TONS . C�
VECTOR ATTRACTION EDUCTION
TIME _, ��� =, ���
OPERATOR
INITIAL PH
006j- /�.- i
...3 0 2 HRS.
O 22 HRS. i
,L UDGE PUMP. SPEED, °h
-it 'EED AUGER, % 4:1- LBS/HR__T
AIXER SPEED, % b
evised 8/12/03
POLYMER USAGE
YPE USED `�
ANKS MIXED
ERS/TAN
)6)L90 91

TWSA LIME STABILIZATION
DAILY RECORD
, Lo
DATE
START STOP TOTAL
RUN TIME, HRS
DRY
SLUDGE FEED, GAL�j
r
LIME FEED, LBS
SLUDGE FEED %SOLIDS
LIME/SLUDGE RATIO
Inlet reached temp @ I g
V
Outlet reached temp
4
PATHOGEN REDUCTION
TPnnDGDAT1 Io=
AE
/poq
INTO
VESSEL
1g •
OUT OF
VESSEL
/s?
OPERATOR
co
�;
19 ),
1 q�
co
[�Ajq
/ qy
)`9�
�w
PRESS., % SOLIDS
[:::::=
TOTAL PRODUCTION, DRY TONS E::Io=
VECTOR ATTRACTIO REDUCTI
nor- to ��la ONc'O7�
TIME 14 S' -- rd�8 = `
OPERATOR
INITIAL PH ` /¢/
tJ 2 HRS. f ��
a5.6) K Dz pal
22 HRS. ,
3ELT PRESS SPEED, %
'OLYMER PUMP SPEED, % j
;Li DGE PUMP SPEED, % GPm U-3
Il, `EED AUGER, % !' .LBS/HR /
41XER SPEED, %
avised 8/12103
YM
YPE USED 4 ' & 4
ANKS MIXED
I ERS/TANK W
���•� �1 5

TWSA LIME STABILIZATION
DAILY RECORD
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDS
LIME/SLUDGE RATIO
Inlet reached temp @
Outlet reached temp @
DATE ��% /fit /0'I
START STOP TOTAL
` '7I3
PATHOGEN REDUCTION
TFMPFRATI IRF nF
f '1E
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
���
%s j `
o
TON
PRESS, % SOLIDS
TOTAL PRODUCTION, DRY TONS 1 61 r
VECTOR ATTRACTION REDUCTION
TIME OPERATOR
�3 INITIAL PH ? Qd
jR S.� 2 HRS.
f� J3 1 22 HRS. c�
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, % J
SLUDGE PUMP SPEED, 4! &0 GPM '7d
Llf ,,,EED AUGER, % LBS/HR ff6
MIXER SPEED, % 10-d
Revised 8/12103
POLYMER USAGE
YPE USED J/g 46
ANKS MIXED -hL I if,
lwlQ 9

DAILY RECORD
DATE ZD.
i
START STOP TOTAL
RUN TIME, HRS %OD
DRY TON
SLUDGE FEED, GAL 7) � I
S
LIME FEED, LBS © ©? C) y
SLUDGE FEED % SOLIDS
LIME/SLUDGE RATIO
Inlet reached temp @ I 1 I
Outlet reached temp @ 6 ; [
PATHOGEN REDUCTION
TFMPFPATI IDC -=
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
1,59
G!9
PRESS, % SOLIDS
TOTAL PRODUCTION, DRY TONS l VL
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, % 3
SLUDGE PUMP SPEED, % GPM
LIME FEED AUGER, % LBS/HR
M, -,� SPEED, % _ / / o
Revised 8112103
VECTOR ATTRACTION REDUCTION
,. 03()-r-10. y) = tV� =, /a r
TIME a,,s - 138= %..3CZ OPERATOR
%D INITIAL PH
6y��kl. q)
2 HRS.
�S . ®?� ld.•5�
22 HRS .['ate Jr �.
POLYMER USAGE
YPE USED (4 1
ANKS MIXED
S-7 (p 165

UPULT Mr—UUKU
DATE /f / �/ •�
� )1
START
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDS m
LIME/SLUDGE RATIO
Inlet reached temp @
Outlet reached temp @ p,j g
PATHOGEN REDUCTION
TF=KAPFR®TI IRC nC
TIME
INTO OUT OF
VESSEL VESSEL
OPERATOR
C-�.oa
OPERATIONAL
BELT PRESS SPEED, % 33
POLYMER PUMP SPEED, % 3
STOP TOT
PRESS, % SOLIDS
TOTAL PRODUCTION, DRY TONS /
VECTOR ATTRACTION REDUCTION
f & 3 - ;IL3 , Sj = I s- = 1 oy,S-
TIME /)L• 5,'•Ogs— — /)-- t%S-Y—OPERATOR
SLUDGE PUMP SPEED, % C) GPM
LIME FEED AUGER, % �,� LBS/HR /
M' � SPEED, % / DO
Revised 6/12/03
INITIAL PH - /a S' #/
2 HRS.
22 HRS.
POLYMER USAGE
PE USED =-F•?L� �,j
TANKS MIXED
LITERS/TANK
r]3 fb s

UHILT KtGUKD
DATE N O 4
}t `
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDS
E::�
LIME/SLUDGE RATIO
b L/
Inlet reached temp @
'`
Outlet reached temp @
v o�
PATHOGEN REDUCTION
TEMPERATURE OF
INTO
OUT OF
TIME VESSEL
VESSEL OPERATOR
/JA
CID
3rs��
03 l�
/ 0A�
�P Rldo
DRY TOP
�-5e
PRESS, % SOLIDS
[����
TOTAL PRODUCTION, DRY TONS s f
..............................................................I .......................
OPERATIONAL
BELT PRESS SPEED, %?�
POLYMER PUMP SPEED, % 3
VECTOR ATTRACTION REDUCTION
f 03(d-r— -Jx - l) %z �LrFz •'10
TIME /m - � - . 087 = 14 RS OPERATOR
a, - -Or INITIAL PH_LIL- -5' jj
2 HRS.
23 C ,5,-/F. J= 5, 3 X, o j
22 HRS. a ��
SLUDGE PUMP SPEED, %_ q.0 GPM g
LIME FEED AUGER, % 3 LBS/HR 906
M" Z SPEED, %
Revised 8/12t03
YPE USED cP
i4NKS MIXED
.IWJJ_L_
51U, 1bs

LJr%[L-T Mr-1-UKU
DATEl%
START STOP TOTAL
RUN TIME, HRS t3c I
F
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED °% SOLIDS e
LIME/SLUDGE RATIO E:fa7l::]
Inlet reached temp @
Outlet reached temp (g (' f
PATHOGEN REDUCTION
TEMPERATURE of
INTO I OUT OF
[/'4Z
�d� 1 � b /SR., C 1)
PRESS, °% SOLIDS
[����
TOTAL PRODUCTION, DRY TONS
VECTOR ATTRACTION REDUCTION
TIME /� - , f ri =/,Z �/�/ OPERATOR
1 43- INITIAL PH G
2 HRS. --�
22H RS -s/�may
] �
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, % -30
SLUDGE PUMP SPEED, % GPM aO v �3
LIME FEED AUGER, %_ `�_ LBS/HR
M" Z SPEED, % _ S Q 19
Revised 8/12103
POLYMER USAGE
YPE USED
i4NKS MIXED

DATE _ �% (o I 0 q_
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDS 1 9 ,
LIME/SLUDGE RATIO 1
Inlet reached temp @ 00
Outlet reached temp @ "! ; 0�3
PATHOGEN REDUCTION
TIME
INTO
VESSEL
OUT OF
VESSEL I OPERATO
Co
�Emu'mjgm
........................................................................................................................
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, % 35`
DRY
PRESS, % SOLIDS
E:::���
TOTAL PRODUCTION, DRY TONS .
VECTOR ATTRA TION R DUCTIOV
TIME 4,7- �'`�'-- %� �,/i�'
OPERATOR
INITIAL PH
las.
©3 CAr /�- j ; �6 � z l y
22 HRS.
SLUDGE PUMP SPEED, % 6o GPM o
LIME FEED AUGER, %_ LBS/HR
Mi; I SPEED, % _ z o o
Revised 8/12/03
...................................................................................
POLYMER USAGE
YPE USED _ 4 0 4,443
ANKS MIXED
77- 6 1155

✓nIL I RCl-Vr[LJ
DATE _ 11 11-y A
RUN TIME, HRS I If 4113 a
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDS
LIME/SLUDGE
RATIO
Inlet reached temp @
'
Outlet reached
temp @
PATHOGEN
REDUCTION
TEMPERATURE OF
TIME%
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
1 ✓
t
%j
Z:�C)CD
J
STOP
/30
PRESS, % SOLIDS
[_����
TOTAL PRODUCTION, DRY TONS 4 c3
VECTOR ATTRACTION REDUCTION
6j,
TIME
�� (P - .f���%� �/3�'
OPERATOR
INITIAL PH
-e 6r-- mj- =
7y
G ``- � _
2 HRS. �.
-a
003
s a c 1
`3
(7`
22 HRS. a , S
eA
.....................................................................................................................................
OPERATIONAL
BELT PRESS SPEED, % 3 7
POLYMER PUMP, SPEED, % 3
SLUDGE PUMP SPEED, % S-19, GPM J Ir
LIME FEED AUGER, %_ LBS/HR
M( Z SPEED, %' t
Revised 8112103
YPE USED 6 �p
ANKS MIXED
_ITERS/TANK `p
' s- 7,Ag- V1 -5

unll- i mr_k,umjj
DATE
START
RUN TIME, HRS 9 : 6-D
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED % SOLIDS
LIME/SLUDGE RATIO
E:j=
Inlet reached temp @
Outlet reached temp @
°
PATHOGEN
REDUCTION
TEMPERATURE OF
TIME
INTO
VESSEL
OUT OF
VESSEL OPERATOR
�f6
C
xos
................................................................................................................
OPERATIONAL
BELT PRESS SPEED, %
POLYMER PUMP SPEED, % 3
AL
{?Q
DRY TON
PRESS, % SOLIDS
[:::::::::=
TOTAL PRODUCTION, DRY TONS
VECTOR ATTRACTION REDUCTION
Ito3 ( a1`.? a /ql_ ") _? - e i—/
TIME 116 )L I = /1-3- 1
OPERATOR
/
®� INITIALPH
%
2 HRS.
e0_?04 =i•(. �16,)L Z- ,
Irr�
14�' � 22 HRS. ./�, q
SLUDGE PUMP SPEED, % GPM Irk 3.3O
LIME FEED AUGER, %_ LBS/HR
M' Z SPEED, % p
Revised all2103
........................................................................
POLYMER u�ar�
YPE USED Cam%
ANKS MIXED
Y 7. 6 1

✓+"%IL 1 rRGVIJPUJ
DATE
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
START STOP TOTAL
a S",
SLUDGE FEED % SOLIDS '7005
d
LIME/SLUDGE RATIO
Inlet reached temp @ % ; 911,1
Outlet reached temp @
PATHOGEN REDUCTION
TIME
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
1
$rs
JS0
��-
Igo
y
Ar
TON
PRESS, % SOLIDS
TOTAL PRODUCTION, DRY TONS
VECTOR ATTRACTION REDUCTION
TIME OPERATOR
fsS INITIAL PH
2 HRS.
�o aCs 5aa��_ f'?,4x,&2 ,aaa
22 HRS. . j�► •3
OPERATIONAL
BELT PRESS SPEED, % Alt
POLYMER PUMP SPEED, % 3
SLUDGE PUMP SPEED, % GPM-70-17
LIME FEED AUGER, % S-O LBS/HR O -
W R SPEED, % o n
Revised 8/12/03
POLYMER USAGE
YPE USED
ANKS MIXED
,13•� Ibs
m

vr��L � RGIiV RU
DATE -
i , F i
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE FEED e% SOLIDS ^ 7 p
LIME/SLUDGE RATIO.
Inlet reached temp @ F%
Outlet reached temp @
PATHOGEN REDUCTION
TEMPERATURE of
TIME
INTO
I VESSEL
OUT OF
VESSEL
OPERATOR
to
f
v`�
d,03
l0
CIO
DRY
PRESS, °% SOLIDS
TOTAL PRODUCTION, DRY TONS 1.0 ~
......................................................................................................................................
OPERATIONAL
BELT PRESS SPEED, % :3 6
VECTOR. ATTRACTION REDUCTION
TIME OPERATOR
'l r ,S'— INITIAL PH
r (� 2 HRS. A ,
S .4a 22.HRS.
.....................................................................:...............................
POLYMER `USAGE
TYPE USED ' 1'? /" A 1110
POLYMER PUMP SPEED, % TANKS MIXED
SLUDGE PUMP SPEED, % 5- GPM
LIME FEED AUGER, % YY LBS/HR
M. Z SPEED, % Ion
Revised 8/12J03
� I, �v Ib's

DATE 1�2
START . " STOP TOTAI
RUN TIME, HRS
SLUDGE FEED, GAL
LIME FEED, LBS
SLUDGE.FEED % SOLIDS / a 0
LIME/SLUDGE RATIO .
Inlet reached temp @
Outlet reached temp
PATHOGEN REDUCTION
TFMPFRATI IRG ni=
TIME-
INTO
VESSEL
OUT OF
VESSEL
OPERATOR
'Al
1919
/S9
C 0
/ 0
q
e- 40
347
Cf.
S ` "/
l
PRESS, %.SOLIDS
TOTAL PRODUCTION, DRY.TONS , Cr .
VECTOR ATTRACTION REDUCTION
f.02 Cyr — fro
TIME S_ /yY����3dX OPERATOR
ICJ
3! INITIAL PH 143
o, , a,s' �a 38T4
—
�r 2 HRS.
a 22 HRS.
OPERATIONAL
BELT PRESS SPEED, % 3
POLYMER PUMP SPEED, % q-3
SLUDGE PUMP SPEED, % GPM W, /O
LIME FEED AUGER, % q 3 LBS/HR
M, 3 SPEED, %
Revised 8/12103
PE USED
TANKS MIXED
I�a•0, rbs