NC0000272_2001ColorTechAssessmentReport_20010201

I
TABLE 1-1 SUMMARY OF 2001 ASSESSMENT OF COLOR REMOVAL TECHNOLOGIES
2001 Color Removal Technology Assessment
Blue Ridge Paper Products Inc.
Canton, North Carolina
COLOR REDUCTION
CAPABILITY
80-90%
80-90%
50-60%
95%
90%
N/A
80-85%
100%
THEORETICAL MAXIMUM
EFFLUENT COLOR, color units
64
64
159
16
32
318 (before mixing)
64
290
THEORETICAL AVERAGE
EFFLUENT COLOR, color units
31
31
94
10
21
208 (before mixing) :
36
190
DEMONSTRATED ABILITY
TO CONSISTENTLY -ACHIEVE
NO
NO
NO
YES
YES
YES
NO
NO
50 COLOR UNITS
ESTIMATED
OPERATING COST
N COST
$26,407,504
$19,341,523
$12,868,528
$28,304,090
$21,890,847
$4,374,404
$6,647,723
$2,137,053
ESTIMATED CAPITAL COST
$57,373,000
$60,884,000
$40,203,000
$149,768,000
$99,289,000
$34,789,000
$38,140,000
$11,151,000
ISSUES
a. No known commercial
a. No known commercial
a. No known commercial installations
a. No known commercial
a. No known commercial
a. This technology does not remove
a. No known commercial
a. No known commercial installations
installations for an application
installations for an application
for an application similar to the Canton
installations for an application
installations for an application
color. It relies on the assimilative
installations for an application
for an application similar to the
similar to the Canton Mill.
similar to the Canton Mill.
Mill.
similar to the Canton Mill.
similar to the Canton Mill.
color capacity of the river.
similar to the Canton Mill.
Canton Mill.
b. Plants using alum as an end -of-
b: Full-scale lime treatment for
b. Treatment process is incapable of
b. Color reduction capability
b. No pilot tests have been
b. This technology is very sensitive
b. An extensive research
b. Assumes color remaining in waste -
pipe color removal technology
color removal at other facilities was
achieving color target of 50 color units.
removal percent is based on an
conducted using this technology.
to increases in treated effluent color
effort by EPRI and Bowater
water treatment influent would still
abandoned those operations due to
abandoned due to inability to
engineering,judgment.
and/or drought conditions. Either
achieved a much lower
undergo a 25% color reduction across
operating difficulties and
achieve color objective.
c. Downstream site required due to
c. Color reduction capability
condition can result in a significant
actual color removal
the treatment plant.
inconsistent performance.
insufficient land on site.
c. Downstream site required due
removal percent is based on an
increase in the required pond
efficiency (25-30% removal).
c. Downstream site required due
to insufficient land on site.
engineering judgment.
volume.
c. Assumes excess steam is available
c. Downstream site required due
to insufficient land on site.
d. Incinerator and air permitting
c. Downstream site required
at the Mill.
to insufficient land on site.
required.
d. Incinerator and air permitting
d. Downstream site required due
c. If the river flow decreases by
due to insufficient land on
d. Effluent total dissolved solids
required.
to insufficient land on site.
13% (drought), the river will not
site.
d. Effluent total dissolved solids
(TDS) likely to increase by 20 to
have the needed assimilative color
(TDS) likely to increase by 20 to
25%.
capacity.
25%.
e. May require add -on process for
d. This scheme would result in
e. May require add -on process for
TDS removal at additional cost.
nearly depleting the river flow
TDS removal at additional cost.
during drought conditions.
f. Incinerator and air permitting
f. Incinerator and air permitting
required.
required.
tablet -1.xls 1-3 Rev. 5

MILL WATER DRY
POLYMER
a ALUM TANKS
40'DIA x40'H EA
5 DAYS CAP
SEA
c(\
I TRUCK
DELIVERY
O DRY
POLYMER
FEED
SYSTEM
ALUM FEED PUMPS (2) 0
.. - 40 GPM EA 50' TDH,
1 HP EA
SECONDARY 60' DIA
TREATMENT 24.6 MGD AVG
PLANT
EFFLUENT 26.7 MGD MAX
pH ADJUSTMENT
BASIN
2 MIN RETENTION
35'L x 16'W x 11' D WI
MIXERS
2 0 10 HP EACH
SCREEN
SEPARATOR
v
TO LANDFILL
DREGS
WASHING
TANK
10'DIAx10'H
DREGS PUMPS (2)
50 GPM EA 0 100' TDH
2 HP EA
30 PSI STEAM
FROM MILL
REACTOR CLARIFIERS (2)
170' DIA x 15' SWD
60% CAPACITY
4 HOURS RET
50% CAUSTIC
STORAGE TANK
24' DIA x 24' H
ELECTRIC TRACED
7 DAY CAP
TRUCK DELIVERY
CAUSTIC METERING
PUMPS (2)
6.50 GPM EA
0.5 HP EA
30' DIA
DISCHARGE 0 EXISTING OUTFALL
TREATED WASTEWATER
pH ADJUSTMENT
72
TRANSFER PUMPS (3)
BASIN
10,000 GPM EA E100' TDH
MIN RETENTION
350 HP EA
35'L xIVWx11'D
SLUDGE TRANSFER 706 GPM
PUMPS (3)
1,632 GPM EA 0 75'
TDH, 60 HP EA
2,966 GPM
SLUDGE 0
1% SOLIDS
RECYCLE PUMPS (2)
DISSOLVED AIR 594 GPM EA 0 160' TDH
40 HP EA
FLOTATION THICKENER
40' DLA
SCREW PRESS
SLUDGE FEED PUMPS (2)
STORAGE TANK
26 DIA x 36' H SULFURIC ACID BLEND TANK 653 GPM EA 0 100' TDH 25
METERING PUMPS 15' DIA x 15' H HP EA
7 DAY CAP 6.5 GPM 00.5 HP EA 30 MIN
0 594 GPM RETENTION O 80 TPD (DRY)
5%SOLIDS 1600 TPD(WET
O 05% SOLIDS
AIR
AIR COMPRESSOR
SATURATION
BATCH REACTOR SULFURIC TANK
SCREW PRESSES (4)
ACID FEED PUMPS \ \ \ / ID 60 TPD EA
200 GPM EA 0 20 PSI
5 HP EA
CYCLONE
STORAGE SEPARATOR
SILO
10, DIA X25'H BUCKET ELEVATOR 0 �_ SCREW PRESS
FILTRATE PUMPS (2) 653 GPM
STACK SCRUB- EA 0 50' TDH 15 HP EA CONCRETE PAD FOR
BER 24 HR STORAGE
VENT �..REWCO.VEYOR SCREW CONVEYOR (PD(W ')
891 TPD (WET) 0
20% SOLIDS
SCREW CONVEYOR
BATCH FLUIDIZED SLUDGE
REACTOR BED ® MIXER
INCINERATOR
16'D01X 16'H
NO.2 FUEL OIL HEATER
STORAGE
TANK AIR SUPPLY
FAN (g—
ALUM MUD TO MILL SCREW CONVEYOR
TRANSFER PUMPS PUMP & HEATER CAGE Ell
(2) 900 GPM EA 0 MILL
100' TDH SET 10 HP EA

Pigeon
River
Transfer
Pump
Sump
Reactor Clarifier
No. t
_—.—.—.—.—. SludgeT
ank
I
I O DAF Sludge
O Clarifier Presses
I
Retention
Basin
i
i Alum
U
U
�
�
Sludge
S
Storage
0
Incinerator
0
'o
U
Building
Tank
Reactor Clarifier Alum O O No. 2 Fuel Oil
No.2 I Silo O
Caustic Dregs
— O C
—•—•—•---•—�---•—•—•—•— Batch Washer
Tank Reactor
Bark Storage Area North of Fibreville
Pigeon
River
Highway
North
JACOBS
ENGINEERING 1
Figure 3.2
End -Of -Pipe Color Treatment
Alum Color Removal System
General Arrangement
Scale: 1" =100 Ft.

35 PSI STEAM
9,468 LBSMR
MILL WATER 600 GPM
35°F MIN
HEAT EXCHANGER
CONDENSATE TO BOILER
FEEDWATER SYSTEM
I SECONDARY TREATMENT
PLANT EFFLUENT
24.8 MGD AVG, 28.7 MOD MAX ,
30C
STACK
SCRUBBER
LIME SLURRY
LIME SLURRY FEED PUMPS (2) TRANSFER PUMPS
500 GPM 0 100- TDH 20 HP EA 600 GPM 0 50' TDH
30 HP EACH
LIME SLURRY
STORAGE TANK
23'DIA x24'H
2 HR CAP
PNEUMATIC UNLOADING LINE FOR
TRUCK DELIVERY
30 TPD
FANS (2)
5 HP EA
825 TON
STORAGE
LIME SILO
27,500 FTC
33' DIA x 33' H
3 DAY CAP -
IF SCREW FEEDERS (2)
0100% CAP EA
LIME SLAKERS (2) 0.083 TPD 0 25 HP EA
0 80% CAP,
10HPEA
GRIT
HANDLING
SYSTEMS
BUCKET
ELEVATION
25 HP
1
PRIMARY A R
FAN 75 HF'
LIME KILN
275 TPD
DRAG LINE CONVEYOR
275 TPD 25 HP
CRUSHER
15 HP
SECONDARY AIR
FLOW
150 HP
10 GPM
VENTURI
SCRUBBER
SCRUBBER
RECIRCULATING
TANK
W 15'Dx15'H
30 MIN RETENTION
SCRUBBER RECIRCULATING PUMPS (2)
500 GPM 0 100' TDH,
20 HP EA
STACK
FUEL OIL PUMPS (2)
10 GPM 0 300' TDH EA,
2 HP EA
CONDENSATE TO
MILL
SULFURIC ACID
182,000 LBSTORAGE TANK
S/DAV 64,018 GAL II F VAPORIZERS CO2 SYSTEM pH ADJUSTMENT 24' DIA x 24' H
BASIN
VERTICAL STORAGE TANKS (9) 2 MIN RETENTION
2VDV. x4VH 35'Lx 17'W x11'D
SULFURIC ACID TREATED WASTE
METERING PUMPS (2) TRANSFER PUMPS
9 GPM 0 100' TDH EA, (3)10,000 GPM 0 .
1 HP EA 10V TDH
350 HP EA TO DISCHARGE 0 EXISTING OUTFALL
REACTION BASIN III
68'Lx 34'W xIVD 24.8 MGD AVG, 29.1 GPM 30'DIA
TPD EA 0 40% 10 HP MO
15 MIN RETENTION SCREW CONVEYORS MOTOR
OR
COLOR CLARIFIERS (2) RECARBONATION CLARIFIERS (2)
60% CAPACITY EA 60 % CAP EA
170' DIA x 15' SIDEWALL DEPTH
17V DIA x 15' SWO
RECAR ON BASIN VACUUM
35' L x x 1 17' WT W x 11' D FILTERS (3)
631 GPM 0 3% SOLIDS 2 MIN RETENTION 501/6 CAP EA
160 TPD EA LIME KILN FEED SCREW CONVEYOR
30 HP 1200 TPD 0 40 %
SLUDGE TRANSFER PUMPS (3) SLUDGE TRANSFER PUMPS (3) SILENCER
315 GPM EA 0 100' EA 573 GPM EA 0 11XT EA 20 HP EA
15 HP EA -
1778GPM
SLUDGE 0 3% SOLIDS
374 TPD VACUUM FILTER FEED PUMPS (3)IF
977 GPM EA ® 25' TDH 10 HP EA
O
VACUUM PUMPS (3) PRECOAT CALCIUM
SLUDGE BLEND TANK 25 HP EA PUMPS (2) CARBONATE
1 HR STORAGE 5 HP PRECOAT MIX TANK
28'DIAX28'H 8'DIAx VH
NO.2 FUEL OIL
STORAGE TANK
83,160 G4L
24' DIA x 24' H
FILTRATE PUMPS (3)
977 GPM 050' TDH EA
20 HP EA

Recarbonation i
Clarifier No. 2
I
I
I
Sludge Dewalering Building
w/ Precoat Filters \Scruccer
Sludge :G
Transfer —� I . _.
Pumps ❑
i O
Tank
I
I
Recarbonation
Clarifier No. t Control Rm/
MCC
---•—•—•—•—L.................... ` Lime Kiln
I
j c c
O N
n �
Sludge Tank
m
I � O
i
Lime Slurry
jStorage Tank
i
ColorClarifier O Pigeon
No. 2 I River
Pigeon — _.—•—•---•—,�—'—•---•—•—• � ❑ i
River
i Highway
Lime
Sludge I Silo
Transfer
Pumps I O
Ool
No. 2 Fuel Oil North
Reaction Basin —- .—._. Tank
OSulfuric Acid
i Tank
C� ❑
ColorClarifier c ��
No. t I E
a C� ❑
N
j m C� ❑
x
j a OBS
ENGINEERING®
L
j Transfer Pump �� ❑
j Pit C� O Constructor!Engineers and
i Figure 4.2
[COTanks ❑
Bark Storaap_* a North of Fibreville C.� ElEnd-Of-PipeColor Treatl
C� Lime Color Removal Sy:
El
General Arrangemen
r= El Scale: 1" =100 Ft.

LIQUID POLYMER
STORAGE TANK
33,486 GAL POLYMER FEED PUMPS (2)
1 B'DIAx 18'H 3GPM EA@100'TDH
7 DAY CAP 4784 GPD 0.6 HP EA
TREATED WASTEWATER
80' DIA
GPM
STATIC MIXER
POLYMER REACTION BASIN
5 MIN RETENTION
47'L x 24'W x14'D
DRY POLYMER
HOPPER 172 PPD
0�
POLYMER
SOLUTION TANK
600 GAL CAP
POLYMER FEED
TANK
500 GAL CAP
POLYMER FEED PUMPS (2)
5 GPM @ 100' TDH EA
0.5 HP EA
TERTIARY CLARIFIERS (2)
170'DIA x 15' SWD EA
30' DIA
WASTE TRANSFER PUMPS (3)
10,000 GPM @ 100' TDH
350 HP EA
SLUDGE TRANSFER PUMPS (3)
79 GPM @ 100, TDH I B.B TPD
5 HP EA 1%SOLIDS
143 GPM
SLUDGE BLEND TANK
30 MIN STORAGE
4,302 GAL
10'DIAx VYH
SCREW PRESS FEED PUMPS !3)
RATED FOR 78 GPM @ 100'
5 HP EA
STACK
SCRUBBER
RECIRCULATING
PUMPS 120 GPM @
75V EA 40 HP EA
VENTURI
SCRUBBER
ROTARY SCREEN
THICKENERS (2)
RATED FOR 20 TPD DRY
SOLIDS EA
SCREW PRESSES (2) RATED
FOR 20 TPD DRY SOLIDS
FILTRATE TANK
FILTRATE PUMPS (2)
30 MIN RETENTION
RATED FOR 168 GPM @ 100' TDH
10'DIAx16H O
7.6 HP EA
18 ODTPD @
45% SOLIDS
30 LB'HR 55 PSI STEAM
-� SLUDGE
STORAGE
FROM MILL
W x 25' L
SCREW CONVEYOR //^\2\5'
NO. 2 FUEL OIL
0% 60 TPD/ 2SOLIDS TANK
C�
10,000 GAL
SLUDGE PRIMARY AIR 12' DIA x 12' H
INCINERATOR O FAN �- 7 DAY CAP
PUMP 8
HEATER SET
CONDENSATE TO
,
MILL
DUMPSTER STORAGE
TO EXISTING OUTFALL

Pigeon
River
Reactor I \
Clarifier I
No.2
I
Transfer — PolymE
Pump •---• •� --
Sump Basin
I
I
Reactor
Clarifier i
No. 1
— I
I
Bark Storage Area North of Fibreville
Filtrate
Sludge Tank Sludge
Tank 00 / Presses
il
Sludge
v
Storage
E
O
Incinerator
0
o
U
Building
F7 O No. 2 Fuel Oil
Ash
Hopper
Pigeon
River
Highway
North
OBS
ENGINEERING
Figure 5.2
End -Of -Pipe Color Treatment
Polyamine Color Removal System
General Arrangement
Scale: 1" = 100 Ft.

DETERGENT
CAUSTIC MIX TANK
FEED HOPPER
6,000 GAL CAP I V DIA x I V H
CAUSTIC MAKE-UP PUMPS
50%CAUSTIC
(2)
STORAGE
10 GPM ® 50' TDH EA 0.5
CAUSTIC CLEANING
TANK
HP EA
PUMPS (2)
12,000 OAL
60 GPM ®230' TDH EA 5
HP EA
DETERGENT
DETERGENT PUMPS
MIX TANK
60 GPM Q 250' TPD
GA
10 HP EA
1191A x I I IH
�►
CITRIC ACID
FEED
HOPPER CAUSTIC METERING
PUMPS
10 GPM EA
1 HPEA
SECONDARY TREATMENT
PLANT EFFLUENT
24.8 MOO AVG 28.7 MOD MAX
SAND FILTERS
5 CELLS ® 1760 SF EA
0625 FT' TOTAL
SAND FILTER FEED PUMPS (3)
10,000 GPD Q 25 TDH
100 HP EA
AIR
COMPRESSOR
125 HP
BACKWASH PUMPS (5)
400 GPM @ W TDH
10 HP EA
CI IC
ACID MIX
TANK
6,000 GAL
CA CITRIC ACID
CLEANING PUMPS
60 GPM @ 2W TPD
10 HP EA
BACKWASH
RETURN TANK
36,000 GAL CAP
20' DIA x 20' H
CLEARWELL 600,000 GAL CAP
105x 110,X9'
U.F. FEED PUMPS (5)
5,000 GPM ® 230' EA I♦'-
400 HP EA
RETURN PUMPS (2)
1200 GPM Q 100TDH
50 HP EA
160°F WATER
FOR
CLEAN NO
50.000 GAL
•
DIRTY CAUSTIC
HOT WATER CLEANING PUMPS (2) 270
PUMPS (2)
GPM Q 280' TDH
100 GPM Q 230' EA
30 HP EA
10 HP EA
ULTRAFILTRATION SYSTEM
20 MODULES Q 10000 SF/ MODULE
FLOW RATE • 150 GPDISF
AUXILIARY
FUEL
STORAGE
TANK 20,000
PUMP HEATER
GAL
SET
16'DIAx 1611
2HP
INCINERATOR
[_
AFTER
W R
LOWER
WET DRAG RAM FEEDER
30 HP
CONVENOR
RECYCLE PUMPS (2)
RECYCLE PUMPS (2)
ASH
1058 GPM Q 70' TDH
22 GPM Q 90' TDH
4.i TPD
30 HP EA
1HP EA
80 GPM
PRESCRUSBER SLOWDOWN PUMPS (2)
38 GPM Q 100' TDH
2 HP EA
BURNER
ION12N0
1600°F
WETPRE3CRUBBER
F'E�T
50F
ROTARY KILN
SCRUBBER
SCRUBBER WATER FEED PUMPS (2)
35 GPM hl 120' TDH 2 HP EA
DIRTY CONDENSATE PUMPS (2)
137 GPM ® 100' TDH
5 HP EA
-111 22WF
HEAT EXCHANGER
15 GPM Q 50% SOLIDS
500,000 BTUIHR
DIRTY CAUSTIC
RECYCLE
TANK
15,000 GAL CAP
14'DIAx 14'H
Uf
►
CONCENTRATE
STORAGETANK
100.000 GAL 32
OF CONCENTRATE PUMPS (2)
DIAx32 H
0137 EA
►OPM�61100'TD—HIO—HP
OF PERMEATE
COOLING TOWER
30°F Drop —
Fmt (2) ® 40 HP EA —
COOLING WATER PUMPS _
1367 GPM @ 75' TDH
40 HP EA
CONDENSER
1250 GPM COOLING WATER
DT�O°F
WFOLIDS
35 PSIG STEAM
LEAN
DENSATE
fRET
BOTTOMS PUMPS
RNTANK15
GPM Q 200 TDH
O3HPEA
VACUUM PUMP
125 HP
AXTH
CLARIFIERS AT MILL
TO DISCHARGE AT EXISTING GUTFALL
24.6 MOD AVG 28.5 MOD MAX
No
TREATED WASTE TRANSFER PUMPS (3)
10,000 GPM Q 100' TDH
350 HP EA
CLEAN CONDENSATE RETURN
PUMPS (2) 31 GPM 0 100' TDH
1 HP EA
r7
TO MILL

r-7
Pigeon
River
Ultrafiltralion Building
Sand Filter Building
140' x 120'
140' x 150'
Includes 20 OF Modules, Includes
5 Sand Fillers,
Rom
105' x 110' Clearwell
rn+Tanks(}�C�:ontt"rroll
Transfer
v
——•—•—.—•—•_
—.
Pump
Sump
— —
— — — — — —
1
LJ LJ L1 LJ
o
Detergent
Mix Tank
rj j�
+LJ1—FLJF—
——.—,—.—,—,—,—_
—
Dirty
Qil O
Caustic
Tank
Citric Acid
O O O
Cooling
Q
Tower
Q
O
50%
Mix Tank
OF
Concentrate
Tank
?
Hot Water
Evaporators
Rotary Kiln
Caustic
Backwash Tank
Return
Tank
Cleaning
(i
��
Incinl eratnr
I i�
Bark Storage Area North of Fibreville
Pigeon
River
Highway
North
OBS
ENGINEERING"
Figure 6.2
End -Of -Pipe Color Treatment
Ultrafiltration Color Removal System
General Arrangement
Scale: 1" = 100 Ft.

TO PRIMARY CLARIFIERS IN MILL
SULFURIC ACID
STORAGE TANK
11,840 GAL CAP
14'DIAx 14'H
METERING PU MPS (2)
2.0 GPM @ 20 PSI EA
0.5 HP EA
SECONDARY EFFLUENT
24.8 MOD AVG 28.7 MOO MAX
SPENT CARBON
STORAGE TANK
8500 FT'
20'CIA x20'H
PH ADJUSTMENT BASIN
35'x 18'x11'
2 MIN RETENTION
SPENT CARBON
FROM COLUMNS
TSS-20 MOIL
PH 8.0
SAND FILTER PUMPS (3)
10,000 GPM @ 25 TDH
100 HP EA
STEAM
DEWATERING
SCREW
FEEDER THERMAL
REACTIVATION
UNIT 87fPH CAP
AIR COMPRESSOR
125 HP
SAND FILTERS
S CELLS @ 1,760 SF EA
8,8W SF TOTAL
BACKWASH PUMPS (5)
400 GPM @ 50' TDH
10 HP EA
0
0
0
BACKWASH
RETURN
PUMPS (2)
1,2D0 GPM @
1O0' TDH
BACKWASH
50 HP EA
RETURN TANK
36.000 GAL CAP
-� 20'DIA x 20'H
TSS <5MG/L
CLEARWELL
110'x 105' x V
CARBON COLUMN
FEED PUMPS (3)
10,D00 GPM @ 76 TDH
3DO HP EA
CARBON
CARBON
COLUMN (20)
COLUMN (20)
28,SW #
28,8001
CARBON EA
CARBON EA
18 MIN
18 MIN
RETENTION
RETENTION
12'DIAx 12'H EA
12'DIAx 12'H EA
SPENT CARBON PUMPS (5)
188GPM @100'TOHEA
10 HP EA
PH ADJUSTMENT BASIN
35'x 18'x 1V
2 MIN RETENTION
CAUSTIC METERING
PUMP'S (2) 2.5 GPM EA
0.5 HP EA
TERITARY EFFLUENT PUMPS (3)
10,000 GPM EA @ 100' TDH
40D HP EA
50% CAUSTIC
STORAGE TANI
64,000 GAL
24'DIA x 24'H
_L REGENERATION FEED A- T
��-"
_ PUMPS (2) I
- 275 GPM EA @ 76' TDH _ NATURAL GAS
O
VENTURI
15 HP EA
PREHEATER
CAUSTIC TRANSFER
SECONDARY AIR
PE
tT
PUMPS (2)
FAN
250 GPM EA @ 25'
STACK
4 HP
TDH 3 HP EA
MAKE-UP CARBON
STORAGE TANK
5,428 FT'
CARBON TRANSFER PUMPS (2) CARBON RE -SLURRY
EVAPORATOR
20'DIA x20'H
150 GPM EA@100'TDH TANK
10 HP EA 10,000 GAL CAP
12' DIA x 12'H
STEAM
REGENERANT FEED REGENERANT MAKE-UP
♦-
PUMPS (2)1527 GPM STORAGE TANK
-
EA @ 75' TDH 2O,300 GAL
GOHP EA 18'DIAx 18'H
COLUMN RECHARGE
_
PUMPS (2)
INCINERATORS (1)
100% CAP EA
BOTTOMS PUMPS (2)
EVAPORATOR RECYCLE PUMPS (2)
NO. 2 FUEL OI L
1800 GPM @ 126' TDH
40 GPM E@ 76' TDH
162 GPM @ 60' TDH EA
TANK 204,000
126 HP EA
H
2 HP EA
5 HP EA
GAL
34'DIAx 34'H
FUEL OIL PUMPS (2)
20 GPM EA
ASH TO LANDFILL
1 HP EA
I�
2.6 TPD
J.

Pigeon
River
Sand Filter Building
140'x150'--------
Includes 5 Sand Filters,
105' x 110' Clearwell — -- • — - — • --------------
-
..... .... ...... .. {►{��y�,.
Carbon Adsorption Building
250' x 150'
Includes 40 Carbon Vessels
:....................... ..... .. .
Fuel Oil
Tank
Incin- Control Room
erator
Make-up Carbon O orOo Thermal
Storaqe Tank Reactivation Unit
�V00000
Carbon �O
Reslurry Tank /
Sulfuric Acid Spent Carbon
Storage Tank Storaqe Tank
Caustic Regenerate Make -
Storage Tank up Storaqe Tank
Bark Stora-ge Area North of Fibreville
Backwash
Return
Tank
Transfer
Pump
Sump
Pigeon
River
Highway
North
JACOBS
E N G I N E E R I N G'&
Figure 7.2
End -Of -Pipe Color Treatment
Carbon Adsorption Color Removal System'
General Arrangement
Scale: 1" = 100 Ft.

NEW OUTFALL STRUCTURE
30 MIN CAP
STORAGE POND FEED PUMP:'
(3)
SECONDARY EFFLUENT 10,000 GPM @ 200' TDH EA
1000' PIPE 30' Diameter 750 HP EA 48' Diameter 1000' PIPE
24.8 MGD AVG 28.7 MGD MAX 57,000 GPM Max 24.8 MGD AVG 57 MGD MAX
30' Diameter
30' Diameter
20.000 GPM Max
30' Diameter
Assume 3 Mile Long
STORAGE POND HIGH SPEED
FLOATING AERATORS (7)
10,018 GPM Max 75 Hip EA 30' Diameter
20,000 GPM Max
STORAGE POND ,
175 ACRES
30' Diameter
STORAGE POND RETURN
PUMPS (3)
10,000 GPM @ 100' TDH EA
350 HP EA
J11NBS
ENRING0
FIGURE 8.1
END -OF -PIPE
COLOR TREATMENT
STORAGE AND TIMED RELEASE SYSTEM
FLOW DIAGRAM

Pond Influent/Effluent Line
..............................................................................A
Pump Station/
Maintenance Building
40' x 100'
Provide:
Access Roads
Perimeter Roads
Security Lighting
Security Fencing
Maintenance Trucks
Mowing Equipment ......
Road Upkeep Equipment
Maintenance Boats
Maintenance Barge
I
.....
..........................................................................................................................................
....................................................................................................................................... :
Floating Docks (4)
200' Long Each
O j
i O
i
d
I
I
I
—
I
I
------------------------------------------------------------ I--------------------------- 0•—•—•—•—•—•—•——•—•—•—•—•— — —
I
I
—
Aerators (7)
Storage & Time Release Pond j High Speed
153 Acres Water Surface j Floating
Location Undetermined
I
I O
O I
I
I

144,065 LBS/DAY 02
EFFLUENT BASIN
35'LXITWXIVD
2 MIN CAPACITY
TO DISCHARGE @ 24.8 MGD
EXISTING OUTFALL 28.7 MGD
TREATED WASTEWATER TRANSFER
PUMPS
3 @ 10,000 GPM &100' TDH EA
VAPORIZERS COMPRESSOR

I Reaction Tanks
..........................................
11 00 ❑ Il InfluenU
Ozonalor Effluent
Vaporizers Basins
Oxygen Tanks Control Roots
MCC
Pigeon
River
J
I
Bark Storage Area North of Fibreville
Pigeon
River
Highway
North
OBS
ENGINEERING'
Figure 9.2
End -Of -Pipe Color Treatment
Ozonation Color Removal System
General Arrangement
Scale: 1" =100 Ft.
l

SURFACE CRYSTALLIZER AFTER PURGE FILTER
CONDENSER EJECTOR CONDENSER EJECTOR
OPTIONAL COOLING WATER
RETURN
r---------------------------------------- i------------------------------------ ------------------------------------
VAPOR TO EVAPORATORS I I COOLING WATER
1
I I SUPPLY
I
I I 1 1
I I I I
I I I I
HP STEAM
r----------------------------------------------------------------------- -44-
MISC WATER I I
-�---------- I i CRP FILTER
I
-------------------------------------------------
lip
I----- ----
PURGE CRYSTALLIZER PURGE CRYSTALLIZER I
HEATER VAPOR BODY L________________________
r---0 r ---- - --------
STEAMIVAPOR
I I
I 1
I I
I I
1
I IPROCESS
-----------------------------------------------------------------------------------------------------------------t---------------------------------------------------------------------
AGITATOR I I 1
I I I
SLURRY HOLDING TANK
7,200 GAL CAPACITY CONDENSATE TO
12' DIA X ITHIGH STORAGE
SLURRY PUMPS (2)
15 GPM ® 200' TDH EA
1.5 HP EA
CIRCULATION PUMPS (2)
175 GPM @ 300' TDH EA
30 HP EA
FILTER PRESS FEED PUMPS (2)
15 GPM @ 200' TDH EA
2.5 HP EA
CRYSTALLIZER FEED PUMPS (2)
25 GPM @ 200' TDH EA
2.5 HP EA
PLATE & FRAME FILTERS (3)
20 TPD EA
l�l
CYSTALLIZER FEED TANK
13,200 GAL CAPACITY
14' DIA X 14' HIGH
HOTWELL TANK
SOLIDS TO DISPOSAL
CRP PURGE

Pu,cle
CRP Data - Liquid Purge Stream Solution
CRP Data - iquid Purge Stream Solution
Raw Color
Units
ata by I
mg/L
by ICP
mg/L
Date
Time
IC Data
mg/L mg/L
Metals
oc oF
mg/L
Date
TIC
mg/L
mg1L
Solids
ICP
%
%
mg/L
Units
IiS/cm
mg/L
I mg/L
mg/L
mg/L
mg/L
mg/L
mg /L
mg/L
mg/L
pH
gm/ml
%
%
%
PPM
PM
DATA IS COMPANY CONFIDENTIAL
Data Reported on an "AS IS" Sample Basis.
JWilliam K. Adams Page 1 02/20/2001

Purge
Ld
CRP Data - Liquid Purge Stream Solution
CRP Data - iquid Purge Stream Solution
— - ------
IC Data
Metals
TIC
Solids
ICP
Raw Color
)ata by I
by ICP
Date
Time
mg/L
mg/L
mg/L
Units
pS/cm
mg/L
mg/L
mg/L
mg/L
pH
gm/ml
mg/L
mg/L
%
%
PPM
%
%
----------Units
mg/L
mg/L
oc
oF
mg/L
Date
%
PPM
William K.Adams Page 02/20/2001

I
Purge
I
' I
L
CRP Data - Liquid Purge Stream Solution
CRP Data - iquid Purge Stream Solution
)ata by I
Na-
mg/L
by ICP
mg/L
IC Data
Metals
Date
TIC
mg/L
TOC_
mg/L
Solids
ICp
Raw Color
Pt - Co
Cl-
SO4=
COD
C lor�
C�m__
At
Ba
Ca
Fe
K
Mg
Na
Si
pH
Sp. Gr.
Temperature
AOX
__TS
sot TS
TDS
SS
_SO4_
Date
Time
mg/L
mg/L
mg/L
U its
4n
I"Sj�m
mg1L
mg/L
mg/L
mg/L
mg/L
mg/L
4MnN�_
mg/L
mg /L
mg/L
mg
mg/L
pH
gm/ml
C
&F
mg/L
0/61_
%
%
PIPM
I?pM1
% I
%
Units
Average:
25032
192130
18954
4 1047
137562
11.98
0.87
32.2
11.90
23066
13,7
9.3
110664
89.2
10.10
1.2777
63.5
146.2
17.407
Average:
31808
6416
33.51
4019
1015
5.38
13.75
53402.667
67100
23625
10/14/1996
11:05AM
41700
230100
28850
38322
151000
10.89
0.50
<.026
8.21
32415
1.4
3.4
99090
81.1
10.15
1.2801
10/1411996
27180
7174
31.32
10/1511996
4:45 PM
50400
179100
39150
77514
163100
4.69
0.19
28.0
5.76
34665
10.6
1.9
80200
99.0
10.17
<0.25
10/15/1996
21530
12914
29.42
10/24/1996
2:30 PM
37500
159300
32200
57546
155000
9.35
0.21
61.1
15.83
30790
8.2
2.7
80280
77.1
10.08
10/24/1996
24700
9380
29.24
3:33
47700
157800
33450
46712
156200
9.47
0.33
3.3
16.29
39720
10.7
5.3
94200
52.2
9.96______
10/29/1996
26100
6680
31.72
-10/29/1996
11/05/1996
_PIVI
4:41 PM
42900
153900
21250
36729
164000
6.58
0.14
56.1
13.19
39485
8.6
5.3
95185
67.5
9.93
11/05/1996
57940
12278
_31.27
11/12/1996
4:00 PM
41100
191700
21450
33436
147000
5.03
0.17
10.4
13.33
28600
8.2
6.7
101800
39.0
10.10
1.2991
11.475
11/12/1996
39350
5710
33.84
11/19/1996
3:02 PM
39200
181600
32620
65556
93400
4.46
0.33
"5
16.5
4.59
41140
6.7
4.6
99080
161.0
10.30
11/19/1996
26720
1003.6
33.68
12/01/1996
3:18 AM
24000
236000
22720
42104
95100
7.33
0.72
103.1
4.44
31508
7.2
8.6
104908
102.4
10.29
12/01/1996
32720
7120
34.65
42104
12/04/1996
7:44AM
11200
527200
16880
34204
124500
9.41
1.40
205.2
5.2
13.55
14456
15.9
24.4
259480
29.8
10.81
12104/1996
33180
3876
52.92
34204
12/10/1996
11-49AM
26000
203200
34160
91000
10.27
12/10/1996
31660
10544
41.84
12/11/1996
3:18 PM
3600
314800
21880
53829
112900
10.74
<23.4
12/11/1996
1100
6012
64.16
53829
12/18/1996
9.45 AM
15200
227200
30000
40576
145000
3.690.50
13.8---
5.80
27116
8.3
7.5
101840
77.8
10.27
12/18/1996
44920
4808
40576
12/23/1996
11:30 AM
17778
171481
17593
42995
148600
4.16
0.23
5.5
3.34
25574
4.4
4.2
76072
109.1
10.39
12/23/1996
34220
1608
_32.22
29.87
42995
12/30/1996
2:05 PM
18400
172400
21400
43207
141200
4.02
0.53
14.6
4.02
37360
6.7
6.7
119500
169.1
10.16
12/30/1996
36540
1532
41189
01/09/1997
2:51 PM
13200
202000
19200
64536
129000
50.72
0.66
15.5
11.72
25210
8.8
7.3
132450
94.9
10.05
01/09/1997
43940
6108
33.11
01/16/1997
10:55AM
16400
213200
19120
43380
145800
1.25
0.81
18.6
3.89
21880
7.8
7.0
106040
62.7
10.11
1.2856
71.910
01/16/1997
1204
32.28
01/21/1997
2:50 PM
21600
174400
27200
56380
146200
9.39
0.63
15.1
5.05
26388
5.6
3.0
93960
100.5
9.89
01/21/1997
_23940
39180
7504
31.06
01/29/1997
9:17 AM
9600
196000
12960
26684
140700
3.53
0.57
25.7
2.32
11116
6.9
8.7
100360
43.6
10.17
01/29/1997
53780
31.63
02/0511997
9:10 AM
12800
138000
14640
35604
137300
5.12
0.56
19.4
3.42
12390
5.9
4.4
65600
10.1
10.10
02/05/1997
20300
_2308
3260
21.84
02/11/1997
36400
174000
38880
58292
156500
13.58
0.42
<.104
5.59
30292
7.3
5.1
92000
172.6
10.24
1.2940
40.000
02/11/1997
26760
1_892
32.58
02/18/1997
2:05 PM
25200
196000
21120
55148
129000
6.42
0.54
11.7
4.71
19456
6.0
4.4
108000
90.2
10.02
02/18/1997
33960
1505
32.86
02/24/1997
4:27 PM
25200
188400
21560
44100
150400
7.18
0.75
21.8
5.17
24248
7.3
5.8
99140
102.0
10.07
02/24/1997
30680
1485
31.31
03/10/1997
9:58 AM
15200
204400
20640
50516
135500
<.035
0.47
3.4
4.04
14432
6.0
6.4
96360
17.9
10.17
03/10/1997
30680
5376
30.74
03/13/1997
2:10 PM
24400
228800
14640
22988
132700
5.29
0.36
<.026
5.23
15660
4.9
3.4
97920
65.6
10.24
03/13/1997
37200
4052.
31._60.______
03/18/1997
2:22 PM
35385
196154
18769
39873
149000
5.75
0.19
35.1
10.86
23169
4.9
4.1
93846
116.5
9.93
0.110
03/18/1997
28423
5354
30.82
03/24/1997
1:17 PM
20400
180400
8800
19544
146400
<.035
0.56
2.3
4.47
13724.
8.4
8.0
91640
66.610.09
03/24/1997
34780
13260
26.22
04/04/1997
9:00 AM
32000
252000
16960
39556
133800
<.035
0.98
2.4
11.42
16760
10.1
12.4
110380
50.7
10.01
04/04/1997
11216
- 5648
_34,34
04/09/1997
2:20 PM
24400
183200
16640
40704
145300
<.035
0.75
<.104
6.96
17048
8.5
11.2
87080
54.0
9.96
14970
7117728.31
- -----
04/16/1997
2:48 PM
28800
210800
18400
44524
139700
7.95
0.76
8.8
6.03
24084
7.715.8
110520
115.4
10.08
___________0.165._04/09/1997
04/16/1997
27070
4907
31.56
04/24/1997
10 M
19600
228000
17080
29488.130900
14.62,
0.88
10.6
9.04
15740
7.9
7.6
10.6000
83.7
10.03
- -
--------
04/24/1997
29464
___
3891
05/02/1997
_12: _P
2:22 PM
9200
226400
9880
20520
125300
3.12
0.58
1.1
4.74
9916
____
1.1
7.8
114760
44.6
10.30
05/02/1997
23360
3338
30.88
05/07/1997
1:04 PM
16000
211600
15760
35180
130500
9.65
0.85
<.104
5.78
17264
3.9
10.7
111920
67.3
10.21
05/07/1997
28164
4226
31.96
05/13/1997
1:19 PM
13600
173600
10160
19672
138800
2.99
0.67
<.104
3.09
11668
<.0012
5.1
72680
61.2
10.19
<.032
05/13/1997
22740
3096
25.02
05/2211997
2:05 PM
25200
202400
18680
40276
140500
6.52
0.76
31.4
5.76
21832
10.0
6.5
106120
84.3
9.98
05/22/1997
24680
30.59
-
05/28/1997
1:43 PIVI
28000
203600
17560
28168
143100
<.14
0.71
66.5
2.12
22060
12.1
4.2-
107720
102.2
10.15
05/28/1997
19048
_4320.__
4512
30.77
06/2511997
2:34 PM
8800
254400
11460
20520
114400
<.035
0.48
23.0
2.51
8103
6.1
6.7
120640
<.037
10.00
16.7
06/25/1997
27060
2428,
39.42
07/02/1997
10:05 AM
-
23200
214000
23720
44952
134400
1.25
0.70
87.2
6.40
25476
8.5
6.3
116920
112.1
10.02
07/02/1997
34440
6416
32.81
07/10/199710:40AM
228002252010
25280
42188
128800
12.12
0.81
242.2
12.25
22356
11.6
7.6
123360
135.1
9.97
07/10/1997
28040
6460
34.05
07/21/1997
4:07 PM
37600
216800
28800
66404
144000
3.84
0.70
180.0
7.78
30004
12.5
6.9
112640
145.4
10.11
07/21/1997
23760
7148
32.16
07/2.8/1997
2:05 PM
33200
232000
26960
36536
139800
<.140
0.64
31.6
6.02
25856
11.7
8.5
126880
127.0
9.90
0.190
07/28/1997
23260
6054
3139
07/30/1997
___
10:59 AM
31600
244800
24840
39582
133800
2.41
0.86.91.1
6.86
24612
13.0
12.2
1138920�
113.7
9.96
07/30/1997
18898
6188
34.78
08/06/1997
2:12 PM
41600
218400
29640
49624
139200
<.140
0.46
41.3
8.65
23820
11.5
7.0
111240
64.3
10.05
18784
7096
__
33.75
08/12/199.7
10:22
39600
190800
25640
50048
145100
<.140
0.58
157.1...
6.70
22216
8.6
6.3
94680
9.98
26260
7716
31.54
08/20/1997
-AM
4:04 PM
26800
209600
16960
39216
153600
2.59
0.58
26.7
4.92
16384
8.5
6.9
108560
_53.3
93.0
10.16
<.10
36420
5320
32.62
10/97-Cl
[10/27-10/29
34800
174800
150550,
140
0.54
6.7
6.91
16920
6.5
4.5
102680
56.1
9.98
31400
5000
30.40
-
1,1hiii,44f 4:00 PM
12:30 PM
11/1111 99T, 4:30 PM
6:15 PIVI
7:25 PM
'11/1 107�i
11/97-Cl 11/18-11/19
12/97-Cl
01/08/1998 2:07 PM
1/98-Cl 1/19-1/21
0 . 2 /98-C 1
34200
169800
.17600
36925
-<.
_41750
41775
29620
5860
5635
5470
3705
6740-
6190
5056
- ------
16340
22520
32912
47440
51156�
32.57
32.21
188400
207200
181500
209200
19 960 . 0,
26400
18400
36300
14000
20800,
132600
133000
129000
133900,
11.71
9.78
0.70
0.58
24.3
37.2
8.18
17920
13.2
8.5
129480
98.9
10.00
6.37
5
9.8
8.8
111120
89.5
9.91
<.140
5 . 00,
26340
6323
1585
6180
34.14
31.71
32.21
0.05
0.69-1
34.3
31.4
2.29
7.78
12196
17212
6.9[
5.9
107320
46.5
9.96
40480
35120
10.9
7.1
100360
47.6
9.86.
jWilliam K. Adams Page 3 02/20/2001

Purge
'j,
CRP Data - Liquid Pure Stream Solution
CRP Data - Liquid Pure Stream Solution
IC Data
Metals
TIC
Solids _
ICP
_
Raw_Color
ata by I
by ICP_
_
Cl-
SO4=
COD
Color
Cond.
At
Be
Ca
Fe
K
Mg
Mn
Na
Si
pH
Sp. Gr.
_ _
AOX
mg/L
TOC
TS
sol TS
TDS
TSS
VSS
S
SO4
Pt - Co
Na
K
-
Date
Time
mg/L
m /L
mg/L
Units
µS/cm
mg/L
mg/L
mg/L
mg/L
mg/L
mg/L
mg/L
mg/L
mg/L
H
gm/ml
_Temperature
oC
_of
mg/L
_
Date
mg/L
%
%
%
PPM
PPM
%
%
Units
mg/L
mg/L
Average:
25032
192130
18954
41047
137562
11.98
0.87
32.2
11.90
23066
13.7
9.3
110664
89.2
10.10
1.2777
63.5
146.2
17.407
Average:
31808
6416
33.51
4019
1015
5.38
13.75
53402.667
67100
23625
-
03/20/1998
_ _
24000
198000
9356
129800
3.52
1 A 3
<.026
8.65
18060
12.5
13.6
110840
84.6
9.84
38700
4004
32.54
_
_ - _
_
03/25/1998
21600
200800
9784
115800
4.16
0.69
18.5
6.14
15660
7.6
5.2
96800
58.7
9.98
_
30700
3804
29.81
04/20/1998
4:03 PM
16215
147385
10590
385982
2.54
0.831
35.6
10.031
238001
11.8
7.2
138120
161.5
9.93
21455
4050
31.50
05/06/1998
11:46 AM
14767
176052
399592
10.36
0.621
34.1
6.23
22156
9.4
7.6
162560
11.2
10.16
_
_
11045
1801
35.50
05/26/1998
2:57 PM
23640
208820
15327
152700
1.03
0.60
24.3
2.35
22504
3.9
2.4
123520
146.9
10.05
_
41700
5118
33.76
06/15/1998
9:50 AM
23902
189278
134331
138000
17.13
0.71
12.6
16.62
20200
11.4
8.4
108200
<.148
10.01
26030
4189
34.82
06/29/1998
10:00 AM
15912
207480
104861
120400
21.54
1.72
14.0
10.28
19312
11.2
8.6
146560
70.3
9.87
_
39000
2661
37.33
07/16/1998
9:40 AM
182401
162735
9385
102500
23.45
0.63
21.4
1.60
18200
11.6
8.5
126300
32.6
10.09
_
12810
376
30.00
07/28/1998
9:00 AM
19968
177216
12445
132800
25.74
1.38
18.0
4.98
185401
8.2
9.3
161000
21.8
9.91
_
37910
3897
36.21
_
08/07/1998
3:02 PM
13821
305688
6967
156600
9.82
1.191
58.6
11.11
16040
12.7
10.3
112200
73.9
9.56
24740
2916
43.47
08/18/1998
9:21 AM
18615
205860
14929
146300
11.30
1.09
22.7
6.75
15550
12.7
19.2
107740
76.91
10.07
41208
4719
38.53
09/09/1998
6:19 AM
18609
207316
8684
178900
8.16
1.58
21.5
10.55
19690
15.4
14.5
135100
<.148
9.64
_1
25465
2635
35.26
10.78
09/21/1998
6:20 AM
27448
216576
9625
135100
7.28
1.21
31.5
16.87
25490
0.3
15.0
142200
129.4
9.75
_
_
12784
4865
40.30
10.69
10/05/1998
_
6:36 AM
28651
174168
6567
145400
15.91
1.24
21.9
19.86
19490
18.6
11.3
101500
42.7
10.03
_ 25640
2138
36.52
8.76
_
10/15/1998
_
10:40 AM
15792
209808
10687
150800
23.70
1.87
187.3
27.76
49250
41.0
36.1
489200
131.9
9.94
22616
3612
33.77
11.98
10/29/1998
9:06 AM
31527
242730
8928
150100
21.84
1.16
<.026
12.34
22450
24.4
13.1
163100
22.0
10.07
_
25933
2935
37.30
13.38
_
_
11/12/1998
12:28 PM
25704
164832
15096
68300
12.96
0.91
<.026
11.69
20140
15.9
8.8
102900
118.5
10.65
_
14668
6393
32.60
7.99
_
11/26/1998
9:43 AM
19008
188320
19258
101200
28.21
0.85
<.026
21.86
24550
83.8
9.7
131100
67.4
10.24
19853
6294
32.95
9.35
12/08/1998
8:50 AM
21224
189121
17737
155200
36.37
4.78
57.0
63.95
?90300
45.8
65.2
?532600
277.5
10.06
25468
6746
37.73
9.95
12/14/1998
8:33 AM
16065
160650
11340
146200
8.01
0.59
12.3
10.92
24680
14.3
11.9
114600
1.9
9.96
19167_
4419
33.25
10.47
_
12/22/1998
13650
195030
12805
141600
12.34
0.59
10.6
7.07
23420
12.9
10.2
119900
0.7
9.95
_
17680
4583
33.10
10.18
_
12/28/1998
8:38 AM
20919
211025
16221
128800
7.77
0.66
2.1
9.35
16480
13.3
15.6
123100
92.2
10.10
_
20845
8455
37.81
10.29
_
01/04/1999
12:03 PM
9504
203280
6124
155500
25.26
0.56
<.026
72.53
7137
8.5
22.4
95210
69.6
10.04
10771
3886
35.45
6.71-
01/12/1999
9:30 AM
9200
311600
6000
140000
8.27
0.47
8.3
3.66
4520
3.4
3.5
64500
28.6
9.89
_
12640
3056
33.27
8.32
01/21/1999
8:30 AM
35200
204800
22440
141400
1.78
<.0001
18.6
14.93
23000
<.0003
10.2
120600
<.037
9.94
21040
6736
35.80
8.95
_
-
01/25/1999
9:38 AM
24800
170800
15280
115200
<.14
<.0001
<.026
1 13.51
19150
<.0003
9.8
125400
<.037
10.00
_-_
21880
15280
32.09
8.02
02/03/1999
8:10 AM
20800
281500
12680
148700
12.12
1.04
24.2
14.09
14010
14.4
16.3
109100
60.0
9.92
35060
5548
35.22
8.81
_
_
-
02/10/1999
8:45 AM
13200
142400
10400
134600
6.02
0.44
20.9
6.35
7314
5.4
4.0
66270
40.9
9.82
_
6540
2756
20.591
5.15
_
02/15/1999
8:38 AM
23600
228000
9880
89300
17.10
1.42
20.35
14950
14.5
12.8
106000
82.4
9.70
_
19460
5535
32.70
8.18
_
02/25/1999
_
7:47 AM
35600
198400
19400
102900
4.48
1.03
_40.6
34.6
10.11
24130
11.3
13.3
127300
20.8
10.05
22920
6900
32.59
8.15
03/01/1999
8:03 AM
33200
203200
16720
128000
9.99
0.74
3.4
16.22
19580
13.1
11.1
110700
146.4
9.94
21380
6872
30.15
7.54
03/08/1999
1:05 PM
23600
226800
18760
100000
12.08
0.99
<.026
23.96
17340
13.9
14.8
107200
0.4
9.95
13040
6404
30.76
7.69
_
03/15/1999
8:40 AM
23200
223120
13800
98700
7.60
0.85
6.4
30.62
17120
<.0003
14.5
112500
27.0
9.77
12320
5104
28.91
7.60
03/22/1999
8:47 AM
25200
181200
166001
1401001
8.99
0.90
9.5
19.96
16410
12.2
12.7
87980
78.7
10.02
_
26520
6904
31.39
9.08
-_
03/31/1999
8:30 AM
18800
222000
11088
145100
13.38
1.05
35.1
30.60
9009
11.3
11.8
103900
84.4
9.74
7380
3936
31.42
9.06
04/07/1999
12:30 PM
20400
216800
9920
83200
16.00
0.80
25.0
16.40
7748
10.1
10.4
114200
100.2
10.34
_
22640
3808
33.33
8.37
04/12/1999
8:36 AM
36800
209600
14840
141000
13.80
0.68
24.5
31.48
12740
15.0
13.2
122000
89.7
10.02
_
22880
5668
33.83
10.09
04/20/1999
9:12 AM
28400
145200
12760
142300
0.81
0.381
26.2
7.61
2063
5.8
4.0
92970
89.1
10.10
28460
4944
27.02
7.76
_
04/27/1999
10:50 AM
28400
166400
13000
154700
13.72
0.68
3.5
14.33
10050
9.1
6.5
95620
64.5
9.89
28880
5468
31.39
8.22
05/10/1999
11:40 AM
192001
196400
7080
143600
6.32
1.12
15.9
18.47
6667
2.2
7.9
120000
43.3
10.00
_
32900
1996
40.47
9.09-
05/17/1999
9:15 AM_
37200
206800
15240
88000
28.13
0.89
43.2
19.24
27450
15.9
10.4
165800
148.5
10.25
23940
5520
33.27
9.71
05/20/1999
8:50 AM
32000
212000
15440
85000
11.77
0.95
25.2
15.22
25690
18.2
11.3
170900
79.6
10.26
_
21340
5500
32.68
9.57
06/07/1999
10:30 AM
30000
168400
142900
14.73
1.13
27.2
12.99
18780
14.3
12.5
123900
91.5
9.90
27240
3276
_33.64
9.59
06/16/1999
8:05 AM
36400
154800
96300
7.06
1.20
13.29
21380
16.1
16.3
114500
99.61
10.48
_
30900
4920
35.72
9.56
06/21/1999
9:08 AM
31200
162000
142700
4.61
0.97
_20.7
13.7
12.69
18510
4.7
13.7
127800
43.8
9.96
_
27600
4875
36.21
9.85
06/28/1999
8:35 AM
31600
21400
137700
11.60
0.88
3.1
10.40
18540
5.7
11.1
121300
83.4
9.80
19100
8628
36.64
10.00
_
_
07/08/1999
4:45 PM
24000
_157200
172400
11120
152900
6.89
0.99
15.8
9.70
13100
11.4
9.9
118400
77.9
9.68
_
_ 15020
5020
31.80
9.64
07/13/1999
2:45 PM
30400
172000
3460
158400
13.36
1.17
3.5
24.07
16660
15.4
14.3
115700
73.6
9.94
_
-
30320
5624
32.34
9.95
07/19/1999
9:52 AM
48800
157200
19840
162500
3.38
0.60
12.8
16.41
25630
18.0
12.1
108000
90.4
9.85
_
_
21860
7468
37.70
10.24
07/26/1999
10:28 AM
47200
158000
7740
153500
21.81
0.73
23.8
18.97
28800
20.8
11.2
132500
166.6
9.96
21160
11764
40.00
10.34
08/05/1999
8:50 AM
47200
147600
21360
107100
35.91
1.02
14.6
23.46
30330
22.4
13.2
114900
37.4
9.85
43860
4832
40.52
10.04
08/10/1999
6:37 AM
32800
158000
21560
142900
8.02
0.86
3.1
22.33
21590
19.9
13.7
125100
5.0
9.97
_
22920
8720
08/16/1999
9:50 AM
43600
147200
23800
144100
12.66
0.86
12.3
23.29
26860
18.6
9.7
119900
73.3
10.06
26680
9348
34.60
10.08
08/26/1999
10:10 AM
23200
188400
13880
133900
18.60
1.54
17.9
24.71
15830
13.2
12.8
138900
88.3
10.04
37140
5852
41.28
9.53
--t­-----1
08/30/1999
11:30 AM
34400
189200
14440
138500
14.73
0.58
13.5
13.97
21800
15.3
10.3
123000
81.0
9.87
25526
5508
.33.94
9.67
09/07/1999
2:05 PM
34000
205600
17000
143000
12.44
1.17
24.4
15.38
22880
15.3
12.0
109200
14.2
9.95
24020
7618
33.00
9.39
William K. Adams Page 4 02/20/2001

Purge
CRP Data - Liquid Purge Stream Solution
CRP Data - Li uid Purge Stream Solution
IC Data
Metals
TIC
Solids
ICP
------..-Raw
_ Color
a_ta by I
by ICP
_
Cl-
SO4=_
COD
Color
Cond.
_
Ba
Ca
Fe
K
Mg
Mn
Na
Si
pH
Sp. Gr.
Temperature
AOX
TOC
TS
sol TS
TDS
TSS
VSS
S
SO4
_P_ t - Co
Na
_K_
Date
Time
mg/L
mg/L
mg/L
Units
µS/cm
_AI
mg/L
mg/L
mg/L
mg/L
mg/L
mg/L
mg/L
mg/L
mg/L
pH
gm/ml
oC
of
mg/L
Date
mg/L
mg/L.
%
%
%
PPM
PPM
%
%
Units
mg/L
mg/L
25032
192130
18954
41047
137562
11.98
0.87
32.2
11.90
23066
13.7
9.3
110664
89.2
10.10
1.2777
63.5
146.2
17.407
Average:
31808
6416
33.51
4019
1015
5.38
13.75
53402.667
67100
23625
_Average:
09/15/1999
12:15 PM
35200
208000
25440
148300
37.77
0.87
3.5
12.26
24300
16.0
9.6
123900
64.1
9.96
21980
9544
39.10
10.43
09/27/1999
_
8:58 AM
28400
219200
110001
140400
17.07
1.63
25.4
26.92
18720
18.6
17.1
132900
55.81
10.07
32560
5008
37.36
10.11
10/05/1999
8:22 AM
26800
267200
10760
112800
13.471
0.781
27.6
14.451
17740
15.21
12.0
125600
60.5
9.99
27240
4764
38.951
10.69
10/11/1999
8:25AM
13200
150400
7720
133700
8.55
0.37
9.2
8.50
9266
8.8
5.1
73250
31.3
10.12
17020
2891
22.74
6.26
10/21/1999
2:53 PM
10400
161600
4480
81300
4.63
0.56
36.4
7.87
6011
8.0
6.6
95590
20.3
10.43
21220
2560
24.51
6.80
_
10/28/1999
8:12 AM
21200
260800
10480
130800
12.19
1.03
23.0
17.02
14960
10.6
10.5
147900
40.7
10.11
32160
4172
42.29
11.80
11/08/1999
9:49 AM
32800
233600
13120
126200
13.52
0.99
14.7
12.99
16800
16.1
13.1
144900
138.7
10.24
_
35880
4560
39.15
11.22
11/19/1999
8:40 AM
35600
234800
19800
1546001
21.10
1.59
9.1
20.56
32420
22.2
14.21
165900
5.6
9.88
17560
3588
36.69
10.45
_
11/22/1999
AM
31600
241600
17720
14600
20.42
1.15
21.6
19.85
33140
19.5
16.8
181100
78.8
9.87
_
19420
5684
36.55
10.49
11/29/1999
_8:30
11:43 AM
25600
240800
15440
98500
28.95
1.77
12.2
18.62
28190
20.1
17.5
177600
10.1
9.96
32940
5260
37.58
11.00
12/08/1999
10:14 AM
18000
206800
13200
148700
3.93
1.21
24.7
15.18
18090
13.8
12.4
132100
21.7
10.09
37300
_3792
43.06
10.96
12/14/1999
10:53 AM
24400
195200
16080
133900
1.52
0.62
27.2
10.13
20630
10.3
9.3
127900
76.0
10.18
31980
5404
32.09
10.19
12/20/1999
12:21 PM
32400
191200
20320
140500
7.15
0.69
20.1
8.82
21440
10.9
8.3
119800
60.8
10.11
33940
5480
38.36
10.17
12/29/1999
11:34 AM
32400
192800
16600
97300
4.77
0.60
5.8
14.02
21510
11.3
9.1
97620
57.6
10.13
20460
7588
38.95
10.38
01/03/2000
9:18 AM
44000
173200
15080
136900
18.35
0.57
22.9
4.53
13590
6.3
5.7
94820
50.1
10.07
_
34460
2316
34.34
9.75
01/10/2000
_
9:35 AM
44400
160800
37600
152100
21.13
0.91
2.2
13.95
30580
16.7
9.4
115100
146.6
10.02
_
25660
6420
34.321
10.22
01/20/2000
9:27 AM
20800
196800
16680
147600
24.32
0.80
7.0
15.86
30270
17.2
11.2
121700
23.0
9.99
29800
6472
36.021
10.27
01/26/2000
9:45 AM
30800
198800
14560
145600
29.08
1.01
23.6
12.66
27030
12.2
12.6
117800
51.6
10.00
_
22560
7916
38.30
10.46
02/01/2000
9:33 AM
28000
194400
18560
127500
20.63
0.46
10.4
13.53
29230
15.6
12.6
122000
76.2
10.11
_
29180
6596
34.94
10.63
02/08/2000
2:10 PM
21200
194000
14920
1079001
10.86
0.57
29.4
9.57
24270
12.3
9.7
134500
71.3
10.14
30840
5916
37.33
10.65
02/15/2000
9:18 AM
26000
190800
14280
133400
7.48
0.75
6.7
11.38
25680
12.1
8.1
126000
92.9
10.05
48680
5664
37.96
10.27
10:12 AM
18800
219200
11280
100000
4.29
1.18
24.4
12.16
20370
14.4
10.0
163200
86.9
10.19
41300
5028
36.92
11.49
_02/23/2000
02/28/2000
1:25 AM
20400
208400
8000
85100
21.71
0.92
15.2
11.14
24340
15.0
12.5
161900
117.8
10.12
17140
512
36.20
10.91
03/10/2000
8:56 AM
32000
146000
16680
55700
0.76
0.59
26.1
5.09
8582
9.4
7.6
121100
67.7
10.18
34580
2456
32.46
12.17
03/14/2000
9:15 AM
14000
172000
8200
136500
0.49
0.79
6.6
11.08
24440
11.0
8.7
127200
67.2
9.98
_
_
32280
6152
36.62
10.21
03/20/2000
1:36 PM
21200
166800
9120
120700
6.70
0.95
14.0
10.27
15070
12.4
12.2
153700
43.1
11.78
_
_
_
52420
3736
37.47
11.78
03/28/2000
10:50 AM
30000
156800
15280
87300
19.62
0.53
19.6
11.56
23040
10.6
9.5
129100
113.3
10.12
24100
5984
35.64
10.82
04/25/2000
3:03 PM
34000
426000
9360
116700
8.24
1.03
7.1
11.14
9102
10.8
14.4
180900
52.8
10.39
_
40880
3836
42.65
13.47
06/09/2000
2:34 PM
32400
235200
26960
139400
16.80
0.66
3.6
12.93
12980
8.4
4.7
103500
54.9
10.12
_
38250
12302
32.27
9.75
07/14/2000
1:26 PM
24800
374400
16280
124100
11.99
1.00
12.2
10.39
12690
10.3
9.3
126700
31.5
10.16
20540
6796
61.15
10.69
08/11/2000
11:30 AM
20000
103000
8410
134300
9.67
0.72
6.4
14.46
12510
17.6
17.4
114900
50.4
10.17
288
17832
43.27
10.44
08/22/2000
12:04 PM
42000
250000
4890
85800
9.97
0.85
25.6
17.23
12960
11.0
10.7
104300
80.6
10.26
_54450
84300
37.70
9.76
09/08/2000
12:24 PM
20000
272000
50001
92900
13.17
0.56
13.9
9.21
13920
7.0
0.0
1172
2.9
9.98
106801
1612
47.24
11.81
09/12/2000
2.92
0.29
29.2
6.91
12430
7.6
5.7
79000
16.5
37.11
11.42
09/15/2000
39.69
0.53
27.2
10.11
12480
8.6
5.4
69080
15.1
_
37.51
10.29
09/20/2000
5.12
0.77
22.2
7.08
12180
9.1
6.2
72890
5.4
39.51
11.08
_
09/22/2000
12:14 PM
36000
242000
8680
88000
9.43
0.48
1,9.3
10.63
11850
8.7
6.0
68360
22.3
10.43
12180
2772
41.20
10.30
09/27/2000
15
0.59
21.0
10.38
12140
8.0
7.1
80450
29.8
40.73
11.35
10/04/2000
2:19 PM
30000
292000
15800
97100
16.29
0.971
19.6
10.57
6137
17.9
10.8
127700
4.0
10.39
14540
3749
46.28
11.57
10/06/2000
18.88
1.011
19.8
11.55
5758
17.6
10.8
143300
2.4
45.18
11.45
10/23/2000
2:21 PM
62000
_
2480001
36601
93500
18.46
0.69
9.3
13.59
6008
20.5
11.1
107200
21.7
10.20
_
255001
6952
42.72
10.68
William K. Adams Page 5 02/20/2001
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