EPA-670/2-75-050C
June 1975
Environmental Protection Technology Series
                        --WAV^• vv>.^'.'->. ^          - - 	

-------
                                          EPA-670/2-75-050C
                                          June 1975
        DIRECT FILTRATION OF LAKE SUPERIOR

        WATER FOR ASBESTIFORM FIBER REMOVAL

                    Appendix B

Design, Installation and Operation of Pilot Filters

                    Appendix C

    Summary of Data for Individual Filter Runs
                        By
       Black £ Veatch,  Consulting Engineers
           Kansas City, Missouri  64114
            Program Element No.  1CB047
          Contract No.  DACW 37-74-C-0079
       Interagency Agreement EPA-IAG-D4-0388
 USEPA,  Region V and Corps of Engineers, St. Paul
                  Project Officer

                  Gary S. Logsdon
         Water Supply Research Laboratory
      National Environmental  Research Center
              Cincinnati, Ohio  45268
      NATIONAL ENVIRONMENTAL RESEARCH CENTER
        OFFICE OF  RESEARCH AND DEVELOPMENT
       U.S.  ENVIRONMENTAL PROTECTION AGENCY
              CINCINNATI, OHIO  45268

-------
                        REVIEW NOTICE
     The National Environmental Research Center -- Cincinnati
has reviewed this report and approved its publication.   Approval
does not signify that the contents necessarily reflect  the views
and policies of the U.S. Environmental Protection Agency, nor
does mention of trade names or commercial products constitute
endorsement or recommendation for use.

-------
                             FOREWORD
     Man and his environment must be protected from the adverse
effects of pesticides, radiation, noise and other forms of pollution,
and the unwise management of solid waste.  Efforts to protect the
environment require a focus that recognizes the interplay between the
components of our physical environment -- air, water, and land.  The
National Environmental Research Centers provide this multidisciplinary
focus through programs engaged in

     •    studies on the effects of environmental contaminants
          on man and the biosphere, and

     •    a search for ways to prevent contamination and to
          recycle valuable resources.

     This report and its appendices present the results of pilot
plant filtration research for the removal of asbestiform fibers
from drinking water.  The several appendices present detailed
information on water quality, pilot plant equipment and operation,
individual filter run data, asbestiform fiber and amphibole mass
concentrations in raw and filtered water, and diatomite filter
optimization.  Appendix B contains data on the pilot filters used
and on operating techniques.  Appendix C consists of tabulated
operating data from all individual filter runs.
                                 A.  W. Breidenbach, Ph.D.
                                 Director
                                 National Environmental
                                 Research Center, Cincinnati
                                  111

-------
                             ABSTRACT
     Pilot plant reserach conducted in 1974 at Duluth, Minnesota,
demonstrated that asbestiform fiber counts in Lake Superior water
could be effectively reduced by municipal filtration plants.  During
the study, engineering data were also obtained from making cost
estimates for construction and operation of both granular and
diatomaceous earth (DE) filtration plants ranging in size from 0.03
to 30 mgd.

     Appendix B contains information on the pilot filters used in
the study.  Data are presented on the physical aspects of the units
(dimensions and equipment configurations) and on the manner in which
the filters were operated.

     Appendix C contains data obtained during the individual pilot
plant filter runs.  This kind of information will be useful to
persons needing to know about specific conditions such as raw water
turbidity, filtration rate, and chemical doses or diatomaceous earth
types and amounts used for precoat or body feed.
                                 IV

-------
                            CONTENTS
Appendix                                             Page


B-l      Equipment Design and Installation            1

B-2      Operation of Pilot Plant Filters            13
C-l      Granular Media Filtration (MM-1) Summary
           of Individual Runs                        17

C-2      Granular Media Filtration (MM-2) Summary
           of Individual Runs                        24

C-3      Vacuum Diatomaceous Earth Filtration
           (BIF) Summary of Individual Runs          36

C-4      Pressure Diatomaceous Earth Filtration
           (ERD) Summary of Individual Runs          56
                             v

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                           APPENDIX B-l




                 EQUIPMENT DESIGN AND INSTALLATION







GENERAL




The pilot filtration study was conducted with two granular filters




and four DE filters installed at the Lakewood Pumping Station in




Duluth, Minnesota.  The granular filters were a skid-mounted and a




trailer mounted "WATER-BOY" unit as manufactured by Neptune MicroFLOC,




Incorporated, Corvallis, Oregon.  The DE filters were two pressure DE




units supplied by the Corps of Engineers and two vacuum DE units as




manufactured by the BIF Corporation, Providence, Rhode Island.




GRANULAR UNITS




The granular units used in the filtration study were designated MM-1




and MM-2 and are described in detail in the main report.   Figures 1-7




are provided to illustrate the various features of the two units




discussed in the report.




DIATOMACEOUS EARTH UNITS




The DE units used in the filtration study were designated as BIF




(vacuum) and ERD-1 and ERD-2 (pressure).   Although two vacuum filters




were installed, only one unit was used for the study, with one unit




provided as standby.  The DE units are illustrated in Figures 8-13.




Additional flow diagrams of the BIF and ERD units are presented in




Figures 14-17.  These diagrams show the alternative mixing modes that




were utilized for some runs with the DE units.

-------
FIGURE  I .GRANULAR  UNITS, MM-I AND MM-2

-------
FIGURE  2 .  FRONT VIEW MM- I
 FIGURE 3  .TOP  VIEW OF MM-I

-------
 FIGURE  4   TOP VIEW MM-2
FIGURE  5
TOP VIEW
LOCATION
OF MM-2
RELATIVE
SHOWING
TO ERD.

-------
 FIGURE 6   .TOP VIEW OF MM-2 SHOWING
            LOCATION RELATIVE TO OTHER  UNITS
FIGURE 7   .55-GALLON DRUMS USED FOR MIXING
            CHAMBER  WITH MM-2.

-------
FIGURE  8   . TOP VIEW OF BIF AND ERD.
FIGURE 9   .TOP VIEW OF BIF AND ERD.

-------
FIGURE
 FIGURE  II . TOP  VIEW ERD

-------
 FIGURE  12 . FILTRATION  SECTION  OF ERD.
FIGURE 13  . BIF BODY FEEDER AND EDUCTOR
            USED  WITH ERQ.

-------
FINISHED
WATER
   WATER
   METER
 HEADLOSS
 GAGE
       Cl
                                   D-
   DE  SLURRY TANK


TEN SQ. FT. DE
FILTER^
                         475 RPM MIXER
CHEMICAL FEED
PUMP
                           DRAIN TO
                           WASTE ^^^
                         —04-
                                    WATER PLUS
                                COATED DIATOMACEOUS
                                EARTH .
                         ^RECIRCULATION LINE
           •EFFLUENT AND
           RECIRCULATION  PUMP
   475 RPM
   MIXER
HOSE  BIBB FOR
BACKWASH;
                                            1
                                                    RAW WATER
                                                 SVALVE CONT-
                                                  ROLLED BY
                                                  WATER LEVEL
                                                  IN TANK.
                                                                DRAIN TO WASTE
              FIGURE  14  . FLOW DIAGRAM  FOR BIF(ALT.2)

-------
                                                          BODY
 FINISHED
 WATER
   WATER
   METER
HEADLOSS
GAGE
                  POLYMER
                  TANK
TEN SQ. FT .
DE FILTER.
                                                FEEDER
                                                   475 RPM MIXER

                                                   HOSE BIBB FOR
                                                   BACKWASH.
                                                      RAW WATER
CHEMICAL
FEED PUMP
                                  DRAIN TO WASTE
                                    -RAW  WATER PLUS
                                    BODY FEED AND  POLYMER
                          ^-RECIRCULATION  LINE
           -EFFLUENT AND
           RECIRCULATION PUMP
                                                     VALVE  CONT-
                                                     ROLLED BY
                                                     WATER LEVEL
                                                     IN TANK.
                                                                 DRAIN TO WASTE
                  FIGURE  15  .FLOW DIAGRAM FOR  BIF  (ALT.3)

-------
     475 RPM MIXER
-DE SLURRY
 TANK
CHEMICAL
FEED
PUMP


    -1X1	
                    r
 UPFLOW  CLARIFIER
     TO MONITEK
  RAW WATER
                              EDUCTOR
                                        	^-RECIRCULATION  LINE
                                           AIR RELEASE
                                           VALVE
                      FILTER PUMP-H
                     TO BIF
                                                         FILTER
                                                         RECYCLE
                                                         VALVE
FILTER  WASH
VALVE ^

    JL
                                                               PRESSURE
                                                               VGAGE
                                                      TO WASTE
                                                      SUMP
                                       FINISHED WATERx
                                                                  RATE OF
                                                                  FLOW
                                                                  CONTROLLER
                                              FLOW  METER
             FIGURE 16 .  FLOW DIAGRAM FOR ERD (ALT. 2)

-------
     475 RPM MIXER
                          BODY  FEEDER
POLYMER
TANK
                             EDUCTOR
UPFLOW  CLARIFIER
    TO
                  -04-
RAW WATER
                                           /RECIRCULATION  LINE
                                          AIR RELEASE
                                          VALVE
                                FILTER  PUMP-
                             TO  BIF
                                     FINISHED WATER_x
                                                                 RATE OF
                                                                 FLOW
                                                                 CONTROLLER
                                             FLOW METER
          FIGURE  17  .  FLOW  DIAGRAM  FOR  ERD (ALT.3)

-------
                           APPENDIX B-2




                    OPERATION OF PILOT FILTERS







RAW WATER SOURCES




With the exception of three runs on the MM-2 unit,  all runs  on the




pilot filtration units were made using the Lakewood wetwell  as the




raw water source.  The intake of the Lakewood Pumping Station extended




approximately 1,500 ft out into Lake Superior and was about  70 ft




below the surface of the lake.  Suction hoses were  placed  directly in




the wetwell and raw water was pumped to each of  the filter units so




that the raw water supplied to the units was the same as  that being




supplied to the City of Duluth.




Raw water from the Cloquet Pipeline Intake was used for three runs on




the MM-2 units.  The Cloquet raw water was transported from  the Cloquet




raw water pumping station on Minnesota Point to  the Lakewood Pumping




Station in a A,800 gal tank truck.  The suction  of  one of  the pilot




plant raw water pumps was connected to the discharge from  the tank




truck and the water pumped to the MM-2 unit.  An illustration of the




tank truck and raw water pump is given in Figure 18.




GRANULAR UNITS - CHEMICAL ADDITIONS




The solution concentration and point of application of the polymers




were varied during the testing of the MM-1 unit, but the most common




points of chemical application were the flocculation chamber when  no




sedimentation was provided, and the entrance to  the sedimentation




chamber when the tube settlers were installed.  Several runs at the




beginning of the study were conducted with the polymer added into  the
                                  13

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FIGURE 18 .  4800 GALLON  TANK TRUCK TRANS-
            PORT CLOQUET  PIPELINE  WATER
            TO PILOT PLANT.
                    14

-------
mixing chamber with the alum.  However, the purpose of the polymer as




used during the pilot filter studies was to strengthen the floe produced




by the primary coagulant and it was decided this could best be




accomplished by adding the polymer subsequent to the coagulation step




in the process.  A summary of chemical solution strengths and  points




of application is given in Table 1.
TABLE 1.  SUMMARY OF CHEMICAL ADDITIONS TO MM-1

Chemical
Alum

Alum
FeCl3
NP-10
N-17
N-17
84 7A
985N
985N
985N
985N
Solution
concentration ,
per cent
1.19
1.19
1.19
0.0299
0.0599
0.0599
0.0567
0.0299
0.0149
0.0149
0.0149
Run No .
1-44
45-63
64-87
1-2
4-11
12-19
20-24
25-29
30-49
50-64
65-87
Point of application
Mixing chamber
Mixing chamber
Mixing chamber
Mixing chamber
Mixing chamber
Flocculation chamber
Flocculation chamber
Flocculation chamber
Flocculation chamber
Just prior to filter
Entrance to sedimentation basin

Alum was used as the primary coagulant in 117 of the runs conducted




on the unit and FeCl^ in 23 runs.  Alum dosages ranged from 5.44




mg/1 to 37.86 mg/1 with an average dosage of about 15 mg/1.  FeCl3




dosages ranged from 6.22 mg/1 to 17.4 mg/1 with an average dosage




of about 11 mg/1.  Numerous polymer solution concentrations and




points of application were used during the pilot studies with the




MM-2 unit, and are summarized in Table 2.
                                   15

-------
TABLE 2.  SUMMARY OF CHEMICAL ADDITIONS TO MM-2.
            Solution
         Concentration,
Chemical	per cent
Run No.
Point of Application
Fed         1.19               1-23
Alum         1.19              24-92
Alum         1.19          93-120, 138-140
Alum         1.19         121-123, 129-137
Alum         1.19             124-128

C-31         0.119              1-16
N-17         0.0599            17-18
N-17         0.0599        20, 22-27, 34-41
N-17         0.0599            19, 21
985N         0.0599         28-33, 42-51
985N         0.0299            52-53
985N         0.0149            54-92
985N         0.0149    93-115, 119, 120, 138, 140
A-23         0.0599            116, 118
Catfloc B    0.119           116, 117, 118
A-23         0.0299      119, 120, 138, 139
985N         0.0149      121-123, 129-133
A-23         0.0599           124-128
985N         0.0149         124, 127, 128
C-31         0.119            125, 126
C-31         0.119               134
C-31         0.119            135-137      Prior to
C-31         0.119               139
                          Mixing Chamber
                          Mixing Chamber
                          1st mixing tank
                     Prior to 1st Kenics mixer
                     Prior to 2nd Kenics mixer

                          Mixing Chamber
                          Mixing Chamber
                        1st floe Chamber
                        2nd floe Chamber
                        1st floe Chamber
                        1st floe Chamber
                        1st floe Chamber
                        2nd mixing tank
                        1st mixing tank
                        2nd mixing tank
                        1st mixing tank
                     Prior to 2nd Kenics mixer
                     Prior to 1st Kenics mixer
                     Prior to 3rd Kenics mixer
                     Prior to 3rd Kenics mixer
                     Prior to 2nd Kenics mixer
                     2nd pair of Kenics mixers
                        2nd mixing tank
                                       16

-------
APPENDIX c-1   GRANULAR MEDIA FILTRATION (MM-1) SUMMARY OF INDIVIDUAL RUNS
Run
No.
Dual
1
2
3
4
5
6
7
8
9
10
11
Polyn
12
13
14
OaCe
media
S/13
5/13
2 Hr
S/14
S/15
5/15
5/16
5/16
5/17
S/17
S/18
er fee
S/20
S/20
5/21
Filter
rate,
gpm/ft2
(m3/m2 day)
filtra. w/o sedi.
3.89
(228.23)
4.18
(245.24)
run terminated
4.04
(237.03)
3.28
(192.44)
3.19
(187.16)
3.46
(203.00)
3.64
(213.56)
3.57
(209.45)
3.61
(211.80)
3.72
(218.25)
1 moved to inf
3.77
(221.19)
3.83
(224.71)
3.99
(234.09)
Coag.,
mg/l
, Alum &
Alum
12.3
Alum
12.3
Polymer
Alum
16.61
Alum
18.6
Alum
20.48
Alum
17.88
Alum
17.82
Alum
18.1
Alum
17.5
Alum
17.6
lent of fl(
Alum
16.96
Alum
16.2
Alum
18.28
Polymer,
mg/l
Jolymer ad
Separan
NP-10
0.17
Separan
NP-10
0.26
not mixed.
N-17
0.22
N-17
0.35
N-17
0.39
N-17
0.38
N-17
0.286
N-17
0.25
N-17
0.23
N-17
0.27
c. chamber
N-17
0.272
N-17
0.33
N-17
0.293
Coag.,
Ib
1000 gal.
led to mi
0.102
0.103
0.139
0.155
0.171
0.149
0.149
0.151
0.146
0.147

0.142
0.135
0.152
j
Polymer,
Ib
1000 gal.
ing cham
0.0014
0.0022
0.0018
0.0029
0.0032
0.0031
0.0024
0.0021
0.001 9
0.0023

0.0023
0.0028
0.0025
Backwash solids,
Ib /1 000 gal
Sedi. Filter Total
er, L

-
-
-
-
-
-
-
-

-
-
—
tewoo

-
-
—
-
-
-
-
-

-
-
0.034
wat*

—
—
—
-
-
-
-
-

-
-
0.034
B.W. vol.,
as % of
treated
water
4.97%
3.43%
4.94%
5.18%
6.30%
3.61%
2.66%
3.09%
3.25%
5.52%"

2.53%
3.66%
2.72%
Avg. turb.
(Turb @ time
of sample),
TU .
Raw Filter
0.90
0.90
2.4
1.3
1.4
0.80
(0.74)
1.1
1.14
0.85
0.95

0.85
1.09
0.90
0.40
0.32
0.24
0.20
0.21
0.20
(0.15)
0.21
0.15
0.25
0.30

Q.23
Q.14
0.25
ORF
FibersxlO6/!
Raw Filter





A=2.6!
C=1.35













A=BD1
C=0.13








NWQL
Amphibole
mg/l
Raw Filter





0.14













0.005








UMD
FibersxlO6/!
Raw Filter




























Term
HL
Ft.
H20
8.0
8.0
8.0
8.0
8.0
8.0
8.0
8.0
8.0
6.4

8.0
8.0
8.0
inal
Turb.
TU
0.73
0.38
0.14
0.58
0.26
0.16
0.16
(0.11
0.32
0.19

0.15
0.11
0.26
Run
Length, Hrs.
(Time to
Sample)
9.23
10.25
7.50
10.75
8.33
6.75
(4.9)
8.25
7.17
8.73
6.08

7.83
6.07
7.71

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APPENDIX C-l   (CONTINUED).
Run
No.
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
Date
5/21
5/22
5/22
5/22
5/23
5/23
5/23
5/24
5/28
5/28
5/29
5/30
5/31
6/3
6/4
Filter
rate
gpm/ft2
(n>3/m2 day)
3.44
(201.83)
3.86
(226.47)
3.92
(229.99)
3.98
(233.51)
4.16
(244.07)
3.96
(232.33)
3.83
(244.71)
3.79
(222.36)
3.82
(224.12)
4.13
(242.31)
3.83
(224.71)
3.65
(214.15)
4.14
(242.89)
4.05
(237.61)
4.01
(235.27)
Coag.,
mg/1
Alum
15.51
Alum
14.32
Alum
14.79
Alum
15.42
Alum
14.23
Alum
15.71
Alum
15.51
Alum
16.65
Alum
21.36
Alum
16.04
Alum
13.18
Alum
14.15
Alum
12.46
Alum
13.3
Alum
14.2
Polymer,
mg/1
N-17
0.35
N-17
0.339
N-17
0.37
N-17
0.41
N-17
0.418
847-A
0.232
847-A
0.260
847-A
0.098
847-A
0.110
847-A
0.099
985-N
0.123
98S-N
0.123
985-N
0.054
985-N
0.061
985-N
0.062
Coag.,
Ib
1000 gal.
0.130
0.119
0.123
0.129
0.119
0.131
0.129
0.139
0.178
0.134
0.110
0.118
0.104
0.111
0.118
Polymer,
Ib
1000 gal.
0.0029
0.0028
0.0027
0.0034
0.0035
0.0019
0.0022
0.00082
0.00092
0.00083
0.0010
0.0010
0.00045
0.00051
0.00052
Backwash solids,
Ib /10OO gal.
Sedi. Filter Total
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
0.022
0.055
0.022
0.036
0.069
0.028
0.049
0.044
0.062
0.039
0.021
0.037
0.030
0.025
0.018
0-022
0.055
0,022
0.036
0,069
0,028
0,049
0.044
0.062
0.039
0.021
0.037
0.030
0.025
0.018
B.W. vol.,
as % of
treated
water
2.59%
4.09%
3.70%
3.78%
5.31%
3.00%
2.43%
1.56%
2.13%
1.31%
2.59%
2.62%
1.13%
1.45%
1.42%
Avg. turb.
(Turb @ time
of sample),
TU
Raw Filter
0.80
0.89
(0.94)
0.85
0.92
0.90
1.4
0.95
1.2
0.82
0.85
0.83
0.82
(0.80)
0.85
0.78
0.82
(0.86)
0.32
0.30
(0.42)
0.45
0.35
0.42
0.15
0.15
0.15
0.16
0.20
0.15
0.15
(0.15)
0.19
0.11
0.10
(0.10)
ORF
FibersxlO6/!
Raw Filter











A=1.4;
C=1.83


i\=1.74
C=2.91











A=BDL
C=0.26


A=BDL
C=0.47f
NWQL
Amphibole
mg/1
Raw Filter

0.20









0.19


0.26

<0.01









<0.01


<• 0.006
UMD
FibersxlO6/!
Raw Filter






























Terrr
HL
Ft.
H2O
8.0
8.0
8.0
8.0
8.0
8.0
8.0
8.0
8.0
8.0
8.0
8.0
8.0
8.0
8.0
linal
Turb.
TU
0.22
0.41
0.33
0.25
0.47
0.15
0.11
0.34
0.38
1.50
0.13
0.19
0.15
0.07
0.12
Run
Length, Hrs.
(Time to
Sample)
8,28
7.85
(6.1)
6.60
6.70
6.09
8.49
8.93
14.00
13.02
17.33
13.70
16.33
(2.6)
20.16
19.75
18.68
(3.2)

-------
APPENDIX  c-l   (CONTINUED)
Run
No.
30
31
32
33
34
35
36
37
38
39
40
Sedii
41
42
43
44
Date
6/5
6/6
6/7
6/10
6/11
6/12
6/13
No A
6/14
6/17
6/18
lentat
6/19
6/20
6/21
6/2<
Filter
rate
gpm/ft2
(m3/m2 day)
4.03
(236.44)
3.93
(230.57)
4.09
(239.96)
3.89
(228.23)
3.92
(229.99)
4.10
(240.55)
4.07
(238.79)
lum added — M
4.07
(238.79)
4.06
(238.20)
3.91
(229.40)
on tube settlers
3.81
(223.53)
3.75
(220.01)
4.05
(237.61)
13.98
(233.51)
Coag.,
mg/1
Alum
13.7
Alum
12.6
Alum
11.95
Alum
12.43
Alum
12.21
Alum
13.08
Alum
16.13
chanica) f
Alum
14.48
Alum
16.85
Alum
17.01
installed.
Alum
19.01
Alum
18.28
Alum
14.27
Alum
14.81
Polymer,
mg/1
985-N
0.047
985-N
0.062
985-N
0.022
98S-N
0.055
985-N
0.08
985-N
0.074
985-N
0.071
ilure
985-N
0.063
985-N
0.057
985-N
0.048
985-N
0.054
985-N
0.085
98S-N
0.066
98S-N
0.078
Coag.,
Ib
1000 gal.
0.114
0.105
0.100
0.104
0.102
0.109
0.134

0.121
0.141
0.142
0.159
0.152
0.119
0.124
Polymer,
Ib
1000 gal.
0.00039
0.00053
0.00018
0.00046
0.00067
0.00062
0.00059

0.00053
0.00048
0.00040
0.00046
0.00071
0.00055
0.0006!
Backwash solids,
Ib /1 000 gal.
Sedi. Filter Total
-
~
-
-
"
-
-

-
-
~
0.015
0.021
0.022
0.014
0.038
0.026
0.048
-
-
0.046
0.028

0.048
-
0.050
-
-
-
—
0.038
0,026
0.048
-
-
0.046
0.028

0.048

0.050
0015
0.021
0.022
0.014
B.W. vol.,
as % of
treated
water
1.95%
1 .62%
1.50%


1.25%
2.85%

1.81%

1.93%
1 .63%
1.22%
3.53%"
1.16%
Avg. turb.
(Turb @ time
of sample),
TU
Raw Filter
0.80
1.53
(0.74)
3.6
3.9
2.98
(1.90)
2.2
2.1
(2.1)

1.8
0.95
(0.96)
0.90
0.90
1.25
1.1
0.66
(0.66)
0.11
0.12
(0.09)
0.16
0.19
0.15
(0.25)
0.12
0.13
(0.16)

0.12
0.11
(0.10)
0.12
0.09
0.10
0.09
0.09
(0.11)
ORF
FibersxlO6/!
Raw Filter

\=1.5
C=2.3


A=1.0
C=1.6

\=0.48
C=0.41


A=0.6
C=2.15




A=1.0
C=3.9

A=BDL
C=0.35


A =0.17
C=0.17

A=BDL
C=0.57


A=BDL
C=0.44




^=BDL
C=0.13
NWQL
Amphibole
mg/1
Raw Filter

0.18


0.18




0.17






< 0.005


0.006




< 0.006





UMD
FibersxlO6/!
Raw Filter






33.25


10.6'




6.03






0.53


0.23




0.92
Tern
HL
Ft.
H2O
8,0
8.0
8.0
6.8
8.0
8.0
8.0

8.0
8.0
5.1
6.1
8.0
3.6
8.0
linal
Turb.
TU-
0,09
0.15
0.12
1.7
0.16
0.11
0.14

0.07
0.11
0.85
0.80
0.10
0.07
0.04
Run
Length, Mrs.
(Time to
Sample)
18,25
19.73
(6.7)
21.58
24.75
17.92
(1.0)
17.50
11.75
(8.0)

16.18
14.71
(1.9)
16.53
26.83
25.03
11.66
25.83
(3.7)

-------
        APPENDIX c-1   (CONTINUED)
Run
No.
Now
45
46
47
48
49
Polyi
50
51
52
53
54
55
56
57
Date
using 1
6/25
6/26
6/27
6/28
6/28
ler in I
7/1
7/2
7/3
7/3
7/4
7/4
7/8
7/9
Filter
rate
gpm/ft2
(m3/m2 day)
erric Chloride a
4.06
(238.20)
4.28
(251.11)
4.10
(240.55)
4.12
(241.72)
4.11
(241.13)
ut just ahead of
4.06
(238.20)
3.69
(216.49)
3.86
(226.47)
4.08
(239.37)
4.10
(240.55)
4.08
(239.37)
4.08
(239.37)
3.98
(228.23)
Coag.,
mg/1
> a coagula
FeCl3
12.16
FeCls
11.42
FeCls
11.81
FeCl3
12.0
FeCl3
12.24
filter bed.
Fed 3
12.21
FeCl3
12.25
FeCls
16.49
FeCl3
13.78
FeCI3
14.97
FeCls
14.77
FeCIs
14.29
Fed 3
16.35
Polymer,
mg/1
it added to
985-N
0.058
985-N
0.071
985-N
0.073
985-N
0.094
985-N
0.094

985-N
0.103
985-N
0.105
985-N
0.087
985-N
0.057
985-N
0.062
985-N
0.035
985-N
0.055
985-N
0.048
Coag.,
Ib
1000 gal.
mixing ch
0.101
0.095
0.098
0.100
0.102

0.102
0.102
0.138
0.115
0.125
0.123
0.119
0.136
Polymer,
Ib
1000 gal.
imber.
0.00048
0.00060
0.00062
0.00078
0.00079

0.00086
0.00088
0.00073
0.00048
0.00052
0.00029
0.00046
0.00040
Backwash solids,
Ib /1 000 gal.
Sedi. Filter Total

0.021
0.026
0,059
0.083
0.066

0.028
0,042
0.040
0.036
0.039
0.044
0.106
0.077

-
—
—
-
—

-
-
-
-
-
-



0.021
0.026
0.05^
0.083
0.066

0.028
0.042
0.040
0.03(
0.039
0.044
0.106
0.077
B.W. vol.,
as % of
treated
water

1.45%
2.70%
2.33%
2.50%
3.14%a

1.53%
1.92%
3.81%
2.87%
3.74%
2.31%
2.52%
2.15%
Avg. turb.
(Turb @ time
of sample),
TU
Raw Filler

0.66
0.68
0.73
0.65
(0.64)
0.69

0.78
0.77
0.77
(0.69)
0.73
0.67
0.62
0.67
0.65

0.25
0.12
0.11
0.09
(0.14)
0.10

0.12
0.09
0.07
(0.07)
0.11
0.08
0.11
0.09
0.09
ORF
FibersxlO6/!
Raw Filter




A=l.ll
C=8.12





-------
APPENDIX C-l    (CONTINUED)
Run
No.
58
59
60
61
62
63
Chan
64
Poly
65
66
67
68

69

70
71
Date
7/9
7/10
7/11
7/11
7/12
7/12
ged to
7/lS
ner du
7/16
7/17
7/19
7/19

7/22

7/23
7/24
Filter
rate
gpm/ft2
(m3/m2 day)
3.68
(215.91)
4.08
(239.37)
3.64
(213.56)
3.94
(231.16)
3.93
(230.57)
3.89
(228.23)
Alum as a coag
3.89
(228.23)
charge moved f
3.90
(228.81)
3.87
(227.05)
3.85
(225.88)
3.93
(230.57)
3.97
(232.92)
3.88
(227.64)
3.83
Coag.,
mg/1
FeCl3
17.54
FeCl3
7.36
FeCl3
14.79
FeCls
12.81
FeCls
12.36
Fed 3
12.73
lant to mi
Alum
12.99
om filter t
Alum
11.82
Alum
12.10
Alum
10.99
Alum
11.67
Alum
11.86
Alum
12.20
Alum
11.24
Polymer,
mg/1
985-N
0.069
985-N
0.061
985-N
0.054
98S-N
0.059
985-N
0.065
985-N
0.067
King chamb
985-N
0.041
3 Sediment
985-N
0.037
985-N
0.039
985-N
0.039
985-N
0.050
985-N
0.025
985-N
0.026
985-N
0,025
Coag.,
Ib
1000 gal.
0.146
0.061
0.123
0.107
0.103
0.106
r.
0.108
tion Basil
0.099
0.101
0.092
0.097

0.099

0.102
0.094
Polymer,
Ib
1000 gal.
0.00057
0.00051
0.00045
0.00050
0.00055
0.00056

0.00034

0.00031
0.00033
0.00033
0.00042

0.00021

0.00022
0.00021
Backwash solids,
Ib /1 000 gal.
Sedi. Filter Total
0.070
0.151
0.055
0.071
0.061
0.084

0.045

0.0 IS
0.027
0.024
0.039

0.030

0.019
0.027
-
-
-
-
-
_

-

-
-
-
_

-

-
-
0.070
0.151
0.0 55
0.071
0.061
0.084

0.045

0.015
0,027
0.024
0.039

0.030

0.019
0.027
B.W. vol.,
as % of
treated
water
3.66%
2.18%
3.23%
2.76%
2.38%
4.47%3

2 .00%

1.81%
1 .83%
1 .67%
2.62%a

1.93%

2.02%
—
Avg. turb.
(Turb @ time
of sample),
TU
Raw Filter
0.97
1.2S
1.01
1.81
1.15
0.77

0.68

0.70
0.72
0.83
(0.90)
0.68

0.65

0.60
(0.57)
0.82
0.14
0.21
0.10
0.10
0.10
0.12

0.09

0.11
0.10
0.11
(0.10)
0.10

0.09

0.08
(0.07)
0.09
ORF
FibersxlO6/!
Raw Filter











V=0.52
C=0.3S




C=0.0?












A=BDL
C=0.15




A=BDI
C=0.07

NWQL
Amphibole
mg/1
Raw Filter











0.13




0.09












< 0.003




<0.003

UMD
FibersxlO6/!
Raw Filter











266.0




26.0












0.66




0.35

Tern
HL
Ft.
H2O
8.0
8.0
8.0
8.0
8.0
4.1

7.1

8.0
8.0
8.0
5.8

8.0

8.0
8.0
linal
Turb.
0.44
0.06
0.11
0.08
0.10
0.11

0.49

0.17
0.12
0.12
0.10

0.14

0.10
0.11
Run
Length, Mrs.
(Time to
Sample)
ifl.73'
12.81
10.25
13.20
11.23
9.58

21.92

22.76
21.05
21.03
(20.1)
14.17

20.08

19.72
(4.5)
18.49

-------
APPENDIX c-l   (CONTINUED)
Run
No.
72
73
74
75
76
77
78
79
80
81
82
83
84
85
86
Date
7/25
7/26
7/30
7/30
8/1
8/2
8/6
8/6
8/8
8/9
8/13
8/13
8/15
8/16
8/21
Filter
rate
gpm/ft2
(m3/m2 day)
3.86
(226.47)
3.31
(194.20)
3.27
(191.85)
3.31
(194.20)
3.13
(183.64)
3.08
(180.70)
3.28
(192.44)
3.44
(201.825)
3.81
(223.53)
3.82
(224.12)
3.69
(216.49)
3.76
(220.60)
3.74
(219.43)
3.61
(211.80)
3.75
(220.01)
Coag.,
mg/l
Alum
10.71
Alum
13.09
Alum
15.56
Alum
15.28
Alum
15.73
Alum
16.30
Alum
15.08
Alum
15.43
Alum
13.69
Alum
13.35
Alum
15.49
Alum
14.72
Alum
15.13
Alum
14.62
Alum
17.96
Polymer,
mg/l
985-N
0.029
985-N
0.041
985-N
0.034
985-N
0.034
985-N
0.037
985-N
0.031
985-N
0.039
985-N
0.035
985-N
0-038
985-N
0.034
985-N
0.033
985-N
0.033
98S-N
0.036
985-N
0.033
985-N
0.060
Coag.,
Ib
1000 gal.
0.089
0.109
0.130
0.127
0.131
0.136
0.126
0.129
0.114
0.111
0.129
0.123
0.126
0.122
0.150
Polymer,
Ib
1000 gal.
0.00024
0.00034
0.00028
0.00029
0.00031
0.00026
0.00033
0.00029
0.00032
0.00028
0.00028
0.00027
0.00030
0.00027
0.00050
Backwash solids,
Ib /1000 gal.
Sedi. Filter Total
0.076
0.046
0.060
0.057
0,024
0.060
0.009
0.006
0.004
0,012
0.010
(0.009
0.020
0.022
0.014
-
0.032
0.024
0.049
0.037
0.025
0.039
0.058
0.059
0.076
O.D51
0.045
0.045
0.021
0.028
0.076
0.078
0.084
0.106
0.061
0.085
0.048
0.06'
0.063
0.08!
0.061
0.054
0.065
0.043
0.042
B.W. vol.,
as % of
treated
water
1.85%
1.93%
1.48%
1 .70%
1 .63%
3.96%
1 .35%
1 .50%
1.83%
1.82%
1.62%
1 .57%
1 .36%
1.86%a
2.00%
Avg. turb.
(Turb @ time
of sample),
TU
Raw Filter
0.73
(0.66)
0.66
0.73
(0.69)
0.79
1.07
(0.87)
0.97
0.64
(0.58)
0.65
1.12
(0.68)
1.12
0.66
(0.60)
0.71
0.61
(0.71)
0.76
0.65
(0.58)
0.11
(0.07)
0.10
0.10
(0.08)
0.09
0.09
(0.07)
0.09
0.09
(0.07)
0.10
0.12
(0.08)
0.14
0.09
(0.10)
0.08
0.06
(0.06)
0.09
0.08
(0.08)
ORF
FibersxlO6/!
Raw Filter
*.-0,li
c=i.4:

A=0.1
OO.ll

A=o.2:
C=0.1!

\=0.6
C=0.3

\=0.0<
C=0.0<

\=o..i :
C=0.2

\=0.0<
C=0. 1 '

\=o.i:
C=0.37
AsBDL
00,37

A=BDL
OBDL

A=BDL
C=0.22

A=BDL
C=0.06

A=0.04
C=0.2

A=BDL
C=0.03

A=BDL
C=0.52

A=BDL
C=0.13
NWQL
Amphibole
mg/l
Raw Filter
0.04

0.06

0.08

0.09

0.05

0.06

0.06

0.03
<0,005

<0.003

•C0.004

<0,004

•C0.003

<0.003

<0.003

< 0.003
UMD
FibersxlO6/!
Raw Filter
60,5

26.6

30.0

10.2

15.1

20.0

8.98

13.6
0,46

0.18

0.72

0.20

0.45

0.38

0.55

0.31
Tern
HL
Ft.
H2O
8,0
8.0
6.6
5.0
8.0
8.0
8.0
5.1
4.7
7.9
8.0
7.5
8.0
4.8
8.0
ninal
Turb.
TU
0,12
0.14
0.31
0.35
0.12
0.10
0.09
0.42
0.40
0.21
0.15
0.32
0.07
0.11
0.06
Run
Length, Hrs.
(Time to
Sample)
22.58
(7.8)
24.58
34.33
(22.8)
29.67
32.06
(7.3)
9.78
30.92
(23.3)
32.33
23.97
(2.7)
24.00
25.83
(22.5)
28.08
30.87
(12.3)
24.83
20.25
(0.8)

-------
APPENDIX  C-l    (CONTINUED)
Run
No.




Used
87





Date
8/22

8/22

coagul
9/18





Filter
rate
gpm/ft2
(m3/m2 day)




nt aid. Backwa
3.49
(204.76)




Coag.,
mg/1




ti solids ca
Alum
21.46
Coagulant
Aid
Bentonite
26.83
Polymer,
mg/1




culated fro
985-N
0.067




Coag.,
Ibs.
1000 gal.




m Chem. j





0.224
Polymer,
Ibs.
1000 gal.




dditions.






Backwash solids,
Ibs/lOOO gal.
Sedi. Filter Total





_





















0.403





B.W. vol.,
as % of
treated
water





2.39%





Avg. turb.
(Turb @ time
of sample),
TU
Raw Filter
(0.68)

(0.76)


0.55
(0.52)




(0.06)

(0.15)


0.12
(0.10)




ORF
FibersxlO6/!
Raw Filter
A=0,J3
>0,37
A=0.13
C=0.37

A=0.6
C=0.09




AHBDL
>0,22
A=BDL
C=0.80

A=1.0
C=0.7




NWQL
Amphibole
mg/1
Raw Filter
003

0,03


0.10





.003





UMD
FibersxlO6/!
Raw Filter
1-3.6

13.6


13.8





0,49

0.37


1.46





Term
HL
Ft.
H20





8.0





inal
Turb.
TU





0.10





Run
Length, Mrs.
(Time to
Sample)
O6.D

(22.0)


18.53
(18.1)




  a Run did not reach terminal HL or turbidity.
 k A=amphibole,  C-chrysotile

-------
APPENDIX  C-2  GRANULAR MEDIA FILTRATION (MM-2) SUMMARY OF INDIVIDUAL RUNS
Run
No.
Filtra
1
2
3
4
S
6
7
8
9
10
11
12
13
14
IS
Date
ion w/
4/19
4/22
4/23
4/24
4/24
4/25
4/25
4/26
4/26
4/26
4/29
4/30
4/30
Run
Run
Filter
rate
gpm/ft2
(m3/m2 day)
> sedimentatioi
4.96
(291.00)
4.5
(264.02)
4.2
(246.41)
3.66
(214.73)
5.48
(321.51)
4.56
(267.54)
4.26
(249.93)
3.89
(228.23)
4.19
(245.83)
4.22
(247.59)
4.18
(245.24)
4.25
(249.35)
4.1
(240.55)
oo short for ci
oo short for cj
Coag.,
mg/l
, dual me
Fed 3
6.22
FeCl3
6.82
FeCl3
7.66
Fed 3
9.91
FeCl3
10.11
FeCl3
11.35
FeCI3
8.61
FeCl3
11.29
FeCl3
8.67
FeQ3
8.53
FeCl3
7.90
FeQ3
8.75
FeCl3
17.21
dilations
culations
Polymer,
mg/l
iia, 450 rpr
C-31
0.518
C-31
0.682
C-31
0.725
C-31
0.595
C-31
0.59
C-31
0.486
C-31
0.626
C-31
0.678
C-31
0.64
C-31
0.62
C-31
0.526
C-31
0.583
C-31
0.573


Coag.,
Ib
1000 gal.
i mixer i
0.052
0.057
0.064
0.083
0.084
0.095
0.072
0.094
0.072
0.071
0.066
0.073
0.144


Polymer,
Ib
1000 gal.
i mixing cha
0.0043
0.0057
0.0061
0.0050
0.0049
0.0041
0.0052
0.0057
0.0053
0.0052
0.0044
0.0049
0.0048


B.W.
solids,
Ib
1000 gal.
nber FeCl3,S
-
-
_
_
_
_.
~
-
-
-
-
_
—


B.W. vol.
as % of
treated
watera
polymer
-
-
-
-
-
_


-
-


-


Avg. turb.
(Turb. ® time
of sample),
TU
Raw Filter
dded to mixin
1.0
(1.3)
1.3
1.3
1.1
1.0
1.0
D.90
1.0)
1.90
).85
0.95
5.85
0.85
D.84


0.35
(0.22)
0.30
0.64
0.55
0.52
0.25
0.31
(0.10)
0.06
0.28
0.50
0.31
0.27
0.63


ORF
FibersxlO6/!
Raw Filter

V= 304
C=.217





A=.34f
C=.174









A=BDL
C=.043!





A=BDL
C=.348








NWQL
Amphibole
mg/l
Raw Filter

0.1





0.12









<0.02





<0.02








UMD
FibersxlO6/!
Raw Filter
































Tern
HL
Ft.
H2O

6.2
6.4
5.3
4.3
3.3
3.8
4.4
2.1
3.9
2.9
4.2
4.3
2.4


ninal
Turb.
TU

1.1
0.82
0.68
1.10
0.95
0.88
0.95
0.15
0.96
0.45
0.87
0.65
1.3


Run
Length, Hrs.
(Time to
Sample)

14.58
(6.5)
16.25
14.25
10.33
5.42
6.75
15.00
(4.5)
6.00
13.08
7.62
13.66
12.10
4.25



-------
         APPENDIX C-2   (CONTINUED)
Run
No.
16
17
18
Polym
19
Polym
20
Polym
21
Polyrr
22
23
Now i
24
25
26
27
Date
5/1
Run 1
Efflui
'.r addt
5/2
:r addi
5/2
IT add>
5/3
3r add*
5/3
5/6
sing A
5/6
5/7
5/8
5/9
Filter
rate
gpm/ft2
(m3/m2 day)
4.285
(251.40)
oo short for ca
nt turbidity to
d to 2nd floe.
4.2
(246.41)
d to 1st floc.cl
4.21
(247.00)
d to 2nd floc.l
4.21
(247.00)
d to 1st floe, c
3.82
(224.12)
4.24
(248.76)
um as coag. ad
4.25
(249.35)
3.82
(224.12)
3.8
(222.95)
3.67
(215.32)
Coag.,
mg/l
FeCl3
16.75
culations.
> high.
chamber.
FeCl3
11.71
amber.
FeCI3
11.36
hamber.
FeCI3
12.21
lamber.
FeCl3
11.48
FeCl3
11.78
led to mi
Alum
16.74
Alum
18.85
Alum
18.54
Alum
19.62
Polymer,
mg/l
C-31
0.492



N-17
0.320

N-17
0.317

N-17
0.106

N-17
0.121
N-17
0.330
;ing chamb
N-17
0.20
N-17
0.269
N-17
0.394
N-17
0.48
Coag.,
1000 gal.
0.140



0.098

0.095

0.102

0.096
0.098
r.
0.140
0.157
0.155
0.164
Polymer,
Ib
1000 gal.
0.0041



0.0027

0.0027

0.00089

0.0010
0.0028

0.0017
0.0022
0.0033
0.0040
B.W.
solids,
Ib
1000 gal.










_
_

_
— ,
_
-
B.W. vol.
as % of
treated
watera











-




•-
Avg. turb.
Turb. @ time
of sample),
TU
Raw Filter
0.77



0.80

0.60

8.75

J.75
(.70

(.70
(.70
1.68
1.80
0.39



0,34

0.23

0.39

0.51
0.33

0.24
0.12
0.16
0.12
ORF
FibersxlO6/!
Raw Filter


































NWQL
Amphibole
mg/l
Raw Filter


































UMD
FibersxlO6/!
Raw Filter


































Tern
HL
Ft.
H2O
2.9



6.4

6.3

6.8

4.0
6.0

6.2
6.5
7.0
7.0
linal
Turb.
TU
1.1



0.33

0.64

1.75

1.50
1.5

0.70
0.17
0.80
0.11
Run
Length, Mrs.
(Time to
Sample)
5.92



5.58

13.03

11.17

10.83
12.50

14.75
17.0
16.66
17.00
r-o
on

-------
APPENDIX C-2   (CONTINUED)
Run
No.
28
29
30
31
32
33
34
35
36
37
38
39
40
Polyrr
41
Date
5/9
5/10
5/10
S/13
5/13
5/14
5/14
5/15
5/15
5/16
5/16
5/17
5/17
er fed
5/20
Filter
rate
gpm/f|2
(m3/m2 day)
3.47
(203.59)
3.96
(232.33)
5.28
(309.78)
3.78
(221.37)
3.614
(212.03)
3.75
(220.01)
3.91
(229.40)
3.95
(231.75)
3.52
(206.52)
3.86
(226.47)
4.13
(242.31)
3.876
(227.41)
3.93
(230.57)
8 entrance to :
3.85
(225.88)
Coag.,
mg/l
Alum
21.59
Alum
18.93
Alum
10.54
Alum
14.75
Alum
20.0
Alum
18.65
Alum
18.57
Alum
18.5
Alum
20.44
Alum
18.62
Alum
17.46
Alum
19.4
Alum
18.77
st floe, cl
Alum
17.92
Polymer,
mg/l
985-N
0.968
985-N
0.710
985-N
0.251
985-N
0.148
985-N
0.25
985-N
0.175
N-17
0.133
N-17
0.15
N-17
0.265
N-17
0.24
N-17
0.22
N-17
0.194
N-17
0.156
amber.
N-17
0.132
Coag.,
Ib
1000 gal.
0.180
0.158
0.088
0.123
0.167
0.1S6
0.1S5
0.154
0.170
0.155
0.146
0.162
0.157

0.149
Polymer,
Ib
1000 gal.
0.0081
0.0059
0.0021
0.0012
0.0021
0.0015
0.0011
0.0013
0.0022
0.0020
0.0018
0.0016
0.0013

0.0011
B.W.
solids,
Ib
1000 gal.
-
-
-
-
-
-
-
-
-
-
-
-
_

-
B.W. vol.
as % of
treated
watera
-
-
-
-
-
-
-
-
5.68%b
3.46%b
4.09%b
2.80%b
4.59%b

1.80%
Avg. turb.
Turb. @ time
of sample),
TU
Raw Filter
0.70
0.75
0.65
0.95
0.95
0.80
2.3
1.5
1.3
1.0
(0.8)
1.1
1.0
1.0

0.88
0.11
0.13
0.11
0.49
0.48
0.17
0.24
0.30
0.24
0.19
(0.19)
0.23
0.19
0.20

0.20
ORF
FibersxlO6/!
Raw Filter









^.=2.61
C=1.35














A=BDL
C=.174





NWQL
Amphibole
mg/l
Raw Filter









0.14














0.003





UMD
FibersxlO6/!
Raw Filter






























Tern
HL
Ft.
HiP
6.6
6.6
6.3
5.8
6.1
7.0
5.8
6.8
7.0
6.4
6.3
6.5
4.0

6.9
ninal
Turb.
TU
0.15
0.10
0.09
1.8
0.12
0.15
0.20
0.25
0.11
0.20
0.21
0.11
0.24

0.15
Run
Length, Hrs.
(Time to
Sample)
9.66
8.0
9.42
8.95
8.3
11.41
9.63
12.65
9.38
12.16
(9.8)
11.08
14.95
10.15

19.57

-------
APPENDIX  C-2   (CONTINUED)
Run
No.
42
43
44
45
46
47
48
49
SO
51
52
53
54
55
56
Date
5/21
5/22
5/22
5/23
5/23
5/24
5/28
5/29
5/30
5/31
6/3
6/4
6/6
6/11
6/11
Filter
rate
gpm/ft2
(m3/m2 day)
4.03
(236.44)
3.84
(225.29)
3.87
(227.05)
3.71
(217.67)
3.87
(227.05)
3.95
(231.75)
3.88
(227.64)
3.88
(227.64)
4.01
(235.27)
5.09
(298.63)
4.51
(264.60)
4.15
(243.48)
1.97
(115.58)
1.86
(109.13)
1.97
(115.58)
Coag.,
mg/l
Alum
19.6
Alum
19.09
Alum
19.02
Alum
19.24
Alum
19.1
Alum
18.77
Alum
18.46
Alum
18.85
Alum
16.05
Alum
10.48
Alum
11.1
Alum
11.19
Alum
12.8
Alum
13.72
Alum
12.23
Polymer,
mg/l
985-N
0.28
985-N
0.108
985-N
0.116
985-N
0.093
985-N
0.093
985-N
0.074
985-N
0.053
985-N
0.067
985-N
0.054
985-N
0.031
985-N
0.048
985-N
0.053
985-N
0.052
985-N
0.050
985-N
0.076
Coag.,
Ib
1000 gal.
0.163
0.159
0.157
0.160
0.159
0.157
0.154
0.157
0.134
0.087
0.093
0.110
0.107
0.114
0.102
Polymer,
Ib
1000 gal.
0.0024
0.00090
0.00097
0.00078
0.00078
0.00061
0.00044
0.00056
0.00045
0.00026
0.00040
0.00045
0.00043
0.00042
0.00064
B.W.
solids,
Ib
1000 gal.
0.057
0.025
0.032
0.050
0.110
0.051
0.115
0.083
0.065
0.031
0.031
0.011
0.066
0.059
0.017
B.W. vol.
as % of
treated
water
3.79%b
2.89$'
2.32%b
4.14%b
3.11%b
1.84%b
2.72%
2.36%
2.01%
1.77%
1.18%
1 .27%
1 .26%b
2.19%b
4.2S%b
Avg. turb.
Turb. @ time
of sample),
TU
Raw Filter
0.85
0.88
0.94)
0.92
1.0
1.3
1.1
0.86
0.85
0.82
0.80)
0.85
0.79
0.85
0.86)
2.0
0.74)
3.5
(1.9)
2.5
0.17
0.16
(0.15)
0.13
0.14
0.15
0.12
0.23
0.20
0.16
(0.12)
0.44
0.12
0.10
(0.09)
0.09
(0.05)
0.15
(0.06)
0.18
ORF
FibersxlO6/!
Raw Filter








A=1.4:
C=1.8:


A=1.7<
C=29.0
A=1.5
C=2.3
A=1.0
C=1.6









A=BDI
C=.913


A=BD1
C=1.87
A=0.09
C=0.09
A=BDL
C=2.3

NWQL
Amphibole
mg/l
Raw Filter

0.20






0.19


0.26
0.18
0.18


<0.003






0.005


<0.006
< 0.005
< 0.004

UMD
FibersxlO6/!
Raw Filter






























Term
HL
Ft.
HZ©
6.6
6.7
7.0
4.8
6.6
6.9
6.0
5.2
6.8
7.0
6.8
6.7
4.3
1.2
1.5
inal
Turb.
TU
0.08
0.15
0.10
0.10
0,05
0.15
1.0
0.83
0.68
0.80
0.10
0.05
0.11
0.11
0.11
Run
Length, Hrs.
(Time to
Sample)
12.00
15.00
(10.0)
13.92
10.83
13.83
17.17
18.13
19.13
23.68
(7.5)
28.08
21.91
24.03
(4.7)
.67.33
(2S.6)
33.13
(26.9)
24.91

-------
        APPENDIX C-2   (CONTINUED)
Run
No.
57
58
59
60
61
62
63
64
65
66
67
68
69
70
71
Date
6/13
6/13
6/14
6/14
6/17
6/18
6/18
6/19
6/19
6/20
6/20
6/?0
6/21
6/21
6/24
Filter
rate
gpm/ft2
(m3/m2 day)
6.31
(370.21)
5.33
(312.71)
5.65
(331.49)
6.82
(400.13)
6.77
(397.20)
6.84
(401.30)
6.91
(405.41)
6.86
(402.48)
6.87
(403.06)
7.82
(458.80)
6.82
(400.13)
6.89
(404.24)
7.47
(438.27)
6.78
(397.78)
6.86
(402.48)
Coag.,
mg/l
Alum
11.17
Alum
13.2
Alum
13.6
Alum
10.43
Alum
10.25
Alum
10.033
Alum
9.46
Alum
9.35
Alum
14.98
Alum
16.12
Alum
12.29
Alum
11.86
Alum
6.99
Alum
8.175
Alum
7.10
Polymer,
mg/l
98S-N
0.051
985-N
0.075
985-N
0.061
98S-N
0.042
985-N
0.037
985-N
0.064
985-N
0.089
985-N
0.058
985-N
0.084
985-N
0.082
985-N
0.086
985-N
0.082
985-N
0.058
985-N
0.068
985-N
0.079
Coag.,
Ib
1000 gal.
0.093
0.1H
0.113
0.087
0.085
0.084
0.079
0.078
0.125
0.134
0.102
0.099
0.058
0.068
0.059
Polymer,
Ib
1000 gal.
0.00042
0.00062
0.00051
0.00035
0.00031
0.0028
0.00074
0.00048
0.00070
0.00068
0.00072
0.00069
0.00049
0.00057
0.00066
B.W.
solids,
Ib
1000 gal.
0.028
0.029
0.080
0.032
0.058
0.095
0.022
0.021
0.053
0.049
0.014
0.034
0.027
0.027
0.042
B.W. vol.
as % of
treated
water
1 .48%
1.52%
2.91%
1.55%
2.11%
2.20%
1 .97%
1 .46%
3.03%
3.90%
1.80%
2.93%
1.22%
2.14%
1.98%
Avg. turb.
Turb. @ time
of sample),
TU
Raw Filter
.15
2.1)
1.9
1.95
1.7
0.95
0.96)
0.95
0.90
0.95
0.89
0.90
1.92
1.1
1.3
1.1
.70
).66)
0.3
(0.34)
0.10
0.19
0.21
0.20
(0.14)
0.20
0.17
0.18
0.14
0.13
0.13
0.15
0.22
0.20
0.16
(0.20)
ORF
FibersxlO6/!
Raw Filter
A=0,48
C=0,41



A=0.61
C=2.15









\=1.0
^=3.9
A=0,15
C=2.02



A=0.04
C=0.37









A=0.02
C=0.98
NWQL
Amphibole
mg/l
Raw Filter




0.17














<0.01










UMD
FibersxlO6/!
Raw Filter
33.25



10.64









6.03
0.07



0.41









0.825
Tern
HL
Ft.
H2O
6.7
8.0
8.0
6.6
8.0
8.0
8.0
8.0
8.0
8.0
8.0
8.0
8.0
8.0
8.0
tinal
Turb.
TU
0.99
0.10
0.09
0.20
0.20
0.35
0.14
0.11
0.10
0.13
0.12
0.17
0.16
0.27
3.10
Run
Length, Mrs.
(Time to
Sample)
. 15.58
(13.5)
12.90
12.05
9.83
11.57
(4.0)
12.68
11.02
10.80
7.58
6.32
7.47
7.87
10.20
10.64
12.75
(4.3)
f-J
oo

-------
APPENDIX C-2   (CONTINUED)
Run
No.
72
73
74
Cloqu
75
1725
76
Lakew
77
78
79
80
81
82
83
84
Date
6/25
6/25
6/25
t watt
6/26
.p.m.
6/28
ood w
7/2
7/3
7/4
7/8
7/9
Efflu
Efflu
7/10
Filter
rate
gpm/ft2
(m3/m2 day)
6.17
(361.99)
6.64
(389.57)
6.91
(405.41)
r.
4.08
(239.37)
nixer in mixing
1.79
(105.02)
iter. Tri-Media.
3.86
(226.47)
3.15
(184.81)
3.75
(220.01)
4.06
(238.20)
4.77
(279.86)
nt turbidity to
nt turbidity to
4.78
(280.44)
Coag.,
mg/l
Alum
15.50
Alum
11.81
AJum
17.25

AJum
26.48
chamber.
Alum
26.89

Alum
12.03
Alum
14.66
Alum
12.09
Alum
11.15
Alum
10.38
> high.
> high.
Alum
16.23
Polymer,
mg/l
985-N
0.086
985-N
0.083
985-N
0.050

985-N
0.110

98S-N
0.159

985-N
0.048
985-N
0.079
985-N
0.052
985-N
0.040
985-N
0.032


985-N
0.042
Coag.,
Ib
1000 gal.
0.129
0.098
0.144

0.221

0.224

0.108
0.122
0.101
0.093
0.087


0.135
Polymer,
Ib
1000 gal.
0.00072
0.00069
0.00041

0.00092

0.0013

0.00040
0.00066
0.00043
0.00033
0.00027


0.00035
B.W.
solids,
Ib
1000 gal.
0.025
0.031
0.063

0.066

0.029

0.0010
-
-
—
0.027


0.027
B.W. vol.
as % of
treated
water
1.80%
2.76%
3.31%

7.36% b

12.21%

2.01%
2.50%b
2.97%
_
4.33% b


2.63%
Avg. turb.
Turb. @ time
of sample),
TU
Raw Filter
0.64
0.66
0.66

3.48

2.9
(2.9)

0.77
0.75
0.69)
0.62
0.67
0.65


1.51
0.12
0.14
0.21

0.11

0.07
(0.06)

0.10
0.10
(0.12)
0.11
0.09
0.11


0.10
ORF
FibersxlO6/!
Raw Filter






A=0.91
C=3.3!


A=0.5<
A=3.5'i












A=BDL
C=0.52


A=0.02
C=0.5






NWQL
Amphibole
mg/l
Raw Filter






0.11


0.07












<0.005


C0.003






UMD
FibersxlO6/!
Raw Filter






5.54


2.99












0.53


0.16






Tern
HL
Ft.
HS.0.
8,0'
8.0
7.2

1.7

1.5

5.2
7.5
8.0
8.0
7.4


8.0
linal
Turb.
IU_
0,23'
0.27
1.50

0.25

0.13

0.10
0.06
0.05
0.09
0.15


0.06
Run
Length, Hrs.
(Time to
Sample)
8,63'
8.67
8.78

4.17

9.35
(4.9)

10.75
23.73
(3.3)
20.09
14.77
10.08


11.21

-------
APPENDIX C-2   (CONTINUED)
Run
No.
85
86
87
88
89
90
91
92
55 gal
93
94
95
96
97
98
Date
7/10
7/11
7/11
7/12
7/12
7/15
7/15
7/16
Hash
7/17
7/18
7/18
7/19
7/19
7/22
Filter
rate
gpm/ft2
(m3/m2 day)
4.85
(284.55)
4.91
(288.07)
4.94
(289.83)
4.86
(285.14)
4.79
(281.03)
4.22
(247.59)
3.23
(189.50)
4.30
(252.28)
nix tanks with
3.70
(217.08)
3.89
(228.23)
4.52
(265.19)
3.75
(220.01)
3.51
(205.93)
3.68
(215.91)
Coag.,
mg/l
Alum
14.84
Alum
9.52
Alum
9.37
Alum
9.69
Alum
11.26
Alum
13.59
Alum
16.54
Alum
10.82
one 1725
Alum
12.55
Alum
10.20
Alum
5.54
Alum
6.98
Alum
9.08
Alum
10.72
Polymer,
mg/l
985-N
0.045
985-N
0.040
985-N
0.045
985-N
0.048
985-N
0.058
985-N
0.059
985-N
0.069
985-N
0.042
rpm mixer
985-N
0.046
985-N
0.052
985-N
0.042
985-N
0.060
985-N
0.060
985-N
0.036
Coag.,
Ib
1000 gal.
0.124
0.070
0.078
0.081
0.094
0.113
0.138
0.090
in each in
0.105
0.085
0.046
0.058
0.076
0.089
Polymer,
Ib
1000 gal.
0.00037
0.00033
0.00038
0.00040
0.00048
0.00050
0.00057
0.00035
tailed ahead
0.00038
0.00044
0.00035
0.00050
0.00050
0.00030
B.W.
solids,
Ib
1000 gal.
0.020
0.027
0.020
0.016
0.019
0.020
0.019
0.020
of floe, chan
0.024
0.033
0.017
0.038
0.026
0.019
B.W. vol.
as % of
treated
water
3.60%
4.19%
4.01%
4.41%
4.64%
4.53%
4.66%
4.51%
, Alum ad
3.58%
3.02%
2.68%b
5.39%b
3.56%b
2.38%
Avg. turb.
(Turb. @ time
of sample),
TU
Raw Filter
0.86
1.9
1.46
1.2
0.88
0.70
0.67
0.67
0.09
0.08
0.13
0.12
0.09
0.07
0.06
0.08
led to first tan
0.72
0.76
0.85
0.85
;o.9o)
0.70
0.62
0.07
0.09
0.59
0.31
(0.16)
0.29
0.08
ORF
FibersxlO6/!
Raw Filter












A=o.s:
C=0.3!














A=0.02
C=0.04


NWQL
Amphibole
mg/l
Raw Filter












0.13














<0.005


UMD
FibersxlO*/!
Raw Filter












266.0














0.95


Terr
HL
Ft.
HjO
8.6
8.0
8.0
8.0
8.0
8.0
8.0
8.0

8.0
8.0
3.7
3.1
4.7
8.0
ninal
Turb.
TU.,-
0.09
0.07
0.13
0.08
0.11
0.06
0.06
0.05

0.07
0.09
0.58
0.60
0.19
0.12
Run
Length, Hrs.
(Time to
Sample)
9.9 i
8.82
9.62
7.97
6.86
8.04
9.60
8.11

11.92
12.75
13.75
7.83
(2.1)
13.33
16.74

-------
APPENDIX C-2   (CONTINUED)
Run
No.
99
100
101
102
103
104
105
CloqiM
106
Lakew
107
108
109
110
111
Date
7/23
7/24
7/25
7/25
7/26
7/30
7/30
t wate
7/31
aod w
8/1
8/2
8/6
8/7
8/8
Filter
rate
gpm/ft2
(m3/m2 day)
4.41
(258.74)
4.23
(248.71)
4.55
(266.95)
4.43
(259.91)
•1.32
(253.45)
4.32
(253.45)
4.41
(258.74)

4.17
(244.65)
ter
3.20
(187.74)
4.01
(235.27)
3.38
(198.31)
4.07
(238.79)
4.47
(232.26)
Coag.,
mg/l
Alum
8.77
Alum
10.80
Alum
9.99
Alum
10.84
Alum
10.89
Alum
11.00
Alum
10.97

Alum
20.97

Alum
16.19
Alum
13.11
Alum
15.10
Alum
13.63
Alum
11.73
Polymer,
mg/l
985-N
0.029
985-N
0.031
985-N
0.013
985-N
0.0014
985-N
0.0076
985-N
0.0016
985-N
0.029

985-N
0.122

985-N
0.040
985-N
0.032
985-N
0.043
985-N
0.031
985-N
0.034
Coag.,
1000 gal.
0.073
0.090
0.083
0.090
0.091
0.092
0.091

0.175

0.135
0.109
0.129
0.114
0.098
Polymer,
1000 gal.
0.00025
0.00026
0.00011
0,00001 2
0.000063
0.000013
0.00024

0.0010

0.00033
0.00026
0.00036
0.00026
0.00028
B.W.
solids,
Ibs
1000 gal.
0.023
0.057
0.033
0.069
0.014
0.023
0.018

0.018

0.041
0.032
0.069
0.067
0.019
B.W. vol.
as % of
treated
water
1.96%
2.05%
2.30%
1.90%
2.03%
2.16%
1.46%

10.00%

1.69%
1.59%
1.19%
1.59%
1.40%
Avg. turb.
Turb. @ time
of sample),
TU
Raw Filter
0.60
0.57)
0.75
0.75
0.66)
0.73
0.60
0.73
(0.76)
0.75
(0.69)

3.68
(4.00)

0.90
(0.87)
1.11
0.62
[0.58)
0.66
0.92
(0.68)
0.12
(0.11)
0.09
0.14
(0.09)
0.13
0.13
0.15
(0.40)
0.10
(0.09)

0.06
(0.06)

0.08
(0.08)
0.08
0.10
(0.06)
0.12
0.11
(0.08)
ORF
FibersxlO6/!
Raw Filter
A=O,S.
C=0.09

A=0.11
C=1.4;



A=O.I;
C=0.11

A=O.S:
C=0.22

A=0.22
C=0.15

A=0.6
C=0.3

\=0.06
C=0.09
A=BDL
C=0.20

A=BD1
C=0.15



A=BDL
C=BDL

A=BDL
C=BDL

A=BDL
C=BDL

A=BDL
C=BDL

A=BDL
C=0.09
NWQL
Amphibole
mg/I
Raw Filter
0,09

0.04



0.06

0.10

0.08

0.09

O.OS
<0,004

«.005



fD.OOS

(0.003

<0.003

<0.003

<0.003
UMD
FibersxlO6/!
Raw Filter
26.0

60.5


0.10
26.6

106.6

30.0

10.2

15.1
0.23

0.43


0.02
0.10

0.64

0.14

0.19

0.16
Term
HL
Ft.
H2O
8,0
8.0
8.0
4.5
4.8
3.4
5.5

2.2

5.0
8.0
8.0
5.1
8.0
inal
Turb.
TU
0.09
0.08
0.10
0.36
0.45
0.40
0.36

0.05

oas
0.07
0.17
0.48
0.12
Run
Length, Hrs.
(Time to
Sample)
17.95
(7.9)
18.25
14.68
(13.1)
19.75
19.00
17.87
(17.7)
25.83
(4.3)

4.00
(2.4)

30.83
(17.9)
24.63
34.26
(23.5)
22.50
25.55
(9.9)

-------
APPENDIX C-2   (CONTINUED)
Run
No.
112
113
114
115
Alum
116



Alum
117

Alum
118



119



120



Date
8/9
8/13
8/1 S
8/16
nd ani
8/19



ddecl
8/19

nd ani
8/20



8/23



8/23



Filler
rate
gpm/ft2
(m3/m2 day)
4.18
(245.24)
3.88
(227.64)
1.97
(115.58)
4.25
(249.35)
onic polymer j
3.88
(227.64)


o first tank, ca'
3.95
(231.75)
mic polymer a
4.01
(235.27)


4.24
(248.76)


3.75
(220.01)


Coag.,
mg/l
Alum
12.76
Alum
15.30
Alum
18.93
Alum
14.67
dded to f
Alum
15.32


ionic pol)
Alum
16.08
ided to ft
Alum
15.43


Alum
14.24


Alum
12.90


Polymer,
mg/l
985-N
0.041
985-N
0.041
985-N
0.042
985-N
0.030
rst tank, ca
A-23
0.385
Catfloc B
0.602
mer added
Catfloc B
0.533
st tank, cat
A-23
0.648
Catfloc B
0.562
A-23
0.281
985-N
0.042
A-23
0.311
985-N
0.044
Coag.,
Ibs.
1000 gal.
0.106
0.128
0.158
0.122
ionic polj

0.128


:o second

0.134
onic or n

0.129



0.119



0.108


Polymer,
Ibs.
1000 gal.
0.00034
0.00034
0.00035
0.00025
mer added t

0.00032

0.0050
tank.

0.0044
mionic poly:

0.0054

0.0047

0.0023

0.00035

0.0026

0.00037
B.W.
solids,
Ibs
1000 gal.
0.026
0.032
0.078
0.095
> second tan)

0.090




0.073
ler added to

0.130



0.124



0.018


B.W. vol.
as %of
treated
water
1.80%
1 .82%
1.37%
1 .58%


2.23%




2.22%
second tan

2.06%



1 .70%



5.12%"


Avg. turb.
Turb. @ time
of sample),
TU
Raw Filter
1.23
0.64
0.60)
0.65
0.71)
0.77

0.57




0.71


0.82
0.84)


0.59
0.63)


0.53



0.18
0.07
(0.06)
0.05
(0.04)
0.09

0.07




0.06


0.11
(0.08)


0.08
(0.08)


0.09



ORF
FibersxlO6/!
Raw Filter

A=O.I;
C=0.2
A=0.0!
c=o.n










\=0.30
C=0.72


\=0.72
:=0.44







A=BD1
C=1.4
A=0.02
C=0.22










A=0.02
C=2.1


A=BDL
C=0.28






NWQL
Amphibole
mg/l
Raw Filter

0.06
0.06










0.02



0.04








< 0.003
<0.003










<0.003



<0.003







UMD
FibersxlO6/!
Raw Filter

20.0
8.98










25.3



17.0








0.37
0.43










0.15



0.26







Tern
HL
Ft.
H2°,
8.0
8.0
8.0
8.0

3.5




1.7


7.4



8.0



1.4



linal
Turb.
TU
O.fS
0.06
0.04
0.35

0.39




0.23


0.20



0.06



0.11



Run
Length, Mrs.
(Time to
Sample)
20.51
22.55
(22.3)
58.63
(45.7)
22.68

19.25




14.25


20.17
(1.9)


21.83
(18.5)


8.67




-------
APPENDIX C-2   (CONTINUED)
Run
No.
3 In-I
121

122

123

Anion
124



125



126



127



128




Alum
129

Date
ne Kir
8/27

8/28

8/29

c poly
8/30



9/3



9/4



9/5



9/6




dded
9/9

Filter
rate
gpm/f|2
'm3/m2 day)
ecs mixers inst
4.32
(253.45)
4.33
(254.04)
3.79
(222.36)
ner added ahea
3.92
(229.99)


4.14
(242.89)


4.00
(234.68)


4.33
(254.04)


4.12
(241.72)



head of first m
6,16
(361.41)
Coag.,
mg/l
lied, Alui
Alum
10.13
Alum
11.58
Alum
13.13
1 of first
Alum
14.93


Alum
13.92


Alum
16.95


Alum
13.86


Alum
13.38



xer, poly
Alum
15.59
Polymer,
mg/l
added atu
985-N
0.041
985-N
0.049
985-N
0.065
nixer, Alun
A-23
0.160
985-N
0.064
C-31
0.437
A-23
0.133
C-31
0.567
A-23
0.158
985-N
0.040
A-23
0.149
985-N
0.060
A-23
0.124

ler added a
985-N
0.051
Coag.,
Ihs.
1000 gal.
ad of first

0.084

0.097

0.110
added ah

0.125



0.116



0.141



0.116



0.112



lead of s

0.130
Polymer,
Ibs.
1000 gal.
mixer, poly

0.00035

0.00040

0.00055
ead of secon

0.0013

0.00053

0.0036

0.0011

0.0047

0.0013

0.00034

0.0012

0.00050

0.0010

cond mixer.

0.00042
B.W.
solids,
Ibs
1000 gal.
ner added ah

0.025

0.031

0.034
1 mixer, non

0.044



0.052



0.107



0.011



0.017





0.039
B.W. vol.
as % of
treated
water
ad of seci

1 .74%

1.69%

1.55%
onic or ca

1.63%



2.16%



2.92%



2.63%



2.39%





2.08%
Avg. turb.
Turb. @ time
of sample),
TU
Raw Filter
d mi?
0.46

0.47
0.43)
0.50

onic |
0.69
0.39)


0.62



0.66
(0.71)


0.68



0.51
(0.51)




0.51

ter.
0.07

0.06
(0.04)
0.06

olymer
0.07
(0.05)


0.09



0.08
(0.06)


0.08



0.08
(0.10)




0.09

ORF
FibersxlO6/!
*aw Filter

A

A=0.3<
C=0.4f



A=0.7f
C=0.33






A=1.61
C=0.3






A=0.7;
C=0.39

A=1.4<
C=0.28






A=BDL
C=0.04



A =0.02
C=0.30






A=BDL
C=BDL






A-BDL
C=0.37
EPA C
9 A=0.0
) C=0.1



NWQL
Amphibole
mg/l
Raw Filter



0.09




0.07







0.10







0.07

ncinna
36
8






< 0.003




<0.003







<0.003







<0.003







UMD
Fibersxlo6/l
Raw Filter






10.4 0.11




17.8







30.3







13.6











0.18







0.33







0.17







Term
HL
Ft.
H20

5.5

6.2

5.8


4.8



3.2



2.8



3.3



8.0





7.8

inal
Turb.
TU

0.32

0.30

0.33


0.34



1.0



0.65



0.34



0.39





0.58

Run
Length, Hrs.
(Time to
Sample)

20.57

19.92
(3.7)
24.22


19.55
(3.7)


16.28



17.82
(9.6)


14.33



21.00
(8.7)




13.00



-------
APPENDIX C-2   (CONTINUED)
Run
No.
130

131
132

133

134

3 addi
135

136

137

55 gal.
138



139



Date
9/10

9/10
9/11

9/11

9/11

ional ]
9/12

9/13

9/13

Hash
9/16



9/17



Filter
rate
gpm/ft2
(m3/m2 day)
6.09
(357.30)
6.18
(362.58)
5.97
(350.26)
5.98
(350.85)
4.12
(241.72)
i-Line Kinecs i
4.02
(235.85)
4.05
(237.61)
3.98
(233.51)
lix tanks instal
4.29
(251.69)


4.35
(255.21)


Coag.,
mg/l
Alum
12.56
Alum
13.36
Alum
24.17
Alum
24.56
Alum
16.63
lixers inst
Alum
18.97
Alum
37.86
Alum
19.66
ed, Alum
Alum
14.62


Alum
14.70


Polymer,
mg/l
985-N
0.085
985-N
0.053
985-N
0.051
985-N
0.077
C-31
0.586
lied, Alum
C-31
0.628
C-31
0.793
C-31
0.790
and anionic
985-N
0.065
A-23
0.126
C-31
0.622
A-23
0.123
Coag.,
Ihs.
1000 gal.

0.105
0.111

0.202

0.205

0.139
added ah*

0.158

0.316

0.164
polymer

0.122



0.123


Polymer,
Ibs.
1000 gal.

0.00071
0.00044

0.00042

0.00065

0.0049
ad of first p

0.0053

0.0066

0.0066
idded to firs

0.00054

0.0010

0.0052

0.0010
B.W.
solids,
Ibs
1000 gal.

0.050
0.031

0.037

0.034

0.061
ir, polymer i

0.061

0.086

0.051
tank, cation

0.028



0.022


B.W. vol.
as % of
treated
water

2.40%
2.35%
fo
2.64%

3.85%

3.21%
dded ahea

4.62%

7.89%

4.92%
c or noni<

1.61%



2.01%


Avg. turb.
Turb. @ time
of sample),
TU
Raw Filter
0.51

0.58
0.64)
0.83

0.60
0.45)
0.47

007

0.07
(0.06)
0.11

0.16
(0.07)
0.07

of second pai
0.42

0.47

0.44
0.40)
0.07

0.06

0.07
(0.05)
nic polymer at
0.42
0.37)


0.51
0.47)


0.06
(0.04)


0.07
(0.05)


ORF
FibersxlO6/!
Raw Filter


^=0.6
2=0.5


4=0.3
>0.3







^=0.02
>0.06

\=0.9
>0.1


^=0.2
C=0.1




A=BDL
C=0.5


A =0.02
C=0.3







A=0.02
C=0.1

A=0.02
C=0.3


A=BDL
C=0.1


NWQL
Amphibole
mg/l
Raw Filter


0.05


0.06








0.09


0.08



0.06





•C0.003


<0.003








<0.003


-C0.003



<0.003



UMD
FibersxlO6/!
Raw Filter





13.0








30.0


20.3



12.8





0.27


0.30








0.24


0.51



0.64



Term
HL
Ft.
H2O
8,0

8.0
5.2

4.6

3.1


2.8

2.1

2.6


8.0



6.8



inal
Turb.
TU
0,08

0.23
0.20

0.43

9.0


0.25

0.55

0.21


0.06



B.24



Run
Length, Hrs.
(Time to
Sample)
11.06

10.05
(2.8)
9.25)

7.40
(4.3)
12.62


8.97

5.22

9.6
(5.3)

21.84
(1.9)


21.41
(1.5)



-------
APPENDIX C-2    (CONTINUED)
Run
No.
Sedim
140






Date
ntatio:
9/19






Filter
rate
gpm/ft2
(m3/m2 day)
tube settlers i
3.85
(225.88)





Coag.,
mg/l
istalled. f
Alum
14.02





Polymer,
mg/l
lum added
985-N
0.066





Coag.,
Ibs.
1000 gal.
o first tai

0.117





Polymer,
Ibs.
1000 gal.
k, polymer ;

0.00055





B.W.
solids,
Ibs
1000 gal.
dded to seco

From Sed.
0.0065
From B.W.
0.014
Total Solids
0.020
B.W. vol.
as % of
treated
water
nd tank.

1.45%





Avg. turb.
Turb. @ time
of sample),
TU
Raw Filter

0.47
(0.52)






0.06
(0.06)





ORF
Fibersxio6/!
Raw Filter

A=0.6
C=0.09






A=BDL
C=0.3





NWQL
Amphibole
mg/l
Raw 1 Filter

0.10







0.003






UMD
FibersxlO6/!
Raw Filter

13.8







0.33






Term
HL
Ft.
H2O

8.0






inal
Turb.
TU

0.10






Run
Length, Hrs.
(Time to
Sample)

31.98
(1.8)





 a B.W. volume was not measured in Runs 1-35.
 b Runs did not reach terminal HL or turbidity.
 c A=amphibole, C=chrysotile

-------
APPENDIX C-3   VACUUM DIATOMACEOUS EARTH FILTRATION (BIF) SUMMARY OF INDIVIDUAL RUNS
Run
No.
One
1-T
J.M.
2-T
E.P.
3-T
4-T
J.M.
5-T
6-T
7-T
M.
8-T
J.M.
9-T
10-T
Dical
11-T
Date
tepp
4/24
:elite
4/26
TV-Si
4/29
4/30
Hyflo
5/2
Run
Run
•iyflo
5/3
Celite
5/6
5/7
teSi
5/8
Filter
rate
gpm/ft2
(m3/m2 day)
•ecoat, E.P. FV
0.843
(49.46)
512 to precoa
0.913
(53.57)
to precoat.
1.015
(59.55)
0.895
(52.51)
Super Cel to r.
0.915
(53.68)
ailed due to h
ailed due to hi
Super Cel & ai
0.927
(54.39)
512 & anionic
1.019
(59.785)
1.035
(60.72)
eed flow & ani
1.065
(62.48)
Precoat,
Ibs./ft2
r-50 to pi
FW-50
0.1

512
0.1

FW-50
0.1
FW-50
0.1
•ecoat.
Super Cel
0.15
3hHL.
ShHL.
ionic pol
3uper Cel
0.1
polymer
512
0.1
512
0.1
>nic poly
Speed
flow
0.1
Precoat,
Ibs.
1OOO gal.
:coat, J.M
0X155

0.059

0.071
0.061

0.082


ymei to pr
0.093
to precoat
0.084
0.070
ner to pre
0.104
Polymer or
coag. in
precoat,
g./g. of D.E.
Celite512 to
-

-

-
-

-


•coat.
A-23
0.00005

A-23
0.00003
A-23
0.00003
oat
A-23
0.00003
Polymer or
coag. in
precoat,
Ibs
1000 gal.
body feed.
-

-

-
-

-



A-23
4.67xlO-6

A-23
2.51xlO-6
A-23
2.1X10'6

A-23
3.13X10'6
Other
chem. in
precoat,
Ibs
1000 gal.


















Body
feed,
mg/1

89.09

82.30

73.99
67.01

65.54



64.68

48.05
57.90

56.27
Body
feed,
Ib.
1000 gal.

512
0.743

512
0.686

512
0.617
512
0.559

512
0.547



512
0.539

512
0.401
512
0.483

512
0.469
B.W. solids,
Ibs
1000 gal.
(B.W. vol. as
% of treated
water)"

0.798

0.746

0.688
0.620

0.628



0.633

0.485
0.553

0.574
Avg. turb.
(Turb. @ time
of sample),
TU
Raw Filter

0.98

0.85

0.81
0.79

0.65



0.69

0.69
0.72
(0.76)

0.68

0.61

0.65

0.65
0.33

0.18



0.16

0.19
0.19
(0.18)

0.15
ORF
FibersxlO6/!
Raw Filter















\=0.52:

















A=BDL
C=1.43


NWQL
Amphibole
mg/1
Raw Filter















0.06

















< 0.01


UMD
FibersxlO6/!
Raw Filter




































Tern"
HL
Ft
H20

16.9

15.3

16.2
17.0

16.4



11.6

16.8
16.3

16.8
jnal
Turb.
TU

0.45

2.S

0.83
0.33

0.15



0.15

0.18
0.24

0 12
Run
Length, Hrs
(Time to
Sample)

36.00

30.75

23.08
30.50

33.50



19.50

19.50
22.92
(2.2)

15.00

-------
APPENDIX C-3   (CONTINUED)
Run
No. Date
12-T


13-T


14-T


Non
1


Anio
Ci-l
•~j 2


3


4


E.P.
5




5/9


5/9


5/10


>mc i
5/13


lie p<

5/13


5/14


5/14


FW-6
5/14




Filter
rate
gpm /ft 2
(m3/m2 day)
0.979
(57.44)

0.983
(57.67)

i.012
(59.37)

olymer to prec
1.17
(68.64)

lymer to prec<

0.954
(55.97)

1.057
(62.01)

1.007
(59.08)

Si Dicalite Spe
1.056
(61.96)



Precoat,
Ibs./ft2
Speed
flow
0.1S
Speed
flow
0.15
Speed
flow
0.15
oat, Dica
Speed
flow
0.15
at.

Speed
flow
0.15
Speed
flow
0.15
Speed
flow
0.15
dflow&
FW-6
0.1
Speed
flow
0.05
Precoat,
Ibs.
1 000 gaf.


0.138


0.199


0.127
ite Speedf


0.227




0.520


0.728


0.406
mionic po

0.557


0.278
Polymer or
coag. in
precoat,
g./g. of D.E.
A-23
0.00003

A-23
0.00003

A-23
0.00003

ow to body f
98S-N
0.00003



A-23
0.00003

A-23
0.00003

A-23
0.00003

ymer to precc
A-23
0.00003



Polymer or
coag. in
precoat,
Ibs
1000 gal.
^-23
4.1xlO'6

A-23
5.96X10'6

A-23
3.8xlO-6

-A.
98S-N
6.797xlO-f



A-23
1. 561X10'5

A-23
2.183xlO-5

A-23
1.217xlO-S

at, E.P. FW-
A-23
2.5x10-5



Other
chem. in
precoat,
Ibs
1000 gal.
























p to body f





Body
feed,
mg/1

61.25


60.72


59.25



49.7




59.3


56.71


59.51

;ed.

56.75



Body
feed,
Ib.
1000 gal.
512
0.511

512
0.506

512
0.494


Speedflow
0.414



Speedflow
0.524

Speedflow
0.473

Speedflow
0.496


FW-6
0.473



B.W. solids,
Ibs
1000 gal.
(B.W. vol. as
% of treated
water)3
0.649


0.705


0.621



0.641




1.044


1.201


0.902



1.309




Avg. turb.
[Turb. @ time
of sample),
TU
Raw Filter
0.85
(0.65)

0.75


0.70



0.92




0.96


0.90


0.74



0.84




0.15
(0.14)

0.16


0.18



0.35




0.23


0.20


0,22



0,28




ORF
FibersxlO6/!
Raw Filter
A=0.87
:=1.78




























)A=BDl
C=BDL




























NWQL
Amphibole
mg/1
Raw Filter
0.22





























0.003





























UMD
FibersxlO6/!
Raw Filter




























































Term
HL
Ft.
H2O
16.7


10.1


15.0



16.8




17.0


17.0


17.0



16.7




inal
Turb.
TU
0.10


0.18


0.23



0.45




0.18


0.23


0.22



0.40




Run
Length, Mrs.
(Time to
Sample)
18.47
(14.5)

12.83


19.SO



9.42




4.73


3.25


6.12



2.83





-------
APPENDIX C-3   (CONTINUED)
Run
No. Date
F..P.
6

E.P.
7



E.P.
8



Catic
9



E.P.
10



J.M.
1 1




FW-6
5/14

W~5<
5/15



FW-S
5/16



me p
5/17



l-W-5
5/20



Hyfk
5/22




Filter
rate
gpm/f|2
(m3/m2 day)
to precoat.
0.988
(57.97)
& E.P. FW-6 t
0.968
(56.79)


)& E.P. FW-6
0.948
(55.62)


>lymer to prec
0.948
(55.62)


)& J.M. Celite
0.864
(50.69)


Super Cel & J
0.953
(55 91)



Precoat,
Ibs./ft2

FW-6
0.15
> precoat
FW-50
0.1
FW-6
0.05
& aniomc
FW-50
0.1
FW-6
O.OS
>at.
FW-50
0.1
FW-6
O.OS
5 1 2 & ca
FW-50
0.1
512
0.05
M. Celite
Super Cel
0.1
512
0.05

Precoat,
Ibs.
10OO gal.


0.258


0.085

0.043
polymer t

0.079

0.039


0.061

0.031
ionic polj

0.060

0.030
512 & cat

0.062

0.031

Polymer or
coag. in
precoat,
g./g. of D.E.








) precoat.
A-23
0.00001



C-31
0.00005


mer to precoa
C-31
0.0005


onic polymer
C-31
0.0006



Polymer or
coag. in
precoat,
Ibs
1000 gal.









A-23
1.18xlO"6



C-31
4.6X10-6


, J.M. Celite
C-31
4.47xlO'5


o precoat.
C-31
5.6x10-5



Other
chem. in
precoat,
Ibs
1000 gal.


















512 to bo'










Body
feed,
mg/l


60.7


61.93




66.05




63.27


y feed

69.4



45.24




Body
feed,
Ib.
1000 gal.

FW-6
0.506

FW-6
0.517



FW-6
0.550



FW-6
0.528



512
0.579



512
0.377



B.W. solids,
Ibs
1000 gal.
(B.W. vol. as
% of treated
water)3

0.764


0.644




0.668




0.620




0.668




0.471




Avg. turb.
(Turb. @ time
of sample),
TU
Raw Filter

2.2


1.3




0.95
(0.80)



0.90




0.93




0.88
0.94)




0.60


0.3




0.22
(0.18)



0.30




0.275




0.30
(0.36)



ORF
FibersxlO6/!
Raw Filter









A=2.61
C=1.35



























A=0.565
C=0.652


















NWQL
Amphibole
mg/l
Raw Filter









0.14














0.2













0.006














< 0.03




UMD
FibersxlO6/!
Raw Filter


























































Terr
HL
Ft.
H2O

12.3


16.0




17.0




16.0




17.0




16.9




ninal
Turb.
TU

1.25


0.30




0.26




0.35




0.23




0.20




Run
Length, Hrs.
(Time to
Sample)

9.80


20.25




23.05
(12.0)



28.67




31.61




28.05
(15.3)




-------
APPENDIX C-3   (CONTINUED)
Run
No.
J.M.
12
Dica
13
Dica
14
E.P.
15
16
J.M.
17
Date
Celit
5/22
ite S|
5/23
ite S;
5/24
FW-5
5/28
S/28
Celitf
5/30
Filter
rate
gpm/ft2
(m3/m2 day)
: 5 1 2 & DicalH
0.904
(53.04)
eedflow & J.M
0.895
(52.51)
eedflow & E.I
0.945
(55.44)
1 & E.P. FW-2
0.877
(51.45)
0.844
(49.52)
512 &Dicalit
0.843
(49.46)
Pre coat,
Ibs./ft2
e Speedfl
512
0.1
Speed
Flow
0.05
Celite 5
Speed
flow
0.1
512
0.05
FW-60 i
Speed
flow
0.1
FW-60
0.05
& cationi
FW-50
0.05
FW-2
0.1
FW-50
0.1
FW-2
0.05
Speedflc
512
L 0-I
Speedfloi
0.05
Precoat,
Ibs.
10OO gal.
>w &. catic
0.099
0.049
2 & catio
0.070
0.035
cationic |
0.184
0.092
polymer
0.078
0.155
0.113
0.056
w & catioi
0.074
0.037
Polymer or
coag. in
precoat,
g./g. of D.E.
lie polymer t
C-31
0.0006
ic polymer tc
573-C
0.0006
olymer to pre
C-31
0.0005
o precoat.
573-C
0,0008
573-C
0.0005
ic polymer to
573-C
0.0007
Polymer or
coag. in
precoat,
Ibs
1000 gal.
precoat.
C-31
8.88xlO-5
precoat.
S73-C
6.32xlO-5
coat.
C-31
0.00014

573-C
0.00017
573-C
8.46X10-5
precoat, E.P
573-C
5.57x10-5
Other
chem. in
precoat,
Ibs
1000 gal.









FW-12to

Body
feed,
mg/1

82.26

93.3

84.55

52.42
162.58
body ft
183.7
Body
feed,
Ib.
1000 gal.

512
0.686

512
0.778

512
0.705

512
0.437
512
1.356
ed.
FW-12
1.532
B.W. solids,
Ibs
1000 gal.
(B.W. vol. as
% of treated
water)3

0.834

0.884

0.981

0.670
1.525

1.644
Avg. turb.
Turb. @ time
of sample),
TU
Raw Filter

0.93

0.98

1.25

0.83
0.9

0.82
;o.so)

0.30

0.30

0.35

0.75
0.35

0.23
(0.33)
ORF
FibersxlO6/!
Raw Filter










\=1A3
C=1.83










A=0.739
C=1.83
NWQL
Amphibole
mg/1
Raw Filter










0.19










< 0.02
UMD
FibersxlO6/!
Raw Filter






















Term
HL
Ft.
H2O

11.9

17.0

5.6

16.9
16.2

16.9
inal
Turb.
TU

1.6

0.35

0.40

0.56
0.33

0.23
Run
Length, Hrs.
(Time to
Sample)

18.67

26.50

9.58

12.25
17.50

26.S8

-------
APPENDIX C-3   (CONTINUED)
Run
No.
Two
18




19




Dica
20




21



22




23




Date
itep
5/30




6/4




iteSi
6/6




6/7



6/10




6/11




Filter
rate
gpm/ft2
(m3/m2 day)
recoat, J.M. C
0.834
(48.93)



0.807
(47.35)



eedflow to bo
0.871
(51.10)



0.918
(53.86)



0.900
(52.80)



0.853
(50.05)



Precoat,
Ibs./ft2
lite 503
503
0.1
Speed
flow
0.05
503
0.1
Speed
flow
o.os
y feed.
503
0.1
Speed
flow
0.05
503
0.1
Speed
flow
0.05
503
0.1
Speed
flow
0.05
503
0.1
Speed
flow
0.05
Precoat,
Ibs.
1000 gal.
j, cationic

0.056


0.028

0.047


0.024


0.043


0.022
0.071


0.035

0.144


0.072

0.221


0.110
Polymer or
coag. in
precoat,
g./g. of D.E.
x>lymer to fir
S73-C
0.0005

573-C
0.0007
573-C
0.0005

573-C
0.0007

573-C
0.0005

573-C
0.0007
573-C
0.0005

573-C
0.0007
573-C
0.00005



573-C
0.0005



Polymer or
coag. in
precoat,
Ibs
1000 gal.
it step, Dica]
573-C
4.78X10-5



S73-C
4.03x10-5




573-C
3.66x10-5



573-C
6.03x10-5



573-C
1.08x10-5



573-C
0.00017



Other
chem. in
precoat,
Ibs
1000 gal.
te Speedfl






























Body
feed,
mg/1
iw & a

62.4




109.86





168.46



297.93




86.05




149.8



Body
feed.
Ib.
1000 gal.
ionic polyi
FW-12
0.520



FW-12
0.916




Speedflow
1.405



Speedflow
2.485



Speedflow
0.718



Speedflow
1.249



B.W. solids,
Ibs
1000 gal.
(B.W. vol. as
% of treated
water)3
ler to second j
0.605




0.988





1.470




2.591



0.934




1.581




Avg. turb.
(Turb. @ time
of sample),
TU
Raw Filter
lep.
0.85




0.8
(0.86




0.8
(0.74



3.8



4.5




4.0





0.2




0.15
(0.15)




0.20
(0.20)



0.40



0.70




0.67




ORF
FibersxlO6/!
Raw Filter






A=1.74
C=2.91




A=1.5
C-2.3























A=0.217
C=0.087




A=0.08
C=0.7

















NWQL
Amphibole
mg/1
Raw Filter






0.26





0.18
























0.004





0.004


















UMD
FibersxlO6/!
Raw Filter






























































Terrr
HL
Ft.
H2O

9.0




16.8





17.0




17.0



17.0




17.0




inal
Turb.
TU

0.24




0.15





0.60




0.31



0.50




0.54




Run
Length, Hrs.
(Time to
Sample)

35.50




43.50
(28.1)




44.33
(31.4)



25.58



12.83




8.75





-------
APPENDIX C-3   (CONTINUED)
Run
No.
24
J.M.
25
J.M.
26
27
E.P.
28
J.M.
29
Dica
30
Date
6/11
Celitt
6/11
"elitl
6/12
Run
TV-5
6/13
"elite
6/14
te S|
6/15
Filter
rate
gpm/ft2
(m3/m2 day)
0.879
(51.57)
545 & cationi
0.855
(50.16)
503 & cationi
0.969
(56.85)
vas terminatec
& cation ic po
0.899
(52.74)
503 & cationi
0.867
(50.87)
eedflow & cati
0.982
(57.61)
Precoat,
Ibs./ft2
503
0.1
Speed
flow
0.05
polymei
545
0.1
iuper Ce
0.1
: polymei
503
0.1
juper Ce
0.15
due to p
ymer to
FW-50
0.1
503
0.1
polymei
503
0.15
FW-2
0.05
)nic poly
503
0.1
Speed floi
0.1
Precoat,
Ibs.
1000 gal
0.270
O.I 35
to first sti
0.088
0.088
to first stf
0.133
0.199
>or qualit!
irst step o
0.108
0.108
to first st
0.228
0.076
mer to sec
0.242
O.242
Polymer or
coag. in
precoat,
g./g. of D.E.
S73-C
0.0005
p of precoat,
573-C
0.0005
p of precoat,
S73-C
0.0005
effluent.
' precoat, J.M
573-C
O.OOOS
p of precoat,
573-C
0.0007
>nd step of pr
573-C
0.0007
Polymer or
coag. in
precoat,
Ibs
1000 gal.
573-C
0.00020
.M. HyfloS
573-C
3.82x1 0-5
.M. Hyflo S
573-C
0.00017

Celite 503 i
573-C
0.0001 1
i.P. FW-2 &
573-C
0.00012
'.coat, Dicalii
573-C
0.00034
Other
chem. in
precoat,
Ibs
1000 gal.

per Cel &

per Cel &


cationic ]

^tionic po

e Speedflo

Body
feed,
mg/l
247.37
:ationi<
312.2
:ationi(
264.8

iiymer
371.87
,ymer 1
378.26
v to boi
53.17
Body
feed,
Ib.
10OO gal.
Speedflow
2.063
polymer to
Super Cel
2.604
polymer to
Super Cel
2.208

to second s
503
3.101
> second st<
503
3.155
y feed.
Speedflow
0.443
B.W. solids,
Ibs
1000 gal.
(B.W. vol. as
% of treated
water?
2.468
second step o
2.780
second step a
2.540

ep of precoat
3.318
p of precoat.
3.458

0.928
Avg. turb.
Turb. @ time
of sample),
TU
Raw Filter
1.9
(1.9)
precc
3.0
preco
2.2

J.M. C
2.0
(2-1)

1.9

1.7
0.45
(0.50)
at, J.M.
0.90
it.
0.45

:lite 50
0.5
(0.68)

0.3

0.3
ORF
FibersxlO6/!
Raw Filter
\=1.0
:=1.6






\=0.48
C=0.41




A=0.02
C=0.26






A=0.8
C=0.46




NWQL
Amphibole
mg/l
Raw Filter
0.18











0.008











UMD
FibersxlO6/!
Raw Filter
























Term
HL
Ft.
H2O
16.8

17.0

15.4


5.9

16.4

11.1
inal
Turb.
TU
0.26

0.60

0.40


0.55

0.37

0.30
Run
Length, Hrs.
(Time to
Sample)
7.03
(2.3)

22.08

12.97


17.10

12.67

7.00

-------
      APPENDIX C-3    (CONTINUED)
Run
No. Date
J.M.
31




J.M.
32



33



34



35



Anio
36



37



"elite
6/17




CeliK
6/18



6/18



6/19



6/20



lie p<
6/21



6/24



Filter
rate
gpm/ft2
(mJ/ml day)
512 & cationi
0.868
(50.93)



503 & cationi
0.842
(49.40)


0.917
(53.80)


0.984
(57.73)


0.903
(52.98)


lymer used in
0.943
(55.33)


0.866
(50.81)


Precoat,
Ibs./ft2
: polyme
512
0.1
Speed
flow
0.1
: polyme
503
0.1
FW-6
0.1
503
0.1
FW-6
0.1
503
0.1
FW-6
0.1
503
0.1
FW-6
0.1
place of c
503
0.1
FW-6
0.1
503
0.1
FW-6
0.1
Precoat,
Ibs.
1OOO gal.
to first st

0.137


0.137
to first st

0.089

0.089

0.111

0.111

0.067

0.067

0.121

0.121
ationic po

0.084

0.084

0.174

0.174
Polymer or
coag. in
precoat,
g./g. of D.E.
p of precoat.
S73-C
0.0007



p of precoat,
573-C
0.0007


573-C
0.0007


573-C
0.0007


573-C
0.0007


rmer.
A-23
0.00002


A-23
0.00002


Polymer or
coag. in
precoat,
Ibs
1000 gal.

573-C
0.00019



l.P. FW-6 &
573-C
0.00013


573-C
0.00016


573-C
0.00009


573-C
0.00017



A-23
3.0X10'6


A-23
7.0xlO'6


Other
chem. in
precoat,
Ibs
1000 gal.






cationic p<

























Body
feed,
mg/l


147.0



ymer t

201.91



72.47



52.79



123.20




54.26



69.25


Body
feed,
Ib.
1000 gal.

Speedflow
1.226



> second stt
FW-6
1.684


FW-6
0.605


FW-6
0.440


FW-6
1.028



FW-6
0.453


FW-6
0.577


B.W. solids,
Ibs
1000 gal.
(B.W. vol. as
% of treated
water)"

1.500




P of precoat,
1.863



0.827



0.574



1.269




0.621



0.926



Avg. turb .
[Turb. @ time
of sample),
TU
Raw Filter

0.95
(0.96)



:.P. FV
0.92



0.92



0.9



1.2




1.2



Q.7
0.66)



0.27
(0.65)



-6 to b
0.20



0.20



0.25



0.25




0.20



0.15
(0.20)


ORF
Fibersxl06/\
Raw Filter

A=0.61
C=2.15

























\=1.0
C=3.9



A=0.09
C=0.39

























A=BDL
C=0.2


NWQL
Amphibole
mg/l
Raw Filter

0.17































<0.03






























UMD
FibersxlO6/!
Raw Filter

10.64


























6.03




7.59


























8.17



Tern
HL
Ft.
H2O

17.0





16.8



10.7



13.4



12.8




13.6



10.5



unal
Turb.
TU

0.26





0.18



0.15



0.15



0.21




0.18



0.13



Run
Length, Mrs.
(Time to
Sample)

14.00
(4.3)




22.20



16.37



25.40



15.32




20.97



11.05
(5.0)


-pi
t-o

-------
APPENDIX C-3   (CONTINUED)
Run
No.
38
39
40
41
Alun
42
43
44
45
J.M
46
Date
6/24
6/25
6/2S
6/26
i use(
6/26
Run
Run
Run
Celitf:
6/27
Filter
rate
gpm/ft2
(m3/m2 day)
0.953
(55.91)
0.857
(50.28)
0.874
(51.28)
0.938
(55.03)
in place of an
0.839
(49.22)
:erminated du<
terminated dus
terminated du<
503 to first st
0.904
(53.04)
Precoat,
Ibs./ft2
503
0.1
FW-6
0.1
503
0.1
FW-6
0.1
503
0.1
FW-6
0.1
503
0.1
FW-6
0.1
onic poly
503
0.1
FW-6
0.1
to inade
to inade
to inade
:p of pre<
503
0.1
super Ce
0.1
Precoat,
Ibs.
1000 gal.
0.136
0.136
0.169
0.169
0.291
0.291
0.402
0.402
mer, J.M.
0.125
0.125
(uate prec
luate prec
juate prec
oat, JM. r
0.138
0.138
Polymer or
coag. in
precoat,
g./g. of D.E.
A-23
0.00002
A-23
0.00002
A-23
0.00002
A-23
0.00002
Mite 512 to t
Alum
0.01
>at.
>at.
tat.
yflo Super Ce
Alum
0.02
Polymer or
coag. in
precoat,
Ibs
1000 gal.
A-23
SxlO'6
A-23
6.8xlO-6
A-23
1.2x10-5
A-23
2x10-5
ody feed.
Alum
0.0025



& Alum to
Alum
0.0028
Other
chem. in
precoat,
Ibs
1000 gal.









econd ste]

tody
feed.
mg/1
94.79
151.73
308.17
341.3

45.03



of pre
41.50
Body
feed,
Ib.
1000 gal.
FW-6
0.790
FW-6
1.265
FW-6
2.570
FW-6
2.846

512
0.376



oat, J.M. H
Super Cel
0.346
B.W. solids,
Ibs
1000 gal.
(B.W. vol. as
% of treated
water)a
1.061
1.603
3.152
3.650

0.628



'flo Super Cel
0.628
Avg. turb.
Turb. @ time
of sample),
TU
Raw Filter
0.66
0.67
0.65
0.65

0.68



to bod
0.65
0.15
0.15
0.12
0.11

0.12



V feed.
0.30
ORF
FibersxlO6/!
Raw Filter






















NWQL
Ampmbole
mg/1
Raw Filter






















UMD
FibersxlO6/!
Raw Filter






















Term
HL
Ft.
H2O
12.5
14.5
17.0
16.4

17.0




6.9
inal
^urb.
TU
0.14
0.10
0.17
0.09

0.11




0.50
Run
^ength, Hrs.
(Time to
Sample)
12.45
11.5
5.83
4.42

15.92




13.33

-------
     APPENDIX C-3   (CONTINUED)
Run
No.
E.P.
47



48
J.M.
49



SO



51



E.P.
52



53



Date
FW-6
6/28



Nor
Hyfl<
7/1



7/2



7/3



FW-5
7/3



7/8



Filter
rate
gpm/ft2
(m3/m2 day)
& Alum to sec
0.870
(51.04)


m conducted.
Super Cel to i
0.905
(53.10)


0.992
(58.20)


0.916
(53.74)


) to first step <
0.929
(54.50)


1.019
(59.79)


Precoat,
Ibs./ft2
>nd step
503
0.1
FW-6
0.1

rst step <
Super Ce
0.1
FW-6
0.1
super Ce
0.1
FW-6
0.1
Super Cel
0.1
FW-6
0.1
f precoat
FW-50
0.1
512
0.1
FW-50
0.1
512
0.1
Precoat,
Ibs.
1000 gal.
if precoat.

0.106

0.106

f precoat.

0.053

0.053

0.164

0.164

0.264

0.264
J.M. Celil

0.046

0.046

0.160

0.160
Polymer or
coag. in
precoat,
g./g. of D.E.

Alum
0.02




Alum
0.02


Alum
0.02


Alum
0.02


e 512 & Alum
Alum
0.03


AI+++
0.01


Polymer or
coag. in
precoat,
Ibs

Alum
0.0021




Alum
0.0011


Alum
0.0033


Alum
0.0053


to second st
Alum
0.0014


Alum
0.018


Other
chem. in
precoat,
Ibs
1000 gal.



















:p of precc








Body
feed,
mg/l


44.03





42.61



70.17



72.62


at.

54.89



47.66


Body
feed,
Ib.
1000 gal.

Super Cel
0.367




Super Cel
0.355


Super Cel
0.585


Super Cel
0.606



Super Cel
0.458


Super Cel
0.398


B.W. solids,
Ibs
1000 gal.
(B.W. vol. as
% of treated
water)3

0.582





0.463



0.919



1.139




0.551



0.735



Avg. turb.
(Turb. 
-------
APPENDIX C-3   (CONTINUED)
Run
No. Date
J.M. i
54



55



56



E.P. 1
57



Soda
58



59



]ellte
7/8



7/10



7/10



W-SO
7/11



^sha
7/11



7/12



Filter
rate
gpm/ft2
(m3/m2 day)
545 to first ste
0.911
(53.45)


0.965
(56.62)


0.936
(54.92)


to first step of
0.969
(56.85)


so added to se
0.871
(51.10)


0.951
(55.80)


Precoat,
Ibs./ft2
) of prec<
545
0.1
512
0.1
545
0.1
512
0.1
545
0.1
512
0.1
precoat.
FW-50
0.1
512
0.1
ond step
FW-50
0.1
512
0.1
FW-50
0.1
512
0.1
Precoat,
Ibs.
1000 gal.
at, J.M. C

O.O66

0.066

0.189

0.189

0.129

0.129


0.099

0.099
of precoat

0.103

0.103

0.215

0.215
Polymer or
coag. in
precoat,
g./g. of D.E.
lite 512 to be
A1+++
0.01


Alum
0.01


A1+++
0.01



A1+++
0.005



A1+++
0.005


A1+++
0.01


Polymer or
coag. in
precoat,
Ibs
1000 gal.
dy feed.
Alum
0.0073


Alum
0.0019


Alum
0.014



Alum
0.0055



Alum
0.0057


Alum
0.024


Other
chem. in
precoat,
Ibs
1000 gal.



















Soda Ash
0.0059


Soda Ash
0.025


Body
feed,
mg/1


46.94



71.14



67.43




48.23




50.63



44.72


Body
feed,
Ib.
1000 gal.

512
0.391


512
0.593


512
0.562



512
0.402



512
0.422


512
0.373


B.W. solids,
Ibs
1000 gal.
(B.W. vol. as
% of treated
water)3

0.531



0.973



0.834




0.606




0.635



0.850



Avg. turb.
Turb. @ time
of sample),
TU
Raw Filter

0.74



1.02



1.31




1.25




1.52



0.99




0.24



0.35



0.37




0.23




0.33



0.27



ORF
FibersxlO6/!
Raw Filter






















































NWQL
Amphibole
mg/1
Raw Filter






















































UMD
FibersxlO6/!
Raw Filter






















































Term
HL
Ft.
H20

16. 8S



16.0



16.7




16.4




14.8



17.0



inal
Turb.
TU

0.25



0.41



0.29




0.31




0.33



0.24



Run
Length, Mrs.
(Time to
Sample)

27.73



9.13



13.83




17.33




18.50



8.17




-------
      APPENDIX C-3    (CONTINUED)
Run
No. Date
J.M.
60


61


J.M.
62





E.P.
63




64




65




lytlo
7/1


7/15


:elite
7/16





FW-2
7/16




7/17




7/17




Filter
rate
gpm/ft2
(m3/m2 day)
Super Cel to
0.958
(56.21)


0.893
(52.69)


512 & Alum i
0.950
(55.74)




to first step o
0.920
(53.98)




0.888
(52.10)




0.859
(50.40)




Precoat,
lbs./R2
rst step
Super Ce
0.1
512
0.1
iuper Ce
0.1
512
0.1
Soda As
Super Ce
0.1
512
0.1


precoat,
FW-20
0.1
uper Ce
0.1


FW-20
0.1
uper Ce
0.1


FW-20
0.1
uper Cel
0.1


Precoat,
Ibs.
1000 gal
precoat.
0.220

0.220
0.081

0.081
i to body

0.264

0.264


J.M. Hyfl
0.199

0.199


0.169

0.169


0.182

0.182


Polymer or
coag. in
precoat,
g./g. of D.E.

A1+++
0.005


AI+++
0.005


eed.
AI+++
0.005




Super Cel &
A-23
0.00002




A-23
0.00002




A-23
0.00002




Polymer or
coag. in
precoat,
Ibs
1000 gal.

Alum
0.012


Alum
0.0045



Alum
0.01 5




inionic poly
A-23
3.99x10-'




A-23
3.38X10'6




A-23
3.64xlO-6




Other
chem. in
precoat,
Ibs
1000 gal

Soda Ash
0.013


Soda Ash
0.0046



Soda Ash
0.015




ler to seco















Body
feed,
mg/l

52.66


72.96




87.21

4.79

4.99
id step
19.12

1.051

1.09
76.04

2.51

2.61
08.02

5.95

6.19
Body
feed,
Ib.
1666 gal.

512
0.439


512
0.609



512
0.727
Alum
0.040
Soda Ash
0.042
of precoat.
512
0.159
Alum
0.0088
Soda Ash
0.009 1
512
0.634
Alum
0.021
Soda Ash
0.022
512
0.901
Alum
0.050
Soda Ash
0.052
B.W. solids,
Ibs
1000 gal.
(B.W. vol. as
% of treated
water)8

0.903


0.780



1.368






0.576




1.015




1.366




Avg. turb.
(Turb. @ tim
of sample),
TU
Raw Filter

0.72


0.70



0.66






0.68




0.69




0.73





0.32


0.38



0.52






0.13




0.16




0.15




ORF
FibersxlO6/!
Raw Filter




























































NWQL
Amphibole
mg/l
Raw Filter




























































UMD
FibersxlO6/!
Raw Filter




























































Tern
HL
Ft.
H2O

11.7


15.8



15.9






10.2




16.5




16.4




ninal
Turb.
TU

0.29


0.32



0.36






0.08




0.12




0.21




Run
Length, Hrs.
(Time to
Sample)

7.92


22.92



6.63






9.08




11.15




10.67




ON

-------
APPENDIX C-3   (CONTINUED)
Run
No. Date
E.P.
66





67
68
69





J.M.
70




71





J.M.
72





•'W-2
7/18





Run
Run
7/18





Celite
7/19




7/22





Celite
7/23





Filter
rate
gpm/ft2
(m3/m2 day)
& anionic pol
0.904
(53.04)




erminated du<
erminated du(
0.856
(50.22)




512 & anionic
0.925
(54.27)




0.877
(51.45)




503 to first st
0.920
(53.98)




Precoat,
Ibs./ft2
/mei to s
FW-20
0.1
FW-20
0.1


to inade
to inade
FW-20
0.1
FW-20
0.1


polymer
FW-20
0.1
512
0.1


FW-20
0.1
512
0.1


p of prec
503
0.1
512
0.1


Precoat,
Ibs.
IOOO gal.
:cond step

0.186

0.1 86


uate prec
uate prec

0.185

0.185


:o second
0.099

0.099



0.077

0.077


oat.

0.063

0.063


Polymer or
coag. in
precoat,
g./g. of D.E.
of precoat.
A-23
0.00002




at.
at
A-23
0.00002




tep of precoa
A-23
0.00002




A-23
0.00003





A-23
0.00003




Polymer or
coag. in
precoat,
Ibs
1000 gal.

A-23
3.72X10'6






A-23
3.71xlO'6





A-23
1.98X10'6




A-23
2.30xlO'6





A-23
1.89xlO'6




Other
chem. in
precoat,
Ibs
1000 gal.


































Body
feed,
mg/1


66.89

3.68

3.83



55.00

3.027

3.150

29.12

1.603

1.668

27.61

1.520

1.581


20.83

1.146

1.193
Body
feed.
Ib.
1000 gal.

512
0.558
Alum
0.031
Soda Ash
0.032


512
0.459
Alum
0.025
Soda Ash
0.026

512
0.243
Alum
0.013
Soda Ash
0.014
512
0.230
Alum
0.013
Soda Ash
0.013

512
0.174
Alum
0.0096
Soda Ash
0.0099
B.W. solids,
Ibs
1000 gal.
(B.W. vol. as
% of treated
water)3

0.992







0.881






0.468




0.410






0.320





Avg. turb.
(Turb. @ time
of sample),
TU
Raw Filter

0.71







0.87






0.76
(0.90)




0.59






0.66
(0.57)





0.20







0.33






0.28
(0.26)




0.16






0.17
(0.17)




ORF
FibersxlO6/!
Raw 1 Filter
















A=0.52
C=0.3S











A=0.54
C=0.09




















A=BDL
C=BDI











A=BDL
C=0.76




NWQL
Amphibole
mg/1
Raw J Filter
















0.13











0.09





















<0.003











0.007





UMD
FibersxlO6/!
Raw Filter
















266.0











26.0





















2.0











4.41





Term
HL
Ft.
H20

16.0







7.9






16.7




14.7






17.0





inal
Turb.
TU

0.30







0.32






0.32




0.50






0.14





Run
Length, Mrs.
(Time to
Sample)

9.92







10.50






18.17
(3.8)




24.75






28.67
(1.7)





-------
APPENDIX C-3   (CONTINUED)
Run
No. Dale
73





E.P
74





J.M
75




76




J.M
77





7/25





FW-5
7/25





Celit
7/26




7/29




Celit
7/30





Filter
rate
gpm/ft2
(m3/m2 day)
1.00
(58.67)




0 to first step
1.011
(59.32)




: 545 to first s
0.977
(57.32)



0.987
(57.38)



: 545 & anioru
0.958
(56.21)




Precoat,
Ibs./ft2
503
0.1

512
0.1

f precoa
FW-20
0.1

512
01
.1

ep of pre
S4S
0.1
Super Ce
01
.1

545
0.1
Juper Ce
0. 1

: poly me
545
0.1
545

0.1

Precoat,
Its.
1000 gal.

0.067


0.067



0.114

Olid.
.lit

:oat, J.M.

O.O92
Onoo
.uy 2,


0.126

0.126

to second

0.053


O.OS 3

Polymer or
coag. in
precoat,
g./g. of D.E.
A-23
0.00003





A-23
0.00003




lyflo Super C
A-23
0.00005



A-23
0.00005



step of preco:
A-23
0.00005




Polymer or
coag. in
precoat,
Ibs
A-23
2.00X10'6





A-23
3.41X10'6




?t & anionic
A-23
4.62x10-6



A-23
6.30X10"6



t.
A-23
2.67X10'6




Other
chem. in
precoat,
Ibs
1000 gat.













lolymer to

















Body
feed,
mg/l

18.98

1.045

0.5434


49.43

2.721

1.416
second

24.93
1.367

0.7138

18.88
1.039

0.5405


25.57

1.408

0.732
Body
feed,
Ib.
1000 gal.
512
0.158
Alum
0.0087
Soda Ash
0.0045

512
0.412
Alum
0.023
Soda Ash
0.012
step of prec
512
0.208
Alum
0.011
Soda Ash
0.0060
512
0.157
Alum
0.0087
Soda Ash
0.0045

512
0.213
Alum
0.012
Soda Ash
0.0061
B.W. solids,
Ibs
1000 gal.
(B.W. vol. as
% of treated
water)3
0.305






0.674





oat.
0.410




0.423





0.338





Avg. turb.
(Turb. @ time
of sample),
TU
Raw Filter
0.74
(0.66)





0.75






0.59




0.73





0.76
(0.69)




0.18
(0.23)





0.24






0.12




0.12





0.11
(0.12)




ORF
FibersxlO6/!
Raw Filter
^=0.11
C=1.43























A=6.11
C=0.11




A=0.04
C-0.35























A=BDL
C=0.07




NWQL
Amphibole
mg/l
Raw Filter
0.04
























0.06





C0.004
























<0.003





UMD
FibersxlO6/!
Raw Filter
60.5
























26.6





0.921
























1.01





Tern
HI-
FI.
H2O
16.4






17.O






14.2




17.0





16.8





linal
Turb.
TU
0.19






0.22






0.15




0.11





0.08





Run
Length, Hrs.
(Time to
Sample)
25.00
(16.2)





14.50






18.47




13.53





32.62
(10.4)





-------
APPENDIX 03   (CONTINUED)
Run
No.
78





J.M.
79


80


81
J.M.
82


E.P.
83



J.M.
84



Date
7/31





Celit
8/1


8/2


Run
Celit
8/6


FW-S
8/7



Celit
8/8



Filter
rate
gpm/ft2
(m3/m2 day)
0.935
(54.86)




! 512 to body
0.877
(51.45)


0.770
(45.18)


:erminated du<
: 512 to secon<
0.818
(47.99)


0 to first step c
0.870
(51.04)


! 545 to first s
0.826
(48.46)


Pre coat,
Ibs./ft2
545
0.1

545
0.1

eed.
545
0.1
545
0.1
545
0.1
545
0.1
to inade
step of ]
545
0.1
512
0.1
f precoal
FW-50
0.1
512
0.1
ep of pre
545
0.1
Super Ce
0.1
Pre coat,
Ibs.
1000 gal.

0.081


0.081


0.056

0.056
0.250

0.250
luate poly
recoat , Ca
0.051

0.051
. Catfloc

0.126

0.126
»at, J.M.

0.114

0.114
Polymer or
coag. in
precoat,
g./g. of D.E.
A-23
0.00005





A-23
0.00005


A-23
o.oooos


ner setting.
tfloc B to raw



1 to raw watet

—


iyflo Super C

-


Polymer or
coag. in
precoat,
Ibs
1000 gal.
A-23
4.03X10'6





A-23
2.82X10'6


A-23
12.5X10-6



water.





-


:1 to second

-


Other
chem. in
precoat,
Ibs
1000 gal.























tep of pre




Body
feed,
mg/l

35.77

1.970

1.024

69.24


87.84




36.63

1.646


59.70

0.302
oat, Ca

56.26

0.178
Body
feed.
Ib.
1666 gal.
512
0.298
Alum
0.016
Soda Ash
0.0085

512
0.577


512
O.733




512
0.306
Catfloc B
0.014

512
0.498
Catfloc B
0.0025
floe B to T:
512
0.469
Catfloc B
0.0015
B.W. solids,
Ibs
1000 gal.
(B.W. vol. as
% of treated
water) a
0.485






0.690
(0.1955%)


1.232
(0.529%)




0.421
(0.228%)



0.753
(0.4344%)


w water.
0.699
(0.527%)


Avg. turb.
Turb. @ time
of sample),
TU
Raw Filter
0.80






1.07
[0 .87)


0.96




0.61
(0.58)



0.68




0.75
(0.68)


0.11






0.16
(0.17)


0.27




0.20
(0.22)



0.24




0.22
(0.23)


ORF
FibersxlO6/!
Raw Filter







A=0-.22
C=0.15







A=0.6
C-0.28








A=0.06










A=BDL
C=0.04







A=BDL
C=0.06








A=BDL



NWQL
Amphibole
mg/l
Raw Filter







0.08







0.09








0.05










0.01







< 0.007








<0.006



UMD
FibersxlO6/!
Raw Filter







30.2







10.2








15.1










1.70







0.42








1.52



Term
HL
Ft.
H20
16.8






16.3


16.5




15.6



16.8




15.3



inal
Turb.
TU
0.09






0.13


0.42




0.25



0.27




0.41



Run
JLength, Hrs.
(Time to
Sample)
22.12






33.72
(28.9)


8.67




40.05
(17.4)



15.20




17.65
(7.9)



-------
     APPENDIX C-3    (CONTINUED)
Run
No.
85
86



J.M.
87



88



E.P.
89



90



91



92



Date
Run
8/8



:elitt
8/9



8/13



TV-S'
8/15



8/16



8/16



8/19



Filter
rate
gpm/ft2
(m3/m2 day)
ermmated for
0.807
(47.35)


512 to second
0.974
(57.15)


0.914
(53.62)


to first step o
1.007
(59.08)


0.977
(57.32)


0.953
(55.91)


0.928
(54.45)


Precoat,
Ibs./ft2
jquipmei
545
0.1
Super Ce1
0.1
step of p
545
0.1
512
0.1
545
0.1
512
0.1
1 precoat,
FW-50
0.1
512
0.1
FW-SO
0.1
512
0.1
FW-50
0.1
512
0.1
FW-50
0.1
512
0.1
Precoat,
Ibs.
1000 gal.
t repair

0.106

0.106
ecoat, E.F

0.140

0.140

0.036

0.036
J.M. Celit

0.041

0.041

0.173

0.173

0.138

0.138

0.083

0.083
Polymer or
coag. in
precoat,
g./g. of D.E.





FW-50 to bo








512 & Alum
A1+++
0.01


A1+++
0.01


A1+++
0.01


A1+++
0.01


Polymer or
coag. in
precoat,
Ibs
1000 gal.





ly feed, Catl








& Soda Ash
Alum
0.0046


Alum
0.019


Alum
0.015


Alum
0.009 1


Other
chem. in
precoat,
Ibs
1000 gal.





loc B to ra








o second s
Soda Ash
0.0028


Soda Ash
0.0095


Soda ^sh
O.OO76


Soda Ash
0.0045


Body
feed,
mg/l


65.74

0.444
v water

86.81

0.387

105.17

0.378
epof J

54.04



77.25



152.63



125.16


Body
feed,
Ib.
1000 gal.

512
0.548
Catfloc B
0.0037

FW-50
0.724
Catfloc B
0.0032
FW-50
0.877
Catfloc B
0.0032
recoat, J.M
Super Cel
0.451


Super Cel
0.644


Super Cel
1.273


Super Cel
1.042


B.W. solids,
Ibs
1000 gal.
(B.W. vol. as
% of treated
water)

0.764
(0.158%)



1.008
(0.220%)b


0.953
(0.109%)b


Hyflo Super (
0.540
(0.748%)b


1.018
(0.247)b


1.573
(0.356%)


1.223
(0.470%)b


Avg. turb.
(Turb. @ time
of sample),
TU
Raw Filter

1.32




1.06



0.65
(0.60)


:ei to t
0.63
[0.71)


0.70



0.83



0.58




0.30




0.23



0.17
(0.12)


ody fee
0.15
(0.16)


0.21



0.14



0.14



ORF
FibersxlO6/!
Raw Filter










A=0.13
C=0.2


d. No <
A=0.09
C=0.17
























A=BDL
C=0.1


atfloc £
A=0.15
C=0.44














NWQL
Amphibole
mg/l
Raw Filter










0.06




0.06

























<0.005




C0.003















UMD
FibersxlO6/!
Raw Filter










20.0




8.98

























0.59




1.27















Tern
HL
Ft.
H2O

16.8




6.6



10.8




9.3



4.2



7.6



8.5



linal
Turb.
TU

0.40




0.25



0.10




0.21



0.23



0.34



0.14



Run
Length, Hrs.
(Time to
Sample)

19.50




12.20



50.28
(22.0)



39.92
(18.3)


9.88



12.63



21.75



on
O

-------
APPENDIX C-3   (CONTINUED)
Run
No
93



J.M.
94



95



96



97



98



E.P.
99


Date
8/19



Celit
8/20



8/21



8/22



8*/22



8/23



FW-2
8/23


Filter
rate
gpm/ft2
(m3/m2 day)
0.847
(49.69)


512 to body
0.830
(48.70)


0.868
(50.93)


0.952
(55.85)


0.916
(53.74)


0.953
(55.91)


& Alum & So
0.994
(58.32)


Precoat,
Ibs./ft2
FW-50
0.1
512
0.1
eed.
FW-50
0.1
512
0.1
FW-50
0.1
512
0.1
FW-50
0.1
512
0.1
FW-50
0.1
512
0.1
FW-50
0.1
512
0.1
a Ash to
FW-50
0.1
FW-2
0.1
Precoat,
Ibs.
1000 gal.

0.088

0.088


0.084

0.084

0.184

0.184

0.292

0.292

0.113

0.113

0.356

0.356
lecond ste
1.118

0.745
Polymer or
coag. in
precoat,
g./g. of D.E.
A1+++
0.01



AI+++
0.01


A1+++
0.01


A1+++
0.01


A1+++
0.01


A1+++
0.02


) of precoat.
A1+++
0.01


Polymer or
coag. in
precoat,
Ibs
10OO gal.
Alum
0.0097



Alum
0.0093


Alum
0.020


Alum
0.032


Alum
0.012


Alum
0.078



Alum
0.082


Other
chem. in
precoat,
Ibs
10OO gal.
Soda Ash
0.0049



Soda Ash
0.0046


Soda Ash
0.010


Soda Ash
0.016


Soda Ash
0.0062


Soda Ash
0.039



Soda Ash
0.041


Body
feed,
mg/1

275.6




78.21



98.01



175.53



102.35



98.41



94.09


Body
feed,
Ib.
1000 gal.
Super Cel
2.294



512
0.652


512
0.817


512
1.464


512
0.854


512
0.821



512
0.745


B.W. solids,
Ibs
1000 gal.
(B.W. vol. as
% of treated
water)
2.485
(0.641%)



0.835
(0.266%)b


1.216
(0.6894%)


2.086
(0.892%)


1.099
(0.254%)b


1.649
(0.931%)



2.423
(1.924%)b


Avg. turb.
Turb. @ time
of sample),
TU
Raw Filter
0.76




0.72



0.67



0.68



0.60



0.55




0.54


0.19




0.15



0.30



0.40



0.24



0.21




0.36


ORF
FibersxlO6/!
Raw Filter


























































NWQL
Amphibole
mg/1
Raw Filter


























































UMD
FibersxlO6/!
Raw Filter


























































Term
HL
Ft.
H20
9.3




9.6



15.6



10.2



10.5



15.6




10.0


mal
'urb.
TU
0.28




0.15



0.53



0.57



0.25



0.18




0.25


Run
^ength, Hrs.
(Time to
Sample)
22.33




23.83



10.42



6.00



16.08



4.92




2.25



-------
     APPENDIX C-3    (CONTINUED)
Run
No.
J.M
100



J.M
101



102



103


J.M
104





105





Date
Hyfl
8/23



Celit
8/26



8/27



8/28


Hyfl
8/29





8/30





Filter
rate
gpm/ft2
(m3/m2 day)
> Super Cel & .
0.876
(51.40)


• 512 & Alum
0.934
(54.80)


0.952
(55.85)


0.972
(57.03)


> Super Cel &
0.888
(52.10)




0.937
(54.97)




Precoat,
Ibs./ft2
Llum & S
FW-50
0.1
Super Ce
0.1
it Soda A
FW-50
0.15
512
0.1
FW-50
0.15
512
0.1
FW-50
0.15
512
0.1
Llum & S
FW-50
0.15

512
0.1

FW-50
0.15

512
O.I

Precoat,
Ibs.
1OOO gal.
>da Ash to

0.387

0.387
ih to secoi

0.111

0.074

0.126

0.084
0.113

0.075
)da Ash tc

0.127


0.084


0.229

Of c o
.1 b L

Polymer or
coag. in
precoat,
g./g. of D.E.
second step o
A1+++
0.01


d step of prec
A1+++
0.01


A1+++
0.01


A1+++
0.01


body feed.
A1+++
0.01




A1+++
0.01




Polymer or
coag. in
precoat,
Ibs
1000 gal.
' precoat.
Alum
0.043


>at, E.P. FW
Alum
0.0081


Alum
0.0092


Alum
0.0083



Alum
0.0093




Alum
0.017




Other
chem. in
precoat,
Ibs
1000 gal.

Soda Ash
0.021


20 to bod:
Soda Ash
0.0041


Soda Ash
0.0046


Soda Ash
0.0041



Soda Ash
0.0046




Soda Ash
0.0084




Body
feed,
mg/1


59.37


feed.

63.76



140.85


257.01




11.81

1.298

0.650

48.75

S.358

2.685
Body
feed.
Ib.
1000 gal.

512
0.495



FW-20
0.532


FW-20
1.175


FW-20
2.143



Super Cel
0.098
Alum
0.011
Soda Ash
0.0054
Super Cel
0.407
Alum
0.045
Soda Ash
0.022
B.W. solids,
Ibs
1000 gal.
(B.W. vol. as
% of treated
water)

1.333
(1.155%)



0.729
(0.02 !%)*>


1.399
(0.226%)b


2.344
(0.338%)b



0.340
(0.164%)




0.880
(0.189%)




Avg. turb.
(Turb. @ time
of sample),
TU
Raw Filter

0.52




0.49



0.47



0.47
(0.43)



0.50





0.46
(0.39)





0.45




0.13



0.09



0.12
(0.16)



0.09





0.12
(0.12)




ORF
FibersxlO6/!
Raw Filter














A=0.39
C=0.48









A=0.78
C=0.33


















A=0.15
C=0.24









A=0.04
C=0.17




NWQL
Amphibole
mg/1
Raw Filter














0.09









0.07



















<0.003









<0.003





UMD
FibersxlO6/!
Raw Filter














10.4









17.8



















1.05









0.65





Term
HL
Ft.
H2O

5.8




6.1



8.5



8.2



17.0





16.4





inal
Turb.
TU

0.67




0.16



0.09



0.10



0.06





0.11





Run
Length, Hrs.
(Time to
Sample)

4.92




24.12



20.83



22.75
(6.4)



21.60





11.67
(8.3)




cn
r-o

-------
APPENDIX C-3   (CONTINUED)
Run
No. Date
106





J.M
107





108





109





J.M
110



8/30





Celit
9/3





9/4





9/4





Hyfl
9/5



Filter
rate
gpm/ft2
(m3/m2 day)
0.918
(53.86)




; 512 & Alum
0.822
(48.23)




0.915
(53.68)




0.916
(53.74)




i Super Cel to
0.929
(54.50)


Precoat,
Ibs./ft2
FW-50
0.15
512
0.1


i Soda A
FW-50
0.15
512
0.1


FW-50
0.15
512
0.1


FW-50
0.15
512
0.1


)ody feec
FW-50
0.15
512
0.1
Precoat,
Ibs.
1000 gal.

0.300

0 200


ih to body

0.148

0.099



0.223

0.149



0.318

0.212


, Catfloc

0.131

0.088
Polymer or
coag. in
precoat,
g./g. of D.E.
A1+++
0.01




feed.
Alum
0.01




Alum
0.01




Alum
0.01




5 to raw watei
A1+++
0.01


Polymer or
coag. in
precoat,
Ibs
1000 gal.
Alum
0.022





Alum
0.00099




Alum
0.0015




Alum
0.0021





Alum
0.0096


Other
chem. in
precoat,
Ibs
1000 gal.
Soda Ash
0.011





Soda Ash
0.0054




Soda Ash
0.0082




Soda Ash
0.012





Soda Ash
0.0048


Body
feed,
mg/1

83.84

9.215

4.617


29.19

3.208

1.607

42.78

4.702

2.356

106.72

11.73

5.877


57.17

0.199
Body
feed,
Ib.
1000 gal.
Super Cel
0.699
Alum
0.077
Soda Ash
0.039

512
0.243
Alum
0.027 .
Soda Ash
0.013
512
0.357
Alum
0.039
Soda Ash
0.020
512
0.890
Alum
0.098
Soda Ash
0.049

Super Cel
0.477
Catfloc B
0.0017
B.W. solids,
Ibs
1000 gal.
(B.W. vol. as
% of treated
water)
1,347
(0.448%)





0.537
(0.164%)




0.797
(0.334%)




1.580
(0.249%)





0.712
(0.1395%)*>


Avg. turb.
(Turb. @ time
of sample),
TU
Raw Filter
0.78






0.62





0.67
(0.71)




0.65






0.68



0.20






0.165





0.22
(0.22)




0.31






0.14



ORF
FibersxlO6/!
Raw Filter













A=1.61
C=0.33




























A=0.17
C=1.15















NWQL
Amphibole
mg/1
Raw Filter













0.10





























<0.006
















UMD
FibersxlO6/!
Raw Filter













30.3





























0.96
















Tern
HL
Ft.
H2O
17.0






17.0





17.0





17.0






11.2



linal
Turb.
TU
0.19






0.19





0.27





0.45






0.08



Run
Length, Hrs.
(Time to
Sample)
9.08






19.81





12.25
(8.2)




8.21






20.50




-------
APPENDIX C-3    (CONTINUED)
Run
No. Dale
Anio
111





J.M
112




J.M
113


114


J.M
115



116



nic pi
9/6





Hyfl
9/7




Celit
9/9


9/10


Celit
9/11



9/12



Filter
rate
gpm/ft2
(m3/m2 day)
lymer added i
0.946
(55.50)




> Super Cel & i
1.008
(59.14)




: 512 & Alum
1.002
(58.79)


0.969
(56.85)


512 to body
0.862
(50.57)


0.783
(45.94)


Precoat,
Ibs./ft2
place of
FW-50
0.15

512
0.1

rtionic p<
FW-50
0.15

Super Ce
0.1

i Soda A
FW-50
0.15
512
0.1
FW-50
0.15
512
0.1
eed, Catf
FW-50
0.15
512
0.1
FW-50
0.15
512
0.1
Precoat,
Ibs.
1000 gal.
Alum am

0.1«6


0.1 1 1

lymer to s
0.377


0.25 1

h to secor
0.109

0.072
0.111

0.072
oc B to ra

0.131

0.088

0.124

0.083
Polymer or
coag. in
precoat,
g./g. of D.E.
Soda Ash
A-23
0.00003




;cond step of
A-23
0.00003




d step of prec
AI+++
0.01


AI+++
0.01


v water.
A1+++
0.01


A1+-H-
0.01


Polymer or
coag. in
precoat,
Ibs
1000 gal.
l second ste
A-23
3.32xlO-6




ttecoat.
A-23
7.53X10'6




>at, J.M. Hy
Alum
0.0080


Alum
0.0081



Alum
0.0096


Alum
0.0091


Other
chem. in
pvecoat,
Ibs
1000 gal.
i of precoa












lo Super C
Soda Ash
0.0040


Soda Ash
0.0041



Soda Ash
0.0048


Soda Ash
0.0046


Body
feed,
mg/l
, J.M. <

27.44

3.016

1.511

20.07

2.206

1.105
J to bo
14.17

0.286
221.79

0.407


55.15

0.557

123.40

0.477
Body
feed,
Ib.
1666 gal.
elite 51 2 &
512
0.229
Alum
0.025
Soda Ash
0.013

512
0.167
Alum
0.018
Soda Ash
0.0092
ly feed, Ca'
Super Cel
0.952
Catfloc B
0.0024
Super Cel
1.850
Catfloc B
0.0034

512
0.460
Catfloc B
0.0046
512
1.029
Catfloc B
0.0040
B.W. solids,
Ibs
1000 gal.
(B.W. vol. as
% of treated
water)
Alum & Soda
0.543
(0.195%)





0.823
(0.325%)b




loc B to raw •
1.145
(0.217%)b


2.050
(0.276%)b



0.698
(0.131%)


1.254
(0.217%)


Avg. turb.
(Turb. @ time
of sample),
TU
Raw Filter
Ashte
0.47
(o.si;





0.39




rater.
0.50
(0.46)


0.63



0.53
(0.45;


0.42



body f(
0.09
(0.13)





0.06





0.08
(0.08)


0.08



0.09
(0.15)


0.06



ORF
FibersxlO6/!
Raw Filter
ed.
A=0.72
C=0.39











A- 1.0
C=0.5






A=0.3
C=0.3







A=0.02
C=0.59











A=0.04
C=1.0






A=BDL
C=0.13






NWQL
Amphibole
mg/l
Raw Filter

0.07












0.04






0.06








<0.003












<0.003






<0.005







UMD
Fibersxio6/!
Raw Filter

13.6












15.4






13.0








0.36












0.33






0.28







Terr
HL
Ft.
H2O

17.0






8.8





10.1


11.9



16.9



14.8



ninal
Turb.
TU

0.09






0.05





0.10


0.10



0.05



0.05



Run
Length, Mrs.
(Time to
Sample)

15.82
(2.9)





6.85





23.00
(4.1)


23.33



22.07
(6.0)


25.67




-------
  APPENDIX C-3    (CONTINUED)
Run
No. Date
J.M.
117
118
J.M.
119
J.M.
120
121
122
^qua
>/13
9/16
^qua
1/17
"elit<
9/19
9/20
9/20
Filter
rate
gpm/ft2
(m3/m2 day)
Cel to body fe
0.930
(54.56)
0.826
(48.46)
Cel to body fe
0.8445
(49.55)
503 & Alum i
0.861
(50.52)
0.864
(50.69)
0.795
(46.61)
Precoat,
Ibs./ft2
;d, Catflc
FW-50
0.15
512
0.1
FW-SO
0.15
512
0.1
:d for fir;
FW-50
0.15
512
0.1
Soda As
FW-SO
0.15
512
0.1
FW-50
0.15
512
0.1
FW-50
0.15
512
0.1
Precoat,
Ibs.
1000 gal.
c B to raw
0.130
0.086
0.141
0.094
1 half of n
0.120
0.080
i to body
0.207
0.138
0.235
0.156
0.297
0.198
Polymer or
coag. in
precoat,
g./g. of D.E.
water.
A1+++
0.01
A1+++
0.01
n, E.P. FW-2(
A1+++
0.01
eed.
A1+++
0.01
A1+++
0.01
AI+++
0.01
Polymer or
coag. in
precoat,
Ibs
1000 gal.
Alum
0.0095
Alum
0.010
to body fee
Alum
0.0088
Alum
0.015
Alum
0.017
Alum
0.022
Other
chem. in
precoat,
Ibs
1000 gal.
Soda Ash
0.0048
Soda Ash
0.0052
1 for remai
Soda Ash
0.0044
Soda Ash
0.0076
Soda Ash
0.0086
Soda Ash
0.011

Body
feed,
mg/1
70.46
0.414
54.74
0.584
ider of
183.05
0.566
22.66
i.4905
1.248
49.99
5.495
2.753
75.26
8.272
4.144
Body
feed,
Ib.
1000 gal.
Aqua Cel
0.588
Catfloc B
0.0035
Aqua Cel
1.291
Catfloc B
0.0049
run, Catfloc
Aqua Cel
FW-20
2.361
Catfloc B
0.0047
503
0.189
Alum
0.021
Soda Ash
O.010
503
0.417
Alum
0.046
Soda Ash
0.023
503
0.628
Alum
0.069
Soda Ash
0.035
B.W. solids,
Ibs
1000 gal.
(B.W. vol. as
% of treated
water)
0.821
(0.074%)b
1.545
(0.210%)b
B to raw watt
2.579
(0.239%)b
0.589
(0.207%)°
0.902
(0.054%)
1.259
(0.222%)

Avg. turb.
Turb. @ time
of sample),
TU
Haw Filter
0.45
:o.4o)
0.42
0.37)
0.49
0.50
0.52)
0.45
0.46
0.06
(0.08)
0.08
(0.08)
0.07
0.08
(0.11)
0.06
0.09
ORF
FibersxlO6/!
Raw Filter
A=0.02
C=0.06
A=0.9
C=0.15
A=0.6
C=0.09
A=0.02
C=0.4
A=BDL
C=1.3
A=0.02
C=1.8
NWQL
Amphibole
mg/1
Raw Filter
0.09
0.08
0.10
<0.003
< 0.004
•JO. 004
UMD
FibersxlO6/!
Raw Filter
30.0
20.3
13.8
0.47
4.89
0.76
Terir
HL
Ft.
H2O
7.4
6.9
7.4
14.2
16.8
16.3
inal
Turb.
TU
0.04
0.07
0.10
0.07
0.06
0.12
Run
Length, Mrs.
(Time to
Sample)
20.75
(2.7)
21.53
(4.5)
24.67
14.00
(2.0)
12.33
10.58
a B.W. volume was not measured until Run 79.
  Runs did not reach terminal HL or turbidity.
c A=amphibole, C=chrysotile

-------
 APPENDIX C-4    PRESSURE DIATOMACEOUS EARTH FILTRATION (ERD-1) SUMMARY OF INDIVIDUAL RUNS
Run
No. Date
One
1A



J.M
2A



J.M
3A




4A




5A



6A



step
6/11


6/13
Celit
6/13



Celit
6/14




6/17




6/18



6/19



Filter
rate
gpm/ft2
(m3/m2 day)
irecoat, E.P F
1.189
(69.76)


: 503 & J.M. C
1.3S8
(79.67)


! 503 & Dicalii
1.215
(71.28)



1.227
(71.99)



1.213
(71.17)



1.199
(70.35)



Precoat,
Ibs./ft2
V-50 & J
FW-50
0.1
503
0.1
:hte 545
503
0.1
545
0.1
e Speedfl
503
0.1
Speed
flow
0.05
503
0.05
Speed
flow
0.1
503
0.05
Speed
flow
0.1
503
0.05
Speed
flow
0.1
Precoat,
Ibs.
1000 gal.
M. Celite i

0.027

0.027
Si. cationic

0.091

0.091
>w & catic

0.069


0.035

0.028


O.OS7
0.034


0.067
0.042


0.085
Polymer or
coag. in
precoat,
g./g. of D.E.
03 & cationic
573-C
0.0005


3olymer to pr
573-C
0.0005


nic polymer t
573-C
0.0007



573-C
0.0008



573-C
0.0008



573-C
0.0008



Polymer or
coag. in
precoat,
Ibs
1000 gal.
polymer to
573-C
2.7xlO-5


:coat, J.M. C
573-C
9.14x10-5


» precoat, Di
573-C
7.29X10'5



573-C
6.81x10-5



573-C
8.04x10-5



573-C
10.16xlO-;



Other
chem. in
precoat,
Ibs
1000 gal.
recoat, Di




elite 503 t.




:aliteSpe&


















Body
feed,
mg/l
alite S[

30.88


body

110..20


flow tc

122.96




41.34



195.98



37.68



Body
feed,
Ib.
1000 gal.
eedflow to
Speedflow
0.258


eed.
503
0.919


body feed.
Speedflow
1.025



Speedflow
0.345



Speedflow
1.635



Speedflow
0.314



B.W. solids,
Ibs
1000 gal.
(B.W. vol. as
% of treated
water)3
>odyfeed. B.
0.312




1.102




1.130




0.430




1.735



0.441



Avg. turb.
(Turb. @ time
of sample),
TU
Raw Filter
V. soli
2.7
(1.9)

(2.1)

1.9




1.9




0.91
(0.96)



0.91



0.90



Is calc.
0.25
(0.36)

(0.15)

0.55




0.17




0.14
(0.15)



0.10



0.16



ORF
FibersxlO6/!
Raw Filter
•om ch
A=1.0
C=1.6
A.=0.48
C=0.41











A=0.61
C=2.15











im. & E
A=1.0
C=9.3
A=0.09
C=0.71











A=BDL
C=1.37











NWQL
Amphibole
mg/l
Raw Filter
.F. add
0.12














0.17












tions.
< 0.0 1














0.005












UMD
FibersxlO6/!
Raw Filter

33.25














10.64













6.93














7.07












Tern
HL
Ft.
H2O

104.0




9.2




63.5




55.4




98.1



47.3



unal
Turb.
TU

0.14




0.55




0.10




0.11




0.07



0.15



Run
Length, Hrs.
(Time to
Sample)

49.80
(2.8)
(49.8)


13.42




19.75




23.90
(4.9)



20.5



16.42



a B.W. volume was not measured.
 A^amphibole, C-chrysotile

-------
APPENDIX C-4 PRESSURE DIATOMACEOUS EARTH FILTRATION (ERD-2) SUMMARY OF INDIVIDUAL RUNS
Run
No.
One
1
J.M.
2

J.M.
3



4
5
6
J.M.
7




Dica
8




9




Bate
tep t
Efflu
Hyfk
5/2

Hyfk
5/3



Efflu
Efflu
Efflu
Celit«
5/9




ite S)
5/10




5/13




Filter
rate
gpm/ft2
(m3/m2 day)
recoat. B.W. S.
nt turbidity t(
Super Cel to I
1.572
(92.23)
Super Cel & E
1.641
(96.28)


:nt turbidity t(
:nt turbidity t<
:nt turbidity t<
512 & Dicalit
1.600
(93.87)



eedflow & E.P
1.S89
(93.23)



1.566
(91.88)



Hrecoat,
Ibs./ft2
lids calc.
o high.
recoat an
Super Cel
0.15
.P. FW-5C
Super Ce
0.05
FW-SO
0.1
o high.
o high.
o high.
SpeedfU
512
0.1
Speed
flow
0.05
FW-50t
Speed
flow
0.1
FW-50
0.05
Speed
flow
0.1
FW-SO
0.05
Precoat,
Ibs.
1000 gal.
from cher

I to body
M
0.070
&. anionic
M-C
0.034

0.069



w to prec<
F-F
0.053


0.027
) precoat.
F-C

0.053

0.027
F-C

0.02S

0.012
Polymer or
coag. in
precoat,
g./g. of D.E.
. & D.E. addi<

eed.
_

polymer to p
A-23
0.00005





at.
_





_




_




Polymer or
coag. in
preeoat,
Ibs
ons.


_

ecoat.

S.lxlO'6






_





_




-




Other
chem. in
precoat,
Ibs
1000 gal.






























Jody
feed,
mg/1




29.97


26.75







68.75





69.16




70.19



Body
feed,
Ib.
1000 gal.



Super Cel
0.233

Super Cel
0.223






Super Cel
0.573




Super Cel
0.577



Super Cel
0.586



B.W. solids,
Ibs
1000 gal.
(B.W. vol. as
% of treated
water)3



0.304


0.326







0.653





0.657




0.623




Avg. turb.
Turb. @ time
of sample),
TU
Raw Filter



0.66


0.67







0.72





0.70




1.0







0.56


0.82







0.16





0.17




0.29




ORF
FibersxlO6/!
Raw Filter




























































NWQL
Amphibole
mg/1
Raw Filter




























































UMD
FibersxlO6/!
Raw Filter




























































Term
HL
Ft.
H20



19.6


36.9







50.8





68.1




92.4




inal
'urb.
TU



0.62


0.98







0.18





0.26




0.50




Run
Length, Hri
(Time to
Sample)



22. 58


14.75







19.66





19.75




42.58





-------
APPENDIX C-4   (CONTINUED)
Run
Noj
10
11
Catic
12
13
14
J.M.
15
15

Date
5/16
5/16
nic p
5/17
5/22
5/30
Celit
6/4
6/6

Filter
rate
gpm/ft2
(m3/m2 day)
1.553
(91.12)
1.728
(101.38)
>lymer also ad<
1.204
(70.64)
1.153
(67.65)
1.135
(66.59)
503 & Dicalit
1.069
(62.72)

Precoat,
Ibs./ft2
Speed
flow
0.1
FW-50
0.05
Speed
flow
0.1
FW-50
0.05
led to prt
Speed
flow
0.1
FW-50
0.05
Speed
flow
0.1
FW-50
0.05
Speed
flow
0.1
FW-50
0.05
Speedflc
503
0.1
Speed
flow
0.05

Precoat,
ibs.
1000 gal.
F - C
0.028
0.014
F - C
O.060
0.030
coat.
F - C
0.094
0.047
F - C
0.013
0.0064
F - C
0.020
0.010
w & catio
MC-F
0.019
0.0095

Polymer or
coag. in
precoat,
g./g. of D.E.



C-31
O.OOOS
C-31
0.0005
573C
0.0005
»ic polymer tc
573C
0.0006

Polymer or
coag. in
precoat,
Ibs
10OO gal.



7.06xlO's
0.96x10-5
1.51x10-5
precoat, Di<
1.7XIO-5

Other
chem. in
precoat,
Ibs
1000 gal.






llite Speec


Body
feed,
mg/1
70.8
63.59

?1.30
79.40
55.17
flow to
86.01

Body
feed,
Ib.
1000 gal.
Super Cel
0.590
Super Cel
0.530

Super Cel
0.761
Super Cel
0.662
Super Cel
0.460
body feed.
Speed plus
0.717

B.W. solids,
Ibs
1000 gal.
(B.W. vol. as
% of treated
water)3
0.633
0.621

0.903
0.682
0.490

0.746

Avg. turb.
(Turb. @ time
of sample),
TU
Raw Filter
1.2
(0.8)
1.1

0.87
0.98
(0.94)
0.85
(0.80)

0.75
(0.86)
(0.74)

0.29
(0.1 3)
0.35

0.32
0.18
(0.17)
0.175
(0.14)

0.15
(0.15)
(0.15)

ORF
Fibersxio6/!
Raw Filter
1=2.61
C=1.35




1=1.43

1=1.74
>2.91
1=1.5
>2.3

A=0.261
C=1.04




A=BD1
C=0.04

A=.039
C=1.00
A=0.1
C=0.4

NWQL
Amphibole
mg/1
Raw Filter
0.14



0.20
0.19
5

1 0.26
0.18

0.003



0.002
0.004

0.003
<0.004

UMD
FibersxlO6/!
Raw Filter


















Term
HL
Ft.
H2O
104.0
103.9

25.4
104.0
104.0

L04.0

inal
Turb.
TU
0.35
0.25

0.25
0.25
0.20

0.12

Run
Length, Mrs.
(Time to
Sample)
37.43
(30.6)
16.00

14.7
112.89
(47.3)
71.84
(46.0)

78.97
(27.7)
(75.4)


-------
       APPENDIX C-4   (CONTINUED)
Run
No.
16
17
18
19
Dica
20
Alur
21
22
23
24
Date
Efflu
Efflu
Efflu
Run
ite S
6/20
i usec
6/21
6/24
6/24
6/25
Filter
rate
gpm/ft2
(m3/m2 day)
;nt turbidity t<
:nt turbidity t<
:nt turbidity t<
ermmated due
eedflow & J.N
1.039
(60.96)
in place of cai
1.0S8
(62.07)
1.046
(61.37)
1.021
(59.90)
1.179
(69.17)
Precoat,
Ibs./ft2
o high.
o high.
o high.
to failure
. Cehte 5
Speed
flow
0.1
503
0.05
ionic pol
Speed
flow
0.1
503
0.05
Speed
flow
0.1
503
0.05
Speed
flow
0.1
503
0.05
Speed
flow
0.1
503
0.05
Precoat,
Ibs.
1000 gal.



in body ft
)3 & catio
F-MC
0.108
0.054
rmer.
F-MC
0.073
0.037
F-MC
0.126
0.063
F-MC
0.156
0.078
F-MC
0.127
0.064
Polymer or
coag. in
precoat,
g./g. of D.E.



ed system.
ic polymer tc
573C
0.0008

Alum
0.01
Alum
0.01
Alum
0.01
Alum
0.019
Polymer or
coag. in
precoat,
Ibs
1000 gal.




precoat.
0.00013

0.0011
O.OO19
0.0023
0.0036
Other
chem. in
precoat,
Ibs
1000 gal.











Body
feed,
mg/l





19.57

19.97
16.92
38.82
105.44
Body
feed,
Ib.
1000 gal.





Speed flow
0.163

Speedflow
0.167
Speedflow
0.141
Speedflow
0.324
Speedflow
0.879
B.W. solids,
Ibs
1000 gal.
(B.W. vol. as
% of treated
water)3





0.326

0.277
0.332
0.560
1.074
Avg. turb.
(Turb. @ time
of sample),
TU
Raw Filter





1.12

1.16
0.69
0.66)
0.65
0.66





0.17

0.11
0.10
(0.06)
0.13
0.10
ORF
FibersxlO6/!
Raw Filter








\=1.0
C=3.91










A=0.02
C=0.24


NWQL
Amphibole
mg/l
Raw Filter






















UMD
FibersxlO6/!
Raw Filter








6.03










1.85


Tern
HL
Ft.
H2O





39.3

55.4
32.4
35.8
67.0
linal
Turb.
TU





0.22

0.14
0.11
0.08
0.18
Run
Length, Hrs
(Time to
Sample)





14.83

21.55
12.65
(4.5)
10.48
11.08
t-n
to

-------
    APPENDIX C-4   (CONTINUED)
Run
No. Date
25
26
E.P.
27
Two
28
29
30
31
6/25
6/26
TV-li
6/27
ptep i
6/28
6/28
7/1
7/3
Filter
rats
gpm/ft2
(m3/m2 day)
1.099
(64.48)
1.088
(63.83)
& J.M. Celite
1.122
(65.83)
recoat, E.P. F'
1.194
(70.05)
1.167
(68.47)
1.160
(68.06)
1.165
(68.35)
Hrecoat,
Ibs./ft2
Speed
flow
0.1
503
0.05
Speed
flow
0.1
503
0.05
503 & Al
FW-10
0.1
503
0.05
/-SO to fl
FW-50
0.1
FW-6
0.1
FW-50
0.1
FW-6
0.1
FW-50
0.1
FW-6
0.1
FW-50
0.1
FW-6
0.1
Precoat,
Ibs.
1000 gal.
F-MC
0.104
0.052
F-MC
0.101
0.050
im to pre(
M-MC
0.145
0.072
st step of
C-F
O.OS7
0.057
C-F
0.103
0.103
C-F
0.036
0.036
C-F
0.262
0.262
Polymer or
coag. in
precoat,
g./g. of D.E.
Alum
0.01
Alum
0.01
Dat, E.P. FW-!
Alum
0.02
>recoat, E.P. I
Alum
0.01
Alum
0.01
Alum
0.01
Alum
0.01
Polymer or
coag. in
precoat,
Ibs
1000 gal.
0.0016
0.0015
0 to body fe
0.0043
W-6 & Alun
0.00057
0.0010
0.00036
0.0026
Other
chem. in
precoat,
Ibs
1000 gal.


ed.

to second




Body
feed,
mg/l
114.14
226.35

40.23
itep of
36.27
54.51
26.19
76.01
Body
feed,
Ib.
Speedflow
0.952
Speedflow
1.888

FW-10
0.336
jrecoat.
FW-10
0.302
FW-16
0.455
FW-10
0.218
FW-10
0.634
B.W, solids,
Ibs
1000 gal.
(B.W. vol. as
% of treated
water)3
1.109
2.041

0.557

0.417
0.662
0.292
1.160
Avg. turb.
'Turb. @ time
of sample),
TU
Raw Filter
0.66
0.68

0.64

0.66
(0.64)
0.67
0.78
0.74
0.09
0.09

0.10

0.10
(0.07)
0.12
0.14
0.15
ORF
FibersxlO6/!
Raw Filter





\=1.M
>8.12








A=0.11
C=5.3



NWQL
Amphibole
mg/l
Raw Filter





0.16








<0.01



UMD
FibersxlO6/!
Raw Filter





5.54








0.73



Terrr
HL
Ft.
H2O
64.7
72.2

25.4

26.6
16.2
27.7
10.4
linal
Turb.
TU
0.05
0.09

0.11

0.07
0.15
0.14
0.16
Run
Length, Hr;
(Time to
Sample)
14.58
15.16

10.25

24.41
(27.3)
13.83
39.42
S.47
ON
O

-------
APPENDIX C-4   (CONTINUED)
Run
No.
J.M.
32
33
J.M.
34
35
36
37
E.P.
38
Date
Cellti
7/3
7/4
Celiti
7/8
7/9
7/11
7/15
FW-5
7/16
Filter
rate
gpm/ft2
(m3/m2 day)
512 & Alumt
1.204
(70.64)
1.107
(64.95)
545 to first st
1.135
(66.59)
1.196
(70.17)
1.120
(65.71)
1.098
(64.42)
) to first step c
1.23
(72.16)
Pre coat,
Ibs./ft2
3 second
FW-50
0.1
512
0.1
FW-50
0.1
512
0.1
:p of pre<
545
0.1
Super Ce
0.1
545
0.1
Super Ce
0.1
545
0.1
Super Ce
0.1
545
0.1
Super Ce
0.1
f precoat
FW-50
0.1
FW-20
0.1
Precoat,
Ibs.
1000 gal.
itep of pre
C-F
0.062
0.062
C-F
0.067
0.067
oat, J.M. ]
VC-M
0.047
0.047
VC-M
0.031
0.031
VC-M
0.038
0.038
VC-M
0.067
0.067
E.P. FW-:
C-MC
0.044
0.044
Polymer or
coag. in
precoat,
g./g. of D.E.
:oat.
Alum
0.01
Alum
0.01
[yflo Super C<
AI+++
0.01
A1+++
0.01
A1+++
0.01
A1+++
0.01
0 & Alum & i
A1+++
0.01
Polymer or
coag. in
precoat,
Ibs
1000 gal.

0.00062
0.00067
1 & Alum to
0.0052
0.0034
0.0041
0.0074
oda Ash to s
0.0048
Other
chem. in
precoat,
Ibs
1000 gal.



second ste




:cond step
Soda Ash
0.0051
Body
feed,
mg/1

71.42
151.53
of pre
29.07
116.58
86.25
156.41
of prec
34.56
Body
feed,
Ib.
1000 gal.

FW-10
0.59
FW-10
1.264
:oat.
FW-10
0.242
FW-10
0.972
FW-10
0.719
FW-10
1.304
>at, E.P. FV\
FW-20
0.297
B.W. solids,
Ibs
1000 gal.
(B.W. vol. as
% of treated
water)a

0.721
1.398

0.342
1.083
0.799
1.447
-20 to body fe
0.390
Avg. turb.
[Turb. @ time
of sample),
TU
Raw Filter

0.73
(0.69!
0.62

0.66
1.08
1.3
0.70
ed.
0.71

0.14
(0.17)
0.11

0.09
0.15
0,11
0.11

0.09
ORF
FibersxlO6/!
Raw Filter

A=0.5(
C=3.57









A=0.1
C=0.8








NWQL
Amphibole
mg/1
Raw Filter

0.07









0.003








UMD
FibersxlO6/!
Raw Filter

2.99









1.22








Term
HL
Ft.
H2O

23.1
23.1

63.5
55.4
50.8
37.0

23.1
inat
Turb.
TU

0.15
0.09

0.08
0.11
0.12
0.13

0.11
Run
Length, Hrs.
(Time to
Sample)

22.2
(2.0)
22.50

31.08
45.47
39.58
22.5

30.75

-------
APPENDIX C-4   (CONTINUED)
Run
No.
39



40



41



J.M.
42



43



44



J.M.
45



Date
7/17



f7/19



7/23



Celiti
7/23



7/25



7/25



Celits
7/30



Filter
rate
gpm/ft2
(m3/m2 day)
1.075
(63.07)


1.155
(67.76)


1.195
(70.11)


512 & Alum i
1.11
(65.24)


1.024
(60.08)


1.018
(59.73)


545 to first st
1.01
(59.26)


Precoat,
Ibs./ft2
FW-50
0.1
FW-20
0.1
FW-50
0.1
FW-20
0.1
FW-50
0.1
FW-20
0.1
Soda As
FW-50
0.1
512
0.1
FW-50
0.1
512
0.1
FW-SO
0.1
512
0.1
p of prec
545
0.1
512
0.1
Precoat,
Ibs.
1000 gal.
C-MC
0.056

0.056
C-MC
0.050

0.050
C-MC
0.049

0.049
i to secon
C-F
0.054

0.054
C-F
0.073

0.073
C-F
0.049

0.049
oat, J.M. (
VC-F
0.036

0.036
Polymer or
coag. in
precoat,
g./g. of D.E.
AH++
0.01


A1+++
0.01


AI+++
0.01


step of prec<
A1+++
0.01


A1+++
0.01


A1+++
0.01


elite 512 to st
_



Polymer or
coag. in
precoat,
Ibs
1000 gal.

0.0062



0.0055



0.0052


at, J.M. Celi

0.0060



0.0080



0.0054


cond step of




Other
chem. in
precoat,
Ibs
1000 gal.
Soda Ash
0X1065


Soda Ash
0.0057


Soda Ash
0.0056


e 545 to b
Soda Ash
0«062


Soda Ash
0.0043


Soda Ash
0.0029


precoat, J




Body
feed,
mg/l

63.89



116.62



200.51


>dy fee

26.12



42.04



60.16


M. Celi

58.29

0.483
Body
feed,
Ib.
1000 gal.
FW-20
0.533


FW-20
0.974


FW-20
1.672



545
0.218


545
0.351


545
0.502


e 545 to bo
545
0.486
Catfloc B
0.0040
B.W. solids,
Ibs
1000 gal.
(B.W. vol. as
% of treated
water)8
0.658



1.083



1.781




0.339



0.509



0.603



ly feed, Catfk
0.563



Avg. turb.
(Turb. @ time
of sample),
TU
Raw Filter
0.71



0.78
(0.90)


0.59
(0.57)



0.71



0.73
(0.66)


0.66



c B to
0.73
(0.69)


0.10



0.11
(0.12)


0.12
(0.09)



0.12



0.13
(0.09)


0.15



raw wa
0.11
(0.10)


ORF
FibersxlO6/!
Raw Filter




A=0.52
:>o.35


A=0.54
C=0.09







A=0.11
C=1.43






er.
A=0.1!
C=0.11






A=0.11
C=0.22


A=0.09
C=0.09







A=BD1
C=0.44







A=BDL
C=0.07


NWQL
Amphibole
mg/l
Raw Filter




0.13



0.09








0.04








0.06







C0.003



<0.003








< 0.003








<0.003



UMD
FibersxlO6/!
Raw Filter




266.0



26.0








60.5








26.6







4.16



2.04








0.964








0.87



Tern
HL
Ft.
H2O
16.2



18.5



23.1




21.9



47.4



18.5




18.5



linal
Turb.
TU
0.11



0.14



0.09




0.18



0.14



0.21




0.08



Run
Length, Mrs.
(Time to
Sample)
27.5



29.08
(9.9)


28.52
(27.5)



27.52



22.33
(13.8)


33.42




45.42
(21.5)



-------
      APPENDIX C-4  (CONTINUED)
Run
No. Date
46



47



48



J.M.
49



E.P.
SO



E.P.
51



52
S3
5/1



8/1



8/6



Hyfk
8/8



FW-2
8/8



FW-5
8/13



Run I
Run 1
Filter
rate
gpm/ft2
(m3/m2 day)
1.087
(63.77)


1.005
(58.96)


1.261
(73.98)


Super Cel to s
1.266
(74.28)


1 to second ste
1.173
(68.82)


( to first step o
1.059
(62.13)


erminated, did
erminated, did
Precoat,
Ibs./ft2
545
0.1
512
0.1
545
0.1
512
0.1
545
0.1
512
0.1
:cond ste
545
0.1
uper Cel
0.1
> of prec<
545
0.1
FW-20
0.1
r precoat
FW-50
0.1
iuper Cel
0.1
not prect
not prec<
Precoat,
Ibs.
10OO gal.
VC-F
0.054

0.054
VC-F
0.049

0.049
VC-F
0.050

0.050
> of precoi
VC-M
0.030

0.030
at.
VC-MC
0.038

0.038
J.M. Hyfl
C-M
O.066

0.066
at.
at.
Polymer or
coag. in
precoat,
g./g. of D.E.
—



_



	



t, E.P. FW-50
_




_



i Super Cel to
_





Polymer or
coag. in
precoat,
Ibs
1000 gal.
_



_



_



to body fee<
_




—



second step
—





Other
chem. in
precoat,
Ibs
1000 gal.












, Catfloc I









if precoat.






Body
feed,
mg/l

105.74

0.449

60.94

0.559

42.08

0.532
to raw

58.84

0.533


102.68

0.398
Catflo<

81.06

0.677


Body
feed.
Ib.
1000 gal.
545
0.882
Catfloc B
0.0037
545
0.508
Catfloc B
0.0047
545
0.351
Catfloc B
0.0044
water.
FW-50
0.491
Catfloc B
0.0044

FW-50
0.856
Catfloc B
0.0033
B to raw
FW-50
0.676
Catfloc B
0.0057


B.W. solids,
Ibs
1000 gal.
(B.W. vol. as
% of treated
water)*
0.994



0.609



0.455




0.554




0.935



water.
0.815





Avg. turb.
(Turb. @ time
of sample),
TU
Raw Filter
0.83
;o.87)


1.10



0.61
;0.58)



0.64
;0.68)



1.18




O.64
;o.6o)




0.12
(0.12)


0.13



0.09
(0.07)



0.11
(0.10)



0.20




0*9
(0.09)




ORF
FibersxlO6/!
Raw Filter
\=0.22
C=0.15






^=0.6
C=0.3



A =0.06
C=0.09








A=0.13
C=0.20




A=BDL
C=0.13






A=0.02
C=0.04



A=BDL
C=0.04








A=0.04
C=O.S




NWQL
Amphibole
mg/I
Raw Filter
0.08







0.09




0.05









0.06





<0.002








-------
APPENDIX  C-4  (CONTINUED)
Run
No
J.M.
54
55
56
57
58
J.M.
59
60
61
Date
Celiti
8/13
8/15
8/15
8/16
8/19
Celite
8/20
8/21
Filter
Filter
rate
gpm/ft2
(m3/m2 day)
512 & Alum t
1.040
(61.02)
1.031
(60.49)
1.024
(60.08)
1.069
(62.72)
1.048
(61.49)
512 to body f
1.058
(62.07)
1.088
(63.83)
pump trip out
Precoat,
Ibs./ft2
Soda As
FW-50
0.1
512
0.1
FW-50
0.1
512
0.1
FW-50
0.1
512
0.1
FW-50
0.1
512
0.1
FW-50
0.1
512
0.1
:ed.
FW-50
0.1
512
0.1
FW-50
0.1
512
0.1
during pi
Precoat,
Ibs.
1OOO gal.
i to secon
C-F
0.081
0.081
C-F
0.072
0.072
C-F
0.072
0.072
C-F
0.078
0.078
C-F
0.072
0.072

C-F
0.069
0.069
C-F
0.066
0.066
ecoat, coo
Polymer or
coag. in
precoat,
g./g. of D.E.
step of prec<
Alum
0.01
AI+++
0.01
A1+++
0.01
A1+++
0.01
A1+++
0.01

A1+++
0.01
AI+++
0.01
ed 1 V4 hrs.
Polymer or
coag. in
precoat,
Ibs
1000 gal.
at, J.M. Hyf
0.00081
Alum
0.0079
Alum
0.0079
Alum
0.0086
Alum
0.0080

Alum
0.0076
Alum
0.0073

Other
chem. in
precoat,
Ibs
1000 gal.
o Super Ce
Soda Ash
0.0040
Soda Ash
0.0039
Soda Ash
0.0039
Soda Ash
0.0043
Soda Ash
0.0040

Soda Ash
0.0038
Soda Ash
0.0036

Body
feed,
mg/l
to bo(
23.38
35.12
47.69
73.40
132.25

27.69
43.94

Body
feed,
Ib.
1000 gal.
y feed, no <
Super Cel
0.195
Super Cel
0.293
Super Cel
0.398
Super Cel
0.612
Super Cel
1.103

512
0.231
512
0.366

B.W. solids,
Ibs
1000 gal.
(B.W. vol. as
% of treated
water)a
latfloc B.
0.357
0.448
0.549
0.781
1.260

0.380
0.510

Avg. turb.
(Turb. @ time
of sample),
TU
Raw Filter

0.66
0.71
0.71)
0.60
0.80
0.58

0.77
0.84)
0.72


0.15
0.10
(0.18)
0.10
0.12
0.08

0.09
(0.10)
0.11

ORF
FibersxlO6/!
Raw Filter


A=0.0<
C=0.17




A=0.3(
C=0.72




A=0.04
C=O.04




A=BDL
C-0.17


NWQL
Amphibole
mg/l
Raw Filter


0.06




0.02




<0.003




•C0.003


OMD
FibersxlO6/!
Raw Filter


8.98




25.3




1.53




0.81


Term
HL
Ft.
H2O

11.6
23.1
16.2
20.8
20.8

27.7
22.0

inal
Turb.
TU

0.22
0.18
0.14
0.16
0.18

0.27
0.13

Run
Length, Hrs.
(Time to
Sample)

19.92
22.57
(21.9)
22.75
20.00
21.95

22.83
(14.5)
23.12


-------
APPENDIX  C-4  (CONTINUED)
Run
No. Date
62



E.P.
63



64



65



66



J.M.
67





68





8/22



="W-2
8/23



8/26



8/27



8/27



Hyflc
8/28





8/30





Filter
rate
gpm/ft2
(m3/m2 day)
1.073
(62.95)


i to body feed.
1.061
(62.25)


1.116
(65.48)


1.123
(65.89)


1.002
(58.79)


Super Cel & A
1.044
(61.25)




1.062
(62.31)




Precoat,
Ibs./ft2
FW-50
0.1
512
0.1

FW-50
0.1
512
0.1
FW-50
0.1
512
0.1
FW-50
0.1
512
0.1
FW-50
0.1
512
0.1
um& So
FW-50
0.1
512
0.1


FW-50
0.1
512
0 1


Precoat,
Ibs.
1000 gal.
C-F
0.071

0.071

C-F
0.074

0.074
C-F
0.075

0.075
C-F
0.186

0.186
C-F
0.070

0.070
ia Ash to
C-F
0.072

0.072


C-F
0.040

0 040


Polymer or
coag. in
Precoat,
g./g. of D.E.
A1+++
0.01



A1+++
0.01


A1+++
0.01


A1+++
0.01


A1+++
0.01


>ody feed.
A1+++
0.01




A1+++
0.01




Polymer or
coag. in
precoat,
Ibs
Alum
0.0079



Alum
0.0082


Alum
0.0082


Alum
0.0204


Alum
0.0077



Alum
0.0080




Alum
0.0044




Other
chem. in
precoat,
Ibs
1000 gal.
Soda Ash
0.0039



Soda Ash
0.0049


Soda Ash
0.0041


Soda Ash
0.010


Soda Ash
0.0038



Soda Ash
0.0040




Soda Ash
0.0022




Body
feed,
mg/l

92.57




39.83



80.94



163.45



179.23




27.49

3.021

1.511

52.47

5.769

2.892
Body
feed,
Ib.
1000 gal.
512
0.772



FW-20
0.332


FW-20
0.675


FW-20
1.363


FW-20
1.495



Super Cel
0.229
Alum
0.025
Soda Ash
0.013
Super Cel
0.438
Alum
0.048
Soda Ash
0.024
B.W. solids,
Ibs
1000 gal.
(B.W. vol. as
% of treated
water)3
0.927




0.493



0.836



1.765



1.646




0.424





0.597





Avg. turb.
(Turb. @ time
of sample),
TU
Raw Filter
0.68




0.55
(0.63)


0.48



0.47



0.46




0.48





0.62
0.39)




0.09




0.09
(0.07)


0.08



0.08



0.07




0.05





0.06
(0.05)




ORF
FibersxlO6/!
Raw Filter





A=0.7:
C=0.4^





















A=0.7i
c=o.3:









A=0.02
C=0.59





















A=BDL
C=0.54




NWQL
Amphibole
mg/l
Raw Filter





0.04






















0.07










< 0.003






















< 0.003





UMD
FibersxlO6/!
Raw Filter





17.0






















17 8










17.1






















0.29





Terrr
HL
Ft.
H2O
26.6




20.8



18.5



18.5



15.0




60.1





79.7





inal
Turb.
TU
0.47




0.17



0.10



0.08



0.07




0.05





0.05





Run
Length, Hrs.
(Time to
Sample)
21.77




21.17
(7.4)


20.03



8.0



23.83




22.05





38.83
(21.8)





-------
APPENDIX  C-4   (CONTINUED)
Run
No. Date
69
J.M.
70
71
J.M.
72
J.M.
73
74
9/3
Celitc
9/4
9/5
:elite
9/6
:elite
9/9
9/10
Filter
rate
gpm/ft2
(m3/m2 day)
1.048
(61.49)
512 & Alum,
1.035
(60.72)
1.086
(63.72)
512 & anlonic
1.108
(65.01)
512 & AlumS
1.146
(67.24)
1.131
(66.36)
Precoat,
Ibs./ft2
FW-50
0.1
512
0.1
; Soda Ai
FW-50
0.1
512
0.1
FW-50
0.1
512
0.1
polymer
FW-50
0.1
512
0.1
Soda As
FW-50
0.1
512
0.1
FW-50
0.1
512
0.1
Pre coa t ,
Ibs.
1000 gal
C-F
0.070
0.070
h to body
C-F
0.071
0.071
C-F
0.065
0.065
o second !
C-F
0.067
0.067
itosecom
C-F
0.068
0.068
C-F
0.089
0.089
Polymer or
coag. in
precoat,
g./g. of D E
A1+++
0.01
feed.
Alum
0.01
Alum
0.01
tep of precoat
A-23
0.00003
step of piece
AI+++
0.01
A1+++
0.01
Polymer or
coag. in
precoat,
Ibs
1000 gal.
Alum
0.0077
0.00071
0.00065
2.02X10-6
it, J.M. Hyfl
Alum
0.0074
Alum
0.0098
Other
chem in
precoat,
Ibs
1000 gal.
Soda Ash
0.0038
Soda Ash
0.0039
Soda Ash
0.0036
i Super Ce
Soda Ash
0.0037
Soda Ash
0.0049
Body
feed,
mg/l
91.82
10.09
5.059
28.47
3.126
1.572
41.57
4.568
2.292
27.95
3.072
1.539
to bod
20.51
a. 5678
61.33
0.6102
Body
feed,
Ib.
1000 gal.
Super Cel
0.766
Alum
0.084
Soda Ash
0.042
512
0.237
Alum
0.026
Soda Ash
0.013
512
0.347
Alum
0.038
Soda Ash
0.019
512
0.233
Alum
0.026
Soda Ash
0.013
y feed, Catf
Super Cel
0.171
Catfloc B
0.0047
Super Cel
0.512
Catfloc B
0.0051
B.W. solids,
Ibs
1000 gal.
(B.W. vol. as
% of treated
water)3
1.043
0.424
0.538
0.406
oc B to raw w
0.322
0.710
Avg. turb.
(Turb. @ time
of sample),
TU
Raw Filter
0.63
0.67
0.71)
0.67
0.44
0.51)
ter.
0.50
0.46)
0.56
0.06
0.06
(0.06)
0.06
0.05
(0.08)
0.05
(0.05)
0.05
ORF
I-°ibersxl06/l
Raw Filter
A=1.61
C=0.33
A =0.72
C=0.39
EPA
A=1.4^
C=0.28
A=1.0
C=0.5

A=BDL
C=0.54
A=BDL
C=1.67
Cmcinn
9 A=0.0
) C=0.2
A=BDL
c-i.o

NWQL
Amphibole
mg/l
Raw Filter
0.10
0.07
ti
4
5
0.04
< 0.003
< 0.003
<0.003
UMD
FibersxlO6/!
Raw Filter
30.3
13.6
15.4
0.70
0.26
0.64
Tern
HL
Ft
H20
85.5
88.9
104 0
101.6
32.3
31.2
nnal
Turb.
TU
0.05
0.09
0.1 1
0.03
0.06
0.06
Run
Length, Hr
(Time to
Sample)
22.83
22.6
(4.6)
22.76
22.37
(2.4)
21.5
(3.5)
16.5

-------
APPENDIX  C-4  (CONTINUED)
Run
No. Date
75



J.M.
76



77
78



J.M.
79



80



81



9/11



Celiti
9/12



Pum[
9/13



Aqua
9/16



9/17



9/18



Filter
rate
gpm/ft2
(m3/m2 day)
1.181
(69.29)


512 to bodyi
0.940
(55.15)


Malfunction
1.093
(64.13)


Cel to body fe
1.092
(64.07)


1.120
(65.71)


1.062
(62.31)


Precoat,
Ibs./ft2
FW-50
0.1
512
0.1
;ed, Catf!
FW-50
0.1
512
0.1

FW-50
0.1
512
0.1
:d, Catflc
FW-50
0.1
512
0.1
FW-50
0.1
512
0.1
FW-50
0.1
512
0.1
Precoat,
Ibs.
1000 gal.
C-F
0.067

0.067
>c B to rai
C-F
0.085

0.085

C-F
0.111

0.111
c B to raw
C-F
0.077

0.077
C-F
0.085

0.085
C-F
0.074

0.074
Polymer or
coag. in
Precoat,
g./g. of D.E.
A1+++
0.01


' water.
A1+++
0.01



A1+++
0.01


water.
A1+++
0.01


AI+++-
0.01


A1+++
0.01


Polymer or
coag. in
precoat,
Ibs
Alum
0.0074



Alum
0.0093



Alum
0.012



Alum
0.0085


Alum
0.0093


Alum
0.0081


Other
chem. in
precoat,
Ibs
1000 gal.
Soda Ash
0.0037



Soda Ash
0.0047



Soda Ash
0.0061



Soda Ash
0.0042


Soda Ash
0.0047


Soda Ash
0.0041


Body
feed,
mg/1

1 30.78

0.5786


22.22

0.6605


48.80

0.5983


27.33

0.3323

71.57

0.3455

135.23

0.3094
Body
feed,
Ib.
1000 gal.
Super Cel
1.091
Catfloc B
0.0048

512
0.18S
Catfloc B
0.0055

512
0.407
Catfloc B
0.0050

Aqua Cel
0.228
Catfloc B
0.0028
Aqua Cel
0.597
Catfloc B
0.0029
Aqua Cel
1.128
Catfloc B
0.0026
B.W. solids,
Ibs
1000 gal.
(B.W. vol. as
% of treated
water) a
1.241




0.374




0.652




0.397



0.783



1.290



Avg. turb.
(Turb. @ time
of sample),
TU
Raw Filter
0.68




0.40




0.44
[0.40)



0.42
;0.37)


0.50



0.52



0.06




0.06




0.05
(0.08)



0.05
(0.04)


0.06



0.07



ORF
Fibersxl06/l
Raw Filter










A=0.02
C=0.0«



A=0.9
C=0.1




















A=BDL
C=0.06



A=0.02
C=0.06










NWQL
Amphibole
mg/1
Raw J Filter










0.09




0.08





















•C0.003




<0.003











UMD
FibersxlO6/!
Raw FUter










30.0




20.3





















0.51




0.81











Term
HL
Ft.
H2O
23.1




13.9




32.3




25.4



18.5



18.5



mal
Turb.
TU
0.04




0.06




0.04




0.06



0.05



0.07



Run
Length, Hrs.
(Time to
Sample)
21.05




20.92




13.75
(1.7)



19.83
(1.5)


17.53



21.28




-------
      APPENDIX C-4   (CONTINUED)
Run
No. Date
J.M.
82




83
84
J.M.
85





86





Celitt
9/19




Run
Run
"elite
9/20





9/20





Filter
rate
gpm/ft2
(m3/m2 day)
512 & Mam t
1.054
(61.84)



erminated due
erminated due
503 & Alum i
1.069
(62.72)




1.043
(61.19)




Precoat,
Ibs./ft2
Soda As
FW-50
0.1

512
0.1

to overh«
to overhi
Soda As
FW-50
0.1

512
01
fi

FW-50
0.1

512
0.1


Precoat,
Ibs.
1OOO gal.
i to body
C-F
0.238

0.238

ated moto
ated mote
i to body
C-F
0.153

0.1 53


C-F
O.143

0.143


Polymer or
coag. in
precoat,
g./g. of D.E.
eed, no Catflc
A1+++
0.01





eed.
A1+++
0.01




A1+++
0.01




Polymer or
coag. in
precoat,
Ibs
1000 gai.
cB.
Alum
0.026






Alum
0.017




Alum
0.016




Other
chem. in
precoat,
Ibs
1000 gal.

Soda Ash
0.013






Soda Ash
0.0084




Soda Ash
0.0079




Body
feed,
mg/l


97.15

10.68

5.35




61.10

6.716

3.365

62.93

6.917

3.465
Body
feed,
Ib.
1000 gal.

512
0.810
Alum
0.089
Soda Ash
0.045



503
0.510
Alum
0.056
Soda Ash
0.028
503
0.525
Alum
0.058
^>oda Ash
0.029
B.W. solids,
Ibs
1000 gal.
(B.W. vol. as
% of treated
water)3

1.460







0.925





0.921





Avg. turb.
(Turb. @ time
of sample),
TU
Raw Filter

0.53







0.45





0.49






0.06







0.05





0.06





ORF
FibersxlO*/!
Raw Filter

A=







A=1.3
C=0.2



















A=0.02
C=0.33










NWQL
Amphibole
mg/l
Raw Filter









0.07




















0.003











UMD
FibersxlO6/!
Raw 1 Filter









19.1




















0.45











Tern
HL
Ft.
H20

101.6







46.2





37.0





linal
Turb.
TU

0.05







0.05





0.06





Run
Length, Hrs.
(Time to
Sample)

6.62







10.2
(S.S)




11.17





00
    a B.W. volume was not measured.
    k A=amphibole, C=chrysotile

-------
                                   TECHNICAL REPORT DATA
                            (Please read Instructions on the reverse before completing)
1 REPORT NO.
      EPA-670/2-75-050C
                                                           3. RECIPIENT'S ACCESSIOWNO.
4. TITLE ANDSUBTITLE
  DIRECT FILTRATION  OF  LAKE SUPERIOR WATER
  FOR ASBESTIFORM  FIBER REMOVAL
  Appendixes B and C
                                                          5. REPORT DATE
                                                           June 1975; Issuing  Date
                                                          6. PERFORMING ORGANIZATION CODE
7. AUTHOR(S)
                                                           8. PERFORMING ORGANIZATION REPORT NO.
  Black £ Veatch, Consulting Engineers
9. PERFORMING ORGANIZATION NAME AND ADDRESS

  Black £ Veatch, Consulting Engineers
  1500 Meadow Lake  Parkway
  Kansas City, Missouri   64114
                                                          10. PROGRAM ELEMENT NO.
                                                           1CB047; ROAP 21AQB; Task 024
                                                          11. CONTRACT/feWWKW NO.
                                                           DACW 37-74-C-0079
                                                           IAG #EPA-IAG-D4-0388
12. SPONSORING AGENCY NAME AND ADDRESS
  National Environmental  Research Center
  Office of Research  and  Development
  U.S.  Environmental  Protection Agency
  Cincinnati, Ohio  45268
                                                          13. TYPE OF REPORT AND PERIOD COVERED
                                                           Final
                                                          14. SPONSORING AGENCY CODE
15. SUPPLEMENTARY NOTES
  This work conducted  through interagency agreement  between EPA Region V  and the Corps
  of Engineers, St. Paul  District.  See also EPA-670/2-75-050a, b, d, e,  f,  and g.
16. ABSTRACT
  Pilot plant research  conducted in 1974 at Duluth,  Minnesota, demonstrated that
  asbestiform fiber counts  in Lake Superior water  could be effectively reduced by
  municipal filtration  plants.   During the study,  engineering data were  also obtained
  for making cost estimates  for construction and operation of both granular and
  diatomaceous earth  (DE) filtration plants ranging  in size from 0.03 to 30 mgd.
  Appendix B contains information on the pilot filters used in the study.   Data are
  presented on the physical  aspects of the units  (dimensions and equipment  configura-
  tion) and on the manner in which the filters were  operated.  Appendix  C contains
  data obtained during  the  individual pilot plant  filter runs.  This kind of informatior
  will be useful to persons  needing to know about  specific conditions such  as  raw water
  turbidity,  filtration rate,  and chemical doses or  diatomaceous earth types and amounts
  used for precoat or body  feed.
17.
                                KEY WORDS AND DOCUMENT ANALYSIS
                  DESCRIPTORS
                                              b.lDENTIFIERS/OPEN ENDED TERMS
                                               Mixed media  filtration
                                               Diatomaceous earth fil-
                                                 tration
                                               Asbestiform
                                               Chrysotile
                                               Fiber removal
                                               Duluth  (Minnesota)
                                               Lake Superior	
                                                                       c.  COSATI Field/Group
Asbestos
Amphiboles
Serpentine
Water supply
Filtration
Water treatment
Pilot plants
13B
13. DISTRIBUTION STATEMENT
 RELEASE  TO  PUBLIC
                                              19. SECURITY CLASS (ThisReport)
                                                   UNCLASSIFIED
                                                                       21. NO. OF PAGES
                                                                              75
                                            20. SECURITY CLASS (Thispage)
                                                  UNCLASSIFIED
                                                                         22. PRICE
EPA Form 2220-1 (9-73)
                                            69
                                                   U. S. GOVERNMENT PRINTING OFFICE: 1975-657-59V5396  Region No. 5-II

-------