PB8 3-121749
EPA-600/2-82-087b
October 1982
FEASIBILITY STUDY OF GRANULAR ACTIVATED
CARBON ADSORPTION AND ON-SITE REGENERATION
Volume 2. Supplemental Figures and Data.
Richard Miller
David J. Hartman
Cincinnati Water Works
Cincinnati, Ohio 45232
Cooperative Agreement No. CR805443
Project Officers
Jack DeMarco and Ben W. Lykins, Jr.
Drinking Water Research Division
Municipal Enviromental Research Laboratory
Cincinnati, Ohio 45268
MUNICIPAL ENVIRONMENTAL RESEARCH LABORATORY
OFFICE OF RESEARCH AND DEVELOPMENT
U. S. ENVIRONMENTAL PROTECTION AGENCY
CINCINNATI, OHIO 45268
KPROOUCfD 8Y ~'"
NATIONAL TECHNICAL
INFORMATION SERVICE
U.S. DEPMnKNI OF COMMOCt
sNtuKfitio,M am
-------
TECHNICAL REPORT DATA
(Please read Instructions on the reverse before completing)
1. REPORT NO.
EPA-600/2-82-087b
3. RECIPIENT'S ACCESSION NO.
4. TITLE AND SUBTITLE
Feasibility Study of Granular Activated Carbon and
On-Site-Regeneration
Volume 2. Supplemental Figures and Data.
5. REPORT DATE
October 1982
6. PERFORMING ORGANIZATION CODE
7. AUTHORIS)
Richard Miller, David J. Hartman
8. PERFORMING ORGANIZATION REPORT NO.
9. PERFORMING ORGANIZATION NAME AND ADDRESS
Cincinnati Water Works
4747 Spring Grove
Cincinnati, Ohio 45232
10. PROGRAM ELEMENT NO.
11. CONTRACT/GRANT NO.
CR805443
12. SPONSORING AGENCY NAME AND ADDRESS
13. TYPE OF REPORT AND PERIOD COVERED
Municipal Environmental Research Laboratory - Cin., OH
Office of Research and Development
U.S. Environmental Protection Agency
Cincinnati, Ohio 45268
Final
14. SPONSORING AGENCY CODE
EPA/600/14
15. SUPPLEMENTARY NOTES
Project Officer: Ben W. Lykins, Jr. (513-684-7460)
16. ABSTRACT
Most research pertaining to water quality and treatment methods conducted in the
United States in the last decade utilized pilot-scale components. This project em-
ployed full-sized filters, post-filtration contactors and carbon regeneration furnace
at one site to study carbon's ability to remove organics from Ohio River Water.
Various GAC bed depths and types were studied in order to compare organic removal
efficiencies, bed lives, general water quality characteristics, the need of a sand
underlayer and operational problems. Pilot-scale GAC components were also used to
determine the reliability of pilot columns as indicators of the performance of full-
scale components. The relative performance of lignite and bituminous-based GAC was
also studied in pilot columns.
In the most important phase of this project, the relative performance of GAC filters
to post-filtration GAC contactors was studied along with the most advantageous empty
bed contact time for the GAC contactors and the effectiveness of on-site GAC regener-
ation. Finally, a significant aspect of this project was the development of prelim-
inary cost estimates for full-plant conversion to GAC.
Volume I is the detailed report. Volume II includes data graphs not included in
Volume I and microfilm images of all raw data developed under the project.
KEY WORDS AND DOCUMENT ANALYSIS
DESCRIPTORS
b.lDENTIFIERS/OPEN ENDED TERMS
c. COSATI Field/Group
18. DISTRIBUTION STATEMENT
Release to Public
19, SECURITY CLASS (This.Report)
Unclassified
21. NO. OF PAGES
20..SECU-RHTY CLASS (This fage.j
Unclassified
22. PRICE
EPA Form 2220-1 (9-73)
-------
NOTICE
This document has been reviewed in accordance with
U.S. Environmental Protection Agency policy and
approved for publication. Mention of trade names
or commercial products does not constitute endorse-
ment or recommendation for use.
11
-------
FOREWORD
The U.S. Environmental Protection Agency was created because of increas-
ing public and government concern about the dangers of pollution to the
health and welfare of the American people. Noxious air, foul water, and
spoiled land are tragic testimonies to the deterioration of our natural
environment. The complexity of that environment and the interplay of its
components require a concentrated and integrated attack on.the problem.
Research and development is that necessary first step -in problem
solution; it involves defining the problem, measuring its impact, and
searching for solutions. The Municipal Environmental Research Laboratory
develops new and improved technology and systems to prevent., treat, and
manage wastewater and solid and hazardous waste pollutant discharges from
municipal and community sources, to preserve and treat public drinking water
supplies, and to minimize the adverse economic, social, health, and aesthetic
effects of pollution. This publication is one of the products of that
research and provides a most vital communication link between the researcher
and the user community.
This report presents the results of a field-scale research effort to
evaluate granular activated carbon (GAG) adsorption and on-site fluidized
bed reactivation. GAC units consisting of converted sand filters and
contactors were studied to determine their performance relative to virgin
and reactivated granular carbon. Extensive organic analyses were performed
along with general water treatment plant parameters. Cost of GAC treatment
and reactivation were collected and preliminary cost estimates of full-scale
plant conversion to GAC were developed.
Francis T. Mayo
Director
Municipal Environmental Research Laboratory
111
-------
ABSTRACT
This project determines whether the use of granular activated carbon (GAG)
is feasible for removing certain trace organics from Ohio River water while
treating it for human consumption. The study used either deep-bed contact-
ors or conventional-depth gravity filters and on-site GAC regeneration. To
be considered feasible, the facility had to be able to remove selected
organics to a predesignated level at a cost acceptable to consumers without
adversely affecting the level of treatment provided by the existing plant.
A secondary objective was to develop plant design and operating parameters
for full-scale plant conversion to GAC treatment. The study was unusual in
that it employed full-sized filters, contactors, and carbon regeneration
furnace instead of the pilot-scale components used by most water quality
researchers.
In the first phase of the project, three existing rapid sand filters
were converted to GAC filter adsorbers. Various GAC bed depths and types
were studied to compare organic removal efficiencies, bed lives, general
water quality characteristics, the need of a sand underlayer and operational
problems.
The second phase involved the use of pilot-scale GAC components to investi-
gate the effects of regeneration on the carbon's adsorptive capability and
to determine the reliability of pilot column as performance indicators for
full-scale components. The relative performances of lignite and bituminous-
based GAC were also studied.
The last phase of this project studied the relative performance of GAC
filters to post-filtration GAC contactors, the most advantageous empty bed
contact time for the contactors and the effectiveness of on-site GAC regener-
ation. Pilot columns were also operated in parallel with the full-sized
units to assess the usefulness of pilot columns as predictors of full-scale
operation. During this phase, an attempt was made to maximize the use of
currently available organic analysis techniques. Additional organic analyti-
cal techniques such as acid extract GC/FID profiles, Grob closed loop strip-
ping analyses and carbon-adsorbable organohalides provided a broad data
base. Finally, a significant aspect of this project was the development of
preliminary cost estimates for full-plant conversion to GAC.
This report was submitted in fulfillment of Cooperative Agreement
No. CR805443 by the Cincinnati Water Works under the sponsorship of the U.S.
Environmental Protection Agency. This report covers the period from
August, 1977 to May, 1982, and work was completed as of April, 1982.
IV
-------
FIGURES
Number Page
THM formation potential (FTTT) breakthrough curves for GAG
Filter 19A, Phase 1-0
THM formation potential (FTTT) breakthrough curves for GAG
Filter 21A, Phase 1-0
THM formation potential (FTTT) breakthrough curves for GAG
Filter 21A, Phase 3-1
THM formation potential (FTT.T) breakthrough, curves for, GAG
Filter 21A, Phase 3-2 . Y '
5 THM formation potential (FTTT) breakthrough curves for-GAG
Filter 21A, Phase 3-3
THM formation potential (FTTT) breakthrough curves for GAG
Filter 23A, Phase 1-0
7 THM formation potential (FTTT) breakthrough curves for
Contactor A, Phase 3-0
THM formation potential (FTTT) breakthrough curves for
Contactor A, Phase 3-1
THM formation potential (FTTT) breakthrough curves for
Contactor A, Phase 3-2
10 THM formation potential (FTTT) breakthrough curves for
Contactor B, Phase 3-0 10
11 THM formation potential (FTTT) breakthrough curves for
Contactor BB, Phase 3-0 11
12 THM formation potential (FTTT) breakthrough curves for
Contactor BB, Phase 3-1 12
13 THM formation potential (FTTT) breakthrough curves for
Contactor C, Phase 3-0 13
14 THM formation potential (FTTT) breakthrough curves for
Contactor C, Phase 3-1 14
15 THM formation potential (FTTT) breakthrough curves for
Contactor C, Phase 3-2 15
16 THM formation potential (FTTT) breakthrough curves for
Contactor D, Phase 3-1 16
-------
17 THM formation potential (FTTT) breakthrough curves for
Contactor D, Phase 3-2 17
18 THM formation potential (FTTT) breakthrough curves for
bituminous pilot contactors, Phase 2-0 18
19 THM formation potential (FTTT) breakthrough curves for
bituminous pilot contactors, Phase 3-0 19
20 THM formation potential (FTTT) break-through curves for
pilot contactors, Phase 3-1 20
21 THM formation potential (FTTT) breakthrough curves for
pilot contactor^, Phase 3-2 21
22 THM formation potential (FTTT) breakthrough curves for
lignite pilot contactors, Phase 2-0 22
23 Instantaneous chloroform (ICLR) breakthrough curves for GAG
Filter 19A, Phase 1-0 23
24 Instantaneous chloroform (ICLR) breakthrough curves for GAC
Filter 21A, Phase 1-0 24
25 Instantaneous chloroform (ICLR) breakthrough curves for GAC
Filter 21A, Phase 3-1 25
26 Instantaneous chloroform (ICLR) breakthrough curves for GAC
Filter 21A, Phase 3-2 26
27 Instantaneous chloroform (ICLR) breakthrough curves for GAC
Filter 21A, Phase 3-3 27
28 Instantaneous chloroform (ICLR) breakthrough curves for GAC
Filter 23A, Phase 1-0 28
29 Instantaneous chloroform (ICLR) breakthrough curves for
Contactor A, Phase 3-0 29
30 Instantaneous chloroform (ICLR) breakthrough curves for
Contactor A, Phase 3-1 30
31 Instantaneous chloroform (ICLR) breakthrough curves for
Contactor A, Phase 3-2 31
32 Instantaneous chloroform (ICLR) breakthrough curves for
Contactor B, Phase 3-0
33 Instantaneous chloroform (ICLR) breakthrough curves for
Contactor BB, Phase 3-0 33
VI
-------
34 Instantaneous chloroform (ICLR) breakthrough curves for
Contactor .BB, Phase 3-1 34
35 Instantaneous chloroform (ICLR) breakthrough curves for
Contactor C, Phase 3-0 35
36 Instantaneous chloroform (ICLR) breakthrough curves for
Contactor C, Phase 3-1 36
37 Instantaneous chloroform (ICLR) breakthrough curves for
Contactor C, Phase 3-2 .37
38 Instantaneous chloroform (ICLR) breakthrough curves for
Contactor D, Phase 3-1 . 38
39 Instantaneous chloroform (ICLR) breakthrough curves for
Contactor D, Phase 3-2 39
40 Instantaneous chloroform (ICLR) breakthrough curve for
bituminous pilot contactor, Phase 2-0. 40
41 Instantaneous chloroform (ICLR) breakthrough curves for
bituminous pilot contactors, Phase 2-0 41
42 Instantaneous chloroform (ICLR) breakthrough curves for
pilot contactors, Phase 3-0 42
43 Instantaneous chloroform (ICLR) breakthrough curves for
pilot contactors, Phase 3-1 43
44 Instantaneous chloroform (ICLR) breakthrough curves for
pilot contactors, Phase 3-2 44
45 Instantaneous chloroform (ICLR) breakthrough curves for
lignite pilot contactors, Phase 2-0 45
46 Instantaneous chloroform (ICLR) breakthrough curves for
virgin pilot GAC filter. Phase 1-0 46
47 Instantaneous chloroform (ICLR) breakthrough curve for
virgin pilot GAC filter, Phase 2-1 47
48 Instantaneous chloroform (ICLR) breakthrough curve for
virgin pilot GAC filter, Phase 2-2 48
49 Instantaneous bromodichloromethane (ICL2) breakthrough
curves for GAC Filter 19A, Phase 1-0 49
50 Instantaneous bromodichloromethane (ICL2) breakthrough
curves for GAC Filter 21A, Phase 1-0 50
vii
-------
51 Instantaneous bromodichloromethane (ICL2) breakthrough
curves for GAG Filter 21A, Phase 3-1
52 Instantaneous bromodichloromethane (ICL2) breakthrough
curves for GAG Filter 21A, Phase 3-2 52
53 Instantaneous bromodichloromethane (ICL2) breakthrough
curves for GAG Filter 21A, Phase 3-3 53
54 Instantaneous bromodichloromethane (ICL2) breakthrough
curves for GAG Filter 23A, Phase 1-0 54
55 Instantaneous bromodichloromethane (ICL2) breakthrough
curves for Contactor A, Phase 3-0 55
56 Instantaneous bromodichloromethane (ICL2) breakthrough
curves for Contactor A, Phase 3-1 55
57 Instantaneous bromodichloromethane (ICL2) breakthrough
curves for Contactor A, Phase 3-2 57
58 Instantaneous bromodichloromethane (ICL2) breakthrough
curves for Contactor B, Phase 3-0 53
59 Instantaneous bromodichloromethane (ICL2) breakthrough
curves for Contactor BB, Phase 3-0 59
60 Instantaneous bromodichloromethane (ICL2) breakthrough
curves for Contactor BB, Phase 3-1 60
61 Instantaneous bromodichloromethane (ICL2) breakthrough
curves for Contactor C, Phase 3-0 61
62 Instantaneous bromodichloromethane (ICL2) breakthrough
curves for Contactor C, Phase 3-1 62
63 Instantaneous bromodichloromethane (ICL2) breakthrough
curves for Contactor C, Phase 3-2 63
64 Instantaneous bromodichloromethane (ICL2) breakthrough
curves for Contactor D, Phase 3-1 64
65 Instantaneous brcraodichloromethane (ICL2) breakthrough
curves for Contactor D, Phase 3-2 65
66 Instantaneous bromodichloromethane (ICL2) breakthrough
curves for bituminous pilot contactors, Phase 2-0. ... 66
67 Instantaneous bromodichloromethane (ICL2) breakthrough
curves for pilot contactors, Phase 3-0 67
-------
68 Instantaneous bromodichloromethane (ICL2) breakthrough
curves for pilot contactors. Phase 3-1 68
69 Instantaneous bromodichloromethane (ICL2) breakthrough
curves for pilot contactors, Phase 3-2 69
70 Instantaneous bromodichloromethane (ICL2) breakthrough
curves for lignite pilot contactors, Phase 2-0 70
71 Instantaneous bromodichloromethane (ICL2) breakthrough
curves for virgin pilot GAC filter, Phase 1-0 71
72 Instantaneous bromodichloromethane (ICL2) breakthrough
curve for bituminous pilot contactor, Phase 2-0» .... • 72
73 Instantaneous bromodichloromethane (ICL2) breakthrough
curve for virgin pilot GAC filter, Phase 2-1 . . . .
74 Instantaneous bromodichloromethane (ICL2) breakthrough
curve for virgin pilot GAC filter,. Phase 2-2 . . . .
75 Instantaneous THM (ITTT) breakthrough curves for GAC
Filter 19A, Phase 1-0 75
76 Instantaneous THM (ITTT) breakthrough curves for GAC
Filter 21A, Phase 1-0 76
77 Instantaneous THM (ITTT) breakthrough curves for GAC
Filter 21A, Phase 3-1 77
78 Instantaneous THM (ITTT) breakthrough curves for GAC
Filter 21A, Phase 3-2 78
79 Instantaneous THM (ITTT) breakthrough curves for GAC
Filter 21A, Phase 3-3 "9
80 Instantaneous THM (ITTT) breakthrough curves for GAC
Filter 23A, Phase 1-0 80
81 Instantaneous THM (ITTT) breakthrough curves for
Contactor A, Phase 3-0 81
82 Instantaneous THM (ITTT) breakthrough curves for
Contactor A, Phase 3-1 82
83 Instantaneous THM (ITTT) breakthrough curves for
Contactor A, Phase 3-2 83
84 Instantaneous THM (ITTT) breakthrough curves for
Contactor B, Phase 3-0 84
.IX
-------
85 Instantaneous THM (ITTT) breakthrough curves for
Contactor BB, Phase 3-0 ................. 85
86 Instantaneous THM (ITTT) breakthrough curves for'
Contactor BB, Phase 3-1 ................. 36
87 Instantaneous THM (ITTT) breakthrough curves for :
Contactor C, Phase 3-0 ............. • . • • S"7
88 Instantaneous THM (ITTT) breakthrough curves for
Contactor C, Phase 3-1 ................. 88
89 Instantaneous THM (ITTT) breakthrough curves for
Contactor C, Phase 3-2 ................. 29
90 Instantaneous THM (ITTT) breakthrough curves for
Contactor D, Phase 3-0 ................. 90
91 Instantaneous THM (ITTT) breakthrough curves for
Contactor D, Phase 3-1 ................. 91
92 Instantaneous THM (ITTT) breakthrough curves for
Contactor D, Phase 3-2 ................. 92
93 Instantaneous THM (ITTT) breakthrough curves for
bituminous pilot contactors, Phase 2-0 ......... 93
94 Instantaneous THM (ITTT) breakthrough curves for
pilot contactors, Phase 3-0 ............... 94
95 Instantaneous THM (ITTT) breakthrough curves for
pilot contactors, Phase 3-1 ............... 95
96 Instantaneous THM (ITTT) breakthrough curves for
pilot contactors, Phase 3-2 ............... 96
97 Instantaneous THM (ITTT) breakthrough curves for
lignite pilot contactors, Phase 2-0 ........... 97
98 Instantaneous THM (ITTT) breakthrough curves for
virgin pilot GAC filter, Phase 1-0 98
99 Three-day simulated distribution system THM (STT3)
breakthrough curves for GAC Filter 21A, Phase 3-1. ... 99
100 Three-day simulated distribution system THM (STT3)
breakthrough curves for GAC Filter 21A, Phase 3-2. . . . 100
101 Three-day simulated distribution system THM (STT3)
breakthrough curves for GAC Filter 21A, Phase 3-3. . . . 101
-------
102 Three-day simulated distribution system THM (STT3)
breakthrough curves for Contactor A, Phase 3-0
103 Three-day simulated distribution system THM (STT3)
breakthrough curves for Contactor A, Phase 3-1 103
104 Three-day simulated distribution system THM (STT3)
breakthrough curves for Contactor A, Phase 3-2 104
105 Three-day simulated distribution system THM (STT3)
breakthrough curves for Contactor B, Phase 3-0 105
106 Three-day simulated distribution system THM (STT3)
breakthrough curves for Contactor BB, Phase, 3-0; • ." . '. ". "- 106
107 Three-day simulated distribution system THM ('STT3)
breakthrough curves for Contactor BB, Phase 3-1 107
108 Three-day simulated distribution system THM (STT3)
breakthrough curves for Contactor C, Phase 3-0
109 Three-day simulated distribution system THM (STT3)
breakthrough curves for Contactor C, Phase 3-1 109
110 Three-day simulated distribution system THM (STT3)
breakthrough curves for Contactor C, Phase 3-2 110
111 Three-day simulated distribution system THM (STT3)
breakthrough curves for Contactor D, Phase 3-1 Ill
112 Three-day simulated distribution system THM (STT3)
breakthrough curves for Contactor D, Phase 3-2 112
113 Three-day simulated distribution system THM (STT3)
breakthrough curves for pilot contactors, Phase 3-0. . . 113
114 Three-day simulated distribution system THM (STT3)
breakthrough curves for pilot contactors, Phase 3-1. . . 114
115 Three-day simulated distribution system THM (STT3)
breakthrough curves for pilot contactors, Phase 3-2. . . 115
116 Seven-day simulated distribution system THM (STT7)
breakthrough curves for GAG Filter 19A, Phase 1-0. . . . 116
117 Seven-day simulated distribution system THM (STT7)
breakthrough curves for GAC Filter 21A, Phase 1-0. . . . 117
118 Seven-day simulated distribution system THM (STT7)
breakthrough curves for GAC Filter 23A, Phase 1-0. . . . 118
-------
119 Seven-day simulated distribution system THM (STT7)
breakthrough curves for bituminous pilot contactors,
Phase 2-0 .
120 Seven-day simulated distribution system THM (STT7)
breakthrough curves for lignite pilot contactors,
Phase 2-0 120
121 Seven-day simulated distribution system THM (STT7)
breakthrough curves for virgin pilot GAC filter,
Phase 1-0 121
122 Total organic carbon (TOC) breakthrough curves for GAC
Filter 19A, Phase 1-0 122
123 Total organic carbon (TOC) breakthrough curves for GAC
Filter 21A, Phase 1-0 123
124 Total organic carbon (TOC) breakthrough curves for GAC
Filter 21A, Phase 3-1
125 Total organic carbon (TOC) breakthrough curves for GAC
Filter 21A, Phase 3-2 125
126 Total organic carbon (TOC) breakthrough curves for GAC
Filter 21A, Phase 3-3 126
127 Total organic carbon (TOC) breakthrough curves for GAC
Filter 23A, Phase 1-0 127
128 Total organic carbon (TOC) breakthrough curves for
Contactor A, Phase 3-0 128
129 Total organic carbon (TOC) breakthrough curves for
Contactor A, Phase 3-1 129
130 Total organic carbon (TOC) breakthrough curves for
Contactor A, Phase 3-2 130
131 Total organic carbon (TOC) breakthrough curves for
Contactor B, Phase 3-0 131
132 Total organic carbon (TOC) breakthrough curves for
Contactor BB, Phase 3-0 132
133 Total organic carbon (TOC) breakthrough curves for
Contactor BB, Phase 3-1 133
134 Total organic carbon (TOC) breakthrough curves for
Contactor C, Phase 3-0 134
XI1
-------
135 Total organic carbon (TOC) breakthrough curves for
Contactor C, Phase 3-1 135
136 Total organic carbon (TOC) breakthrough curves for
Contactor C, Phase 3-2 136
137 Total organic carbon (TOC) breakthrough curves for
Contactor D, Phase 3-1 137
138 Total organic carbon (TOC) breakthrough curves for
Contactor D, Phase 3-2 138
139 Total organic carbon (TOC) breakthrough curves for
bituminous pilot contactors, Phase'2-0 . • .-.- . . . . •• .. 139
140 Total organic carbon (TOC) breakthrough curves for - • .
pilot contactors, Phase 3-0 140
141 Total organic carbon (TOC) breakthrough curves for "
pilot contactors, Phase 3-1 141
142 Total organic carbon (TOC) breakthrough curves for
pilot contactors, Phase 3-2 142
143 Total organic carbon (TOC) breakthrough curves for
lignite pilot contactors, Phase 2-0 143
144 Total organic carbon (TOC) breakthrough curves for
virgin pilot GAG filter, Phase 1-0 144
145 Carbon adsorbable organohalides (CAOX) percent removal
curves for Contactor D, Phase 3-0 145
146 THM formation potential (FTTT) percent removal curves for
GAC Filter 19A, Phase 1-0 146
147 THM formation potential (FTTT) percent removal curves for
GAC Filter 21A, Phase 1-0 147
148 THM formation potential (FTTT) percent removal curves for
GAC Filter 23A, Phase 1-0 148
149 THM formation potential (FTTT) percent removal curves for
Contactor A, Phase 3-0 149
150 THM formation potential (FTTT) percent removal curves for
Contactor A, Phase 3-1 150
151 THM formation potential (FTTT) percent removal curves for
Contactor A, Phase 3-2 151
-------
152 THM formation potential (FTTT) percent removal curves for
Contactor B, Phase 3-0 152
153 THM formation potential (FTTT) percent removal curves for
Contactor BB, Phase 3-0 153
154 THM formation potential (FTTT) percent removal curves for
Contactor BB, Phase 3-1 154
155 THM formation potential (FTTT) percent removal curves for
Contactor C, Phase 3-0 155
156 THM formation potential (FTTT) percent removal curves for
Contactor C, Phase 3-1 156
157 THM formation potential (FTTT) percent removal curves for
Contactor C, Phase 3-2 157
158 THM formation potential (FTTT) percent removal curves for
Contactor D, Phase 3-0 158
159 THM formation potential (FTTT) percent removal curves for
Contactor D, Phase 3-1 159
160 THM formation potential (FTTT) percent removal curves for
Contacror D, Phase 3-2 160
161 THM formation potential (FTTT) percent removal curves for
bituminous pilot contactors, Phase 2-0 161
162 THM formation potential (FTTT) percent removal curves for
pilot contactors, Phase 3-0 162
163 THM formation potential (FTTT) percent removal curves for
pilot contactors, Phase 3-1 163
164 THM formation potential (FTTT) percent removal curves for
pilot contactors, Phase 3-2 164
165 THM formation potential (FTTT) percent removal curves for
lignite pilot contactors, Phase 2-0 165
166 Instantaneous chloroform (ICLR) percent removal curves for
GAC Filter 19A, Phase 1-0 166
167 Instantaneous c. loroform (ICLR) percent removal curves for
GAC Filter 21A, Phase 1-0 167
168 Instantaneous chloroform (ICLR) percent removal curves for
GAC Filter 23A, Phase 1-0 168
xiv
-------
169 Instantaneous chloroform (ICLR) percent removal curves for
Contactor A, Phase 3-0 169
170 Instantaneous chloroform (ICLR) percent removal curves for
Contactor A, Phase 3-1 170
171 Instantaneous chloroform (ICLR) percent removal curves for
Contactor A, Phase 3-2
172 Instantaneous chloroform (ICLR) percent removal curves for
Contactor B, Phase 3-0 173
173 Instantaneous chloroform (ICLR) percent removal curves'for
Contactor BB, Phase 3-0 173
174 Instantaneous chloroform (ICLR) percent removal curves for
Contactor BB, Phase 3-1 174
175 Instantaneous chloroform (ICLR) percent removal curves for
Contactor C, Phase 3-0 175
176 Insrantaneous chloroform (ICLR) percent removal curves for
Contactor C, Phase 3-1 176
177 Instantaneous chloroform (ICLR) percent removal curves for
Contactor C, Phase 3-2 177
178 Instantaneous chloroform (ICLR) percent removal curves for
Contactor D, Phase 3-0 178
179 Instantaneous chloroform (ICLR) percent removal curves for
Contactor D, Phase 3-1 179
180 Instantaneous chloroform (ICLR) percent removal curves for
Contactor D, Phase 3-2 180
181 Instantaneous chloroform (ICLR) percent removal curves for
bituminous pilot contactors, Phase 2-0 181
182 Instantaneous chloroform (ICLR) percent removal curves for
pilot contactors, Phase 3-0 132
183 Instantaneous chloroform (ICLR) percent removal curves for
pilot contactors, Phase 3-1 183
184 Instantaneous chloroform (ICLR) percent removal curves for
pilot contactors, Phase 3-2 184
185 Instantaneous chloroform (ICLR) percent removal curves for
lignite pilot contactors, Phase 2-0 185
-------
186 Instantaneous chloroform (ICLR) percent removal curves for
virgin pilot GAC filter. Phase 1-0 186
187 Instantaneous bromodichloromethane (ICL2) percent removal
curves for GAC Filter 19A, Phase 1-0 187
188 Instantaneous bromodichloromethane (ICL2) percent removal
curves for GAC Filter 2lA, Phase 1-0 188
189 Instantaneous bromodichloromethane (ICL2) percent removal
curves for GAC Filter 23A, Phase 1-0 189
190 Instantaneous hromodichloromethane (ICL2) percent removal
curves for Contactor A, Phase 3-0 190
191 Instantaneous bromodichloromethane (ICL2) percent removal
curves for Contactor A, Phase 3-1 191
192 Instantaneous bromodichloromethane (ICL2) percent removal
curves for Contactor A, Phase 3-2 192
193 Instantaneous bromodichloromethane (ICL2) percent removal
curves for Contactor B, Phase 3-0 193
194 Instantaneous bromodichloromethane (ICL2) percent removal
curves for Contactor BB, Phase 3-0 194
195 Instantaneous bromodichloromethane (ICL2) percent removal
curves for Contactor BB, Phase 3-1 195
196 Instantaneous bromodichloromethane (ICL2) percent removal
curves for Contactor C, Phase 3-0 196
197 Instantaneous bromodichloromethane (ICL2) percent removal
curves for Contactor C, Phase 3-1. 197
198 Instantaneous bromodichloromethane (ICL2) percent removal
curves for Contactor C, Phase 3-2 198
199 Instantaneous bromodichloromethane (ICL2) percent removal
curves for Contactor D, Phase 3-0 199
200 Instantaneous bromodichloromethane (ICL2) percent removal
curves for Contactor D, Phase 3-1 200
201 Instantaneous b omodichloromethane (ICL2) percent removal
curves for Contactor D, Phase 3-2 201
202 Instantaneous bromodichloromethane (ICL2) percent removal
curves for bituminous pilot contactors, Phase 2-0. . . . 101
xvi
-------
203 Instantaneous bromodichloromethane (ICL2) percent removal
curves for pilot contactors, Phase 3-0 203
204 Instantaneous bromodichloromethane (ICL2) percent removal
curves for pilot contactors, Phase 3-1 204
205 Instantaneous bromodichloromethane (ICL2) percent removal
curves for pilot contactors, Phase 3-2 205
206 Instantaneous bromodichloromethane (ICL2) percent removal
curves for lignite pilot contactors, Phase 2-0 206
207 Instantaneous bromodichloromethane (ICL2) percent removal
curves for virgin pilot GAC filter, Phase 1-0 - 207
208 Instantaneous THM (ITTT) percent removal curves for • - -
GAC Filter 19A, Phase 1-0 208
209 Instantaneous THM (ITTT) percent removal"curves for
GAC Filter 21A, Phase 1-0 209
210 Instantaneous THM (ITTT) percent removal curves for
GAC Filter 23A, Phase 1-0 210
211 Instantaneous THM (ITTT) percent removal curves for
Contactor A, Phase 3-0 211
212 Instantaneous THM (ITTT) percent removal curves for
Contactor A, Phase 3-1 212
213 Instantaneous THM (ITTT) percent removal curves for
Contactor A, Phase 3-2 213
214 Instantaneous THM (ITTT) percent removal curves for
Contactor B, Phase 3-0 214
215 Instantaneous THM (ITTT) percent removal curves for
Contactor BB, Phase 3-0 215
216 Instantaneous THM (ITTT) percent removal curves for
Contactor BB, Phase 3-1 216
217 Instantaneous THM (ITTT) percent removal curves for
Contactor C, Phase 3-0 217
218 Instantaneous THM (ITTT) r=rcent removal curves for
Contactor C, Phase 3-1
219 Instantaneous THM (ITTT) percent removal curves for
Contactor C, Phase 3-2 219
•xvij.
-------
220 Instantaneous THM (ITTT) percent removal curves for
Contactor D, Phase 3-0
221 Instantaneous THM (ITTT) percent removal curves for
Contactor D, Phase 3-1 221
222 Instantaneous THM (ITTT) percent removal curves for
Contactor D, Phase 3-2 . . . 222
223 Instantaneous THM (ITTT) percent removal curves for
bituminous pilot contactors, Phase 2-0 223
224 Instantaneous THM (ITTT) percent removal curves for
pilot contactors, Phase 3-0 224
225 Instantaneous THM (ITTT) percent removal curves for
pilot contactors, Phase 3-1 225
226 Instantaneous THM (ITTT) percent removal curves for
pilot contactors, Phase 3-2 226
227 Instantaneous THM (ITTT) percent removal curves for
lignite pilot contactors, Phase 2-0 227
228 Instantaneous THM (ITTT) percent removal curves for
virgin pilot GAC filter, Phase 1-0 228
229 Three-day simulated distribution system THM (STT3) percent
removal curves for Contactor A, Phase 3-0 229
230 Three-day simulated distribution system THM (STT3) percent
removal curves for Contactor A, Phase 3-1 230
231 Three-day simulated distribution system THM (STT3) percent
removal curves for Contactor A, Phase 3-2 231
232 Three-day simulated distribution system THM (STT3) percent
removal curves for Contactor B, Phase 3-0 232
233 Three-day simulated distribution system THM (3TT3) percent
removal curves for Contactor EB, Phase 3-0 233
234 Three-day simulated distribution system THM (STT3) percent
removal curves for Contactor BB, Phase 3-1 234
235 Three-day simulated distribution system THM (STT3) percent
removal curves for Contactor C, Phase 3-0
236 Three-day simulated distribution system THM (STT3) percent
removal curves for Contactor C. Phase 3-1 236
XVlii
-------
237 Three-day simulated distribution'.system THM (STT3) percent
removal curves for Contactor C, Phase 3-2 237
238 Three-day simulated distribution system THM (STT3) percent
removal curves for Contactor D, Phase 3-0 238
239 Three-day simulated distribution system THM (STT3) percent
removal curves for Contactor D, Phase 3-1 239
240 Three-day simulated distribution system THM (STT3) percent
removal curves for Contactor D, Phase 3-2 240
241 Three-day simulated distribution system THM (STT3) percent' • -.
removal curves for pilot contactors, Phase 3-0 241
242 Three-day simulated distribution system THM (STT3) percent
removal curves for pilot contactors, Phase 3-1 242
243 Three-day simulated distribution system THM (STT3) percent
removal curves for pilot contactors, Phase 3-2 243
244 Seven-day simulated distribution system THM (STT7) percent
removal curves for GAC Filter 19A, Phase 1-0 244
245 Seven-day simulated distribution system THM (STT7) percent
removal curves for GAC Filter 21A, Phase 1-0 245
246 Seven-day simulated distribution system THM (STT7) percent
removal curves for GAC Filter 23A, Phase 1-0 246
247 Seven-day simulated distribution system THM (STT7) percent
removal curves for bituminous pilot contactors,
Phase 2-0 247
248 Seven-day simulated distribution system THM (STT7) percent
removal curves for lignite pilot contactors, Phase 2-0 . 248
249 Seven-day simulated distribution system THM (STT7) percent
removal curves for virgin pilot GAC filter. Phase 1-0. . 249
250 Total organic carbon (TOO percent removal curves for
GAC Filter 19A, Phase 1-0 250
251 Total organic carbon (TOC) percent removal curves for
GAC Filter 21A, Phase 1-0 251
252 Total organic carbon (TOC) percent removal curves for
GAC Filter 23A, Phase 1-0 252
253 Total organic carbon (TOC) percent removal curves for
Contactor A, Phase 3-0 253
xix
-------
254 Total organic carbon (TOC) percent removal curves for
Contactor A, Phase 3-1 254
255 Total organic carbon (TOC) percent removal curves for
Contactor A, Phase 3-2 255
256 Total organic carbon (TOC) percent removal curves for
Contactor B, Phase 3-0 256
257 Total organic carbon (TOC) percent removal curves for
Contactor BB, Phase 3-0 257
253 Total organic carbon (TOC) percent removal curves for
Contactor BB, Phase 3-1 253
259 Total organic carbon (TOC) percent removal curves for
Contactor C, Phase 3-0 259
260 Total organic carbon (TOC) percent removal curves for
Contactor C, Phase 3-1 260
261 Total organic carbon (TOC) percent removal curves for
Contactor C, Phase 3-2 261
262 Total organic carbon (TOC) percent removal curves for
Contactor D, Phase 3-0 262
263 Total organic carbon (TOC) percent removal curves for
Contactor D, Phase 3-1 263
264 Total organic carbon (TOC) percent removal curves for
Contactor D, Phase 3-2 264
265 Total organic carbon (TOC) percent removal curves for
bituminous pilot contactors, Phase 2-0 265
266 Total organic carbon (TOC) percent removal curves for
pilot contactors, Phase 3-0 256
267 Total organic carbon (TOC) percent removal curves for
pilot contactors, Phase 3-1 267
268 Total organic carbon (TOC) percent removal curves for
pilot contactors, Phase 3-2
269 Total organic carbon (TOC) percent removal curves for
lignite pilot contactors, Phase 2-0 269
270 Total organic carbon (TOC) percent removal curves for
virgin pilot GAC filter, Phase 1-0 270
-------
271 THM formation potential (FTTT) concentration curves for
GAC Filter 19A and 21A effluents, Phase 1-0 271
272 THM formation potential (FTTT) concentration curves for
GAC Filters 21A level 2 and 19A effluent, Phase 1-0. . . 272
273 THM formation potential (FTTT) breakthrough curves for GAC
Filter ISA effluent and Contactor C level 7, Phase 3-1 . 273
274 THM formation potential (FTTT) breakthrough curves for
pilot GAC filter and GAC Filter ISA effluents,
Phase 3-1
275 TIM formation potential (FTTT) breakthrough.-curves'f6r"
pilot GAC filter and GAC Filter ISA effluents, Phase 3-2 275
276 THM formation potential (FTTT) breakthrough curves for
pilot GAC filter and GAC Filter ISA effluents, Phase 3-3 276
277 THM formation potential (FTTT) breakthrough curves for
pilot GAC filter and GAC Filter ISA effluents, Phase 3-0 277
278 THM formation potential (FTTT) breakthrough curves for
virgin and once regenerated pilot GAC filter effluents,
Phase 2-1 278
279 THM formation potential (FTTT) breakthrough curves for
virgin and twice regenerated pilot GAC filter
effluents, Phase 2-2 279
280 THM formation potential (FTTT) breakthrough curves for
bituminous and lignite pilot contactor effluents,
Phase 2-0 280
281 Instantaneous chloroform (ICLR) concentration curves for
GAC Filter 19A and 21A effluents, Phase 1-0 281
2S2 Instantaneous chloroform (ICLR) concentration curves for
GAC Filters 21A level 2 and 19A effluent, Phase 1-0. . . 282
283 Instantaneous chloroform (ICLR) breakthrough curves for
Filter ISA effluent and Contactor C level 7, Phase 3-1 . 283
284 Instantaneous chloroform (ICLR) breakthrough curves for
GAC Filter ISA effluent and Contactor D level 7,
Phase 3-0 284
285 Instantaneous chloroform (ICLR) breakthrough curves for
pilot GAC filter and GAC Filter ISA effluents,
Phase 3-1 235
xxi
-------
2S6 Instantaneous chloroform (ICLR) breakthrough curves for
pilot GAC filter and GAG Filter ISA effluenrs, Phase 3-2 2S6
287 Instantaneous chloroform (ICLR) breakthrough curves for
pilot GAC filter and GAC Filter ISA effluents, Phase 3-3 237
288 Instantaneous chloroform (ICLR) breakthrough curves for
pilot GAC filter and GAC Filter ISA effluents, Phase 3-0 288
289 Instantaneous chloroform (ICLR) breakthrough curves for
virgin and once regenerated pilot GAC filter effluents,
Phase 2-1 289
290 Instantaneous chloroform (ICLR) breakthrough curves for
virgin and twice regenerated pilot GAC filter effluents,
Phase 2-2 290
291 Instantaneous chloroform (ICLR) breakthrough curves for
bituminous and lignite pilot contactor effluents,
Phase 2-0 291
292 Instantaneous bromodlchloromethane (ICL2) concentration
curves for GAC Filter 19A and 21A effluents, Phase 1-0 . 292
293 Instantaneous bromodichloromethane (ICL2) concentration
curves for GAC Filters 21A level 2 and 19A effluent,
Phase 1-0 293
294 Instantaneous bromodichloromethane (ICL2) concentration
curves for GAC Filter 15A effluent and Contactor C
level 7, Phase 3-1 294
295 Instantaneous bromodichloromethane (ICL2) breakthrough
curves for GAC Filter ISA effluent and Contactor D
level 7, Phase 3-0 925
296 Instantaneous bromodichloromethane (ICL2) breakthrough
curves for pilot GAC filter and GAC Filter ISA
effluents, Phase 3-1 296
297 Instantaneous bromodichloromethane (ICL2) breakthrough
curves for pilot GAC filter and GAC Filter ISA
effluents, Phase 3-2 297
298 Instantaneous bromodichloromethane (ICL2) breakthrough
curves for t lot GAC filter and GAC Filter ISA
effluents, Phase 3-3 298
299 Instantaneous bromodichloromethane (ICL2) breakthrough
curves for pilot GAC filter and GAC Filter ISA
effluents, Phase 3-0 299
xxi i
-------
300 Instantaneous bromodichloromethane (ICL2) breakthrough
curves for virgin and once regenerated pilot GAC
filter effluents, Phase 2-1 300
301 Instantaneous bromodichloromethane (ICL2) breakthrough
curves for virgin and twice regenerated pilot GAC
filter effluents, Phase 2-2 3C1
302 Instantaneous bromodichloromethane (ICL2) breakthrough
curves for bituminous and lignite pilot contactor
effluents, Phase 2-0 302
303 Instantaneous THM (ITTT) concentration curves for GAC
Filters 21A level 2 and 19A effluent, Phase 1-0. . „.• * .., -. 303'
304 Instantaneous THM (ITTT) breakthrough curves for pilot
GAC filter and GAC Filter ISA effluents, Phase 3-1 . .' . 304
305 Instantaneous THM (ITTT) breakthrough curves for pilot
GAC filter and GAC Filter ISA effluents, Phase 3-2 . . . 305
306 Instantaneous THM (ITTT) breakthrough curves for pilot
GAC filter and GAC Filter ISA effluents, Phase 3-3 ... 306
307 Instantaneous THM (ITTT) breakthrough curves for pilot
GAC filter and GAC Filter ISA effluents, Phase 3-0 . . . 307
308 Instantaneous THM (ITTT) breakthrough curves for virgin
and once regenerated pilot GAC filter effluents,
Phase 2-1 308
309 Instantaneous THM (ITTT) breakthrough curves for virgin
and twice regenerated pilot GAC filter effluents,
Phase 2-2 309
310 Instantaneous THM (ITTT) breakthrough curves for bituminous
and lignite pilot contactor effluents, Phase 2-0 .... 310
311 Instantaneous THM (ITTT) breakthrough curves for bituminous
pilot contactor and Contactor D effluents, Phase 3-0 . . 311
312 Instantaneous THM (ITTT) breakthrough curves for bituminous
pilot contactor and Contactor D effluents, Phase 3-1 . . 312
313 Instantaneous THM (ITTT) breakthrough curves for bituminous
pilot contactor and Contactor D effluents, Phase 3-2 . . 313
314 Three-day simulated distribution system THM (STT3)
breakthrough curves for GAC Filter ISA effluent and
Contactor C level 7, Phase 3-1 314
-------
315 Seven-day simulated distribution system THM (STT7)
breakthrough curves for virgin and once regenerated
pilot GAG filter effluents, Phase 2-1. . .•
316 Seven-day simulated distribution system THM (STT7)
breakthrough curves for virgin & twice regenerated
pilot GAC filter effluents, Phase 2-2 316
317 Total organic carbon (TOC) breakthrough curves for GAC
Filters 21A level 2 and 19A effluent, Phase 1-0 317
318 Total organic carbon (TOC) breakthrough curves for GAC
Filter ISA -ffluent and Contactor C level 7, Phase 3-1 .
319 Total organic carbon (TOC) breakthrough curves for virgin
and once regenerated pilot GAC filter effluents,
Phase 2-1 319
320 Total organic carbon (TOC) breakthrough curves for virgin
and twice regenerated pilot GAC filter effluents,
Phase 2-2 320
321 Carbon adsorbable organohalides (CAOX) percent removal
curves for GAC Filter ISA effluent and Contactor D
level 7, Phase 3-0 321
322 THM formation potential (FTTT) percent removal curves for
GAC Filter ISA effluent and Contactor C level 7,
Phase 3-1 322
323 THM formation potential (FTTT) percent removal curves for
pilot GAC contactor and GAC Filter ISA effluents,
Phase 3-1 323
324 THM formation potential (FTTT) percent removal curves for
pilot GAC filter and GAC Filter ISA effluents. Phase 3-2 324
325 THM formation potential (FTTT) percent removal curves for
pilot GAC filter and GAC Filter ISA effluents, Phase 3-3 325
326 THM formation potential (FTTT) percent removal curves for
pilot GAC filter and GAC Filter ISA effluents, Phase 3-0 326
327 THM formation potential (FTTT) percent removal curves fcr
bituminous and lignite pilot contactor effluents.
Phase 2-0 327
328 THM formation potential (FTTT) percent removal curves for
pilot contactor level 2 and Contactor D level 4,
Phase 3-0 328
xxiv
-------
329 THM formation potential (FTTT) percent removal curves for
pilot contactor level 2 and Contactor D level 4,
Phase 3-1 329
330 THM formation potential (FTTT) percent removal curves for
pilot contactor level 2 and Contactor D level 4,
Phase 3-2 330
331 THM formation potential (FTTT) percent removal curves for
pilot contactor level 3 and Contactor D level 7,
Phase 3-0 331
332 THM formation potential (FTTT) percent .removal curves .for
pilot contactor level 3 and Contactor D level 7,
Phase 3-1 332
333 THM formation potential (FTTT) percent removal curves for
pilot contactor level 3 and Contactor D level 7,
Phase 3-2 ".''.. 333"
334 THM formation potential (FTTT) percent removal curves for
pilot contactor and Contactor D effluents. Phase 3-0 . . 334
335 THM formation potential (FTTT) percent removal curves for
pilot contactor and Contactor D effluents, Phase 3-1 . . 335
336 THM formation potential (FTTT) percent removal curves for
pilot contactor and Contactor D effluents, Phase 3-2 . . 336
337 Instantaneous chloroform (ICLR) percent removal curves
for GAC Filter ISA effluent and Contactor C level 7,
Phase 3-1 337
338 Instantaneous chloroform (ICLR) percent removal curves
for GAC Filter ISA effluent and Contactor D level 7,
Phase 3-0 333
339 Instantaneous chloroform (ICLR) percent removal curves
for GAC contactor and GAC Filter ISA effluents,
Phase 3-1 339
340 Instantaneous chloroform (ICLR) percent removal curves
for pilot GAC filter and GAC Filter ISA effluents,
Phase 3-2 340
341 Instantaneous chloroform (ICLR) percent removal curves
for pilot GAC filter and GAC Filter ISA effluents,
Phase 3-3 341
xxv
-------
342 Instantaneous chloroform (ICLR) percent removal curves
for pilot GAG filter and GAG Filter ISA effluents,
Phase 3-0 342
343 Instantaneous chloroform (ICLR) percent removal curves
for virgin and once regenerated pilot GAG filter
effluents, Phase 2-1 343
344 Instantaneous chloroform (ICLR) percent removal curves
for virgin and twice regenerated pilot GAC filter
effluents, Phase 2-2 344
345 Instantaneous chloroform (ICLR) percent removal curves
for bituminous and lignite pilot contactor effluents,
Phase 2-0 345
346 Instantaneous chloroform (ICLR) percent removal curves
for pilot contactor level 2 and Contactor D level 4,
Phase 3-0 346
347 Instantaneous chloroform (ICLR) percent removal curves
for pilot contactor level 2 and Contactor D level 4,
Phase 3-0 347
348 Instantaneous chloroform (ICLR) percent removal curves
for pilot contactor level 2 and Contactor D level 4,
Phase 3-2 348
349 Instantaneous chloroform (ICLR) percent removal curves
for pilot contactor level 3 and Contactor D level 7,
Phase 3-0 349
350 Instantaneous chloroform (ICLR) percent removal curves
for pilot contactor level 3 and Contactor D level 7,
Phase 3-1 350
351 Instantaneous chloroform (ICLR) percent removal curves
for pilot contactor level 3 and Contactor D level 7,
Phase 3-2 351
352 Instantaneous chloroform (ICLR) percent removal curves
for pilot contactor and Contactor D effluents,
Phase 3-0 352
353 Instantaneous chloroform (ICLR) percent removal curves
for pilot CLntactor and Contactor D effluents,
Phase 3-1 353
354 Instantaneous chloroform (ICLR) percent removal curves
for pilot contactor and Contactor D effluents,
Phase 3-2 354
xxvi
-------
355 Instantaneous bromodichloromethane (ICL2) percent removal
curves for GAC Filter ISA effluent and Contactor C
Level 7, Phase 3-1 355
356 Instantaneous bromodichloromethane (ICL2) percent removal
curves for GAC Filter ISA effluent and Contactor D
level 7, Phase 3-0 356
357 Instantaneous broraodichloromethane (ICL2) percent removal
curves for pilot GAC contactor and GAC Filter ISA
effluents, Phase 3-1 357
358 Instantaneous bromodichloromethane (ICL2) percent removal
curves for pilot GAC filter and GAC Filter ISA
effluents, Phase 3-2 358
359 Instantaneous bromodichloromethane (ICL2) percent removal
curves for pilot GAC filter and GAC Filter ISA
effluents, Phase 3-3 359
360 Instantaneous bromodichloromethane (ICL2) percent removal
curves for pilot GAC filter and GAC Filter ISA
effluents, Phase 3-0 360
361 Instantaneous bromodichloromethane (ICL2) percent removal
curves for virgin and once regenerated pilot GAC filter
effluents, Phase 2-1 361
362 Instantaneous bromodichloromethane (ICL2) percent removal
curves for virgin and twice regenerated pilot GAC
filter effluents, Phase 2-2 362
363 Instantaneous bromodichloromethane (ICL2) percent removal
curves for bituminous and lignite pilot contactor
effluents, Phase 2-0 363
364 Instantaneous THM (ITTT) percent removal curves for GAC
Filter ISA effluent and Contactor D level 7, Phase 3-0 . 364
365 Instantaneous THM (ITTT) percent removal curves for pilot
GAC filter and GAC Filter ISA effluents, Phase 3-1 . . . 365
366 Instantaneous THM (ITTT) percent removal curves for pilot
GAC filter and GAC filter ISA effluents. Phase 3-2 . . . 366
367 Instantaneous THM (ITTT) percent removal curves for pilot
GAC filter and GAC Filter ISA effluents, Phase 3-3 . . . 367
368 Instantaneous THM (ITTT) percent removal curves for pilot
GAC filter and GAC Filter ISA effluents, Phase 3-0 . . . 363
xxv 11
-------
369 Instantaneous THM (ITTT) percent removal curves for
bituminous and lignite pilot contactor effluents,
Phase 2-0 369
370 Instantaneous THM (ITTT) percent removal curves for pilot
contactor level 2 and Contactor D level 4, Phase 3-0 . . 370
371 Instantaneous THM (ITTT) percent removal curves for pilot
contactor level 2 and Contactor D level 4, Phase 3-1 . . 371
372 Instantaneous THM (ITTT) percent removal curves for pilot
contactor level 2 and Contactor D level 4, Phase 3-2 . . 372
373 Instantaneous THM (ITTT) percent removal curves for pilot
contactor level 3 and Contactor D level 7, Phase 3-0 . . 373
374 Instantaneous THM (ITTT) percent removal curves for pilot
contactor level 3 and Contactor D level 7, Phase 3-1 . . 374
375 Instantaneous THM (ITTT) percent removal curves for pilot
contactor level 3 and Contactor D level 7, Phase 3-2 . . 375
376 Instantaneous THM (ITTT) percent removal curves for pilot
contactor and Contactor D effluents, Phase 3-0 376
377 Instantaneous THM (ITTT) percent removal curves for pilot
contactor and Contactor D effluents, Phase 3-1 377
378 Instantaneous THM (ITTT) percent removal curves for pilot
contactor and Contactor D effluents, Phase 3-2 378
379 Maximum THM (MTTT) percent removal curves for GAC Filter
19A and 21A effluents, Phase 1-0 379
380 Maximum THM (MTTT) percent removal curves for GAC Filters
21A level 2 and 19A effluent, Phase 1-0 380
381 Three-day simulated distribution system THM (STT3) percent
removal curves for GAC Filter ISA effluent and
Contactor C level 7, phase 3-1 381
382 Three-day simulated distribution system (STT3) percent
removal curves for GAC Filter ISA effluent and
Contactor D level 7, Phase 3-0 382
383 Three-day simulated distribution system THM (STT3) percent
removal curves for pilot contactor level 2 and
Contactor D level 4, Phase 3-0 383
-------
384 Three-day simulated distribution system THM (STT3) percent
removal curves for pilot contactor level 2 and
Contactor D level 4, Phase 3-1 384
385 Three-day simulated distribution system THM (STT3) percent
removal curves for pilot contactor level 2 and
Contactor D level 4, Phase 3-2 335
386 Three-day simulated distribution system THM (STT3) percent
removal curves for pilot contactor level 3 and
Contactor D level 7, Phase 3-0 386
387 Three-day simulated distribution system THM (STT3) percent
removal curves for pilot contactor level 3 and
Contactor D level 7, Phase 3-1 . . 387
388 Three-day simulated distribution system THM (STT3) percent
removal curves for pilot contactor level 3 and
Contactor D level 7, Phase 3-2 388
389 Three-day simulated distribution system THM (STT3) percent
removal curves for pilot contactor and Contactor D
effluents, Phase 3-0 389
390 Three-day simulated distribution system THM (STT3) percent
removal curves for pilot contactor and Contactor D
effluents, Phase 3-1 390
391 Three-day simulated distribution system THM (STT3) percent
removal curves for pilot contactor and Contactor D
effluents, Phase 3-2 391
392 Seven-day simulated distribution system THM (STT7) percent
removal curves for bituminous and lignite pilot
contactor effluents, Phase 2-0 392
393 Total organic carbon (TOC) percent removal curves for GAC
Filters 21A level 2 and 19A effluent, Phase 1-0 393
394 Total organic carbon (TOC) percent removal curves for GAC
Filter ISA effluent and Contactor C level 7, Phase 3-1 . 394
395 Total organic carbon (TOC) percent removal curves for GAC
Filter ISA effluent and Contactor D level 7, Phase 3-0 . 395
396 Total organic carbon (TOC) percent removal curves for
bituminous and lignite pilot contactor effluents,
Phase 2-0 396
xxix
-------
397 Total organic carbon (TOC) percent removal curves for pilot
contactor level 2 and Contactor D level 4, Phase 3-0 . . 397
398 Total organic carbon (TOC) percent removal curves for pilot
contactor level 2 and Contactor D level 4, Phase 3-1 . . 398
399 Total organic carbon (TOC) percent removal curves for pilot
contactor level 2 and Contactor D level 4, Phase 3-2 . . 399
400 Total organic carbon (TOC) percent removal curves for pilot
contactor level 3 and Contactor D level 7, Phase 3-0 . . 400
401 Total organic carbon (TOC) percent removal curves for pilot
contactor level 3 and Contactor D level 7, Phase 3-1 . . 401
402 Total organic carbon (TOC) percent removal curves for pilot
contactor level 3 and Contactor D level 7, Phase 3-2 . . 402
403 Total organic carbon (TOC) percent removal curves for
pilot contactor and Contactor D effluents, Phase 3-0 . . 403
404 Total organic carbon (TOC) percent removal curves for
pilot contactor and Contactor D effluents, Phase 3-1 . . 404
405 Total organic carbon (TOC) percent removal curves for
pilot contactor and Contactor D effluents, Phase 3-2 . . 405
406 THM formation potential (FTTT) percent removal curves for
multiple runs of GAC Filter ISA effluent, Phase 3. ... 406
407 THM formation potential (FTTT) percent removal curves for
multiple runs of GAC Filter 21A effluent, Phase 3. ... 407
408 THM formation potential (FTTT) percent removal curves for
multiple runs of Contactor A effluent, Phase 3 408
409 THM formation potential (FTTT) percent removal curves for
multiple runs of Contactor BB effluent, Phase 3 409
410 THM formation potential (FTTT) percent removal curves for
multiple runs of Contactor C effluent, Phase 3 410
411 THM formation potential (FTTT) percent removal curves for
multiple runs of Contactor D effluent, Phase 3 411
412 Instantaneous chloroform (ICLR) percent removal curves for
multiple runs cf GAC Filter 21A effluent, Phase 3. ... 412
413 Instantaneous chlorofomr (ICLR) percent removal curves for
multiple runs of Contactor A effluent, Phase 3 413
XXX
-------
414 Instantaneous chloroform (ICLR) percent removal curves for
multiple runs of Contactor BB effluent, Phase 3 414
415 Instantaneous chloroform (ICLR) percent removal curves for
multiple runs of Contactor C effluent, Phase 3 415
416 Instantaneous chloroform (ICLR) percent removal curves for
multiple runs of Contactor D effluent, Phase 3 416
417 Instantaneous bromodichloromethane (ICL2) percent removal
curves for multiple runs of GAC Filter ISA effluent,
Phase 3 417
418 Instantaneous bromodichloromethane (ICL2) percent removal
curves for multiple runs of GAC Filter 21A effluent,
Phase 3 418
419 Instantaneous bromodichloromethane (ICL2) percent removal
curves for multiple runs of Contactor A effluent,
Phase 3 419
420 Instantaneous bromodichloromethane (ICL2) percent removal
curves for multiple runs of Contactor BB effluent,
Phase 3 420
421 Instantaneous bromodichloromethane (ICL2) percent removal
curves for multiple runs of Contactor C effluent,
Phase 3
422 Instantaneous bromodichloromethane (ICL2) percent removal
curves for multiple runs of Contactor D effluent,
Phase 3 422
423 Instantaneous THM (ITTT) percent removal curves for
multiple runs of GAC Filter ISA effluent, Phase 3. ... 423
424 Instantaneous THM (ITTT) percent removal curves for
multiple runs of GAC Filter 21A effluent, Phase 3. ... 424
425 Instantaneous THM (ITTT) percent removal curves for
multiple runs of Contactor A effluent, Phase 3 425
426 Instantaneous THM (ITTT) percent removal curves for
multiple runs of Contactor BB effluent, Phase 3 426
427 Instantaneous THM (ITTT) percent removal curves for
multiple runs of Contactor C effluent, Phase 3 427
428 Instantaneous THM (ITTT) percent removal curves for
multiple runs of Contactor D effluent. Phase 3 428
XXXI
-------
429 Three-day simulated distribution system THM (STT3) percent
removal curves for multiple runs of GAG Filter ISA
effluent, Phase 3 429
430 Three-day simulated distribution system THM (STT3) percent
removal curves for multiple runs of GAG Filter 21A
effluent, Phase 3 420
431 Three-day simulated distribution system THM (STT3) percent
removal curves for multiple runs of Contactor A
effluent, Phase 3 431
432 Three-day simulated distribution system THM (STT3) percent
removal curves for multiple runs of Contactor BB
effluent, Phase 3 432
433 Three-day simulated distribution system THM (STT3) percent
removal curves for multiple runs of Contactor C
effluent, Phase 3 433
434 Total organic carbon (TOC) percent removal curves for
multiple runs of GAC Filter 21A effluent, Phase 3. ... 434
435 Total organic carbon (TOC) percent removal curves for
multiple runs of Contactor A effluent, Phase 3 435
436 Total organic carbon (TOC) percent removal curves for
multiple runs of Contactor BB effluent, Phase 3 436
437 Total organic carbon (TOC) percent removal curves for
multiple runs of Contactor C effluent, Phase 3 437
438 THM formation potential (FTTT) adsorbed per GAC weight for
multiple runs of GAC Filter 21A effluent, Phase 3. ... 438
439 THM formation potential (FTTT) adsorbed per GAC weight for
multiple runs of Contactor A effluent. Phase 3 439
440 THM formation potential (FTTT) adsorbed per GAC weight for
multiple runs of Contactor B effluent, Phase 3 440
441 THM formation potential (FTTT) adsorbed per GAC weight for
multiple runs of Contactor BB effluent, Phase 3 441
442 THM formation potential (FTTT) adsorbed per GAC weight for
multiple runs of Contactor C effluent, Phase 3 442
443 THM formation potential (FTTT) adsorbed per GAC weight for
multiple runs of Contactor D effluent, Phase 3 443
444 Instantaneous chloroform (ICLR) adsorbed per GAC weight for
multiple runs of GAC Filter 21A effluent. Phase 3. ... 444
xxxii
-------
Instantaneous chloroform (ICLR) adsorbed per GAC weight for
multiple runs of Contactor A effluent, Phase 3 445
446 Instantaneous chloroform (ICLR) adsorbed per GAC weight for
multiple runs of Contactor B effluent, Phase 3 446
447 Instantaneous chloroform (ICLR) adsorbed per GAC weight for
multiple runs of Contactor BB effluent, Phase 3 447
448 Instantaneous chloroform (ICLR) adsorbed per GAC weight for
multiple runs of Contactor C effluent, Phase 3 448
449 Instantaneous bromodichloromethane (ICL2) adsorbed per GAC
weight for multiple runs of GAC Filter ISA effluent,
Phase 3 449
450 Instantaneous bromodichloromethane (ICL2) adsorbed per GAC
weight for multiple runs of GAC Filter 21A effluent,
Phase 3 453
431 Instantaneous bromodichloromethane (ICL2) adsorbed per GAC
weight for multiple runs of Contactor A effluent,
Phase 3 451
452 Instantaneous bromodichloromethane (ICL2) adsorbed per GAC
weight for multiple runs of Contactor B effluent,
Phase 3 452
Instantaneous bromodichloromethane (ICL2) adsorbed per GAC
weight for multiple runs of Contactor BB effluent,
Phase 3 453
Instantaneous bromodichloromethane (ICL2) adsorbed per GAC
weight for multiple runs of Contactor C effluent,
Phase 3 454
Instantaneous THM (ITTT) adsorbed per GAC weight for
multiple runs of GAC Filter ISA effluent, Phase 3. ... 455
Instantaneous THM (ITTT) adsorbed per GAC weight for
multiple runs of GAC Filter 21A effluent. Phase 3. ... 456
457 Instantaneous THM (ITTT) adsorbed per GAC weight for
multiple runs of Contactor A effluent, Phase 3 457
453 Instantaneous THM (ITTT) adsorbed per GAC weight for
multiple runs of Contactor B effluent, Phase 3 453
453 Instantaneous THM (ITTT) adsorbed per GAC weight for
multiple runs of Contactor BB effluent, Phase 3 459
-------
460 Instantaneous THM (ITTT) adsorbed per GAC weight for
multiple runs of Contactor C effluent, Phase 3 460
461 Instantaneous THM (ITTT) adsorbed per GAC weight for
multiple runs of Contactor D effluent, Phase 3 461
462 Three-day simulated distribution system THM (STT3)
adsorbed per GAC weight for multiple runs of GAC
Filter ISA effluent, Phase 3 462
463 Three-day simulated distribution system THM (STT3)
adsorbed per GAC weight for multiple runs of GAC
Filter 21A effluent, Phase 3 463
464 Three-day simulated distribution system THM (STT3)
adsorbed per GAC weight for multiple runs of
Contactor A effluent, Phase 3 464
465 Three-day simulated distribution system THM (STT3)
adsorbed per GAC weight for multiple runs of
Contactor B effluent, Phase 3 465
466 Three-day simulated distribution system THM (STT3)
adsorbed per GAC weight for multiple runs of
Contactor BB effluent, Phase 3 466
467 Three-day simulated distribution system THM (STT3)
adsorbed per GAC weight for multiple runs of
Contactor C effluent, Phase 3 467
468 Three-day simulated distribution system THM (STT3)
adsorbed per GAC weight for multiple runs of
Contactor D effluent, Phase 3 468
469 Total organic carbon (TOO adsorbed per GAC weight for
multiple runs of GAC Filter 21A effluent, Phase 3. ... 469
470 Total organic carbon (TOC) adsorbed per GAC weight for
multiple runs of Contactor A effluent, Phase 3 470
A -71
71 Total organic carbon (TOC) adsorbed per GAC weight for
multiple runs of Contactor B effluent. Phase 3 471
472 Total organic carbon (TOC) adsorbed per GAC weight for
multiple runs of Contactor BB effluent, Phase 3 472
473 Total organic carbon (TOC) adsorbed per GAC weight for
multiple runs of Contactor C effluent, Phase 3 473
474 Acid extract profiles for GAC Filter 15A, Phase 3-0
runday eight 474
xxx rv
-------
475 Acid extract profiles for GAC Filter ISA, Phase 3-0,
runday 29 475
476 Acid extract profiles for GAG Filter ISA, Phase 3-0,
runday 57 476
477 Acid extract profiles for GAG Filter ISA, Phase 3-0,
runday 85 477
478 Acid extract profiles for GAG Filter ISA, Phase 3-0,
runday 113 478
479 Acid extract profiles for GAG Filter ISA, Phase 3-0,
runday 141
480 Acid extract profiles for GAG Filter ISA, Phase 3-0,
runday 169 480
481 Acid extract profiles for GAG Filter ISA, Phase 3-1,
runday 15
482 Acid extract profiles for GAG Filter ISA, Phase 3-1,
runday 43
491 Acid extract profiles for GAG Filter ISA, Phase 3-4,
runday 29
483 Acid extract profiles for GAG Filter ISA, Phase 3-2,
runday one 483
484 Acid extract profiles for GAG Filter ISA, Phase 3-2,
runday 29 434
485 Acid extract profiles for GAG Filter ISA, Phase 3-3,
runday 22 485
486 Acid extract profiles for GAG Filter ISA, Phase 3-3,
runday 36 486
487 Acid extract profiles for GAG Filter ISA, Phase 3-3,
runday 50 487
488 Acid extract profiles for GAC Filter ISA, Phase 3-3,
runday 64 483
489 Acid extract profiles for GAC Filter ISA, Phase 3-4,
runday one 489
490 Acid extract profiles for GAC Filter ISA, Phase 3-4,
rundav 15 490
XXXV
-------
492 Acid extract profiles for GAC Filter ISA, Phase 3-4,
runday 57 492
493 Acid extract profiles for pilot GAC filter, Phase 3-0,
runday 141 493
494 Acid extract profiles for Contactor A, Phase 3-0,
runday one 494
495 Acid extract profiles for Contactor A, Phase 3-0,
runday 38 495
496 Acid extract profiles for Contactor A, Phase 3-0,
runday 64 496
497 Acid extract profiles for Contactor A, Phase 3-0,
runday 93 497
498 Acid extract profiles for Contactor A, Phase 3-0,
runday 134 498
499 Acid extract profiles for Contactor A, Phase 3-0,
runday 162 499
500 Acid extract profiles for Contactor A, Phase 3-0,
runday 246 500
501 Acid extract profiles for Contactor A, Phase 3-0,
runday 274 501
502 Acid extract profiles for Contactor A, Phase 3-0,
runday 302 502
503 Acid extract profiles for Contactor D, Phase 3-0,
runday eight 503
504 Acid extract profiles for Contactor D, Phase 3-0,
runday 29 504
505 Acid extract profiles for Contactor D, Phase 3-0,
runday 57 505
506 Acid extract profiles for Contactor D, Phase 3-0,
runday 85 506
507 Acid extract profiles for Contactor D, Phase 3-0,
runday 113 507
508 Acid extract profiles for Contactor D, Phase 3-0,
runday 141
xxxv i
-------
509 Acid extract profiles for Contactor D, Phase 3-0,
runday 169 509
510 Acid extract profiles for Contactor D, Phase 3-0,
runday 197 510
511 Acid extract profiles for Contactor D, Phase 3-1,
runday 22 511
512 Acid extract profiles for Contactor D, Phase 3-1,
runday 50 512
513 Acid extract profiles for Contactor D, Phase 3-1,
runday 78 .......... -J. .. ' 513
514 Acid extract profiles for Contactor D, Phase 3-1,
runday 106 514
515 Acid extract profiles for Contactor D, Phase 3-2,
runday 15 515
516 Acid extract profiles for Contactor D, Phase 3-2,
runday 29 515
517 Acid extract profiles for Contactor D, Phase 3-2,
runday 43 517
518 Acid extract profiles for Contactor D, Phase 3-2,
runday 57 513
519 Acid extract profiles for Contactor D, Phase 3-2,
runday 71 519
520 Acid extract profiles for Contactor D, Phase 3-2,
runday 85 520
521 Acid extract profiles for Contactor D, Phase 3-2,
runday 99 521
522 Acid extract profiles for Contactor D, Phase 3-2,
runday 113 522
523 Acid extract profiles for Contactor D, Phase 3-2,
runday 127 523
524 Acid extract profiles for GAC Filter ISA and pilot GAC
filter, Phase 3-0, runday eight 524
525 Acid extract profiles for GAC Filter 15A and pilot GAC
filter, Phase 3-0, runday 29
-XXXVll
-------
526 Acid extract profiles for GAC Filter ISA and pilot GAG
filter, Phase 3-0, runday 85 526
527 Acid extract profiles for GAC Filter 15A and pilot GAC
filter, Phase 3-0, runday 113 527
52& Acid extract profiles for GAC Filter ISA and pilot GAC
filter, Phase 3-0, runday 141 528
329 Acid extract profiles for GAC Filter ISA and regenerated
pilot GAC filter, Phase 3-1, runday 15 529
530 Acid extract profiles for GAC Filter ISA and regenerated
pilot GAC filter, Phase 3-1, runday 43 530
531 Acid extract profiles for GAC Filter ISA and regenerated
pilot GAC filter, Phase 3-2, runday one 531
532 Acid extract profiles for GAC Filter 15A and regenerated
pilot GAC filter, Phase 3-2, runday 29 532
533 Acid extract profiles for GAC Filter ISA and regenerated
pilot GAC filter, Phase 3-3, runday 22 533
534 Acid extract profiles for GAC Filter ISA and regenerated
pilot GAC filter, Phase 3-3, runday 50 534
535 . Acid extract profiles for filter influent, GAC Filter ISA
effluent and Contactor D level 7, Phase 3-0, runday 29 . 535
536 Acid extract profiles for filter influent, GAC Filter ISA
effluent and Contactor D level 7, Phase 3-0, runday 57 . 536
537 Acid extract profiles for Contactor D and pilot contactor,
Phase 3-0, runday eight 537
538 Acid extract profiles for Contactor D and pilot contactor,
Phase 3-0, runday--29 538
539 Acid extract profiles for Contactor D and pilot contactor,
Phase 3-0, runday 57 539
540 Acid extract profiles for Contactor D and pilot contactor,
Phase 3-0, runday '85 .....' '. . ." .' ." . .".• ' 540
541 Acid extract profiles for Contactor D and pilot contactor,
Phase 3-0, runday 141 541
542 Acid extract profiles for Contactor D and pilot contactor,
Phase 3-0, runday 197 542
XXXVlll
-------
543 Acid extract profiles for Contactor D and pilot
contactor, Phase 3-1, runday 22 543
544 Acid extract profiles for Contactor D and pilot
contactor, Phase 3-1, runday 50 544
545 Acid extract profiles for Contactor D and pilot
contactor, Phase 3-1, runday 78 545
546 Acid extract profiles for Contactor D and pilot
contactor, Phase 3-1, runday 106 546
547 Acid extract profiles for Contactor D and pilot
contactor, Phase-3-2, runday 15-.' .«.'.'.-....'..." 547
548 Acid extract profiles for Contactor D and pilot
contactor, Phase 3-2, runday 43 548
549 Acid extract profiles for Contactor D and pilot
contactor, Phase 3-2, runday 71 549
'550 Acid extract profiles for Contactor D and-pilot
contactor, Phase 3-2, runday 99 550
551 Acid extract profiles for Contactor D and pilot
contactor, Phase 3-2, runday 127 551
,xxxix
-------
LEGEND
a
3
o
H
I
I
300
250 .
200
150 .
100 .
0
0
INFLUENT CFLDO
6AC FILTER 19A LEVEL 2
6AC FILTER ISA LEVEL 1 CI8AO
6AC FILTER ISA EFF C19AE)
20
40
80 100
TIME, days
120
140
Figure I. THM formation potential (FTTT) breakthrough
curves for 6AC Filter 19A, Phase 1-0.
160
180
-------
INFLUENT CFLDO
6AC FILTER 2IA LEVEL 2 <21A2>
480
LEGEND
6AC FILTER 2IA LEVEL 1
6AC FILTER 2IA LEVEL 3
6AC FILTER 21A EFF <2IAE>
C2IAO
C2IA3)
0
0
50
100
200 250 300
TIME., days
350
400
450
500
Figure 2. THM formation potential CFTTT) breakthrough
curves for GAC Filter 21 A, Phase 1-0.
-------
INFLUENT CFLBO
LEGEND
6AC FILTER 2IA EFF C2IAE3
X
400
350
300
250
z
H 200
z 150
UJ
o
8 100
0
0
Figure
10 15 20 25
TIME, day*
30
35
45
3. THM formation potential (FTTT) breakthrough curves
for 6AC Filter 21 A, Phase 3-1.
-------
LEGEND
INFLUENT CFLBO
8AC FILTER 21A EFF C21AE3
300
250
200
z
H 150
H
100
50
O
O
0 10 20 30 40 50 60
TIME, days
70
80
Figure 4. THM formation potential (FTTT) breakthrough curves
for GAC Filter 21 A, Phase 3-2.
-------
CONCENTRATION, uO/l
en —
o
CD -*>
>• O
O T
~n a
8
ro
CO
rr o MO
Q — 2
w m
<& «^\ ^
•n
o> —i a.
CT
O)
O
o
00
S)
o>
o
00
l\>
m
o
i I 1 r
m
%
I
ro
i
I
-------
INFLUENT CFLIND
SAC FILTER 23A LEVEL 2 <23A2>
400
350 .
300 .
X
? 250
LEGEND
6AC FILTER 23A LEVEL 1
SAC FILTER 23A LEVEL 3
6AC FILTER 23A EFF <23AE>
C23AI3 » X
C23A3) 1 1-
O
H
<
Of
J-
2
IU
O
z
O
O
200
150 _
100 .
50
0
0
20
160
180
Figure 6. THM formation potential (FTTT) breakthrough
curves for GAC Filter 23A, Phase 1-0.
-------
CONCENTRATION, ug/I
-------
LEGEND
3
300
250
200
H 150
tt
h-
o
2
O
O
50
0
0
INFLUENT CSFEF)
CONTACTOR A LEVEL 7 CA7>
CONTACTOR A LEVEL 4
20
80
100
40 60
TIME, days
Figure 8. THM formation potential (FTTT) breakthrough curves
for Contactor A, Phase 3-1.
120
-------
6
cs>
CD
CONCENTRATION, uO/l
o> oo o ro
CD
O>
CD
00
CD
ro ~n CD
• —« Q.
—i o
A
CT
O
O
< —
CO
CD
r\>
s
m
iS
5!
si
w w
II
-------
01
CONCENTRATION, ug/I
PO
-------
CONCENTRATION, ug/
tn
CO
1
ft
^? —1 -. .
o x &?
O -h
§ R
rf 3
O O
O O
WO
CD O
TJ 3
3- rr-
Q — —I
<0 O H
0 — 2
m
o>
~n
—) a.
—< o
—i •<
w a
o
£ »
o
en
o>
en
CD
II
1
I
/\
QD
3
w
rn
o
m
8
I
51
s
II
-------
LEGEND
O
H
<
U.
Id
O
z
O
O
220
280
180 .
160 _
140 .
120 .
100 .
80 .
60 .
20 I
0
0
INFLUENT CSFEF3
CONTACTOR BB LEVEL 7 CBB7D
CONTACTOR BB LEVEL 4 CBB4)
CONTACTOR BB EFF CBBE)
40
100
60 80
TIME, days
Figure 12. THM formation potential CFTTT) breakthrough curves
for Contactor BB, Phase 3-1.
120
140
-------
LEGEND
Ul
300
250
200
2
H 150
H
U.
H
Z
u '00
O
O
50
0
0
INFLUENT
-------
LEGEND
INFLUENT CSFEF)
CONTACTOR C LEVEL 7
CC7>
CONTACTOR C LEVEL 4 CC4)
CONTACTOR C EFF CCE>
358
0
10
20
30
70
40 50 60
TIME, days
Figure 14. THM formation potential CFTTT) breakthrough curves
for Contactor C,, Phase 3-1.
-------
250
288
o
o
H
jj
iu
o
o
150 .
100 -
50 .
0
0
LEGEND
INFLUENT CSFEF)
CONTACTOR C LEVEL 7 CC7)
CONTACTOR C LEVEL 4 CC4)
CONTACTOR C EFF
20
80
i00
40 60
TIME, days
Figure 15. THM formation potential (FTTT) breakthrough curves
for Contactor C, Phase 3-2.
120
-------
91
CONCENTRATION,
cn
CD
o
en
tn
o
ft
CD
-*> — I
O IE
~t 3
O -•»
O O
O O
"J 3
•>• o
r>-
"D ©
•3- D
Q rr-
W —
d> O
CL
O
CT
O
O
c
(0
CD
ro
Si
I
rn
G>
m
-------
LEGEND
UJ
O
O
O
180
168
140
a
3
z 100
O
H
80
60
40
20
0
a a INFLUENT
A A CONTACTOR D LEVEL 7 CD7>
0
CONTACTOR D LEVEL 4 CM*
CONTACTOR D EFF CDE)
20
40
100
60 80
TIME, days
Figure 17. THM formation potential (FTTT) breakthrough curves
for Contactor D, Phase 3-2.
120
140
-------
00
INFLUENT CSFEF5
PILOT CONTACTOR LEVEL 3
308
LEGEND
PILOT CONTACTOR LEVEL 2 CPFA23
PILOT CONTACTOR LEVEL 4 CPFA43
PILOT CONTACTOR EFF
e
1 00
1 50
200
250
TIME, days
Figure 18. THM formation potential (FTTT) breakthrough curves
for bituminous pilot contactors, Phase 2-0.
-------
6.1
•n
CONCENTRATION, ug/I
en o en
ro
o
en
II
"-I r\
§8
ffi^
J6 w
m
o
m
-------
LEGEND
O
3
o
H
u
o
o
350
300
250
200
158
0
0
INFLUEHT CSFEF>
PILOT CONTACTOR LEVEL 3 CPFA3)
PILOT CONTACTOR LEVEL 2 CPFA25
PILOT CONTACTOR EFF CPFAS)
20
60
TIME, dayi
80
100
120
Figure 20. THM formation potential (FTTT) breakthrough curves
for pilot contactors. Phase 3-1.
-------
IZ
CONCENTRATION, ug/i
-------
LEGEND
300
250 _
200 _
z
H 150
z
o
o
100 _
50
0
0
INFLUENT CSFEF3
PILOT CONTACTOR LEVEL 7
50
200
100 150
TIME, days
Figure 22. THM formation potential (FTTT) breakthrough curves
for lignite pilot contactors, Phase 2-0.
250
-------
CONCENTRATION, uc/
-------
CONCENTRATION, uO/
-------
INFLUENT CFLIN)
LEGEND
8AC FILTER 2IA EFF C2IAE3
70
to
_ 50
o
3
z
o
H
40
30
Ul
o
g 20
o
10
0
0
10 15 20 25
TIME, days
35
40
45
F10'»re 25. Instantaneous chloroform CICLR) breakthrough curves
for 6AC Filter 2!A, Phase 3-1.
-------
INFLUENT
-------
LZ
CONCENTRATION,
01 o en
ro
G>
JV)
en
o>
o
rn
G>
rn
to
S
I
M
i
i
-------
CONCENTRATION, u8/
cn
m
cn
m
CO —
-------
LEGEND
NJ
10
o
H
<
Of.
Id
O
I
0
INFLUENT CSFEFJ
CONTACTOR A LEVEL 7
CONTACTOR A LEVEL 4
-------
LEGEND
OJ
o
8
0
Figure
INFLUENT CSFEF>
CONTACTOR A LEVEL 7 CA7>
CONTACTOR A LEVEL 4 CA4)
CONTACTOR A EFF
80
100
60
TIME, day*
I. Instantaneous chloroform (ICLR) breakthrough curves
for Contactor A, Phase 3-t.
120
-------
LEGEND
o
§
ui
o
o
o
30
25 .
15 .
10 .
5 .
0
0
INFLUENT
CONTACTOR A LEVEL 4 CA4>
CONTACTOR A EFF CAE)
40
80
100
60
TIME, days
Figure 31. Instantaneous chloroform (ICLR) breakthrough curves
for Contactor A, Phase 3-2.
120
-------
LEGEND
INFLUENT CSFEF3
CONTACTOR B LEVEL 7
-------
LEGEND
INFLUENT CSFEF)
CONTACTOR BB LEVEL 7 CBB7>
CONTACTOR BB LEVEL 4 CBB4>
CONTACTOR BB EFF CBBE)
80
100
60
TIME, days
Figure 33. Instantaneous chloroform (ICLR) breakthrough curves
for Contactor BB, Phase 3-0.
120
-------
CONCENTRATION,
-------
CONCENTRATION, ug/
m
-------
LEGEND
INFLUENT CSFEH
CONTACTOR C LEVEL 7 CC7>
CONTACTOR C LEVEL 4 CC4> X X
CONTACTOR C EFF CCE) f 1-
70
50
I 40
Of.
2 30
111
o
I 20
0
0
10
30
TIME, days
Figure 36. Instantaneous chloroform (ICLR) breakthrough curves
for Contactor C, Phase 3-1.
-------
CONCENTRATION, ufl/I
eg ro
O) 00
m
o
m
-------
1
CO
CO
-h I— I
O 3
1 W
<-r-
O O
O 3
3 n-
rf Q
0 D
O
Q O
W -b
(D O
CO 3
I— 1
O
CT
3"
O
o
"J
(D
CO
CONCENTRATION, ug/1
r\> oo -u en
O)
CD
no
o
H
rn
CL
D
«
O>
O
00
I—
m
Q
m
-------
LEGEND
g
H
2
lil
U
O
o
25
15 .
5 _
0
INFLUENT
CONTACTOR D LEVEL 7 CD7>
CONTACTOR 0 LEVEL 4 CD43
CONTACTOR D EFF (CO
140
igure 39. Instantaneous chloroform CICLR) breakthrough curves
for Contactor D, Phase 3-2.
-------
Of*
CONCENTRATION,
rn
3
tf!
-------
CONCENTRATION, ug/I
-------
CONCENTRATION, ug/
-------
CONCENTRATION, uC/
-------
O
3
I
o
o
o
25
20 .
15 .
10
5 .
0
LE6ENO
INFLUENT
PILOT CONTACTOR LEVEL 3 CPFA3)
PILOT CONTACTOR LEVEL 2 CPFA2)
PILOT CONTACTOR EFF CPFAS5
60 80
TIME, daye
100
120
140
Figure 44. Instantaneous chloroform CICLR) breakthrough curves
for pilot contactors,, Phase 3-2.
-------
LEGEND
O
OL
h-
Itl
O
O
O
60
50 .
40 .
R 30 .
20
10 .
0
INFLUENT CSFEFD
PILOT CONTACTOR LEVEL 7 CPFA75
PILOT CONTACTOR LEVEL 8 CPFA6D
PILOT CONTACTOR LEVEL 6 CPFA8)
PILOT CONTACTOR EFF
200
100 150
TIME, days
Figure 45. Instantaneous chloroform (ICLR) breakthrough curves
for lignite pilot contactors, Phase 2-0.
250
-------
INFLUENT CFLBO
LEGEND
PILOT 6AC FILTER LEVEL 4 CRV4)
PILOT 6AC FILTER EFF CRVS)
45
40
- 35
O
3 38
\
| 25
h-
Z
kJ
O
Z
O
O
20
15
10
0
0
20
40
60
140
160
80 100 120
TIME, days
Figure 46. Instantaneous chloroform CICLR) breakthrough curves
for virgin pilot GAC filter. Phase 1-0.
180
200
-------
INFLUENT CFLIN3
LEGEND
VIRGIN PILOT SAC FILTER EFF CRV5)
8
68 80
TIME, days
100
120
140
Figure 47. Instantaneous chloroform CICLR) breakthrough curve for
virgin pilot GAC filter, Phase 2-1.
-------
LEGEND
INFLUENT CFLBO
VIR6IN PILOT GAC FILTER EFF CRVS)
8
0
60
TIME, days
Figure 48- Instantaneous chloroform (ICLR) breakthrough curve for
virgin pilot GAC filter, Phase 2-2.
-------
LEGEND
o
o
H
h-
<
Of.
h-
LJ
O
z
o
o
25
20 .
15 _
18 .
5 .
INFLUENT CFLBO
GAC FILTER 19A LEVEL 2 <19A2>
6AC FILTER I8A LEVEL i CIQAtD
6AC FILTER 19A EFF O8AE)
126
148
80 100
TIME, days
Figure 49. Instantaneous bromodichloromethane (ICL2) breakthrough
curves for GAC Filter 19A, Phase 1-0.
160
180
-------
lil
O
2
O
O
30
25
20 _
1 15
10 _
INFLUENT CFUQO
6AC FILTER 21A LEVEL 2 <2IA2>
LEGEND
6AC FILTER 21A LEVEL 1 C2IAO X X
SAC FILTER 2IA LEVEL 3 C2IA3) i H
6AC FILTER 2IA EFF <2IAE>
350
400
0
0 50 100 150 200 250 300
TIME, days
Figure 50. Instantaneous bromodichloromethane (ICL2) breakthrough
450
500
curves for GAC Filter 2IA, Phase 1-0.
-------
TS
43
C
cn
T W
G~> Q
>- 3
O «*•
Q
— ©
— O
n- C
e> w
O"
ro T
— o
>• 3
^ o
a.
-o —
D- o
o D-
w —
G> O
CO O
I 3
3-
o
D
O
ro
-»
o
o
CONCENTRATION,
v\
51
(^
I
-------
INFLUENT
in
to
\
O
Z
Id
O
O
O
25
20
15
10
0
10
20
30
70
80
90
40 50 60
TIME, days
Figure 52. Instantaneous bromodichloromethane (ICL2) breakthrough curves
for GAC Filter 21 A, Phase 3-2.
100
-------
r\>
CONCENTRATION, ug/l
4k O> GO O
a>
rn
8
-------
X
o
H
h-
<
Of
h-
2
LU
O
2
O
O
25
28 .
15 .
10 -
5 .
INFLUENT CFLDO
6AC FILTER 23A LEVEL 2 <23A2>
LEGEND
SAC FILTER 23A LEVEL I
6AC FILTER 23A LEVEL 3
6AC FILTER 23A EFF <23AE>
C23A1D
C23A3)
120
140
0
0 20 40 60 80 100
TIME, day*
Figure 54. Instantaneous bromodichIoromethane (ICL2) breakthrough
160
180
curves for GAC Filter 23A, Phase 1-0.
-------
LEGEND
Ul
Ln
O
o
a:
l-
UJ
o
o
INFLUENT (SFEF)
CONTACTOR A LEVEL 7
CONTACTOR A LEVEL 4 CA43
CONTACTOR A LEVEL 0 CA9)
CONTACTOR A EFF CAE5
25 .
20 .
15 .
18 -
5 .
0
150 200
TIME, days
250
300
350
Figure 55- Instantaneous bromodichIoromethane (ICL2) breakthrough curves
for Contactor A, Phase 3-0.
-------
95
CD
CONCENTRATION. uO/l
ro
en
CO
(9
m
G>
m
i
-------
CONCENTRATION, ug/i
-^ o>
ro *• o>
m
Q
rn
ro'
-------
8S
Q
-J
CONCENTRATION, ug/
IV)
o>
CO
ro
o>
-------
6S
CONCENTRATION,
-------
09
CONCENTRATION,
-------
T9
CO
c.
CONCENTRATION, ug/
r\>
en
m
I
o
ffi
-------
CONCENTRATION, ug/1
f*
3
rn
o
-------
CONCENTRATION, uo/l
-------
CONCENTRATION,
-------
LEGEND
a
z
a
i-
o
o
e
INFLUENT CSFEF>
CONTACTOR D LEVEL 7 CD7>
CONTACTOR P LEVEL 4
CONTACTOR 0 EFF CDE>
20
100
40 60 80
TIME, days
Figure 65 . Instantaneous bromodichloromethane (ICL2) breakthrough curves
for Contactor D, Phase 3-2.
140
-------
99
0
CONCENTRATION,
cn
cn
IS)
cs
tn
tn
-------
LEGEND
en
•-J
N.
a
z
o
I-
Id
O
O
O
38
25 .
20 .
15 .
10 _
5 _
INFLUENT
PILOT CONTACTOR LEVEL 3 CPFASD
PILOT CONTACTOR LEVEL 2 CPFA2> X X
PILOT CONTACTOR EFF CPFA55 -I ^
100 150
TIME, days
200
250
Figure 67. Instantaneous bromodichloromethane CICL2) breakthrough curves
for pilot contactors, Phase 3-0.
-------
89
c
o
CONCENTRATION, ua/l
— — rv>
-------
LEGEND
en
to
O
2
LJ
O
O
O
16
14
12
10
8
6
4
2
0
INFLUENT (SFEF>
PILOT CONTACTOR LEVEL 3
PILOT CONTACTOR LEVEL 2 CPFA23
PILOT CONTACTOR EFF CPFAS)
20
40
100
120
60 80
TIME, day*
Figure 69. Instantaneous bromodichloromethane QCL2) breakthrough curves
for pilot contactors, Phase 3-2.
148
-------
OL
CONCENTRATION, uC/I
-------
O
H
O
o
25
20 _
15 _
5 .
0
INFLUENT CFLBO
LEGEND
PILOT SAC FILTER LEVEL 4 CRV-O
PILOT SAC FILTER EFF
180
88 108 120
TIME, days
Figure 7!. Instantaneous bromodichIoromethane (ICL2) breakthrough curves
for virgin pilot 6AC filter, Phase 1-0.
200
-------
CONCENTRATION, u8/
— — ro
en co
-------
INFLUENT CFLDO
LEGEND
VIRGIN PILOT 6AC FILTER EFF CRV55
CJ
O
o
H
I
O
8
30
25 .
20 .
15 .
10 .
5 .
20
100
(20
40 60 80
TIME, day.
Figure 73. Instantaneous bror.odichloromethane (ICL2) breakthrough curve for
virgin pilot GAC filter, Phase 2-1.
140
-------
43
CONCENTRATION,
o
IVJ
m
rn
o
-------
sz.
CONCENTRATION, uO/I
ro u> -b. en o>
00
II
m
-------
CONCENTRATION, ug/
O)
©
O)
00
-------
LL
CONCENTRATION, uO/l
2p
c
en
-*> M
O D
n w
rr-
O Q
>• 3
O rr-
Q
-n D
— »
— o
**• c
fl> ffi
en
^ x-» HO
M 2
-o — 4 m
v^/ Q_
0
CT *<
tn
en
ro co
o o
-------
LEGEND
INFLUEHT CFLIhO
6AC FILTER 21A EFF C21AE3 X X
00
O
H
O
o
o
88
70
? 50
40
30
20
10
0
0
20
30
70
80
40 50 60
TIME, days
Figure 78. Instantaneous THM CITTT) breakthrough curves
for GAC Filter 21 A, Phase 3-2.
90
100
-------
INFLUENT CFLBO
LEGEND
6AC FILTER 2IA EFF <2tAE>
0
10
20
30
60
70
40 50
TIME, day*
Figure 79. Instantaneous THM CITTT) breakthrough curves
for GAC Filter 21 A, Phase 3-3.
80
-------
08
CONCENTRATION, ug/
CD
0)
O
cn
o
o>
00
-n
CO
-------
.18
CONCENTRATION, ug/
o>
00
CO
IV)
6)
-------
zs
CO
ro
O Q
rr- Q
Q 3
O O
rf O
O C
1 ft
Q
W
ffi
O
H
0>
O
3-
O
i
O
O
«
CO
CONCENTRATION, ug/I
ro o) 4». tn o> -j
tn
o
CD
©
00
(9
CO
CO
o
ro
o
m
8
51*
fei
\y w
II
-------
CONCENTRATION,
-------
CONCENTRATION,
i\> o> A. tn
o>
C9
00
m
CD
rn
09 03
-------
58
CONCENTRATION,
rs>
©
o>
GO
r\>
rn
rn
c?
-------
98
CONCENTRATION, uo/!
ro
CD
01
O>
m
G>
m
-------
LEGEND
00
100
90 .
O
0
INFLUENT CSFEF)
CONTACTOR C LEVEL 7 CC75
CONTACTOR C EFF CCED
100 150
TIME, days
200
250
Figure 87. Instantaneous THM CITTT) breakthrough curves
for Contactor C, Phase 3-0.
-------
88
S>
oo
o
1 W
r*-
o o
S D
3 rr-
«*• Q
Q 3
O »
«*• O
^ g
ro
o>
.
3" /-\ HO
O M 2
W — I HI
CD
00
CONCENTRATION, UQ/
ro jk o oo
O
8
«••»
Q
\s
m
i
II
-------
68
CONCENTRATION,
— —• l\> w
-------
06
CONCENTRATION, ug/I
N)
O>
©
00
eg
ro
§
m
o
m
-------
CONCENTRATION, ug/1
-------
CONCENTRATION, ug/
I
-------
CD
CONCENTRATION, uC/i
4*. O> 00
es>
ro
-------
LEGEND
X
a
z
o
H
z
ui
o
z
o
o
120
100 _
80
60 .
20 .
INFLUENT CSFEF)
PILOT CONTACTOR LEVEL 3 CPFA35
PILOT CONTACTOR LEVEL 2 CPFA2)
PILOT CONTACTOR EFF CPFA55
200
0 50 100 150
TIME, days
Figure 94. Instantaneous THM CITTT) breakthrough curves
for pi lot contactors, Phase 3-0.
250
-------
LEGEND
o
H
<
a
UJ
o
I
10 .
0
INFLUENT CSFEF)
PILOT CONTACTOR LEVEL 3 CPFA3>
PILOT CONTACTOR LEVEL 2 CPFA25
PILOT CONTACTOR EFF
20
40
80
60
TIME, days
Figure 95. Instantaneous THM (ITTT) breakthrough curves
for pi lot contactors, Phase 3-t.
100
120
-------
LEGEND
N
O
o
H
kl
L)
Z
O
O
INFLUENT «FEF>
PILOT CONTACTOR LEVEL 3
PILOT CONTACTOR LEVEL 2 CPFA2)
PILOT CONTACTOR EFF CPFAS>
60 80 100
TIME, days
Figure 96. Instantaneous THM CITTT) breakthrough curves
for pilot contactors, Phase 3-2.
120
140
-------
£6
CONCENTRATION, u8/I
©
o>
00
C3
(9
CD
-------
86
CONCENTRATION, ug/
CO
C»
00
m
I
-------
66
CONCENTRATION,
rn
o
m
I
-------
DOT
Of
CONCENTRATION, ug/l
o 3"
-> n
»
en o
>• i
o o-
o
o>
CSJ
ro
C9
O>
o 3
n c_
ro o
— <•»-
>. o
*• G.
CO D~
ffi
O
ZE
%
a
cr
o>
Q
7T
o
o
o
-I
r\>
6)
o
Q_
I
O>
o
CO
CD
i
3
IV>
-------
INFLUENT CFLEN>
LEGEND
6AC FILTER 2IA EFF C21AE5
80
70
60
z 50
o
H
30
20
10
0
0
10
20
30
60
70
80
90
40 50
TIME, days
Figure 101. Thr««-day simulated distribution system THM CSTT3) breakthrough curves
for GAC Filter 21 A, Phase 3-3.
-------
LEGEND
288
188 .
INFLUENT (SFEF3
CONTACTOR A LEVEL 7 CA7>
CONTACTOR A LEVEL 4 CA43 X X
CONTACTOR A LEVEL 9 CA05 H 1-
CONTACTOR A EFF
-------
-COT
o
~J
-------
LEGEND
N
O
3
Z
O
H
H
O
O
90
80
70
60
50
40
h-
I 30
20
10
0
0
INFLUENT CSFEF)
CONTACTOR A LEVEL 7 CA7>
CONTACTOR A LEVEL 4 CA45
CONTACTOR A EFF
20
60
TIME, days
100
120
Figure 104. Three-day simulated distribution system THM CSTT3) breakthrough curves
for Contactor A, Phase 3-2.
-------
LEGEND
o
Ul
140
128 .
_ 100 .
o
z
o
H
2
LJ
O
O
O
: 80 .
60 .
40 .
20
0
INFLUENT CSFEF3
CONTACTOR B LEVEL 7 CB7)
CONTACTOR B LEVEL 4
-------
90T
CONCENTRATION, ug/
O> 00
cs>
O> 00
-b —I
o rr
o a>
o i
D a.
<•«- Q
O -<
O
rt- W
O —
-i 3
TO —
CO Q
~D Q.
Q Q-
« —
O CO
rt-
CO 2,
«S> CT
O
rr-
B>
3
(D
Q
O
O
(ft
G>
H
m
*.
i
CL
n
o>
o
09
JS)
i
%
II
-------
LEGEND
o
S
O
3
O
H
h-
h-
Z
Id
O
I
123
108
80
60
20
0
0
INFLUENT CSFEF5
CONTACTOR BB LEVEL 7 CB87)
CONTACTOR BB LEVEL 4 CBB4)
CONTACTOR BB EFF CBBE>
20
40
100
120
140
60 80
TIME, days
Figure 107. Three-day simulated distribution system THM (STT3) breakthrough curves
for Contactor BB, Phase 3-1.
-------
LEGEND
o
CO
0 a INFLUENT
-------
TI
601
03
c
T
ft
CONCENTRATION,
CD
ro
O> 00
ro
a>
CD
oo
a
m
1
c?
-------
LEGEND
o
o
H
O
o
10 _
0
INFLUENT
COHTACTOR C LEVEL 7 CC7)
CONTACTOR C LEVEL 4 CC-O
CONTACTOR C EFF
-------
LEGEND
200
180
160
- 140
G»
3 120
\
H 100
I-
80
o
z
o
o
20
0
INFLUENT CSFEF>
CONTACTOR D LEVEL 7 CD7>
CONTACTOR D LEVEL 4 CD4)
CONTACTOR D EFF CDE>
0 20 40 60 80 100 120
TIME, days
Figure 111. Three-day simulated distribution system THM (STT3) breakthrough curves
for Contactor D, Phase 3-1.
-------
Tl
Q
o :r
"i -j
o
o o>
O I
u o_
«*- o
Q •<
O
-1 1
o —
*• o
o
co a,
CO
t
ro
cr
§
cr
o
o
CO
rn
V
a.
2TT
CONCENTRATION, uO/l
iv) w j>. en CD
-sj
es>
oo
<9
CO
ro
J I ! I I I I
I
p
vj
3
m
o
m
3
o
5
II
-------
00
CIT
CONCENTRATION,
tk CD 00 CD r\>
o>
00
-------
O
— Q.
o o
o w
o —
3 3
**• c
Q —
O Q
rr- <-f-
O
1 QL
(A
" 5:
-TD C5
3- c-f
Q 1
M _.
O CT
C
Oi «T-
I _
~ O
0)
CO
CONCENTRATION,
o>
o
oo
-;--- — r\>
CS f\J «^ O? Ow Q?
G>
N>
4v
O
S
m
- 8-
I 3
o>
o
CO
—i
—i
CO
tr
O
o
T
O
oo
o
m
CD
m
-------
LEGEND
o
o
H
I-
<
(X.
H
UJ
O
O
INFLUENT
PILOT CONTACTOR LEVEL 3 CPFA3}
PILOT CONTACTOR LEVEL 2 CPFA2)
PILOT CONTACTOR EFF CPFA5>
20
60 80
TIME, days
100
120
140
Figure 115. Three-day simulated distribution system THM CSTT3) breakthrough curves
for pilot contactors, Phase 3-2.
-------
LEGEND
INFLUENT CFLBO
GAC FILTER 19A LEVEL 2 <19A2>
6AC FILTER IOA LEVEL I CIQAO
GAC FILTER ISA EFF <19AE)
250
288
150
Z
o
H
UJ
O
Z
O
o
100
50
0
28
80 100
TIME, days
120
140
169
180
Figure !I6. Seven-day simulated distribution system THM CSTT7) breakthrough
curves for GAC Filter !9A, Phase 1-0.
-------
250
208 .
150 _
O
H
H-
£ 100 .
8
o
o
50
0
0
INFLUENT CFLDO
6AC FILTER 21A LEVEL 2 <21A2>
LEGEND
GAC FILTER 21A LEVEL 1 C2IAO
SAC FILTER 21A LEVEL 3 C2tA3>
6AC FILTER 2IA EFF C2IAE)
50
150
200 250 300
TIME, days
350
400
450
500
Figure IS7. Seven-day simulated distribution system THM CSTT7) breakthrough
curves for GAC Filter 21 A, Phase 1-8.
-------
CO
D D INFLUENT CFLDO
A A 6AC FILTER 23A LEVEL 2
C23A2)
250
LEGEND
6AC FILTER 23A LEVEL ! C23AO
SAC FILTER 23A LEVEL 3 C23A3)
SAC FILTER 23A EFF <23AE>
200
N
o
H
h-
<
U.
h-
UJ
o
8
150
100
50
0
26 48 60 80 100
TIME, days
120
140
160
180
Figure 118. Seven-day simulated distribution system THM CSTT7) breakthrough
curves for 6AC Filter 23A, Phase 1-0.
-------
GIT
CD
c
-J
03
-------
02T
CO
C
o
ro
o co
C G>
-5 <
< O
Ct> 3
(0 I
C_
-*» D
-.
O
Q.
«
O —
O O~
3 C
rt- rr-
o —
o o
w
•<
H
m
o.
o
A
ro
©
cr
(D
O
rr
o
o
01
H
00 0»
II
II
-------
258
208 .
150 .
Z
o
H
H
H 100 .
UJ
O
Z
O
o
50 .
0
0
INFLUEMT CFLDO
LEGEND
PILOT 6AC FILTER LEVEL 4 CRV-O
PILOT 6AC FILTER EFF CRV5)
20
60
140
160
180
200
80 100 120
TIME, days
Figure 121. Seven-day simulated distribution system THM (STT7) breakthrough curves
for virgin pilot GAC filter, Phase 1-0.
-------
LEGEND
to
to
O Q INFLUENT CFLDO
& A SAC FILTER 19A LEVEL 2
-------
en
CONCENTRATION, uO/
ro
GJ
cs>
en
ro
tn
o
CO
to
CD
S
CO
en
-------
INFLUENT
-------
SZT
CS)
o
en
-h —I
o o
CD —
>•
O O
ro
o
O
«3
—
O
j /•*» m
Q —» «•
O O O.
0> ^ •<
i cr •>
^^^ *^
* Cv O^
O
«>
G»
00
CD
en
CONCENTRATION, uo/I
~" en c»
cs>
S
CO
O>
o
(9
CS>
(9
es
m
I
IS)
i
<-»
ro
§
I
-------
°sZ1
CONCENTRATION, u«/I
CD CD CD CD CD CD CD
CD CD
ro
o>
o o
n f>-
D
O —
J*
O O
Zl§
o" o
o
ro D
a> cr
" O
•r *-s
Q — I
« O
0> O
ro
CD
CO
CD
HCD
0.
0
I O" « CD
o
7T
o
CD
CD
00
CD
CD
i t I I
rn
o
rn
i
M
>
/N
ro
I
I
-------
3586
3008
_ 2500 _
a
3
z
Id
O
O
2000
1500
1000
500
INFLUENT CFLDO
6AC FILTER 23A LEVEL 2 C23A2)
LEGEND
SAC FILTER 23A LEVEL 1 C23AO
6AC FILTER 23A LEVEL 3 C23A3>
SAC FILTER 23A EFF <23AE>
0 50 100 150
TIME, days
Figure 127. Total organic carbon (TOO breakthrough
curves for GAC Filter 23A, Phase 1-0.
200
250
-------
en
CONCENTRATION, ug/I
— —• ro i\>
o 01 o en
oo
CO
en
G>
(V
00
o o
~J rr-
o
o —
o
o o
<-l- "I
O Q
O O
r*- D
O —
1 O
>• o
* 0
T3 CT
3- O
0 D
CO O
I O
cr
«>
o
7T
o
o
o
(0
en
o
H
m
a.
n
en
GO
I
s
s
m
er>
m
CO
en
-------
631
CONCENTRATION,
CO
§
© en
CO CO
CO CO
CO
l\)
§
0
00
o
o
CO
cn
0
CD
c
ro
CO
-h —I
o o
-7 ci-
Q
O —
O
D O
rf "J
O CD
O Q
r*- D
O —
n o
*» o
" Q
-3 O-
3- O
O 3
W
CO O
I O
— v_/
' o-
&
o
O
O
o
"J
ro
H
H
m
O_
0
O)
CO
CO
CO
ro
o
5
n
rn
&
-------
LEGEND
INFLUENT CSFEF)
CONTACTOR A LEVEL 7
CA7>
CONTACTOR A LEVEL 4
-------
LEGEND
INFLUENT CSFEF3
CONTACTOR B LEVEL 7 CB7)
CONTACTOR B LEVEL 4
CONTACTOR B LEVEL 8 CB9>
3008
CONTACTOR B EFF (BE)
0
(00 150
TIME, days
200
ase
Figure 131 . Total organic carbon (TOO breakthrough curves
for Contactor B, Phase 3-0.
-------
2 re
CONCENTRATION, ug/
— — l\> l\> 03 OJ
ocn®cn®0i
O © G CSD CD CD
CD
CD
a>
ro
-b —f
O O
Q
3 O
rt- 1
Q CQ
O O
~l O
CD O
CD Q
V
™X3 O
3" D
O
o>
H
2
m
— i
o
O CL
w O
<
0" 0
? o>
o ®
-------
rci
8
CD
CONCENTRATION, uC/I
— — r\>
§cn CD
re|i ^a
CD CD 03
ro
§
CO
CO
es>
o o
T n-
Q
o —
§ o
n- 1
Q 43
n o
G9
•> o
Q
W
O
3
cr o>
§ a*
/~\ m
o
to r> Q.
i ^ o
• cr M
T
o
a
o
c
03
O
cs
II
m
o
m
1"
II
-------
en
G>
GJ
CONCENTRATION, uO/I
— — ro
CD {/! G?
IS)
II
si
f*
o co
t?
r
vj
o
m
I
c>
o
II
1"
o
I
II
-------
SCT
CONCENTRATION, uO/l
m
ffi
-------
H O
£ H
O* L
r*
u.
hi
O
O
O
2500
2000 _
1500 .
1000 .
500
0
LEGEND
INFLUENT CSFEF)
CONTACTOR C LEVEL 7 CC7>
CONTACTOR C LEVEL 4 COO
CONTACTOR C EFF
60
TIME, days
80
100
120
Figure 136. Total organic carbon CTOC) breakthrough curves
for Contactor C,, Phase 3-2.
-------
LEGEND
4880
3588
3888
2588
5 H 2888
u.
z 1588
u
o
z
S 1888
588
8
8
INFLUENT CSFEF)
CONTACTOR D LEVEL 7 CD7>
CONTACTOR D LEVEL 4 CM)
CONTACTOR D EFF CDE>
28
48
88
68
TIME, days
Figure 137. Total organic carbon (TOO breakthrough curves
for Contactor D, Phase 3-1.
188
128
-------
8CT
CONCENTRATION,
8
G»
G>
O
I O
ro ^>
o>
es>
H
m
0-
Q
Ǥ
o
o
c
(0
to
U\
O
CD
I
S
o
*+
s§
II
-------
SCI
CONCENTRATION, ug/
-------
LEGEND
3000
0
INFLUENT CSFEF)
PILOT CONTACTOR LEVEL 3 CPFA3>
PILOT CONTACTOR LEVEL 2 CPFA2D
PILOT CONTACTOR EFF CPFA53
200
100 150
TIME, days
Figure 140. Total organic carbon (TOO breakthrough curves
for pilot contactors, Phase 3-0.
250
-------
TfrT
ro co
CD en
CD CD
CD CD
CD
ro
Se
^D
CD CD
CO
Q O CD
W v-x
d>
CT
CO T
I tt>
— O
Q_
0
rr
o
i
o
0)
CO
CD
CD
CD
m
I
l\>
CD
-------
C9
(ft
ro
—«
o
8 -
S o
*t»
82
rt- T
rl
ro o
**•
e>
w
ZVT.
CONCENTRATION.
g i i
N>
II
w
I
i
ii
II
-------
LEGEND
INFLUENT CSFEF3
PILOT CONTACTOR LEVEL 7
-------
O H INFLUENT CFLBO
LEGEND
PILOT GAC FILTER LEVEL 4 CRV43
PILOT 6AC FILTER EFF CRV5J
3008
0
0
20
80 100 120
TIME, days
H0
160
Figure 144. Total organic carbon (TOO breakthrough curves
for virgfH pilot GAC filter, Phase 1-0.
180
200
-------
CONTACTOR 0 LEVEL 7
8
i
168
80
60
40
20
0
_J
I
5 -20
Of.
-40
-60
-80
0
20
40
60
140
160
80 100 120
TIME, day*
Figure 145. Carbon adcorbable organohalidee CCAOX) percent removal curves for
Contactor D, Pha«e 3-0.
180 200
-------
en
-10
6AC FILTER ISA LEVEL 1 CI9AD
LEGEND
6AC FILTER I9A LEVEL 2 C19A23
GAC FILTER 19A EFF C1QAE)
0 20 40 60 80 tOO
TIME, days
Figure 146. THM formation potential (FTTT) percent removal
curves for GAC Filter 19Ay Phase 1-0.
(80
-------
-10
0
LEGEND
GAC FILTER 21A LEVEL I C2IAO
6AC FILTER 21A LEVEL 3 <21A3>
6AC FILTER 21A LEVEL 2 C21A23
GAC FILTER 2IA EFF C21AE>
50
100
150
358
400
200 250 300
TIME, days
Figure 147. THM formation potential (FTTT) percent removal
curves for GAC Filter 21 A, Phase 1-0.
450
500
-------
LEGEND
CD
C
0
L
Q.
O
UJ
100
80
60
40 .
20 .
0 _
-20 .
-40 .
-60
0
6AC FILTER 23A LEVEL t C23AO
SAC FILTER 23A LEVEL 3 <23A3>
6AC FILTER 23A LEVEL 2 C23A23
GAC FILTER 23A EFF <23AED
20
40
120
140
80 100
TIME, days
Figure 148. THM formation potential (FTTT) percent removal
curves for GAC Filter 23A, Phse 1-0.
160
180
-------
.*»
c
0
L
a
UJ
a:
100
-40
0
LEGEND
CONTACTOR A LEVEL 4 CA
CONTACTOR A LEVEL 7 CA75
CONTACTOR A EFF CAE5
100
150
TIME,
250
200
days
Figure 149. THM formation potential CFTTT) percent removal
curves for Contactor A, Phase 3-0.
300
350
-------
LEGEND
Ul
o
CONTACTOR A LEVEL 4 CA4>
CONTACTOR A LEVEL 7 CA7> X X
CONTACTOR A EFF CAE3
60
TIME, days
Figure 150, THM formation potential (FTTT) percent removal curves
for Contactor A, Phase 3-1.
-------
190
88
c
0
c
48
o
2: on
UJ «*
o:
-28
8
LEGEND
CONTACTOR A LEVEL 4 CA4)
CONTACTOR A LEVEL 7 CA7>
CONTACTOR A EFF CAEi
28
48
88
68
TIME, days
Figure 151. THM formation potential (FTTT) percent removal
curves for Contactor A, Phase 3~2.
188
128
-------
LEGEND
Ul
to
-M
c
u
L
a
o
r
Id
108
80
60
40 _
20 .
0 .
-20 .
-40
0
CONTACTOR B LEVEL 4 CB4)
CONTACTOR B LEVEL 9 CB8>
CONTACTOR B LEVEL 7 CB7D
CONTACTOR B EFF CBE3
50
200
100 150
TIME, day*
Figure 152. THM formation potential (FTTT) percent removal
curves for Contactor B, Phase 3-0.
250
-------
Ul
U)
0
0
CONTACTOR BB LEVEL 4 CBB-O
LEGEND
CONTACTOR BB LEVEL 7 CBB7>
CONTACTOR BB EFF
20
40 60
TIME, days
Figure 153. THM formation potential CFTTT) percent removal
curves for Contactor BB, Phase 3-0.
100
120
-------
100
88
0
L
0.
o
S 20
0
-20
0
CONTACTOR BB LEVEL 4
-------
LEGEND
CONTACTOR C LEVEL 7 CC7>
CONTACTOR C EFF CCEJ
Ul
Ul
C
U
L
a
o
z
U
100
80
60
40
20
0
-20
0
50
200
100 150
TIME, days
Figure 155. THM formation potential (FTTD percent removal
curves for Contactor C, Phase 3-0.
250
-------
Ul
en
100
e
LEGEND
CONTACTOR C LEVEL 4 CC4>
CONTACTOR C LEVEL 7 CC7> X K
CONTACTOR C EFF CCE>
10
20
60
70
40 50
TIME, days
Figure 156. THM formation potential CFTTD percent removal
curves for Contactor C, Phase 3-1.
80
-------
LEGEND
tn
-J
180
-40
CONTACTOR C LEVEL 4 CC4>
CONTACTOR C LEVEL 7 CC75
CONTACTOR C EFF CCE>
60 80
TIME, days
Figure 157. THM formation potential (FTTT) percent removal
curves for Contactor C., Phase 3-2.
188
128
-------
LEGEND
Ul
00
100
-p
8
L
0.
o
til
60
40 .
20 .
0 _
-20
0
CONTACTOR D LEVEL 4 CD43
CONTACTOR D LEVEL 7 CD7!> X X
CONTACTOR D EFF CDE>
200
100 150
TIME, days
Figure 158. THM formation potential (FTTT) percent removal
curves for Contactor D., Phase 3-0.
250
-------
in
<£>
0
188
80
60
40
o
Z pa
UJ ^**
0
-20
0
LEGEND
CONTACTOR D LEVEL 4 CD4>
CONTACTOR D LEVEL 7 CD7)
CONTACTOR D EFF CDE>
20
40
80
100
60
TIME, days
Figure 159. THM formation potential (FTTT) percent removal curves
for Contactor D/ Phase 3-1.
120
-------
0
0
LEGEND
CONTACTOR 0 LEVEL 4 CD-O
CONTACTOR D LEVEL 7 CD73
CONTACTOR D EFF
-------
LEGEND
8
L
o
uj
OL
0
PILOT CONTACTOR LEVEL 2 CPFA23
PILOT CONTACTOR LEVEL A CPFAO
PILOT CONTACTOR LEVEL 3 CPFA33
PILOT CONTACTOR EFF
-------
C
0
L
o
hi
180
-20
60 .
40 _
20 _
0 .
0
PILOT CONTACTOR LEVEL 2 CPFA2>
LEGEND
PILOT CONTACTOR LEVEL 3 CPFA35
PILOT CONTACTOR EFF CPFAS5
58
200
100 150
TIME, days
Figure 162. THM formation potential (FTTT) percent removal
curves for pilot contactors, Phase 3-0.
250
-------
LEGEND
c
0
L
a
o
til
OC
0
PILOT CONTACTOR LEVEL 2 CPFA2)
PILOT CONTACTOR LEVEL 3 CPFA3> X K
PILOT CONTACTOR EFF
-------
100
-20
0
LEGEND
PILOT CONTACTOR LEVEL 2 CPFA2>
PILOT CONTACTOR LEVEL 3 CPFA3)
PILOT CONTACTOR EFF CPFASi
20
60 80
TIME, day*
100
120
140
Figure 164. THM formal ion potential CFTTT) percent removal
curves for pilot contactors. Phase 3-2.
-------
LEGEND
-40
PILOT CONTACTOR LEVEL 6 CPFA65
PILOT CONTACTOR LEVEL 8
PILOT CONTACTOR LEVEL 7 CPFA73
PILOT CONTACTOR EFF CPFAO)
8 50 100 150 200
TIME, days
Figure 165. THM formation potential (FTTT) percent removal
curves for lignite pilot contactors, Phase 2-8.
250
-------
CTi
c
0
0
L
o
3E
UJ
ce.
100
50
0
-50
-100
-150
6AC FILTER 19A LEVEL 1 <19AO
LEGEND
6AC FILTER I8A LEVEL 2 C18A23
6AC FILTER ISA EFF <18AE>
60
120
140
80 100
TIME, days
Figure 166. Instantaneous chloroform CICLR) percent removal
curves for GAC Filter 19A, Phase 1-0.
160
180
-------
LEGEND
180
50
c
u
L
0
Q.
O
LJ
0 .
-50 .
-100 .
-150 _
-200
0
6AC FILTER 2IA LEVEL 1 C21AO
6AC FILTER 21A LEVEL 3 <21A3>
6AC FILTER 21A LEVEL 2 C21A2D
6AC FILTER 2IA EFF C2IAE)
50
100
150
350
400
200 250 300
TIME, days
Figure 167- Instantaneous chloroform (ICLR) percent removal
curves for GAC Filter 21 A, Phase 1-0.
450
500
-------
LEGEND
01
03
D H GAC FILTER 23A LEVEL t C23AO
A A GAC FILTER 23A LEVEL 3 <23A3>
6AC FILTER 23A LEVEL 2 C23A23 X X
GAC FILTER 23A EFF C23AE3 i t
100
9
0
L
a
o
0
-50
-100
* -150
-200
-250
0
20
40
60
120
140
80 100
TIME, days
Figure 168. Instantaneous chloroform (ICLR) percent removal
curves for GAC Filter 23A, Phse 1-0.
160
-------
LEGEND
-60
CONTACTOR A LEVEL 4 CAO
CONTACTOR A LEVEL 9
CONTACTOR A LEVEL 7 CA73
CONTACTOR A EFF CAE5
58
tee
250
150 200
TIME, day*
Figure 169- Instantaneous chloroform (ICLR) percent removal
curves for Contactor A, Phase 3-0.
388
358
-------
C
0
C
a.
o
100
50
0
-50
-100
-150
0
LEGEND
CONTACTOR A LEVEL 4 CA
20
80
100
10 60
TIME, day*
Figure 170. Instantaneous chloroform CICLR) percent removal curves
for Contactor A, Phase 3-I.
120
-------
LEGEND
tee
80 _
c
•
0
{.
a
o
Ul
e .
-29 .
-49 .
-69 L
CONTACTOR A LEVEL 4 CA4>
CONTACTOR A LEVEL 7
CONTACTOR A EFF
6e 80
TIME, day*
Figure 171. Instantaneous chloroform (ICLR) percent removal
curves for Contactor A, Phase 3-2.
tee
120
-------
LEGEND
--J
K)
c
0
o
LJ
-60
100
80
60 .
40 .
20 .
0 .
-20 .
-40 .
0
CONTACTOR B LEVEL 4 CB4)
CONTACTOR B LEVEL 9 CB8>
CONTACTOR 0 LEVEL 7 CB7D
CONTACTOR B EFF CBE3
200
100 150
TIME, days
Figure 172. Instantaneous chloroform (ICLR) percent removal
curves for Contactor B, Phase 3-0.
250
-------
188
-88
0
CONTACTOR B8 LEVEL 4
LEGEND
CONTACTOR BB LEVEL 7
CONTACTOR BB EFF CBBE>
20
40 60
TIME, days
Figure 173. Instantaneous chloroform CICLR) percent removal
curves for Contactor BB, Phase 3-0.
100
120
-------
100
80
5 40
a ~~
o
Id
0
-20
-40
-60
0
CONTACTOR BB LEVEL 4 CBB4)
LEGEND
CONTACTOR BB LEVEL 7
CONTACTOR BB EFF CflBE)
20
40
100
120
60 80
TIME, days
Figure 174. Instantaneous chloroform CICLR) percent removal curves
for Contactor BB, Phase 3-1.
140
-------
LEGEND
CONTACTOR C LEVEL 7 CC75
CONTACTOR C EFF CCE3
100
80
C
0
L
a
o
kl
UL
40
20
0
-20
0
50
100 150
TIME, days
200
250
Figure 175- Instantaneous chloroform (ICLR) percent removal
curves for Contactor C, Phase 3-0.
-------
C
0
L
0.
o
UJ
a:
108
50
e
-50
-100
-150
0
LEGEND
CONTACTOR C LEVEL 4 CCO
CONTACTOR C LEVEL 7 CC7>
CONTACTOR C EFF CCO
10
20
30
60
70
40 50
TIME, days
Figure 176- Instantaneous chloroform CICLR) percent removal
curves for Contactor C, Phase 3-1.
-------
100
-40
0
LEGEND
CONTACTOR C LEVEL 4 CC4)
CONTACTOR C LEVEL 7 CC7J
CONTACTOR C EFF CCE3
20
40 60
TIME, days
Figure 177. Instantaneous chloroform (ICLR) percent removal
curves for Contactor C, Phase 3-2.
100
120
-------
00
180
-40
0
LEGEND
CONTACTOR D LEVEL 4 CD43
CONTACTOR D LEVEL 7 CD75 X X
CONTACTOR D EFF CDE)
50
200
100 150
TIME, days
Figure 178. Instantaneous chloroform (ICLR) percent removal
curves for Contactor D, Phase 3-8.
250
-------
LEGEND
.+*
C
0
L
a
o
100
50 .
0 .
-50 _
-100 .
-150 .
-200
CONTACTOR D LEVEL 4 CD4>
CONTACTOR 0 LEVEL 7 CD7J
CONTACTOR P EFF CDE>
20
40
60
TIME, days
80
100
120
Figure 179. Instanlaneoue chloroform CICLR) percent removal curves
for Contactor D, Phase 3-1.
-------
LEGEND
CO
O
100
S
0
L
a.
<
>
111
oc.
40 .
0
-20 .
-40 _
-60
0
CONTACTOR D LEVEL 4
20
CONTACTOR 0 LEVEL 7 CD7)
CONTACTOR D EFT
60 80
TIME, days
Figure 180. Instantaneous chloroform (ICLR) percent removal
curves for Contactor D, Phase 3-2.
-------
LEGEND
a:
-380
PILOT CONTACTOR LEVEL 2 CPFA2D
PILOT CONTACTOR LEVEL 4
-------
LEGEND
PILOT CONTACTOR LEVEL 2 CPFA2) PILOT CONTACTOR LEVEL 3 CPFA3)
A A PILOT CONTACTOR EFF CPFA53
c
0
0
o
UJ
ft
80
20
-20
-40
0
50
200
100 150
TIME, days
Figure 182. Instantaneous chloroform CICLR) percent removal
curves for pilot contactors, Phase 3-0.
250
-------
LEGEND
CD
U>
180
0
L
a
O
Id
0 _
-50 .
-100 .
-150 .
-200 .
-250
0
PILOT CONTACTOR LEVEL 2 CPFA25
PHOT CONTACTOR LEVEL 3 CPFA33
PILOT CONTACTOR EFF
20
60
TIME, days
80
100
120
Figure 183. Instantaneous chloroform (ICLR) percent removal curves
for pilot contactors, Phase 3-1.
-------
LEGEND
00
180
80
60
c
0
L
o
2:
UJ
a:
20
0
-20
-40
-60
0
PILOT CONTACTOR LEVEL 2
PILOT CONTACTOR LEVEL 3 CPFA33
PILOT CONTACTOR EFF CPFA55
20
40
100
60 80
TIME, day*
Figure 184. Instantaneous chloroform (ICLR) percent removal
curves for pilot contactors/ Phase 3-2.
120
140
-------
LEGEND
108
50 _
CD
(Jl
0
L
o
UJ
-50 .
-100 .
-150 _
-200 _
-250
0
PILOT CONTACTOR LEVEL 6 CPFA65
PILOT CONTACTOR LEVEL 8 CPFA85
PILOT CONTACTOR LEVEL 7 CPFA73
PILOT CONTACTOR EFF
-------
98T
REMOVAL, percent
< M
•V W
03 r^
— Q
3 3
<-•-
"o o
— a>
o o
n- C
U>
CD
3* O
O IT
""*? ®"
— O
cf -b
0> O
Q O
w r~
4> PD
^
—
I -0
fl>
O
0>
00
H
3
-
Q
•<
ro
(D
O
O
o
V)
o
->
o>
00
CD
I I I I I I
CO CO l\> IS) — — I
cn CD cn c& tf\ ^s cn
cn
i
p
m
o
m
I
-------
CD
c
0
L
0
a
kl
a:
100
50
0
-50
-100
-150
-200
0
6AC FILTER I9A LEVEL I CI9AI)
LEGEND
6AC FILTER ISA LEVEL 2 CI9A2)
SAC FILTER IOA EFF CI9AE)
20
40
60
120
140
80 100
TIME, days
Figure 187. Instantaneous bromodichloromethane (ICL2) percent removal
curves for GAC Filter 19A, Phase 1-8.
160
180
-------
LEGEND
00
00
6AC FILTER 2IA LEVEL t C2JAO
SAC FILTER 2IA LEVEL 3 <21A3>
6AC FILTER 21A LEVEL 2 C21A23 X X
6AC FILTER 21A EFF <21AE> < »-
100
0
-100
-*i
C
0
L -200
V
CL
o
UJ
-300
-400
-500
-600
0
50
100
150
350
400
200 250 300
TIME, days
Figure 188. Instantaneous bromodichloromethane CICL2) percent removal
curves for GAC Filter 21 A, Phase 1-0.
450
500
-------
LEGEND
-380
0
6AC FILTER 23A LEVEL 1 C23AO
6AC FILTER 23A LEVEL 3 C23A3>
6AC FILTER 23A LEVEL 2 C23A23
GAC FILTER 23A EFF <23AE)
20
40
120
140
100
TIME, days
Figure 189. Instantaneous bromodichloromethane QCL2) percent removal
curves for GAC Filter 23A, Phse 1-8.
160
180
-------
LEGEND
c
0
L
0.
O
LJ
U.
100
80
60 J
40 .
20 .
0 .
-20 .
-40 .
-60
CONTACTOR A
CONTACTOR A
LEVEL 4
LEVEL 8
CA4)
CA9>
CONTACTOR A LEVEL 7 CA7D
CONTACTOR A EFF CAE5
100
250
300
150 200
TIME, days
Figure 190. Instantaneous bromodichloromethane (ICL2) percent removal
curves for Contactor A, Phase 3-8.
350
-------
LEGEND
-80
CONTACTOR A LEVEL 4 CA4)
CONTACTOR A LEVEL 7 CA7>
CONTACTOR A EFF CAE>
80
108
60
TIME, day*
Figure 191. Instantaneous bromodichloromethane (ICL2) percent removal curves
for Contactor A, Phase 3-1.
120
-------
LEGEND
10
NJ
.*>
c
0
L
o
LJ
100
80
60
40
20
0
-20
-48
-60
0
CONTACTOR A LEVEL 4 CA4>
CONTACTOR A LEVEL 7
-------
LEGEND
CONTACTOR B LEVEL 4 CB4>
CONTACTOR B LEVEL 9 CB9)
CONTACTOR B LEVEL 7 CB7)
CONTACTOR B EFF CBE)
100
50
«^»
o
L
0.
_J
o
u
-50
-100 .
-150 .
-200
0
50
200
100 150
TIME, days
Figure 193. Instantaneous bromodichI oromethane CICL2) percent removal
curves for Contactor B, Phase 3-0.
250
-------
0
CONTACTOR BB LEVEL -4
LEGEND
CONTACTOR 88 LEVEL. 7
CONTACTOR BB EFF
28
40
60
TIME, days
Figure 194, Instantaneous bromodichloromethane CICL2) percent removal
curves for Contactor BB, Phase 3-0.
120
-------
1X1
Ul
-80
0
CONTACTOR BB LEVEL 4 CB8-O
LEGEND
CONTACTOR BB LEVEL 7 CBB7)
CONTACTOR BB EFF CBBE3
20
40
68 80
TIME, day.
Figure 195. Instantaneous bromodichloromethane CICL2) percent removal curves
for Contactor BB, Phase 3-1.
-------
LEGEND
CONTACTOR C LEVEL 7 CC7)
CONTACTOR C EFF
-------
100
-80
0
LEGEND
CONTACTOR C LEVEL 4 CC4>
CONTACTOR C LEVEL 7 CC7>
CONTACTOR C EFF CCO
10
30
60
70
80
40 50
TIME, day.
Figure 197. Instantaneous bromodichIoromethane CICL2) percent removal
curves for Contactor C, Phase 3-1.
-------
LEGEND
00
c
0
L
a
o
LJ
a
100
80 .
60 -
40 _
20 .
0 .
-20 .
-40 .
-60
0
CONTACTOR C LEVEL 4 CC4>
CONTACTOR C LEVEL 7
CONTACTOR C EFF
-------
LEGEND
ID
•**
«
0
L
a
180
80 .
60 .
40 .
20 .
O 0
-20 .
-40 .
-60
0
CONTACTOR D LEVEL 4 CD43
CONTACTOR D LEVEL 7 CD73
CONTACTOR D EFF CDE>
50
200
100 150
TIME, days
Figure 199. Instantaneous bromodichloromethane CICL2) percent removal
curves for Contactor D, Phase 3-0.
250
-------
10
O
O
-80
LEGEND
CONTACTOR 0 LEVEL -4 CD4>
CONTACTOR D LEVEL 7 CD7J
CONTACTOR D EFF CDE>
20
40
80
100
60
TIME, days
Figure 200. Instantaneous bromodichI oromethane (ICL2) percent removal curves
for Contactor D, Phase 3-1.
120
-------
LEGEND
to
o
108
80 .
.*»
c
0
i
>
UJ
-20 .
-40 .
-68
CONTACTOR 0 LEVEL 4 CD-O
CONTACTOR 0 LEVEL 7 CD7>
CONTACTOR D EFF
28
40
100
120
60 80
TIME, day*
Figure 201. Instantaneous bromodichloromethane (ICL2) percent removal
curves for Contactor D, Phase 3-2.
140
-------
LEGEND
to
O
W
-600
0
PILOT CONTACTOR LEVEL 2 CPFA23
PILOT CONTACTOR LEVEL 4 CPFA4)
PILOT CONTACTOR LEVEL 3 CPFA3D X X
PILOT CONTACTOR EFF CPFAS) 1 h
50
200
100 150
TIME, days
Figure 202. Instantaneous bromodichloromethane (ICL2) percent removal
curves for bituminous pilot contactors, Phase 2-0.
250
-------
O
u>
-60
LEGEND
PILOT CONTACTOR LEVEL 2 CPFA25 PILOT CONTACTOR LEVEL 3 CPFA33
A A PILOT CONTACTOR EFF CPFA53
200
50 100 150
TIME, days
Figure 203. Instantaneous bromodichloromethane (ICL2) percent removal
curves for pi lot contactors, Phase 3-0.
250
-------
LEGEND
c
o
O
UJ
100
80
68
40
20
0
-20
-40
-60
-80
-100
0
PILOT CONTACTOR LEVEL 2 CPFA2)
PILOT CONTACTOR LEVEL 3 CPFA35
PILOT CONTACTOR EFF CPFAW
20
40
80
100
60
TIME, days
Figure 204. Instantaneous bromodichloromethane CICL2) percent removal curves
for pilot contactors, Phase 3~1.
120
-------
LEGEND
ro
o
ui
c
0
L
o
Ul
u.
100 _
80 .
60 .
40 .
20 .
0 .
-20 .
-48 .
-60
PHOT CONTACTOR LEVEL 2
PILOT CONTACTOR LEVEL 3 CPFA33
PILOT CONTACTOR EFF CPTAS)
20
40
100
120
60 80
TIME, day*
Figure 205. Instantaneous bromodichIoromethane CICL2) percent removal
curves for pilot contactors., Phase 3-2.
140
-------
LEGEND
0 Q PILOT CONTACTOR LEVEL 6 CPFA63
A A PILOT CONTACTOR LEVEL 6
o
en
C
a
L
a.
-100 .
-200 _
I -300
Of.
-400 .
-500
0
200
100 150
TIME, days
Figure 206. Instantaneous bromodichloromethane THM (ICL2) percent removal
curves for lignite pilot contactors., Phase 2-0.
250
-------
LEGEND
PILOT GAC FILTER LEVEL 4 CRVO
PILOT 6AC FILTER EFF CRV5>
c
0
to *
o
ui
a:
100
50
0
-50
-108
-150
-200
-250
0
20
40
60
140
160
180
80 100 120
TIME, days
Figure 207. Instantaneous bromodichIoromethane (ICL2) percent removal curves for
virgin pilot GAC filter, Phase 1-0.
200
-------
O
CD
C
0
0
C
a.
o
z:
tu
D B 6AC FILTER 19A LEVEL 1 C19AD
LEGEND
SAC FILTER I9A LEVEL 2 CI9A23
SAC FILTER 19A EFF <19AE>
100
50
0
-50
-100
-150
20
60
120
80 100
TIME, days
Figure 208. Instantaneous THM (ITTT) percent removal
curves for GAC Filter 19A, Phase 1-0.
140
160
180
-------
108
-380
0
LEGEND
6AC FILTER 21A LEVEL 1 C21AO
6AC FILTER 21A LEVEL 3 C2!A3>
6AC FILTER 21A LEVEL 2 C21A2D
6AC FILTER 2IA EFF <2IAE>
100
150
350
200 250 300
TIME, days
Figure 209. Instantaneous THM (ITTT) percent remove
curves for GAC Filter 21 A, Phase 1-0.
400
450
500
-------
01Z
REMOVAL, percent
I
VJ
II
-------
112
REMOVAL, p«rc«nt
1
§
-------
100
60
•£ 40
•
o
t 20
o
LJ
U.
-40
-60
-80
0
LEGEND
CONTACTOR A LEVEL 4 CA4>
CONTACTOR A LEVEL 7 CA75
COKTACTOR A EFF CAE)
20
40
80
60
TIME, days
Figure 212. Instantaneous THM CITTT) percent removal curves
for Contactor A, Phase 3-1.
100
120
-------
LE6END
NJ
h-"
U)
189
-40
e
CONTACTOR A LEVEL 4 CA4>
CONTACTOR A LEVEL 7 CA7>
CONTACTOR A EFF CAE3
120
Figure 213. Instantaneous THM CITTT) percent removal
curves for Contactor A, Phase 3-2.
-------
LEGEND
CONTACTOR B LEVEL 4 CB4)
CONTACTOR B LEVEL Q CB8>
CONTACTOR B LEVEL 7 CB73
CONTACTOR B EFF CBE3
180
-80
0 50 100 150
TIME, day*
Figure 214. Instantaneous THM CITTT) percent removal
curves for Contactor B, Phase 3-0.
200
250
-------
-68
CONTACTOR B8 LEVEL 4 CBB4>
LEGEND
CONTACTOR BB LEVEL 7
CONTACTOR BB EFF CBBE>
60
TIME, days
Figure 215. Instantaneous THM CITTD percent removal
curves for Contactor BB, Phase 3-0.
120
-------
IS B CONTACTOR BB LEVEL 4 CBBO
LEGEND
CONTACTOR BB LEVEL 7 CBB75
CONTACTOR BB EFF CBBE>
100
-60
40
100
60 80
TIME, days
Figure 216- Instantaneous THM (ITTT) percent removal curves
for Contactor BB, Phase 3-1.
120
H0
-------
LEGEND
CONTACTOR C LEVEL 7 CC7)
CONTACTOR C EFF CCE5
100
-20
50 100 150
TIME, days
Figure 217. Instantaneous THM (ITTT) percent removal
curves for Contactor C, Phase 3-0.
200
250
-------
CD
188
jj 49
Q. ~xv
o
0 .
-20 .
-40 .
-60
CONTACTOR C LEVEL 4 CC4>
LEGEND
CONTACTOR C LEVEL 7 CC7)
CONTACTOR C EFF CCE)
60
40 50
TIME, day*
Figure 218. Instantaneous THM (ITTD percent removal
curves for Contactor C, Phase 3-1.
70
80
90
-------
LEGEND
-40
CONTACTOR C LEVEL 4 CC4)
CONTACTOR C LEVEL 7 CC75
CONTACTOR C EFF CCE5
60 80
TIME, days
Figure 219. Instantaneous THM (ITTT) percent removal
curves for Contactor C, Phase 3-2.
100
120
-------
LEGEND
K)
K)
O
100
80
0
t 40
O
z:
UJ
20 .
0 .
-20 _
-40
CONTACTOR 0 LEVEL 4 CD4)
CONTACTOR 0 LEVEL 7 C075
CONTACTOR D EFF CDE>
50 (00 150
TIME, days
Figure 220. Instantaneous THM CITTT) percent removal
curves for Contactor D, Phase 3-0.
200
250
-------
Is)
-80
LEGEND
CONTACTOR 0 LEVEL A COO
CONTACTOR D LEVEL 7 CD7J
CONTACTOR D EFF CDE)
20
40
80
60
TIME, days
Figure 221. Instantaneous THM CITTT) percent removal curves
for Contactor D, Phase 3-1.
100
120
-------
1-0
NJ
LEGEND
a m CONTACTOR D LEVEL 4 CD4)
CONTACTOR D LEVEL 7 CD75
tee
-4e
e
20
CONTACTOR D EFF CDE5
100
40 60 80
TIME, days
Figure 222. Instantaneous THM CITTT) percent removal
curves for Contactor D, Phase 3-2.
120
148
-------
LEGEND
100
50 .
Ul
-P
8
L
«
a
<
>
o
UJ
-350
PILOT CONTACTOR LEVEL 2 CPFA23
PILOT CONTACTOR LEVEL 4 CPFA4D
PILOT CONTACTOR LEVEL 9 CPFA33
PILOT CONTACTOR EFF CPFA5)
50
200
100 150
TIME, days
Figure 223. Instantaneous THM (ITTT) percent removal
curves for bituminous pilot contactors,, Phase 2-0.
250
-------
LEGEND
N)
K>
0
L
Q.
O
UJ
a:
PILOT CONTACTOR LEVEL 2 CPFA2>
PILOT CONTACTOR LEVEL 3 CPFA33
PILOT CONTACTOR EFF CPFAS5
100
80
60
20
0
-20
0 50 100 150
TIME, days
Figure 224. Instantaneous THM CITTT) percent removal
curves for pi lot contactors, Phase 3-0.
200
250
-------
LEGEND
100
80
60
1 40
0
• 20
a
-J
o
UJ
OL
0
-20
-40
-60
-80
0
PILOT CONTACTOR LEVEL 2 CPFA25
PILOT CONTACTOR LEVEL 3 CPFA3)
PILOT CONTACTOR EFF
20
40
80
60
TIME, days
Figure 225. Instantaneous THM CITTT) percent removal curves
for pilot contactors,, Phase 3-1.
100
120
-------
fO
100
80 -
60 .
c
L 40
a
o
20 _
0 .
-20 .
-40
0
LEGEND
PILOT CONTACTOR LEVEL 2 CPFA2> PILOT CONTACTOR LEVEL 3 CPFA3J
A A PILOT CONTACTOR EFF CPFA5)
20
40
60 80
TIME, days
100
Figure 226. Instantaneous THM CITTT) percent removal
curves for pilot contactors, Phase 3-2.
120
-------
LEGEND
IxJ
ho
-308
PILOT CONTACTOR LEVEL 6 CPFA8D
PILOT CONTACTOR LEVEL 8
-------
LEGEND
PILOT 8AC FILTER LEVEL 4 CRV-O
PILOT 6AC FILTER EFF CRVS)
100
S3
CO
0
C
L -50
a
3 -100
o
Ul
* -150
-200
-250
0
20
40
60
140
160
80 100 120
TIME, days
Figure 228. Instantaneous THM CITTT) percent removal curves for
virgin pilot GAC filter,, Phase 1-0.
180 200
-------
LEGEND
c
o
L
a
o
Id
108
18 .
8
8
CONTACTOR A LEVEL 4 CA4)
CONTACTOR A LEVEL 8 CAW
CONTACTOR A LEVEL 7
-------
LEGEND
C
0
0
L
o
kJ
Of
100
80
60
20
0
-20
0
CONTACTOR A LEVEL 4 CA4)
CONTACTOR A LEVEL 7 CA7>
CONTACTOR A EFF CAE>
20
60
TIME, days
Figure 238- Three-day simulated distribution system THM CSTT3) percent removal
curves for Contactor A, Phase 3-1.
-------
LEGEND
•*»
c
9
0
L
0.
bJ
108
80 .
60 .
40 .
20 .
0 .
-20
0
COKTACTOR A LEVEL 4 CA4>
CONTACTOR A LEVEL 7 CA7>
CONTACTOR A EFF CAE)
20
100
40 60
TIME, day*
Figure 231. Three-day simulated distribution system THM (STT3) percent removal
curves for Contactor A, Phase 3-2.
120
-------
LEGEND
100
-40
0
CONTACTOR B LEVEL 4 CBO
CONTACTOR 0 LEVEL 9
CONTACTOR B LEVEL 7 CB7) X X
CONTACTOR B EFF CBED -I 1-
200
100 150
TIME, days
Figure 232. Three-day simulated distribution system THM CSTT3) percent removal
curves for Contactor B, Phase 3-0.
250
-------
C
0
L
0.
o
UJ
100
90
80
70
60
50
40
30
20
10
0
0
CONTACTOR 88 LEVEL 4 (884)
LEGEND
CONTACTOR 88 LEVEL 7
CONTACTOR 88 EFF CBBE>
20
40 60
TIME, days
80
100
120
Figure 233. Three-day simulated distribution system THM (STT3) percent removal
curves for Contactor BB, Phase 3-0.
-------
100
80
60
« 40
L
a
20
o 0
UJ
tt
-20
-40
-60
0
CONTACTOR BB LEVEL 4 CBB4)
LEGEND
CONTACTOR BB LEVEL 7 CBB7>
CONTACTOR BB EFF CBBE3
20
40
60 80
TIME, days
100
120
140
Figure 234. Three-day simulated distribution system THM CSTT3) percent removal
curves for Contactor BB, Phase 3-1.
-------
LEGEND
CONTACTOR C LEVEL 7 CC7)
CONTACTOR C EFF CCE3
OJ
100
90
80
•2 ?0
S 60
L
* 50
o
z
Id
48
30
20
10
0
0
50
200
100 150
TIME, days
Figure 235. Three-day simulated distribution system THM (STT3) percent removal
curves for Contactor C, Phase 3-0.
250
-------
N5
CO
0
0
CONTACTOR C LEVEL 4 COO
LEGEND
CONTACTOR C LEVEL 7 CC7>
CONTACTOR C EFF CC£>
10
20
60
70
80
40 50
TIME, day*
Figure 236. Three-day simulated distribution system THM CSTT3) percent removal
curves for Contactor C, Phase 3-1.
90
-------
108
.*»
c
0
L
a
o
UJ
Of.
-20 _
-40
0
LEGEND
CONTACTOR C LEVEL 4 CC4)
CONTACTOR C LEVEL 7
CONTACTOR C EFF CCE)
20
40
60
TIME, days
100
128
Figure 237. Three-day simulated distribution system THM CSTT3) percent removal
curves for Contactor C, Phase 3-2.
-------
LEGEND
CO
00
CONTACTOR D LEVEL 4 CM3
CONTACTOR D LEVEL 7 CD7)
CONTACTOR D EFF CDE>
§
L
a
^
_J
o
Id
a
0 -
-10
0
200
50 100 150
TIME, days
Figure 238- Three-day simulated distribution system THM CSTT3) percent removal
curves for Contactor D., Phase 3-8.
250
-------
LEGEND
N5
OJ
100
c
0
L
Q.
O
T.
Id
o:
80 .
60 .
40 .
20 .
0 .
-20
0
CONTACTOR D LEVEL 4 CD4)
CONTACTOR D LEVEL 7 CD7>
CONTACTOR D EFF CDE)
20
40 60
TIME, daye
80
100
120
Figure 239. Three-day simulated distribution system THM (STT3) percent removal
curves for Contactor D, Phase 3-1.
-------
LEGEND
-M
c
0
0
a
o
ui
a:
108
88
60
40
20
0
-20
0
CONTACTOR D LEVEL 4 CM)
CONTACTOR D LEVEL 7
CONTACTOR D EFF CDE)
20
40
100
120
60 80
TIME, days
Figure 240. Three-day simulated distribution system THM (STT3) percent removal
curves for Contactor D, Phase 3-2.
140
-------
LEGEND
-40
PILOT CONTACTOR LEVEL 2 CPFA2>
PILOT CONTACTOR LEVEL 3 CPFA3J
PILOT CONTACTOR EFF CPFA53
0
50
200
100 150
TIME, days
Figure 241. Three-day simulated distribution system THM CSTT3) percent removal
curves for pi lot contactors, Phase 3-0.
250
-------
LEGEND
100
80
60
c
0
L
a
o
& 20
0
-20
0
PILOT CONTACTOR LEVEL 2 CPFA2)
PILOT CONTACTOR LEVEL 3 CPFA3>
PILOT CONTACTOR EFF
-------
108
-28
LEGEND
PILOT CONTACTOR LEVEL 2 CPFA2) PILOT CONTACTOR LEVEL 3 CPFA35
A A PILOT CONTACTOR EFF CPFA53
8
28
48
68 88
TIME, days
188
148
Figure 243. Three-day simulated distribution system THM (STT3) percent removal
curves for pilot contactors, Phase 3-2.
-------
e
0
LEGEND
6AC FILTER 19A LEVEL t C19AO
GAC FILTER I9A LEVEL 2 CI9A25 x X
6AC FILTER 19A EFF O9AE>
40
60
120
140
168
80 100
TIME, days
Figure 244. Seven-day simulated distribution system THM (STT7) percent removal
curves for GAC Filter 19A, Phase 1-0.
180
-------
Ol
LEGEND
19 K 6AC FILTER 2IA LEVEL 1 C21AO
h & 6AC FILTER 21A LEVEL 3 <21A3>
6AC FILTER 21A LEVEL 2 C21A23
6AC FILTER 2IA EFF C21AE)
100
0
L
0
a
<
>
o
60 .
20 _
0 _
-20
8
100
150
350
400
450
200 250 300
TIME, days
Figure 245. Seven-day simulated distribution system THM (STT7) percent removal
curves for GAC Filter 21 A, Phase 1-0.
500
-------
LEGEND
ON
c
0
L
1
o
UJ
188
80 .
60 .
40 .
20 .
0 .
-20
0
6AC FILTER 23A LEVEL 1 C23A15
SAC FILTER 23A LEVEL 3 C23A3)
6AC FILTER 23A LEVEL 2 C23A25
SAC FILTER 23A EFF <23AEi>
20
40
140
160
60 80 100
TIME, days
Figure 246. Seven-day simulated distribution system THM (STT7) percent removal
curves for GAC Filter 23A, Phase 1-0.
180
-------
LEGEND
-40
0
PILOT CONTACTOR LEVEL 2 CPFA2D
PILOT CONTACTOR LEVEL 4 CPFA-O
PILOT CONTACTOR LEVEL 3 CPFA3D
PILOT CONTACTOR EFF CPFAS3
258
Figure 247. Seven-day simulated distribution system THM (STT7) percent removal
curves for bituminous pilot contactors., Phase 2-0.
-------
LEGEND
PILOT CONTACTOR LEVEL 6 CPFA63
PILOT CONTACTOR LEVEL 8 CPFA8)
PILOT CONTACTOR LEVEL 7 CPFA75
PILOT CONTACTOR EFF
to
•O
00
-40
0 50 100 150 200
TIME, days
Figure 248. Seven-day simulated distribut ion system THM (STT7) percent removal
curves for lignite pilot contactors,, Phase 2-0.
250
-------
LEGEND
PILOT SAC FILTER LEVEL 4 CRV4)
PILOT 6AC FILTER EFF (RVS)
-*»
c
u
L
a
o
100
80
60
40
20 .
0 .
-20
20 40 60 80 100 120
TIME, days
140
160
180
200
Figure 249. Seven-day simulated distribution system THM (STT7) percent removal
curves for virgin pilot GAC filter, Phase 1-0.
-------
U1
o
-40
8
QIC FILTER I9A LEVEL 1 ClflAO
LEGEND
GAC FILTER \QA LEVEL 2 CJ9A23
6AC FILTER 19A EFF <18AE>
50
100 150
TIME, days
Figure 250. Total organic carbon (TOO percent removal
curves for GAC Filter 19A, Phase 1-0.
200
250
-------
180
-40
LEGEND
6AC FILTER 2IA LEVEL t C21AO
6AC FILTER 21A LEVEL 3 (21A3)
6AC FILTER 2IA LEVEL 2 C2IA25
6AC FILTER 21A EFF C21AE)
100
150
200
TIME, days
250
300
350
400
Figure 251. Total organic carbon (TOO percent removal
curves for GAC Filter 21 A., Phase 1-0.
-------
LEGEND
to
Cn
N>
-60
0
6AC FILTER 23A LEVEL t C23AO
6AC FILTER 23A LEVEL 3 C23A3)
6AC FILTER 23A LEVEL 2 C23A2D
GAC FILTER 23A EFF C23AE)
100 150
TIME, days
Figure 252. Tola I organic carbon (TOO percent removal
curves for GAC Filter 23A, Phse 1-9.
200
250
-------
LEGEND
U>
0
a
o
z
U
108
80
60
20 .
0 .
-20
CONTACTOR A LEVEL 4 CA4)
CONTACTOR A LEVEL 8 CA8>
CONTACTOR A LEVEL 7 CA7)
CONTACTOR A EFF CAE5
50
100
250
150 200
TIME, days
Figure 253. Total organic carbon CTOC) percenl removal
curves for Contactor A, Phase 3-8.
300
350
-------
100
a
hi
QL
70
60
c
0
0
I 50
30
20
10
0
-10
Q
LEGEND
CONTACTOR A LEVEL 4 CA4>
CONTACTOR A LEVEL 7 CA75
CONTACTOR A EFF CAE>
20
80
100
40 60
TIME, days
Figure 254. Total organic carbon (TOO percent removal curves
for Contactor A, Phase 3-1.
120
-------
.*»
c
LJ
80
70
60
t 50
a
J 40
30
20
10
0
0
CONTACTOR A LEVEL 4 CA4>
LEGEND
CONTACTOR A EFF
CONTACTOR A LEVEL 7 CA7)
20
40
80
60
TIME, days
Figure 255. Total organic carbon (TOO percent removal
curves for Contactor A, Phase 3-2.
100
120
-------
LEGEND
Ln
ON
CONTACTOR B LEVEL 4 CB4)
CONTACTOR B LEVEL 9
CONTACTOR B LEVEL 7 CB7) X X
CONTACTOR B EFF CBE5 ^ *
108
80
0
L
a
o
ui
a:
40 .
20 .
0 .
-20
0 50 100 150 200
TIME, days
Figure 256. Total organic carbon CTOC) percent removal
curves for Contactor B,, Phase 3-0.
250
-------
o
u
or
96
88
70
•£ 60
o
« 50
a
30
20
10
0
CONTACTOR B8 LEVEL 4
LEGEND
CONTACTOR BB LEVEL 7
CONTACTOR BB EFF
20
40
80
60
TIME, days
Figure 257. Total organic carbon (TOO percent removal
curves for Contactor BB, Phase 3-0.
100
120
-------
U/l
CO
_J
o
98
88
70
60
.**
o 50
L
40
30
20
10
0
-10
0
CONTACTOR BB LEVEL 4 CBB4>
LEGEND
CONTACTOR BB LEVEL 7
CONTACTOR BB EFF CBBE3
20
100
40 60 80
TIME, day*
Figure 258. Total organic carbon (TOO percent removal curves
for Contactor BB, Phase 3-1.
120
140
-------
LEGEND
N>
Cn
100
80
60
.+>
c
L 40
Q.
O
20
0
-20
-40
0
CONTACTOR C LEVEL A CCO
CONTACTOR C LEVEL 7 CC75
CONTACTOR C EFF (CE>
50
200
100 150
TIME, days
Figure 259. Total organic carbon (TOO percent removal curves
for Contactor C, Phase 3-8.
250
-------
-20
CONTACTOR C LEVEL 4 CC-O
LEGEND
CONTACTOR C LEVEL 7 CC7>
CONTACTOR C EFF CCE>
10
20
30
40 50
TIME, days
Figure 260. Tola! organic carbon CTOC) percent removal
curves for Contactor C, Phase 3-1.
-------
LEGEND
CONTACTOR C LEVEL 4 CC4>
CONTACTOR C LEVEL 7 CC7>
CONTACTOR C EFF COD
ON
C
0
L
a
o
Ui
a
80
70
60
50
40
30
20
10
0
-10
0
20
40
80
60
TIME, days
Figure 261 . Total organic carbon (TOO percenl removal
curves for Contaclor C^ Phase 3-2.
100
120
-------
100
c
0
L
O
LJ
at
80 .
60
20 .
0 .
-20
0
LEGEND
CONTACTOR D LEVEL 4 OVO
CONTACTOR D LEVEL 7 CD7)
CONTACTOR D EFF CDE5
50
100 150
TIME, days
Figure 262. Total organic carbon (TOO percent removal
curves for Contactor D, Phase 3-0.
200
250
-------
LEGEND
ho
Os
OJ
c
0
UJ
100
90
80
70
60
50
40
30
20
10
0
-10
0
CONTACTOR D LEVEL 4 CD43
CONTACTOR D LEVEL 7 CD7>
CONTACTOR D EFF CDE>
20
80
40 60
TIME, days
Figure 263. Total organic carbon (TOO percent removal curves
for Contactor D, Phase 3-1.
100
120
-------
0
C
a
o
UJ
oc
100
0
CONTACTOR D LEVEL 4 CD4)
LEGEND
CONTACTOR D EFF
CONTACTOR D LEVEL 7 CD73
20
40
100
60 80
TIME, days
Figure 264. Total organic carbon (TOO percent removal
curves for Contactor D, Phase 3-2.
120
-------
LEGEND
ON
Ol
-80
PILOT CONTACTOR LEVEL 2 CPFA23
PILOT CONTACTOR LEVEL 4 (PFA4)
PILOT CONTACTOR LEVEL 3 CPFA3D
PILOT CONTACTOR EFF
50 100 150 200
TIME, days
Figure 265. Total organic carbon (TOO percent removal
curves for bituminous pilot contactors, Phase 2-0.
250
-------
LEGEND
NJ
ON
Ox
-*>
0
0
L
a
^
o
LJ
108
88
68 J
48 .
20 .
0 .
-28
0
PILOT CONTACTOR LEVEL 2 CPFA2>
PILOT CONTACTOR LEVEL 3 CPFA3) X X
PILOT CONTACTOR EFF CPFA53
188 150
TIME, days
Figure 266. Total organic carbon (TOO percent removal
curves for pilot contactors/ Phase 3-0.
200
250
-------
ON
tea
90
88
o 60
50
40
30
20
10
0
o
Ui
0
LEGEND
PILOT CONTACTOR LEVEL 2 CPFA2> PILOT CONTACTOR LEVEL 3 CPFA33
A A PILOT CONTACTOR EFF
20
80
40 60
TIME, days
Figure 267. Total organic carbon (TOO percent removal curves
for pilot contactors, Phase 3-1.
100
120
-------
LEGEND
Ov
00
0
L
o
kJ
a
90
80
70
60
50
40
30
20
10
0
-10
PILOT CONTACTOR LEVEL 2 CPFA2)
PILOT CONTACTOR LEVEL 3 CPFA3)
PILOT CONTACTOR EFF CPFA53
20
40
100
60 80
TIME, days
Figure £68. Total organic carbon (TOO percent removal
curves for pi lot contactors, Phase 3-2.
120
140
-------
LEGEND
ISJ
ON
10
-P
c
0
L
0.
O
UJ
108
80
68
48 .
20 _
0 .
-20 .
-40 .
-60
PILOT CONTACTOR LEVEL 8 CPFA63
PILOT CONTACTOR LEVEL 8
PILOT CONTACTOR LEVEL 7 CPFA75
PILOT CONTACTOR EFF
-------
LEGEND
PILOT 6AC FILTER LEVEL 4 CRV-O
PILOT 6AC FILTER EFF CRV5>
NS
-~J
O
C
0
L
o
LJ
oe.
100
80
60 .
40 .
20 .
0 .
-20
20
40
60
140
160
80 160 120
TIME, days
Figure 270. Total organic carbon (TOO percent removal curves for
virgin pilot GAC filter,, Phase 1-0.
180
200
-------
LEGEND
6AC FILTER ISA EFF C19AE3
6AC FILTER 2IA EFF C21AE3
220
200
180
160
? 140
o
z
o
o
120
\
z
o
H
< 100
QL
80
60
40
20
0
0
10
20
30 40
TIME, days
50
60
70
Figure 271. THM formation potential (FTTT) concentration curves for
GAC Filter 19A and 21A effluents, Phase 1-0.
-------
LEGEND
SAC FILTER ISA EFF C18AE>
6AC FILTER 2IA LEVEL 2 C21A23
250
200 .
N>
-~J
N5
\
0»
o
H
QL
H
kl
O
O
O
150 .
100 .
50 .
0
0
10
20
30 40
TIME, day*
50
60
Figure 272. THM formation potential CFTTT) concentration curves for
GAC Filters 21A level 2 and 19A effluent, Phase 1-0.
-------
LEGEND
FILTER INFLUENT CFLBO
CONTACTOR INFLUENT CSFEF)
GAC FILTER ISA EFF CI5AE)
CONTACTOR C LEVEL 7 CC7>
400
350
300
? 250
H 200
tt
111
o
z
158
8 100
50
0
0
10 15 20 25
TIME, day*
30
35
45
FIGURE 273. THM formation potential CFTTD breakthrough curves for GAC
Filter ISA effluent and Contactor C level 1, Phase 3-1.
-------
ho
^J
-p-
480
358
300
? 250
z
H 200
2 150
LJ
O
Z
8 100
50
0
0
INFLUENT CFLDO
LEGEND
PILOT GAC FILTER EFF CRV33
SAC FILTER ISA EFF CISAE)
-a
10
15
30
35
40
20 25
TIME, days
Figure 274. THM formation potential CFTTT) breakthrough curves for
pilot GAC filter and GAC Filter ISA effluents, Phase 3-t.
45
-------
N5
250
200 .
X
o
O
H
fid
H
kl
O
§
O
150 .
100 .
0
INFLUENT CFLBO
LEGEND
PILOT SAC FILTER EFF CRV33
GAC FILTER ISA EFF O5AE>
10
15
30
35
20 25
TIME, day*
Figure 275. THM formation potential (FTTT) breakthrough curves for pilot
GAC filter and GAC Filter ISA effluents, Phase 3-2.
45
-------
X
a
o
H
<
QL
UJ
O
O
O
250
200
150
100
50
0
0
INFLUENT CFLIN)
LEGEND
PILOT 6AC FILTER EFF CRV3)
6AC FILTER ISA EFF CISAE)
10
20
30 40
TIME, days
50
60
70
Figure 276. THM formation potential (FTTD breakthrough curves for pilot
GAC filter and 6AC Filter ISA effluents., Phase 3-3.
-------
450
400
0
0
INFLUENT
LEGEND
PILOT 6AC FILTER EFF CRV53
6AC FILTER ISA EFF C15AE)
50
200
100 150
TIME, days
Figure 277. THM formation potential (FTTT) breakthrough curves for
pilot GAC filter and GAC Filter ISA effluents, Phase 3-0.
250
-------
2}
c
ro
oo
0 3
©
3 -b
O O
" "5
O
-O C
O O
ro T
j_ <
• w
"J
(9
00
-------
Si
480
358
386
? 258
z
H 200
tt
z 150
kl
O
Z
S 100
50
0
0
INFLUEKT CFLIW
LEGEND
TWICE REGENERATED PILOT 6AC FILTER EFF CRV35
VIRGIN PILOT 6AC FILTER EFF CRV5>
28
48
88
188
68
TIME, days
Figure 279. THM formation potential (FTTT) breakthrough curves for virgin and
twice regenerated pilot GAC filter effluents, Phase 2-2.
128
-------
CO
O
300
250
O 200
8 150
O
8
50
0
0
INFLUENT CSFEF3
LEGEND
BITUHINOUS PILOT CONTACTOR EFF CPFAS3
LIGNITE PILOT CONTACTOR EFF CPFA9)
50
100 150
TIME, days
200
250
Figure 280. THM formation potential CFTTT) breakthrough curves for bituminous
and iignite pilot contactor effluents, Phase 2-0.
-------
LEGEND
6AC FILTER ISA EFF C18AE)
6AC FILTER 2IA EFF C21AE3
16
14
12
10
"
N
3
\
O
H
|
i
o
8
0
ie
50
60
20 30 40
TIME, days
Figure 281. Instantaneous chloroform (ICLR) concentration curves for
GAC Filter 19A and 21A effluents, Phase 1-0.
70
-------
Z2Z
• D
o w
0) O
ro w
>• o
o o
< -i
CD O
-- h
o
ro T
CONCENTRATION,
IS) •*• O) 00 CO
ro
o>
o
3
0.
o
3~ O
0 3
0)
O> O
0
tt
IV)
H
m
CO 50 0.
^ w O
(t> O ft <
-h o i
-+i 3
cn
o
O>
O
CS>
I
3
m
rs>
I
-------
LEGEND
N?
00
88
78
68
? 58
I 48
tt
38
o
8 28
18
8
8
FILTER INFLUENT CFLBO
CONTACTOR INFLUENT CSFEF)
GAC FILTER ISA EFF C1SAE3
CONTACTOR C LEVEL 7
-------
LEGEND
FILTER INFLUENT CFLIN)
CONTACTOR INFLUENT CSFEF)
6AC FILTER ISA EFF CI5AE3
CONTACTOR D LEVEL 7 CD7)
70
60
N
? 50
z
o
H
UJ
O
Z
O
o
40
30
20
10
0
0 20 40 60 80 100 120
TIME, days
FIGURE 284. Instantaneous chloroform CICLR) breakthrough curves for GAC
140
160
200
Filter ISA effluent and Contactor D level 1, Phase 3-0.
-------
CONCENTRATION, ug/l
-------
00
25
20 .
N
0»
z
o
H
z
Ul
o
o
o
15 .
ia .
5 _
INFLUENT CFLBO
10
LEGEND
PILOT 6AC FILTER EFF CRV3D
GAC FILTER 15A EFF CISAE5
30
35
40
15 20 25
TIME, days
Figure 286. Instantaneous chloroform CICLR) breakthrough curves for pilot
GAC filter and GAC Filter ISA effluents, Phase 3-2.
-------
00
—I
8
0
INFLUENT CFLIN>
LEGEND
PILOT 6AC FILTER EFF CRV3)
6AC FILTER ISA EFF CI5AE)
10
20
30
TIME, day*
Figure 287. Instantaneous chloroform CICLR) breakthrough curves for pilot
GAC filter and GAC Filter ISA effluents, Phase 3-3.
-------
88Z
CONCENTRATION, UQ/I
I
H
P
m
o
m
tn
-------
00
o
o
H
I-
U
O
O
O
0
INFLUENT CFLBO
20
LEGEND
ONCE REGENERATED PILOT 6AC FILTER EFF CRV35
VIRGIN PILOT 6AC FILTER EFF CRV55
100
120
140
40 60 80
TIME, days
Figure 289. Instantaneous chloroform (ICLR) breakthrough curves for virgin and once
regenerated pilot GAC filter effluents, Phase 2-1.
-------
INFLUENT CFLJJO
NJ
^O
O
35
30 .
_ 25 .
O
z
o
H
<
a:
h-
UJ
o
o
o
20 .
15 .
10 .
5 .
0
LEGEND
TWICE REGENERATED PILOT 6AC FILTER EFF CRV3)
VIR6IN PILOT 6AC FILTER EFF
-------
INFLUENT CSFEF3
LEGEND
BITUMINOUS PILOT CONTACTOR EFT CPFAS)
LIGNITE PILOT CONTACTOR EFF CPFA9)
50 100 150 200
TIME, days
Figure 291. Instantaneous chloroform (ICLR) breakthrough curves for bituminous
and lignite pilot contactor effluents, Phase 2-0.
258
-------
6AC FILTER I9A EFF C18AE3
LEGEND
6AC FILTER 2IA EFF C21AE3
K)
4.5
- 3.5
2.5
LJ
o . c
z 1 .5
o
o
1
0.5
0
20
50
60
30 40
TIME, days
Figure 292. Instantaneous bromodichloromethane (ICL2) concentration curves for
GAC Filter I9A and 21A effluents, Phase 1-8.
70
-------
LEGEND
6AC FILTER ISA EFF C18AE)
6AC FILTER 2IA LEVEL 2 C21A2)
4.5
4
- 3.5
G»
3 3
\
1 2.5
2
hi
O . e
2 I -5
0.5
e
e
20
50
60
30 40
TIME, days
Figure 293. Instantaneous bromodichIoromethane (ICL2) concentration curves for
GAC Filters 2IA level 2 and I9A effluent, Phase 1-0.
70
-------
LEGEND
FILTER INFLUENT CFLBO
CONTACTOR INFLUENT CSFEF)
6AC FILTER ISA EFF CI5AE3
CONTACTOR C LEVEL 7 CC73
25
20 .
o
o
H
U.
Ill
U
8
15 .
5 .
10
15
30
35
20 25
TIME, days
FIGURE 294. Instantaneous bromodichloromethane CICL2) breakthrough curves for GAC
Filter ISA effluent and Contactor C level 7', Phase 3-1.
45
-------
ho
*J3
l/l
X
o
z
o
H
2
O
8
25
20 .
15
10 .
5 .
0
LEGEND
FILTER INFLUENT CFLIN3
CONTACTOR INFLUENT CSFEF)
6AC FILTER ISA EFF CISAE5
CONTACTOR D LEVEL 7 CD7)
60
140
160
180
80 100 120
TIME, days
FIGURE 295. Instantaneous bromodichloromethane CICL2) breakthrough curves for GAC
Filter ISA effluent and Contactor D level 1. Phase 3-0.
208
-------
CD
"J
ro
962
CONCENTRATION, uO/l
en CD on
o
01
-------
CONCENTRATION,
O> CO ®
— — IV)
O> 00 G>
m
CD
2
o
-------
03
C
ro
CONCENTRATION, ug/l
t <& ±
CO
-------
66Z
CONCENTRATION, UQ/
I
e
o
I
-------
ooe
-------
ioe
-i
-------
zoe
CONCENTRATION,
-------
LEGEND
6AC FILTER ISA EFF C18AE)
6AC FILTER 2IA LEVEL 2 C21A23
8
e
te
20
30 40
TIME, days
Figure 303. Instantaneous THM CITTT) concentration curves for
6AC Filters 2IA level 2 and 19A effluent, Phase 1-0
-------
CONCENTRATION, ug/
-------
LEGEND
8AC FILTER 18A EFF C18AE)
6AC FILTER 2IA LEVEL 2 C21A23
o
U)
20
18
16
N
01
3
o
o
o
12
8
6
4
e
e
10
20
50
60
30 40
TIME, days
Figure 303. Instantaneous THM QTTD concentration curves for
6AC Filters 21A level 2 and 19A effluent, Phase 1-0
70
-------
CONCENTRATION, us/I
I
3
G)
I
-------
soe
CONCENTRATION, uO/l
-------
CONCENTRATION, uO/I
en 5 on s>
ro
CO
-------
CONCENTRATION, ug/\
I
I
s
SI
r\
I
m
-------
80S
CONCENTRATION, uO/I
-------
eoe
00
CONCENTRATION, ug/I
-------
INFLUENT CSFEIO
LEGEND
BITUMINOUS PILOT CONTACTOR EFF CPFAS3
LieNTTE PILOT CONTACTOR EFF
50
200
100 150
TIME, days
Figure 310. Instantaneous THM CITTT) breakthrough curves for bituminous
and lignite pilot contactor effluents, Phase 2-0.
250
-------
00
o
-------
zie
-------
eie
CD
O
CONCENTRATION, ug/l
-------
LEGEND
220
200
180
160
140
§ 120
H
< 100
Of.
5 80
o
8 6e
40
20
0
0
FILTER INFLUENT CFLIN3
CONTACTOR INFLUENT CSFEF)
SAC FILTER ISA EFF C15AE3
CONTACTOR C LEVEL 7
10 15 20 25
TIME, days
30
35
40
45
FIGURE 314. Three-day simulated distribution system THM (STT3) breakthrough curves
for GAC Filter ISA effluent and Contactor C level 7, Phase 3-1.
-------
INFLUENT CFLDO
20
LEGEND
ONCE RE6ENERATED PILOT 6AC FILTER EFF CRV3)
VIRGIN PILOT 6AC FILTER EFF CRV5>
100
120
140
40 60 80
TIME, days
Figure 315. Seven-day simulated distribution system THM (STT7) breakthrough curves
for virgin and once regenerated pilot GAC filter effluents, Phase 2-1.
-------
9ie
r\>
rl
2 s-
»
CL
<
•>
00
II
O
» —
to ro
o
en
CD
CONCENTRATION, uO/
5
-------
D
3800
2500 .
2000 .
;:: H 1500
u.
H
Z
8
1000 .
500
0
0
INFLUENT CFLDO
10
20
LEGEND
6AC FILTER I9A EFF CI9AE)
6AC FILTER 2IA LEVEL 2 C2IA2)
30 40
TIME, days
50
60
Figure 317. Total organic carbon (TOO breakthrough curves for GAC Filters 2IA
level 2 and I9A effluent, Phase 1-0.
-------
LEGEND
4080
3500
3080
2500
z
H 2000
on
Z 1500
kJ
O
Z
8 1000
500
0
0
FILTER INFLUENT CFLJN3
CONTACTOR INFLUENT CSFEF)
6AC FILTER ISA EFT CI5AE3
CONTACTOR C LEVEL 7 CC7)
10
15
30
35
20 25
TIME, days
FIGURE 318. Total organic carbon (TOO breakthrough curves for GAC
Filter ISA effluent and Contactor C level 1, Phase 3-1.
45
-------
eie
-3
a>
CO
CO
o> o
OD rt-
a> o_
o
"I O
Q T
rt-flQ
d> Q
Q_ 3
•o o
O Q
rt- T
CT
o
3s- 3
o
— CD
— O
CO
en
ro
H
o>
i®
3 O Q_
ci- C Q
« O •<
^ -3- « oo
•3- c
O 1
w <
d> 0
-*>
8 5
Q
D_
O
O
-------
Ol
CONCENTRATION, uO/
ro
CO 01
01
01
-J —I
a> o
CD rr-
a> Q^
D
O
— O
— O
0)
CT
(D
ro
o
\
e> "J
3 O CL
ft- C 0
« C5 •<
^ 3" (ft 00
T) O
Q 1
(0 <
(D
ro
ro o —
• "^ {£)
-------
LEGEND
6AC FILTER ISA EFT CISAE)
CONTACTOR D LEVEL 7
-------
6AC FILTER ISA EFF C15AE)
LEGEND
CONTACTOR C LEVEL 7 CC73
LO
ro
100
90
80
.*»
C
0
c 70
a
o
r
UJ
a
60
50
40
30
0
10 15 20 25
TIME, days
38
35
45
FIGURE 322. THM formation potential (FTTT) percent removal curves for
GAC Filter ISA effluent and Contactor C level 7, Phase 3-1
-------
LEGEND
PILOT GAC FILTER EFF CRV3)
GAC FILTER ISA EFF CISAE> X K
100
co
N>
CO
c
0
k 7B
a
o
kl
60
50
40
30
0
10
15
30
35
20 25
TIME, days
Figure 323. THM formation potential (FTTD percent removal curves for
pilot GAC contactor and GAC Filter ISA effluents, Phase 3-1
45
-------
PILOT 6AC FILTER EFF CRV33
LEGEND
SAC FILTER ISA EFF C1SAE)
0
L
Q.
O
z
bJ
100
90
80
70
60
50
40
30
0
10
15
30
35
40
20 25
TIME, days
Figure 324. THM formation potential CFTTT) percent removal curves for
pilot 6AC filter and GAC Filter ISA effluents, Phase 3-2.
45
-------
LEGEND
PILOT SAC FILTER EFF CRV35
6AC FILTER ISA EFF CIEAE)
100
90
j
0.
O
til
tt
70
60
50
40
30
0
10
20
30 40
TIME, days
50
60
70
Figure 325. THM formation potential (FTTT) percent removal curves for
pilot GAC filter and GAC Filter ISA effluents, Phase 3-3.
-------
LEGEND
PILOT 6AC FILTER EFF CRV53
GAC FILTER ISA EFF C15AE3
u>
K>
c
-------
LEGEND
BITUMINOUS PILOT CONTACTOR EFF CPFAS3 LIGNITE PILOT CONTACTOR EFF CPFAflD
0
58
208
190 150
TIME, days
Figure 327. THM formation potential (FTTT) percent removal curves for bituminous
and I ignite pi lot contactor effluents, Phase 2-0.
250
-------
LEGEND
PILOT CONTACTOR LEVEL 2 CPFA2>
CONTACTOR D LEVEL 4 CD4>
U)
M
CO
c
U
L
o
U
100
80
60
40 .
0 .
-20
50
200
100 150
TIME, days
Figure 328. THM formation potential (FTTT) percent removal curves for pilot
contactor level 2 and Contactor D level 4, Phase 3-8.
250
-------
LEGEND
PILOT CONTACTOR LEVEL 2 CPFA2>
CONTACTOR 0 LEVEL 4 CM)
-10
0
20
100
40 60
TIME, days
Figure 329. THM formation potential (FTTD percent removal curves for pilot
contactor level 2 and Contactor D level 4, Phase 3-1.
120
-------
LEGEND
PILOT CONTACTOR LEVEL 2 CPFA2)
CONTACTOR D LEVEL 4 CM)
CO
CO
o
c
•
0
c
0
a
_i
<
o
LJ
U.
100
80 .
60 .
40 .
20 .
0 .
-20
20
40
80
100
120
60
TIME, days
Figure 330. THM formation potential (FTTD percent removal curves for pilot
contactor level 2 and Contactor D level 4, Phase 3-2.
140
-------
LEGEND
PILOT CONTACTOR LEVEL 3 CPFA3>
CONTACTOR D LEVEL 7 CD7>
100
80
01 70
C
* 60
L
J 50
O
40
30
20
10
0
0
50
200
100 150
TIME, day*
Figure 331. THM formation potential (FTTT) percent removal curves for pilot
contactor level 3 and Contactor D level 1, Phase 3-0.
250
-------
LEGEND
PILOT CONTACTOR LEVEL 3 CPFA3>
CONTACTOR D LEVEL 7 (D7>
CO
CO
ho
100
90
80
1 70
0
o 60
a
o
£
a:
50
40
30
20
10
0
20
80
100
40 60
TIME, daye
Figure 332. THM formation potential (FTTD percent removal curves for pilot
contactor level 3 and Contactor D level 7, Phase 3-1.
120
-------
LEGEND
PILOT CONTACTOR LEVEL 3 CPFA3>
CONTACTOR D LEVEL 7 CD7)
100
90
80
0
« 60
a
-J 50
^
o
S 40
30
20
10
0
20
40
100
120
60 80
TIME, day*
Figure 333. THM formation potential (FTTD percent removal curves for pilot
contactor level 3 and Contactor D level 7', Phase 3-2.
140
-------
LEGEND
PILOT CONTACTOR EFF CPFA55
CONTACTOR D EFF CDE>
0
L
o
Ul
Of.
100
90
80
70
60
50
30
0
50
200
100 150
TIME, day.
Figure 334. THM formation potential (FTTT) percent removal curves for pilot
contactor and Contactor D effluents. Phase 3-0.
250
-------
LEGEND
PILOT CONTACTOR EFF CPFAS5
CONTACTOR D EFF CDE>
100
CO
CO
Cn
0
0
C
a
$
o
80
70
5 60
40
0
20
80
100
40 60
TIME, days
Figure 335. THM formation potential (FTTT) percent removal curves for pilot
contactor and Contactor D effluents. Phase 3-1.
120
-------
LEGEND
PILOT COKTACTOR EFF CPFAW
CONTACTOR 0 EFF CDE>
U)
LO
ON
c
0
L
a
o
5
DC.
100
95
90
85
75
70
65
60
55
0
20
40
60 80
TIME, day*
108
120
140
Figure 336. THM formation potential (FTTT) percent removal curves for pilot
contactor and Contactor D effluents, Phase 3-2.
-------
8AC FILTER ISA EFF C15AE3
LEGEND
CONTACTOR C LEVEL 7 CC73
tee
CO
CO
-4e
e
10
15
20 25 30
TIME, days
35
•40
FIGURE 337. Instantaneous chloroform CICLR) percent removal curves for
GAC Filter ISA effluent and Contactor C level 7, Phase 3-1
-------
LEGEND
6AC FILTER ISA EFF C15AE3
CONTACTOR D LEVEL 7 CD73
OJ
u>
00
100
80 .
-80
180
80 100 120
TIME, day*
FIGURE 338 . Instantaneous chloroform (ICLR) percent removal curves for
GAC Filter ISA effluent and Contactor D level 1, Phase 3-0.
200
-------
PILOT GAC FILTER EFF
-------
LEGEND
PILOT GAC FILTER EFF CRV3)
8AC FILTER ISA EFF C1EAE5
100
JJ
C
0
L
9
a
o
LJ
Of
40
20
0
-20
0
10
15
30
35
40
20 25
TIME, days
Figure 340. Instantaneous chloroform (ICLR) percent removal curves for
pilot GAC filter and GAC Filter ISA effluents, Phase 3-2.
45
-------
LEGEND
PILOT SAC FILTER EFF CRV3) SAC FILTER ISA EFF CI5AE>
to
-C-
10
30 40
TIME, day*
50
60
70
Figure 341. Instantaneous chloroform (ICLR) percent removal curves for
pilot GAC filter and GAC Filter ISA effluents, Phase 3-3.
-------
LEGEND
PILOT SAC FILTER EFF
-------
LEGEND
ONCE REGENERATED PILOT 6AC FILTER CRV33 VIRGIN PILOT SAC FILTER CRV53
C
0
L
a
_i
<
>
u
Of.
100
50 .
0 .
-50 .
-100 .
-150 .
-200
20
40
100
120
60 80
TIME, days
Figure 343. Instantaneous chloroform CICLR) percent removal curves for virgin and
once regenerated pilot GAC filter effluents,, Phase 2-1.
140
-------
LEGEND
TWICE REGENERATED PILOT SAC FILTER CRV33 VIRGIN PILOT GAC FILTER CRVS>
c
0
L
o
LJ
188
0
-50
•100
-150
'B- •
0
20
40
80
100
60
TIME, days
Figure 344. Instantaneous chloroform (ICLR) percent removal curves for virgin and
twice regenerated pilot GAC filter effluents, Phase 2-2.
120
-------
LEGEND
BITUMINOUS PILOT CONTACTOR EFF CPFAS3 LIGNITE PILOT CONTACTOR EFF CPFA9>
-300
0
50
200
100 150
TIME, days
Figure 345. Instantaneous chloroform (ICLR) percent removal curves for bituminous
and lignite pilot contactor effluents, Phase 2-0.
250
-------
LEGEND
PILOT CONTACTOR LEVEL 2 CPFA2)
CONTACTOR D LEVEL 4
-------
PILOT CONTACTOR LEVEL 2 CPFA2>
LEGEND
CONTACTOR 0 LEVEL 4
-------
LEGEND
PILOT CONTACTOR LEm. 2 CPFA2>
CONTACTOR D LEVEL -4
-------
LEGEND
PILOT CONTACTOR LEVEL 3 CPFA3> CONTACTOR D LEVEL 7 (073
100
83 .
o
c
w
0.
40
-40
100 150
TIME, days
200
250
Figure 349. Instantaneous chloroform CICLR) percent- removal curves for pi lot
contactor level 3 and Contactor D level 7, Phase 3-0.
-------
LEGEND
0 a PILOT CONTACTOR LEVEL 3 CPFA3> CONTACTOR D LEVEL 7 CD7>
180 _
0
c.
O
T.
U
0 .
-50 _
-100 .
•150 „
-200
0
20
40
60
TIME, days
80
Figure 350. Instantaneous chloroform CICLR) percent removal curves for pilot
contactor level 3 and Contactor D level 7'f Phase 3-1.
-------
LEGEND
O B PILOT CONTACTOR LEVEL 3 CPFA3>
CONTACTOR 0 LEVEL 7 CD7) X X
en
e
20
40
120
66 80
TIME, dayc
Figure 35J. Instantaneous chloroform CICLR) percent removal curves for pilot
contactor level 3 and Contactor D level 7, Phase, 3-2.
140
-------
LEGEND
PILOT CONTACTOR EFF CPFAS5
CONTACTOR D EFF CDE)
108
co
Cn
N>
c
0
<
o
60 .
S 28 _
0 .
-20
200
100 150
TIME, day.
Figure 352. Instantaneous chloroform CICLR) percent removal curves for pilot
contactor and Contactor D effluents, Phase 3-0.
250
-------
PHOT CONTACTOR EFF CPFA5)
LEGEND
CONTACTOR D EFF 0>E>
C
0
(.
a
o
100
50
0
-50
-100 .
150 .
-200 .
-250
0
20
40
80
100
60
TIME, day.
Figure 353. Instantaneous chloroform CICLR) percent removal curves for pilot
contactor and Contactor D effluents, Phase 3-1.
-------
LEGEND
PILOT CONTACTOR EFT CPFAS)
CONTACTOR D EFF CDO
100
90
80
70
.+»
c
o 60
c
J 58
o
U
Q£
40
20
10
0
0
20
40
100
120
60 80
TIME, days
Figure 354. Instantaneous chloroform CICLR) percent removal curves for pilot
contactor and Contactor D effluents, Phase 3-2.
140
-------
6AC FILTER ISA EFF CISAE)
LEGEND
COMTACTOR C LEVEL 7 CC7)
Ln
Lh
10
0
15
20 25
TIME, day*
30
35
45
FIGURE 355. Instantaneous bromodichloromethane CICL2) percent removal curves for
6AC Filter ISA effluent and Contactor C level 1, Phase 3-1.
-------
LEGEND
SAC FILTER ISA EfT CI5AE3
CONTACTOR 0 LEVEL 7 CD75
100
Ln
o\
C
0
C
f
a
o
kl
a:
50 .
0 .
-50 .
-100 .
-150
0
20
60
160
180
80 100 120
TIME, day*
FIGURE 356. Instantaneous bromodichioromethane CICL2) percent removal curves for
GAC Filter ISA effluent and Contactor D level 1, Phase 3-0.
200
-------
00
n
GT> rr-
n 8
§ £
**•
Q CT
O ~J
c*- O
O 3
n 8.
Q —
D O
Q_ y
O
O O
:?!.
B_. ^|i»
Cf O
H
ro
O
— r> Q.
cn M Q
3> o < ro
r- « cn
S
3
-D 1
?i
(A O
(fr <
O
CO —
— O
<
en
cs>
cn
P
5
m
8
a
I
I
-------
PILOT 6AC FILTER EFF CRV3)
LEGEND
6AC FILTER ISA EFF CISAE)
180
01
00
-*>
C
0
0
c
o
LJ
a:
80 .
70 .
60 .
40
0
15
20 25
TIME, days
30
35
40
45
Figure 358. Instantaneous bromodichloromethane (ICL2) percent removal curves for
pilot GAC filter and GAC Filter ISA effluents, Phase 3-2.
-------
LEGEND
PILOT 6AC FILTER EFF CRV35
6AC FILTER ISA EFF CISAE!)
tea
LO
Cn
c
I
o
UJ
70 .
60 .
50
40 .
30
0
10
50
60
30 40
TIME, days
Figure 359. Instantaneous bromodichloromethane CICL2) percent removal curves for
pilot GAC filter and GAC Filter ISA effluents, Phase 3-3.
70
-------
LEGEND
PILOT 6AC FILTER EFF CRV5D
6AC FILTER ISA EFF CI5AE)
OJ
ON
O
-P
c
0
0
c
0.
O
z:
UJ
188
58
8
-58
-188
-158
8
28
48
68
148
168
188
88 188 128
TIME, days
Figure 360. Instantaneous bromodichloromethane (ICL2) percent removal curves for
pilot GAC filter and GAC Filter ISA effluents, Phase 3-0.
288
-------
LEGEND
ONCE REGENERATED PILOT 6AC FILTER CRV33
VIReiN PILOT SAC FILTER CRVS)
-900
128
60 80 100
TIME, days
Figure 361. Instantaneous bromodichloromethane (ICL2) percent removal curves for
virgin and once regenerated pilot GAC filter effluents, Phase 2-1.
140
-------
LEGEND
TWICE REGENERATED PILOT 6AC FILTER CRV3D
VIRGIN PILOT 6AC FILTER CRV5)
LO
ON
S3
u
«
Q.
108
88
68
48
28
8
o
Z _pft
LJ ^V
-48
-68
-88
8
40 60
TIME, days
80
100
120
Figure 362- Instantaneous bromodichloromethane (ICL2) percent removal curves for
virgin and twice regenerated pilot GAC filter effluents, Phase 2-2.
-------
LEGEND
BITUMINOUS PHOT CONTACTOR EFF CPFA53 LIGNITE PILOT CONTACTOR EFF CPFAS)
-380
0
50
200
100 150
TIME, days
Figure 363. Instantaneous bromodichloromethane (ICL2) percent removal curves for
bituminous and lignite pilot contactor effluents, Phase 2-0.
250
-------
SAC FILTER ISA EFF CISAE>
LEGEND
CONTACTOR D LEVEL 7
188
0
L
o
LJ
a
8
28
48
68
88 188
TIME, days
FIGURE 364. Instantaneous THM CITTT) percent removal curves for GAC Filter ISA
effluent and Contactor D level 1, Phase 3-0.
-------
PILOT SAC FILTER EFF CRV35
LEGEND
SAC FILTER ISA EFF CISAE>
ON
Oi
.*»
c
f
0
L
a
\
<
o
u
a
100
90 -
80 .
70 .
60 .
50 .
40 .
30 .
20 .
10 .
15
20 25
TIME, day.
30
35
Figure 365. Instantaneous THM (ITTT) percent removal curves for pilot
GAC filter and 6AC Filter ISA effluents, Phase 3-1.
-------
LEGEND
PILOT SAC FILTER EFF CRV35
6AC FILTER ISA EFF C1SAE)
100
CO
ON
CT\
20
10
15
30
35
40
20 25
TIME, days
Figure 366. Instantaneous THM (ITTT) percent removal curves for pilot
GAC filter and GAC filter ISA effluents, Phase 3-2.
45
-------
LEGEND
PILOT SAC FILTER EFF CRV3>
SAC FILTER S5A EFF
-------
LEGEND
PILOT SAC FILTER EFF CRVS3 6AC FILTER ISA EFF C15AED
00
-eee
e
40
60
160
80 iee 120 ne
TIME, days
Figure 368. Instantaneous THM CITTT) percent removal curves for pilot
GAC filter and GAC Filter ISA effluents, Phase 3-0.
180 200
-------
LEGEND
O ffl BITUMINOUS PILOT CONTACTOR EFF CPFA53 LI6NITE PILOT CONTACTOR EFF CPFA83
u>
o\
UD
0
L
O
u
0!!
100
50 .
0 u
-50 .
-100 .
-150 .
-200 .
-250
0
50
200
100 150
TIME, days
Figure 369. Inslanlaneous THM (ITTT) percent removal curves for bituminous
and ! ignite pilot contactor effluents, Phase 2-0.
250
-------
LEGEND
PILOT CONTACTOR LEVEL 2 CPFA2>
CONTACTOR D LEVEL 4 CM)
-40
200
100 150
TIME, days
Figure 378. Instantaneous THM CITTT) percent removal curves for pilot
contactor level 2 and Contactor D level A, Phase 3-0.
250
-------
LEGEND
PILOT CONTACTOR LEVEL 2 CPFA2>
CONTACTOR D LEVEL A
-------
LEGEND
PILOT CONTACTOR LEVEL 2 CPFA2)
CONTACTOR D LEVEL 4 CD4)
100
0
20
60
TIME,
120
140
Figure 372. Instantaneous THM CITTT) percent removal curves for pilot
contactor level 2 and Contactor D level 4, Phase 3-2.
-------
LEGEND
PILOT CONTACTOR LEVEL 3 CPFA3>
CONTACTOR D LEVEL 7 CD7>
100
0
c.
b
kl
a
-20
0
50
188 150
TIME, day*
200
Figure 373. Instantaneous THM CITTT) percent removal curves for pilot
contactor level 3 and Contactor D level 7, Phase 3-0.
250
-------
PILOT CONTACTOR LEVEL 3 CPFA3)
LEGEND
CONTACTOR D LEVEL 7
to
-~4
-C-
-80
8
28
48 68
TIME, days
188
128
Figure 374. Instantaneous THM CITTT) percent removal curves for pilot
contactor level 3 and Contactor D level 7, Phase 3-1.
-------
LEGEND
PILOT CONTACTOR LEVEL 3
CONTACTOR D LEVEL 7 CD7)
uo
~-j
Cn
-40
0
20
40
60 80
TIME, days
100
Figure 375. Instantaneous THM (ITTT) percent removal curves for pilot
contactor level 3 and Contactor D level 1, Phase 3-2.
140
-------
LEGEND
PHOT CONTACTOR EFF CPFAS)
CONTACTOR D EFF CDE>
—J
ON
100
90
80
70
-u
C
o 60
L
9
a 50
%
40
o
15
30
20
10
0
0
50
200
100 150
TIME, days
Figure 376. Instantaneous THM CITTT) percent removal curves for pilot
contactor and Contactor D effluents,, Phase 3-0.
250
-------
LEGEND
PILOT CONTACTOR EFT CPFA6>
CONTACTOR D EFF COO
CO
-------
PILOT COKTACTOR EFF
LEGEND
CONTACTOR D EFF CDO
100
95
90
85
-p
c
o 80
L
J 75
*
i 70
o
Id ftc-
0£ O9
60
55
50
0
20
40
60 80
TIME, day.
100
120
Figure 378. Intantaneous THM CITTT) percent removal curves for pilot
contactor and Contactor D effluents, Phase 3-2.
140
-------
LEGEND
6AC FILTER I9A EFF ClfiAE) SAC FILTER 2IA EFF C2IAE>
100
90
80
•£ 70
•
o
« 60
a
o
Id
Of.
50
40
30
20
10
0
10
20
30 40
TIME, days
60
70
Figure 379. Maximum THM CMTTT) percenl removal curves for GAC Filter
I9A and 21A effluents, Phase t-0.
-------
SAC FILTER ISA EFT C1QAE3
LEGEND
GAC FILTER 21A LEVEL 2 C21A2D
CO
O
100
90
80
70
-+j
o 60
c
tt 50
x
40
O
LJ
30
20
10
0
0
10
20
50
60
70
30 40
TIME, days
Figure 380. Maximum THM (MTTT) percent removal curves for GAC Filters 21A level 2
and I9A effluent, Phase 1-0.
-------
6AC FILTER ISA EFF CISAE)
LEGEND
CONTACTOR C LEVEL 7 CC7)
00
C
0
L
tee
90
se
60
o 50
UJ
30
e
10 15 20 25
TIME, days
30
35
FIGURE 381. Three-day simulated distribution system THM (STT3) percent removal
curves for GAC Filter ISA effluent and Contactor C level 1, Phase 3-1
-------
LEGEND
0 a SAC FILTER ISA EFF C1SAE3
CONTACTOR D LEVEL 7 CD7D
108
LO
CO
0
L
9
a
o
tJ
a
40
60
80 100
TIME, days
120
140
160
180
FIGURE 382. Three-day simulated distribution system (STT3) percent removal curves
for GAC Filter ISA effluent and Contactor D level 7, Phase 3-0.
-------
LEGEND
PILOT CONTACTOR LEVEL 2 CPFA2)
CONTACTOR D LEVEL 4 CM)
100
00
-40
50
200
250
100 150
TIME, day.
Figure 383. Three-day simulated distribution system THM (STT3) percent removal
curves for pilot contactor level 2 and Contactor D level 4, Phase 3-8.
-------
LEGEND
B Q PILOT CONTACTOR LEVEL 2 CPFA2>
CONTACTOR D LEVEL 4 X X
CO
00
c
9
0
L
9
a
o
u
100
80 .
60 _
0 .
-20
60 80
TIME, days
100
120
Figure 384. Three-day simulated distribution system THM (STT3) percent removal
curves for pilot contactor level 2 and Contactor D level 4, Phase 3-1.
-------
LEGEND
PILOT CONTACTOR LEVEL 2 CPFA2>
CONTACTOR D LEVEL 4 CD4)
00
Ln
180
88 .
68 .
48 .
20 .
8 .
-28
60 80
TIME, days
Figure 385. Three-day simulated distribution system THM (STT3) percent removal
curves for pi lot contactor level 2 and Contactor D level 4, Phase 3-2.
c
o
L
a
o
-------
LEGEND
PILOT CONTACTOR LEVEL 3 CPFA3)
CONTACTOR D LEVEL 7
-------
LEGEND
PILOT CONTACTOR LEVEL 3 CPFA3>
CONTACTOR D LEVEL 7 CD7>
108
OJ
00
.**
c
•
0
C
0
Q.
O
z
hi
60
20
0
-20
0
20
40
80
100
120
60
TIME, days
Figure 387. Three-day simulated distribution system THM (STT3) percent removal
curves for pilot contactor level 3 and Contactor D level 7, Phase 3-1.
-------
LEGEND
PILOT CONTACTOR LEVEL 3 CPFA3)
CONTACTOR D LEVEL 7 CD7)
u>
00
CO
10
0
40
tee
120
140
60 80
TIME, day*
Figure 388. Three-day simulated distribution system THM (STT3) percent removal
curves for pilot contactor level 3 and Contactor D level 7, Phase 3-2.
-------
LEGEND
PILOT CONTACTOR EFF CPFAS>
CONTACTOR D EFF CDE)
160
OJ
CO
-p
c
0
C
a
o
iu
tt
80
70
60
50
40
30
20
0
50
100 150
TIME, day.
200
250
Figure 389. Three-day simulated distribution system THM CSTT3) percent removal
curves for pilot contactor and Contactor D effluents, Phase 3-0.
-------
LEGEND
PILOT CONTACTOR EFF CPFAW
CONTACTOR 0 EFF CDE>
•*>
C
0
L
a
<
o
100
90
80
70
60
50
30
0
20
40
80
100
60
TIME, days
Figure 390. Three-day simulated distribution system THM (STT3) percent removal
curves for pilot contactor and Contactor D effluents, Phase 3-1.
120
-------
LEGEND
PILOT CONTACTOR EFF CPFA5>
CONTACTOR 0 EFF CDO
55
60 88
TIME, day*
100
128
148
Figure 391. Three-day simulated distribution system THM (STT3) percent removal
curves for pi lot contactor and Contactor D effluents, Phase 3-2.
-------
LEGEND
BITUMINOUS PILOT CONTACTOR EFF CPFAS) LIGNITE PILOT CONTACTOR EFF CPFA93
c
t
0
L
a
_
o
Z
UJ
106
83
68
48
8
-28
8
58
288
258
188 158
TIME, days
Figure 392. Seven-day simulated distribution system THM (STT7) percent removal
curves for bituminous and lignite pilot contactor effluents., Phase 2-0,
-------
LEGEND
SAC FILTER I9A EFF CI9AE)
6AC FILTER 2IA LEVEL 2 C2IA23
vo
c
o
L
O
IU
01
80
70
60
50
40
30
20
10
0
-10
0
20
30 40
TIME, days
50
60
70
Figure 393. Total organic carbon (TOO percent removal curves for
GAC Filters 21A level 2 and 19A effluent. Phase 1-0.
-------
LEGEND
6AC FILTER ISA EFF C1SAE)
CONTACTOR C LEVEL 7 CC7)
20
10
15
20 25
TIME, days
30
35
FIGURE 394. Total organic carbon (TOO percent removal curves for
GAC Filter ISA effluent and Contactor C level 1, Phase 3-1
-------
LEGEND
6AC FILTER ISA EFF C15AE)
CONTACTOR 0 LEVEL 7
98
88
78
68
.*»
o 58
L
1 48
O
LJ
38
28
18
8
-18
8
28
128
148
48 68 88 188
TIME, day.
FIGURE 395. Total organic carbon (TOO percent removal curves for GAC Filter ISA
effluent and Contactor D level 1, Phase 3-0.
168
-------
LEGEND
BITUHINaUS PILOT CONTACTOR EFF CPFAS3 LIGNITE PILOT CONTACTOR EFF CPFA83
C
0
L
_
i
ui
a
100
90
80
70
60
50
40
30
20
10
0
-10
0
50
100 150
TIME, days
200
250
Figure 396. Total organic carbon (TOO percent removal curves for bituminous
and lignite pilot contactor effluents, Phase 2-8.
-------
LEGEND
PILOT CONTACTOR LEVEL 2 CPFA2>
CONTACTOR D LEVEL 4 CM)
CO
VD
-20
58
200
100 150
TIME, days
Figure 397. Total organic carbon (TOO percent removal curves for pilot
contactor level 2 and Contactor D level 4, Phase 3-0.
250
-------
LEGEND
PILOT CONTACTOR LEVEL 2 CPFA2>
CONTACTOR D LEVEL 4
100
OJ
U3
CO
-10
20
80
100
40 60
TIME, days
Figure 398. Total organic carbon (TOO percent removal curves for pilot
contactor level 2 and Contactor D level 4, Phase 3-1.
120
-------
LEGEND
PILOT CONTACTOR LEVEL 2 CPFA2)
CONTACTOR D LEVEL 4 (04)
c
•
0
O
U
U.
100
90
80
70
60
50
30
20
10
0
-10
0
28
40
60 80
TIME, days
100
120
140
Figure 399. Total organic carbon (TOO percent removal curves for pilot
contactor level 2 and Contactor D level 4,, Phase 3-2.
-------
LEGEND
PILOT CONTACTOR LEVEL 3 CPFA3)
CONTACTOR D LEVEL 7 O7>
O
O
.*»
8
L
o
UJ
70
60
50
40
30
20
10
0
200
50 100 150
TIME, days
Figure 400. Total organic carbon (TOO percent removal curves for pilot
contactor level 3 and Contactor D level 1t Phase 3-0.
250
-------
LEGEND
PILOT CONTACTOR LEVEL 3 CPFA3> CONTACTOR D LEVEL 7
188
98
88
1 ?0
o
« 68
o
58
48
38
28
18
8
28
88
180
48 68
TIME, day*
Figure 401. Total organic carbon (TOO percent removal curves for pilot
contactor level 3 and Contactor D level 7, Phase 3-1.
128
-------
LEGEND
PILOT CONTACTOR LEVEL 3 CPFA3)
CONTACTOR D LEVEL 7 X X
o
N>
-*>
c
«
0
L
0
a
o
LJ
a:
100
90
80
70
60
50
40
30
20
10
0
0
20
40
100
120
60 80
TIME, days
Figure 402. Total organic carbon (TOO percent removal curves for pi lot
contactor level 3 and Contactor D level 7, Phase 3-2.
140
-------
PILOT CONTACTOR EFF CPFA5)
LEGEND
CONTACTOR D EFF CDE>
30
50
100 150
TIME, day.
200
250
Figure 403. Total organic carbon (TOO percent removal curves for pilot
contactor and Contactor D effluents, Phase 3-0.
-------
LEGEND
PILOT CONTACTOR EFF CPFAS5
CONTACTOR 0 EFF CDE>
.*>
C
•
0
L
a
o
5
95
90
85
88
75
70
65
60
55
50
45
40
0
40
80
100
60
TIME, days
Figure 404. Total organic carbon (TOO percent removal curves for pilot
contactor and Contactor D effluents, Phase 3~t.
120
-------
LEGEND
PILOT CONTACTOR EFF CPFAS3
CONTACTOR D EFF
O
01
C
0
L
0.
O
5
tt
95
90
85
80
75
70
85
55
50
45
0
20
60 8(
TIME, days
100
120
140
Figure 485. Total organic carbon (TOO percent removal curves for pilot
contactor and Contactor D effluents, Phase 3-2.
-------
LEGEND
100
90
80
.»>
§
t 70
< 60
o
kl
a 50
40
30
0
VIRGIN C3-03
TWICE REGENERATED <3-2)
ONCE REGENERATED C3-D
THREE-TIMES REGENERATED (3-3)
10
20
30
TIME,
day*
40
50
60
70
FIGURE 406. THM formation potential CFTTT) percent removal curves for
multiple runs of GAC Filter ISA effluent, Phase 3.
-------
C
0
C
>
o
r
UJ
a.
100
90
80
70
60
50
40
20
10
0
ONCE REGENERATED C3-O
LEGEND
TWICE REGENERATED C3-2)
THREE-TIMES REGENERATED C3-3)
10
20
30
70
80
40 50 60
TIME, day.
FIGURE 407. THM formation potential (FTTH percent removal curves for
multiple runs of GAC Filter 21A effluent, Phase 3.
90
100
-------
LEGEND
o
00
0
L
\
o
LJ
oe.
toe
90 .
70 .
60 .
50 .
40 .
30
0
VIRGIN C3-83
ONCE REGENERATED C3-D
TWICE REGENERATED C3-2>
100 150
TIME, day*
200
250
FIGURE 408. THM formation potential (FTTT) percent removal curves for
multiple runs of Contactor A effluent. Phase 3.
-------
VIRGIN C3-8)
LEGEND
ONCE REGENERATED C3-O
100
90
80
i ™
60
%
_J
o 50
lit
40
30
20
0
20
60 80
TIME, day*
100
120
140
FIGURE 409. THM formal ion poieniial CFTTT) percenl removal curves for
multiple runs of Conlaclor BB effluenl, Phase 3.
-------
LEGEND
u
L
9
Q.
O
r
LJ
tt
tee
90
70
60
30
e
VIRGIN (3-83
ONCE REGENERATED C3-13
TWICE REGENERATED C3-2>
50
100 150
TIME, days
200
250
FIGURE 410. THM formation potential CFTTT) percent removal curves for
multiple runs of Contactor C effluent, Phase 3,
-------
LEGEND
55
VIRGIN
ONCE REGENERATED C3-1)
TWICE REGENERATED C3-2)
60
TIME, days
80
100
120
FIGURE 411. THM formation potential CFTTT) percent removal curves for
multiple runs of Contactor D effluent, Phase 3. .
-------
REMOVAL, p«rc«nt
CO
M
C
m
•*w
3 M
C 3
— W
rr- rr-
T> 3
— «t-
fl> Q
~> ®
C O
3 C
(o in
o o
CD O
>• n
o o
® <"•» H
"5 M 2
o m
ro r~ «• 01
— 33 CO
*>• ^-f 0-
o
0) -D •<
-*•> o n
-h i
— o
g §
3 rr-
00
CO
I
0>
CO
I I
-u ro
CO CO
CO
CO
CO
o>
CO
GO
CO
CO
CO
CO
CO
A
-D 3
3~ O
Q <
0) O
CO O
(D
(0
O
CO
CO
(O
CO
I
e
m
CD
rn
S
i
CO
CO
-------
LEGEND
tee
8
L
0.
O
UJ
Of.
e .
-se .
-jee .
-ise
VIR81N
ONCE REGENERATED C3-I)
TWICE REGENERATED C3-2)
280
188 158
TIME, day*
FIGURE 413. Instantaneous chloroform CICLR) percent removal curves for
multiple runs of Contactor A effluent,, Phase 3.
258
-------
.*»
c
o
L
o
z:
UJ
a
180
80
68
40
20
0
-40
-60
-80
0
VIRGIN C3-8)
20
40
LEGEND
TWICE REGENERATED
ONCE REGENERATED C3-I)
60 80
TIME, days
100
120
140
160
FIGURE 414. Instantaneous chloroform (ICLR) percent removal curves for
multiple runs of Contactor BB effluent, Phase 3.
-------
.*»
c
0
L
9
Q.
O
LJ
180
50
0
-50 .
-100 .
-150
0
LEGEND
VIRGIN C3-0)
ONCE REGENERATED C3-1)
TWICE REGENERATED <3-2)
50
200
100 150
TIME, days
FIGURE 415. Instantaneous chloroform (ICLR) percent removal curves for
multiple runs of Contactor C effluent, Phase 3.
250
-------
-f>
(—*
0\
0
L
O
r
UJ
oe.
100
50
0
-50
-100
-150
0
LEGEND
VIRGIN
ONCE REGENERATED C3-O
TWICE REGENERATED C3-2)
20
40
80
100
60
TIME, days
FIGURE 416. Instantaneous chloroform CICLR) percent removal curves for
multiple runs of Contactor D effluent. Phase 3.
120
-------
LEGEND
§
i
o
UJ
VIRGIN <3-8)
TWICE REGENERATED <3-2>
ONCE REGENERATED C3-O
THREE-TIHES REGENERATED C3-3>
tee
50
e .
-50 .
-tee .
-158
e
te
50
60
20 30 40
TIME, days
FIGURE 417. Insianianeous bromodichloromethane (ICL2) perceni removal curves for
multiple runs of GAC Filter ISA effluent, Phase 3.
-------
100
80
60
0
C
o
z
u
a
20
0
-20
-40
ONCE REGENERATED C3-1)
LEGEND
TWICE REGENERATED C3-23
THREE-TIHES REGENERATED (3-3)
10
20
30
70
80
90
40 50 60
TIME, days
FIGURE 418. Instantaneous bromodichI oromethane CICL2) percent removal curves for
multiple runs of 6AC Filter 21A effluent. Phase 3.
100
-------
LEGEND
tee
c
0
L
O
UI
tt
68 .
28 .
e .
-ze
VIRGIN
ONCE REGENERATED C3-D
TWICE REGENERATED C3-25
200
100 150
TIME, days
FIGURE 419. Instantaneous bromodichloromethane CICL2) percent removal curves for
multiple runs of Contactor A effluent, Phase 3.
250
-------
N>
O
100
38
VIRGIN C3-0)
LEGEND
ONCE REGENERATED C3-I)
TWICE REGENERATED <3-2>
100
120
140
60 80
TIME, day*
FIGURE 420. Instantaneous bromodichloromethane (ICL2) percent removal curves for
multiple runs of Contactor BB effluent, Phase 3.
160
-------
LEGEND
-20
e
VIR6IN C3-83
ONCE REGENERATED C3-O
TWICE REGENERATED <3-2)
280
tea 158
TIME, day*
FIGURE 421. Instantaneous bromodichloromethane (ICL2) percent removal curves
for multiple runs of Contactor C effluent,, Phase 3.
258
-------
tee
98
96
"£ 94
0
« 92
a
j 90
o
UJ
U.
5 88
86
84
82
LEGEND
VIRGIN C3-85
ONCE REGENERATED C3-13
TWICE REGENERATED <3-2)
20
40
80
100
60
TIME, days
FIGURE 422. Instantaneous bromodichloromethane CICL2) percent removal curves for
multiple runs of Contactor D effluent, Phase 3.
128
-------
LEGEND
8
L
a
o
LJ
a
-28
VIRGIN C3-«
TWICE REGENERATED <3-2>
ONCE REGENERATED C3-O
THREE-TIMES REGENERATED <3-3>
28
58
38 48
TIME, day*
FIGURE 423. Instantaneous THM (ITTT) percent removal curves for
multiple runs of GAC Filter ISA effluent, Phase 3.
68
78
-------
c
«
0
L
0.
100
80
60
40
20
UJ
* 0
-20
-40
ONCE REGENERATED (3-D
LEGEND
TWICE REGENERATED C3-2)
THREE-TIMES REGENERATED C3-3D
10
20
30
70
80
40 50 60
TIME, days
FIGURE 424. Instantaneous THM CITTT) percent removal curves for
multiple runs of GAC Filter 21A effluent, Phase 3.
90
100
-------
LEGEND
Cn
100
88 .
60 .
c
0
L
a
>
_j
o
a
20 .
0 .
-20 .
-40
VIRGIN (3-8)
50
ONCE REGENERATED C3-13
TWICE REGENERATED C3-2)
200
100 150
TIME, days
FIGURE 425. Instantaneous THM CITTT) percent removal curves for
multiple runs of Contactor A effluent, Phase 3.
250
-------
100
-20
LEGEND
VIRGIN C3-e>
ONCE REGENERATED C3-I)
TWICE REGENERATED C3-2>
20
40
60
100
120
80
TIME, days
FIGURE 426. Instantaneous THM (ITTT) percent removal curves for
multiple runs of Contactor BB effluent, Phase 3.
160
-------
LEGEND
NJ
0
0
VIRGIN CS-W
ONCE REGENERATED C3-O
TWICE REGENERATED C3-2)
50
200
100 150
TIME, days
FIGURE 427. Instantaneous THM (ITTT) percent removal curves for
multiple runs of Contactor C effluent,, Phase 3.
250
-------
LEGEND
|00
90
80
•s 70
s
« 60
a
50
40
30
20
kl
10
0
VIRGIN C3-93
20
ONCE REGENERATED
TWICE REGENERATED <3-2>
80
100
40 60
TIME, days
FIGURE 428. Instantaneous THM CITTT) percent removal curves for
multiple runs of Contactor D effluent, Phase 3.
120
-------
LEGEND
K
tea
98
! 7e
J 68
%
-J
o 58
z
48
38
28
8
VIRGIN C3-8)
TWICE REGENERATED C3-2>
ONCE REGENERATED CS-13
THREE-TIMES REGENERATED C3-3)
18
28
58
68
38 48
TIME, day*
FIGURE 429. Three-day simulated distribution system THH CSTT3) percent removal
curves for multiple runs of GAC Filter ISA effluent, Phase 3.
78
-------
188
88
s
L
Q.
O
UJ
tt
48
28
8
-28
ONCE REGENERATED <3-D
LEGEND
TKECE RE8ENERATED C3-23
THREE-TIMES REBENERATED C3-3D
8 18 28 38 48 58 68
TIME, days
78
88
98
188
FIGURE 430. Three-day simulated distribution system THM (STT3) percent removal
curves for multiple runs of GAC Filter 2IA effluent, Phase 3.
-------
CO
e
VIRGIN C3-W
LESEtiP.
TWICE REGENERATED
ONCE REGENERATED (3-13
tea ise
TIME, day.
280
258
FIGURE 431. Three-day simulaied distributton system THM CSTT3) percent removal
curves for multiple runs of Contactor A effluent, Phase 3.
-------
LEGEND
10
VIR6IN C3-8)
TUICE REGENERATED C3-2>
ONCE REGENERATED C3-I5
60
100
120
M0
80
TIME, day*
FIGURE 432. Three-day eimulaied disiribuiion system THM CSTT3) percent removal
curves for multiple runs of Contactor BB effluent,, Phase 3.
160
-------
LEGEND
to
CO
20
0
VIR6IN C3-0)
ONCE REGENERATED C3-1)
TWICE REGENERATED <3-2)
100 150
TIME, day*
200
250
FIGURE 433. Three-day simulated distribution system THM (STT3) percent removal
curves for multiple runs of Contactor C effluent, Phase 3.
-------
28
ONCE REGENERATED C3-I3
LEGEND
TWICE REGENERATED C3-23
THREE-TZHES REGENERATED C9-35
30
78
88
48 58 68
TIME, day*
FIGURE 434. Total organic carbon (TOO percent removal curves for
multiple runs of 6AC Filter 21A effluent, Phase 3.
98
188
-------
LEGEND
at
100
90
80
§ -
1 60
o 50
Ul
tt
40
30
20
0
VIRGIN C3-0)
50
ONCE REGENERATED C3-1)
TWICE REGENERATED C3-2>
200
100 150
TIME, days
FIGURE 435. Total organic carbon (TOO percent removal curves for
multiple runs of Contactor A effluent, Phase 3.
250
-------
c
0
(.
a
o
LJ
iee
90
80
70
60
50
40
30
20
0
VIRGIN C3-0)
20
40
LEGEND
TWICE REGENERATED
ONCE REGENERATED C3-D
60 80
TIME, days
100
120
140
FIGURE 436. Total organic carbon (TOO percent removal curves for
multiple runs of Contactor BB effluent, Phase 3.
160
-------
LEGEND
00
0
L
•
0.
g
o
Ui
Of.
tee
99
88
78
60
58
48
38
ie
8
VIRGIN C3-85
ONCE REGENERATED C3-O
TUICE REGENERATED <3-2>
58
288
188 158
TIME, days
FIGURE 437. Total organic carbon (TOO percent removal curves for
multiple runs of Contactor C effluent, Phase 3.
258
-------
.p-
u>
00
3.5
3
o
o 2.5
ij «
(0
•s
LJ 1.5
CQ
g
(0
^f \
0.5
0
ONCE RE6EMERATED (5-1 >
LEGEND
TWICE REGENERATED C5-2>
THREE-TIHES REGENERATED <3-3)
234
SUM INFLUENT/GAC WT,
6
FIGURE 438. THM formaiion poUnlial (FTTT) adsorbed per GAC weight
for mulliple runs of GAC Filler 21A effluent, Phase 3.
-------
LEGEND
VIRGIN C3-8>
ONCE REGENERATED C3-O
TWICE REGENERATED <3-2>
6
N 5
O
JK
N
O
(9
m
a
o
(0
(0
468
SUM INFLUENT/GAC WT, g/kg
10
FIGURE 439. THM formation potential (FTTT) adsorbed per GAC weight
for multiple runs of Contactor A effluent, Phase 3.
12
-------
LEGEND
-B VIRGIN C3-93
345
SUM INFLUENT/GAG WT, o/kg
6
8
FIGURE 440. THM formation potential CFTTT) adsorbed per GAC weight
for multiple runs of Contactor B effluent., Phase 3.
-------
LEGEND
VIRGIN C3-8>
ONCE REGENERATED C3-O
4
3.5
I •
o
2.5
o
<
u>
s
Q
i
1.5
8.5
8
1
234
SUM INFLUENT/GAC WT. g/kg
FIGURE 441. THM formation potential CFTTT) adsorbed per GAC weight
for multiple runs of Contactor BB effluent, Phase 3.
6
-------
LEGEND
o
5
4.5
4
3.5
3
2.5
Q
CQ 2
8
2 i.s
<
(0
1
8.5
VIRGIN C3-8)
ONCE REGENERATED C3-O
TWICE REGENERATED C3-2>
1
345
SUM INFLUENT/GAC WT, g/kg
FIGURE 442. THM formation potential CFTTT) adsorbed per GAC weight
for multiple runs of Contactor C effluent, Phase 3.
8
-------
6
LEGEND
VIRSIN <3-8>
ONCE REGENERATED C3-O
TWICE REGENERATED C3-23
o
2 3
8
ffl
8
W
2
£
s,
e
8
I
345
SUM INFLUENT/GAC WT, 0/«<9
6
FIGURE 443. THM formation potential CFTTT) adsorbed per GAC weight
for multiple runs of Contactor D effluent, Phase 3.
8
-------
o
K-
O
<
<0
0.35
0.3
0.25
0.2
Q 0.15
CQ
8
(0
9 0.1
I
0.05
0
0
ONCE REGENERATED C3-D
LEGEND
TWICE REGENERATED C3-23
THREE-TINES REGENERATED <3-3>
0.1 0.2 0.3 0.4 0.5
SUM INFLUENT/GAC WT, g/k0
0.6
0.7
FIGURE 444. Instantaneous chloroform CICLR) adsorbed per GAC weight
for multiple runs of GAC Filter 21A effluent, Phase 3.
0.8
-------
0.4
8.35
;? 0.3
o
0.25
o
o 0.2
Q
Id
£ 0.15
O
<0
SI
(0
0.1
0.05
0
0
VIRGIN C3-8i>
ONCE REGENERATED C3-D
<3-2>
0.1
0.2
0.8 0.9
0.3 0.4 0.5 0.6 0.7
SUM INFLUENT/GAC WT, g/kg
FIGURE 445. Instantaneous chloroform CICLR) adsorbed per 6AC weight
for multiple runs of Contactor A effluent, Phase 3.
-------
LEGEND
-fl VIRGIN C3-6>
-
o
8.25
0.2
:x 0.15
o
o
8
CD
g
(0
0.1
D 0.05
(0
0
e
0.1
0.2 0.3
SUM INFLUENT/SAC WT,
0.4
0.5
0.6
FIGURE 446. Instantaneous chloroform CICLR) adsorbed per 6AC weight
for multiple runs of Contactor B effluent., Phase 3.
-------
0
0.6
8.5
8.4
o
2 8.3
u
CQ
(0
a
8.2
r
§ 8.1
8
8
LEGEND
VIRGIN C3-e>
ONCE REGENERATED C3-O
TWICE REGENERATED <3-2)
8.2
8.4 8.6 8.8
SUM INFLUENT/GAC WT,
1
1.2
FIGURE 447. Instantaneous chloroform CICLR) adsorbed per 6AC weight
for multiple runs of Contactor BB effluent., Phase 3.
1.4
-------
LEGEND
8.6
0.5
0.4
VIRGIN C3-e>
ONCE REGENERATED C3-D
TWICE REGENERATED <3-2>
a
JC
\
a
•\
:*
o
CD 0.3
U
CD
a
O ft 2
CO w-£
Q
s:
0.1
0
0
0.1
0.2
0.8
0.3 0.4 0.5 0.6 0.7
SUM INFLUENT/GAC WT, g/kg
FIGURE 448. Instantaneous chloroform (ICLR) adsorbed per GAC weight
for multiple runs of Contactor C effluent, Phase 3.
0.9
-------
LEGEND
£
"
o
.Y
O
o
a
o
(0
a
z:
CO
0.25
0.2
0.15
0.1
0.05
0
-0.05
0
VIRGIN C3-8)
TWICE REGENERATED (.3-2)
ONCE REGENERATED C3-13
THREE-TIMES REGENERATED C3-33
0.05
0.3
0.35
0.1 0.15 0.2 0.25
SUM INFLUENT/GAC WT, g/kg
FIGURE 449. Instantaneous bromodichloromethane (ICL2) adsorbed per GAG weight
for multiple runs of GAG Filter ISA effluent. Phase 3.
0.4
-------
en
O
0.25
0.2
O
5 0.15
o
o
o,
til
0.1
o
CO
a
j§ 0.05
CO
0
0
ONCE REGENERATED CS-1)
LEGEND
TWICE REGENERATED C3-2)
THREE-TIMES REGENERATED <3-3>
0.1
0.2 0.3 0.4
SUM INFLUENT/GAC WT, 8/kg
0.5
0.6
FIGURE 450. Instantaneous bromodichIoromethane (ICL2) adsorbed per 6AC weight
for multiple runs of GAC Filter 21A effluent, Phase 3.
-------
Cn
8.35
8
8
LEGEND
VIRGIN C3-8)
ONCE REGENERATED C3-13
TWICE REGENERATED C3-2>
8.85 8.1
8.15 8.2 8.25 8.3 8.35
SUM INFLUENT/GAC WT,
8.4 8.45
FIGURE 451. Instantaneous bromod ich I or ome thane (ICL2) adsorbed per GAC weight
for multiple runs of Contactor A effluent, Phase 3.
-------
LEGEND
-a VIRGIN C3-W
0.14
0.12
a
^ 0.1
08
o
<
o
N.
3
CO
o
-------
LEGEND
»
:*
o
£ £
u> \
g
(0
£
(0
0.35
9.3
0.25
8.2
0.15
0.1
0.05
0
VIRGIN C3-8)
ONCE RE6ENERATED C3-1)
TWICE REGENERATED C3-2>
0 0.05 0.1 0.15 0.2 0.25 0.3 0.35 0.4 0.45 0.5
SUM INFLUENT/GAC WT, g/kg
FIGURE 453. Instantaneous bromodichloromethane (ICL2) adsorbed per GAC weight
for multiple runs of Contactor BB effluent, Phase 3.
-------
LEGEND
8.35
0.3
Q
8-25
I-
o
0.2
o
V.
8 0.15
0.05
0.1 0.15 0.2 0.25
SUM INFLUENT/GAC WT,
0.3
0.35
0.4
FIGURE 454. Instantaneous bromodichloromethane (ICL2) adsorbed per 6AC weight
for multiple runs of Contactor C effluent., Phase 3.
-------
LEGEND
0.7
8.6
0-5
<
o
8 0.3
00
o
CO
5
e.2
...
8
VIRGIN C3-0)
TWICE REGENERATED C3-2>
ONCE REGENERATED C3-I3
THREE-TIHES REGENERATED C3-3)
0.2 0.4 0.6 0.8 I
SUM INFLUENT/GAC WT, g/k0
1.2
1.4
FIGURE 455. Instantaneous THM CITTT) adsorbed per GAC weight
for multiple runs of GAC Filter ISA effluent, Phase 3.
1.6
-------
ON
8
8
ONCE REGENERATED <3-l>
LEGEND
TWICE REGENERATED C3-2>
THREE-TIMES REGENERATED C3-3)
8.4 0.6 8.8 I
SUM INFLUENT/GAG WT, o/k8
1.2
1.4
FIGURE 456. Instantaneous THH CITTT) adsorbed per 6AC weight
for multiple runs of GAC Filter 21A effluent, Phase 3.
1.6
-------
LEGEND
0.9
0.8
O 0.7
X
O
, 0-6
H
o 0.5
<
(0
a 0-4
OQ
ft
O a 3
(0 °-°
a
(0
0.2
0.1
0
0
VIRGIN C3-W
ONCE REGENERATED C3-O
TWICE REGENERATED <3-2>
0.2
0.6 0.8
SUM INFLUENT/GAC WT,
1.2
FIGURE 457. Instantaneous THM (ITTT) adsorbed per GAC weight
for multiple runs of Contactor A effluent, Phase 3.
1.4
-------
LEGEND
-0 VIRGIN C3-0)
Ln
00
8.45
0.4
o 0.35
8.3
o 8.25
o
s e-2
00
I 0.15
(0
0.1
0.05
0
0
0.1
0.2 0.3 0.4 0.5
SUM INFLUENT/GAC WT,
0.6
0.7
0.8
FIGURE 458. Instantaneous THM CITTT> adsorbed per GAC weight
for multiple runs of Contactor B effluent, Phase 3.
-------
LEGEND
0
VIR8IN C3-8)
ONCE REGENERATED C3-1)
TWICE REGENERATED C3-2>
8.2
8.4
0.6 0.8 I 1.2 1.4
SUM INFLUENT/GAC WT, g/kg
FIGURE 459. Instantaneous THM CITTT) adsorbed per GAC weight
for multiple runs of Contactor BB effluent, Phase 3.
-------
LEGEND
O\
O
1
0.9
S *'*
"» 0.7
%
5 0.6
o
CD 0.5
X
I 0.4
o
9 0-3
0.2
0.1
0
0
VIRGIN C3-8>
ONCE REGENERATED C3-I)
TWICE REGENERATED C3-2>
0.2
0.4 0.6 0.8
SUM INFLUENT/GAC WT, 8/kg
1
1.2
FIGURE 468. Instantaneous THM (ITTT) adsorbed per GAC weight
for multiple runs of Contactor C effluent. Phase 3.
1.4
-------
LEGEND
O\
VIRGIN C3-0>
ONCE REGENERATED C3-I)
TWICE REGENERATED C3-2)
0.2
0.4 0.6 0.8
SUM INFLUENT/GAC WT,
FIGURE 461. Instantaneous THM (ITTT) adsorbed per GAC weight
for multiple runs of Contactor D effluent. Phase 3.
-------
LEGEND
2.5
a
S i.s
o
i3 .
(0
i
8.5
8
VIRGIN C3-8)
TWICE REGENERATED C3-2>
ONCE REGENERATED C3-O
THREE-TIHES REGENERATED C3-3)
8 8.5 i 1.5 2 2.5 3
SUM INFLUENT/GAC WT,
35
4.5
FIGURE 462. Three-day simulated distribution system THM CSTT3) adsorbed per
GAC weight for multiple runs of GAC Filter ISA effluent, Phase 3.
-------
-P-
O\
CO
o
1.6
1.4
1.2
1
u
O 0.8
0.6
0.4
0.2
0
(0
0
ONCE REGENERATED C3-O
LEGEND
TWICE REGENERATED C3-23
THREE-TIMES REGENERATED C3-3>
0.5
1 15 2 2.5 3
SUM INFLUENT/GAC WT, g/kg
FIGURE 463. Three-day simulaled distribution system THM CSTT3) adsorbed per
GAC weight for multiple runs of GAC Filter 21A effluent, Phase 3.
3.5
-------
LEGEND
2.5
1.5
o
JC
o
U
<
O
a
m
g
to
Q
D 0.5
0
e
VIRGIN <3-e>
ONCE REGENERATED C9-I)
TWICE REGENERATED <3-2J>
0.5
15 2 25 3 35
'SUM INFLUENT/GAG WT, 8/k8
4.5
FIGURE 464. Three-day simulated distribution system THM CSTT3) adsorbed per
GAC weight for multiple runs of Contactor A effluent., Phase 3.
-------
LEGEND
VIRGIN C3-8)
ON
(Ji
8
0.5
1 1.5
SUM INFLUENT/GAC WT, g/kg
FIGURE 465. Three-day simulated distribution system THM CSTT3) adsorbed per
GAC weight for multiple runs of Contactor B effluent, Phase 3.
-------
LEGEND
o
J£
N
O
* 1.5 .
o
<
O
\
Q
LJ
CQ
a
o
(0
a
<
r
e.s .
0
VIRGIN (3-9)
ONCE REGENERATED C3-D
TWICE REGENERATED <3-2>
8.5
1.5 2
SUM INFLUENT/GAC WT,
2.5
g/kg
3.5
FIGURE 466. Three-day simulated distribution system THM CSTT3) adsorbed per
GAC weight for multiple runs of Contactor BB effluent., Phase 3.
-------
2.5
Q
.X
\
O
5 1.!
o
5
8
00
0.5
0
0
LEGEND
VIRGIN <3-e:>
ONCE REGENERATED C3-O
REGENERATED C3-2>
0.5
t t.5 2 2.5
SUM INFLUENT/GAG WT, 8/kg
3.5
FIGURE 467. Three-day simulated distribution system THM CSTT3) adsorbed per
GAC weight for multiple runs of Contactor C effluent, Phase 3.
-------
ON
00
2.5
01
Jd
£ 1.6
o
O
a ,
OQ 1
10
D 0.5
w
0
0
VIRGIN (3-8)
LEGEND
TWICE REGENERATED
ONCE REGENERATED C3-O
0.5
1 1.5
SUM INFLUENT/GAG WT,
2.5
FIGURE 468. Three-day simulated distribution system THM CSTT3) adsorbed per
GAC weight for multiple runs of Contactor D effluent, Phase 3.
-------
35
ONCE REGENERATED C3-O
LEGEND
TWICE REGENERATED C3-23
THREE-TIHES REGENERATED C3-33
25
8 15
CO
g
W
10
I
0
0
10 15 20 25 30
SUM INFLUENT/GAG WT, o/k8
35
40
FIGURE 469. Total organic carbon (TOO adsorbed per GAC weight
for multiple runs of GAC Filter 2IA effluent. Phase 3.
45
-------
LEGEND
--J
O
o
o
%
:*
o
(9
U
OQ
g
(0
(0
68
40
30
20
10
0
0
VIRGIN <3-8>
ONCE REGENERATED C3-O
TWICE REGENERATED <3-2>
20
40 60 80
SUM INFLUENT/GAC WT, 8/k8
100
120
FIGURE 470. Total organic carbon (TOO adsorbed per 6AC weight
for multiple runs of Contactor A effluent, Phase 3.
-------
LEGEND
VIRGIN C3-«5
o
o
<
(•>
a
m
a
o
CO
40
35
30
25
20
15
10
0
0
10
20 30 40 50
SUM INFLUENT/GAC WT, e/kg
60
70
80
FIGURE 471. Total organic carbon (TOO adsorbed per GAC weight
for multiple runs of Contactor B effluent, Phase 3.
-------
LEGEND
VIRGIN CS-M
-
o
o
ID
\
Id
CQ
O
CO
I
ONCE REGENERATED C3-15
45
40 .
35 .
30 .
25 .
20 .
15 .
10 .
5 .
0
TWICE REGENERATED <3-2>
50
68
10 20 30 40
SUM INFLUENT/GAC WT, g/kg
FIGURE 472. Total organic carbon (TOO adsorbed per GAC weight
for multiple runs of Contactor BB effluent, Phase 3
70
-------
LEGEND
0
VIRGIN C3-8)
10
ONCE REGENERATED C3-D
TWICE REGENERATED C3-2>
30 40 50 60
SUM INFLUENT/GAC WT, g/kg
70
FIGURE 473. Total organic carbon (TOO adsorbed per GAC weight
for multiple runs of Contactor C effluent, Phase 3.
90
-------
3
1'
!
I
UJ
-I
Ji
a
1
QQ
t
i t i
•• ' •
i
i
i
|l
•
.!)
i
j
!
s
•
Mi
•
LLiii
L
. i
%
t
5
EL
, j J ,:
IdLJbJ
! 1
LiU-^^--^
i..
,!
I
,jl
.
•-L
*
, i
i
-I
i
)INT. '
STD.
! 5
JLjl>^
INT.
STD.
«j.'_jj>.JLw-/»
INT.
STD.
ii — • i •*
i
^
1
^
Jit
~H^.
FIGURE 474. Acid extract profiles for GAC Filter ISA,
Phase 3-0, runday eight.
-------
Ul
3
Y'<
B
s 5
1
UJ
i
i .
Ml
t
INT.
STD.
5 INT.
STD.
INT.
STD.
FIGURE 475. Acid extroct profiles for GAC Filter ISA,
Phase 3-0, runday 29.
-------
FIGURE 476. Acid extract profiles for 6AC Filter ISA,
Phase 3-8, runday 57.
-------
Lu
II
i t
LL^J^--**-
1
INT.
STD.
INL
STD.
QQ
^UL . r
i
INT.
STD.
FIGURE 477. Acfd extract profiles for GAC Filter ISA,
Phase 3-0, runday 85.
-------
00
5 ?
.MO'
INT.
STD.
n
i
i i
til
t^Ji
••a:
,
LO |
^ "*
r
*— *
1 !
|;
I
liil
•
1
ii
ALA,
t
4
1[
1 1
Ji
a i
m •
f
i
2*: ; •
•z.
•-
INT.
STD.
c
i
JL±>
t
t
UAjLA»_^J
_... L.
. >-^-*^
INT.
STD.
i
i
. i j
Lu— J-^
FIGURE 478. Acid extract profiles for GAC Filter ISA,
Phase 3-9, rundoy 113.
-------
LO
LI
4L
IS
m
U
! 5 • r!
5 INT.
STD
'INT.
STD.
FIGURE 479. Add extract profiles for GAC Filter ISA,
Phase 3-0, runday 141.
-------
LO
00
o
QQ
15,
INT.
STD.
!. i ',<
INT.
STD.
INT.
STD.
i
. f
_— *-
FIGURE 480. Acid extract profiles for GAC Filter ISA,
Phase 3-0, runday 169.
-------
'VSJ
OV9
AopunJ
pjoy '
OO
-------
NFU
3VS!
>INV18
482
-------
00
UJ
CO
INT.
STD
INT.
STD.
FIGURE 483. Acid extract profiles for 6AC Filter ISA,
Phase 3-2., runday one.
-------
LJ
en
INT.
STD.
LJjLLi' L
INT.
STD.
ft^^u-JJL^.
INT.
STD.
FIGURE 484. Acid extract profiles for GAC Filter ISA,
Phase 3-2, runday 29.
-------
00
cn
M
UJ
in
CQ
i i, >
Miife
X
1C
"i !
N--U-
lUJ'*'
.Jib;
1%
INT.
STD.
INT.
STD.
INT.
STD.
FIGURE 485 Acfd extract profiles for GAC Filter ISA,
Phase 3-3., runday 22.
-------
'OiS
'iNI
"v—r
'OiS
'iNI
98 AopunJ 'g-g
rr?
ji
en
m
jrTprr'f
'OiS
'
'iNI
•••'•• j
•1;
!T
1
'!;'
t
h
I
|
VO
00
-------
00
!!,.l
UJ
LO
J T^
t
ca
INT.
STD.
INT.
STD.
FIGURE 487. Acfd extract profiles for GAC Filter ISA,
Phase 3-3, runday 58.
-------
>g Aopunj 'g_£ esoqj
'(IIS
UNI
00
00
-------
CO
l-i
CQ
INT.
STD.
LU
\
^
»
INT.
STD.
INT.
STD.
FIGURE 489. Acid extract profiles for GAC Filter ISA,
Phase 3-4, runday one.
-------
'VSI
OV3
Aopunj '
pjoy '
'iNI
'01S
'iNI
'(US
'INI
CD
it
I'J.
cn
3>
m
on
o
CTv
-------
vo
UJ
LO
CD
r
j
JOJ
INT.
STD.
INT.
STD.
JJL
INT.
STD.
FIGURE 491. Acfd extract profiles for 6AC Filter ISA,
Phase 3-4, runday 29.
-------
LU
•<
LO
OQ
!'•
INT.
STD.
INT.
STD.
FIGURE 492. Acid extract profiles for GAC Filter ISA,
Phase 3-4, runday 57.
-------
"RTTJ
1
^^
..-..£
>lNVia - .J4
(4-
o
Q.
C
CO —
9 TT
•4J L.
C. 0
•*J J
X CO
9
LU
493
-------
IS 3 J 1
CO
593
{5 5
lit f
UUJLJUU!iu*Ju^j_.
5 INT. }
STD.
iINT. J
STD.
FIGURE 494. Acfd extract profiles for Contactor A,
Phase 3-0, runday one.
-------
•gg Aopunj '0-g
'y Jopotjuoo JGJ seji^ojd poj^xe pjoy
'CIS
'INI
r"*'
in
•ais
T^
•
1
i
rrT' '
»
*
1\
M
K
i
i
3>
PI
; r.
t
i
a
\ \ \
in
-------
0\
OQ
JLJL
FIGURE 496. Acid extract profiles for Contactor A,
Phase 3-8, runday 64.
-------
VD
e
jjJJLL
a :
3
OQ
i
juA*-*"*'
INT.
STD.
FIGURE 497. Acid extract profiles for Contactor A,
Phase 3-0, runday 93.
-------
CO
r
ILU
LU
)
1
M
L
P
. s
k *
Juijuui
INT.
STD.
INT.
STD.
FIGURE 498. Acid extract profiles for Contactor A,
Phase 3-8, runday 134.
-------
a :
<0
: s :
nib
, J
INT.
STD.
r
i
J
k
in! I*
i
» *
iilXut-l.
' J J
*Jl .. —^ . ^. n^ .. 1
•LI * 1 .
STD.
J
OQ
i
I
a
INT.
STD.
FIGURE 499. Acid extract profiles for Contactor A,
Phase 3-0, runday 162.
-------
Cn
O
O
UJ
Lt_
UJ
m
INT.
STD.
1 INT.
STD.
INT,
STD.
FIGURE 500. Acid extract profiles for Contactor A,
Phase 3-0, runday 246.
-------
en
O
T-T-_i
K
CO
IxJ
QQ
i 1
1!
Itt
INT.
STD.
1 — - U^__J
INT.
STD.
. . i i
J
INT.
STD.
i'>! 'II I'M
!t ' ,'(liWV
..'liLunJw-«'r>
m
.*»•• .1
V
FIGURE 501. Acid extroct prof i les for Contoctor A,
Phase 3-0, runday 274.
-------
cn
O
to
ft!
UJ
QQ
V
INT.
STD.
INT.
STD.
INT.
STD.
'
' •
FIGURE 502. Acid extract profiles for Contactor A
Phase 3-0, runday 302.
-U-
-------
FIGURE 503. Acid extract profiles for Contactor D,
Phase 3-0, rundoy efght.
503
-------
Cn
O
Si
CO
INT.
STD.
INT.
STD.
FIGURE 504. Acid extract profiles for Contactor D,
Phase 3-8, runday 29.
-------
u_
UJ
UJ
Jr.*
1
1
<*:
—4
OQ
c
iai.
k
>ik
5 " * I
JJLJUL-
INT.
STD.
INT.
STD.
INT.
STD.
JL
f
ill,
s^JJuJ-
iii,.,
t
•1 ' i
L...A 1. . , _
INT.
STD.
i 1
l
J
FIGURE 585. Acid extract profiles for Contactor D,
Phase 3-8, runday 57.
505
-------
u_
LU
U_
CO
INT.
STD.
INT.
STD.
OQ
INT.
STD.
FIGURE 506. Acfd extract profiles for Contactor D,
Phase 3-8, runday 85.
506
-------
lijuta"
3 \
JU-*O^LXJ—^
INT.
STD.
UJ
Ul
o
INT.
STD.
OQ
11
INT.
STD.
FIGURE 507. Acid extract profiles for Contactor D,
Phase 3-0, runday 113.
-------
Ul
o
00
-o
8-2
§>
rr-
Q
O
r»-
O
O
BLANK
DE
.*•-.
F
SFEF
-..
,"
-------
Crt
o
o
W CO
O •
° TJ
Q. C
O
J?
~X CO
0
•o w
— D
U -C
•< o.
%M>^
s
UJ
Qe:
J3JS
Mvia
509
-------
OlS
'iNI
TT
OiS
'INI
" ? rr^' v- '
•ois
UNI
- JJ.V-- ;T-
"iNI
f>
-n
m
-------
FIGURE 511. Acid extract profiles for Contactor D,
Phase 3-t, runday 22.
-------
UI
h^
ho
fc!
CO
1
UJ
o
OQ
J
INT.
STD.
INT.
STD.
INT.
STD.
FIGURE 512. Acid extract profiles for Contactor D7
Phase 3-t/ runday 50.
-------
CIS
BLANK
DE
SFEF
CD
crj
3~ O
Q -~
M Q-
tt>
05 X
I rt-
3 TJ
8-3
ct>
• v>
?
S5
actor
/
,4 ...
*".:."
--
f--_
nafc"
^JT"
0—1
c.
-------
CO
'tf.
INT.
STD.
FIGURE 514. Acid extract profiles for Contactor D,
Phase 3-t, runday 106.
-------
LU
UJ
OQ
I <
.135- !
INT.
STD.
INT.
STD.
FIGURE 515. Acid extract profiles for Contactor D,
Phase 3-2, runday 15.
-------
FIGURE 516. Acfd extroct profiles for Contactor D,
Phase 3-2, runday 29.
516
-------
OQ
INT.
STD.
INT.
STD.
FIGURE 517. Acfd axtroct profiles for Contactor D,
Phase 3-2, runday 43.
517
-------
81S
Aopuna
pjoy *8IS
•
-------
UJ
CO
• : tl 'in
• >: "'I'L
SW
UJ
o
f ; f
INT.
STD.
INT.
STD.
FIGURE 519. Acid extract profI lee for Contactor D,
Phase 3-2, runday 71.
519
-------
_
UJ
INT.
STD.
FIGURE 528. Acid extract profiles for Contactor D,
Phase 3-2, runday 85.
520
-------
CO
UJ
o
OQ
INT.
STD.
INT.
STD.
FIGURE 521. Acid extract prof i les for Contactor D,
Phose 3-2, rundoy 99.
521
-------
INT.
STD.
INT.
STD.
5 =! ; v
L_ii_..: i f
FIGURE 522. Acid extroct profiles for Contactor
Phase 3-2, runday t!3.
522
-------
JLL
FIGURE 523. Acid extract profiles for Contactor D,
Phase 3-2, runday 127.
523
-------
vs J •' .'
ImiJLJ
INT.
STD.
,t
FIGURE 524. Acfd extract profiles for GAC Filter ISA and
pilot GAC filter, Phase 3-0, runday eight.
524
-------
u.
IbJ
IUV/'
&
LU
LO
CO
INT.
STD.
INT
STD
INT.
STD.
FIGURE 525. Acfd extract profiles for SAC Filter ISA
and pilot SAC filter, Phase 3-8, runday 29,
525
-------
II
LU
LO
LO
JL
CD
&
INT.
STD.
INT.
STD.
INT.
STD.
FIGURE 526. Acid extract profiles for GAC Filter ISA
and pilot GAC filter, Phose 3-8, runday 85.
526
-------
U
J.U
UJ
LO
11
Jl
Lrt
IX
B««i
Hi
CD
1
INT.
STD.
INT.
STD.
INT.
STD.
INT.
STD.
FIGURE 527. Acid extract profiles for GAC Filter ISA
and pilot GAC filter, Phase 3-0, runday 113.
527
-------
8ZS
Aopunj
VSl
OV3
'J.NI
OV9 }°) jd puo
nrnn^TfTT
&l!p!';*!: 1
-------
VSi
OV3
OV3
••
r
-------
oes
VSi
QV9
OV9
jd
Aopunj
puo
pjoy '
CD
-------
<
u
VjL
4<
flu Jt.'i
ni
j'a ti.
H-.' •; •
jk'iji .t ;' ;
hixl-i
INT.
STD.
! ! ' •«
tn
INT.
STD.
INT.
STD.
INT.
STD.
FIGURE 531. Acid extract profiles for 6AC Filter ISA
and regenerated pilot GAG filter, Phase 3-2,
runday one.
531
-------
'I ' "r ' ; i
• * ' . '5
^-'JJ,,« „ i .4 „ '*,
*V< ~'>»*v^«
luijJ^^Xr
INT.
STD.
i
L r^^l
...,•;.. ..._. _j.
INT.
STD.
a
-• , ,,, r i - - - (
CQ
INT.
STD,
FIGURE 532. Acfd extract profiles for GAC Filter ISA
and regenerated pilot GAC filter, Phase 3-2,
runday 29.
532
-------
UJ
J
CO
QL
CD
J
f
a ' L *
n ; L '
III •:• M;wfe|'i',Wte
'.', • « 5
J.:. , . .•: . t .
». . > ;
.ft'. , ' .1 . .';...[£. ;
. .
INT.
STD. 4-
I . h . .
i^fjuJiij:iu___
INT.
STD.
• i
INT.
STD.
* « s •
1 • i i -
. U . i L,'
INT.
STD.
* i
FIGURE 533. Acid extroct proffUs for SAC Ff Iter ISA
and regenerated pilot GAG filter, Phase 3-3,
runday 22.
533
-------
LU
LO
ta,i
f. l: ^ t. _, s
INT.
STD.
INT.
STD.
INT.
STD.
FIGURE 534. Acid extract profiles for GAC Filter ISA
and regenerated pilot GAC filter. Phase 3-3,
runday 50.
534
-------
ses
'62 Aopunj '0-g
puo
M\\\$ Joj
C^Tfl
'J 5 t
pjoy *SSS 38091 J
'iNI
-------
LU
Lrt
r-
o
CO
I :
MiJ.ii
INT.
STD.
...
t
t
F
jj
• f
TJ jLjkJ-
1
i.
• 5
• i
jJu^ttl
I
.
i
t
"-*-* 1 i _k, r.
INT.
STD.
: 5
ff •
1 . _^JJ
1
1
5
INT.
STD,
FIGURE 536. Acid extract profiles for filter influent,
GAC Filter ISA effluent and Contactor D
level 7/ Phase 3-0, runday 57.
536
-------
FIGURE 537. Acfd extract profiles for Contactor D and
pilot contactor,, Phase 3-0, runday eight.
537
-------
BLANK
PFA5
C/i
OJ
CO
DE
SFEF
§
CL
o>
-------
Jxii
t
r,
t
1
;
i-uj. I f-L ^. . . ,
,g — . .
INT.
STD.
i
,., ^
OQ
INT.
STD.
FIGURE 539. AcJd extract profiles for Contactor D and
pilot contactor, Phase 3-0, runday 57.
539
-------
CO
jjij J. ..
UJ
o
LO
5
o.
I , « . S
.1 5 ,
ii i L
INT.
STD.
INT.
STD.
INT.
STD.
INT.
STD.
FIGURE 540. Acfd extract profiles for Contactor D and
pflot contactor, Phase 3-0, runday 85.
540
-------
INT.
STD.
ML
FIGURE 541. Acid extract profiles for Contactor D and
pilot contactor, Phase 3-8, runday 141.
541
-------
\
s'l
UJ
J>
I*
Jl'i Ti
INT.
STD.
• I
I .-_
INT.
STD.
FIGURE 542. Acid extract profiles for Contactor D and
pilot contactor, Phase 3-0, runday 197.
542
-------
LO
U_
a.
OQ
INT.
STD.
INT.
STD.
_JL
VJL
FIGURE 543. Acid extract profiles for Contactor D and
pilot contactor., Phase 3-1, runday 22.
543
-------
fe
V5
1
[
|j
,
^—
,
kv.
fj|.
I-:'
I
J
I'll &
sLJ
t'r'jf/. ji"" >
Ja |
rf_LL«A'!>V.n-T,A'
INT.
STD.
; , . .
L^L _L . 1 Ju — ,
LU
LO
{f
Q.
UJL
INT.
STD.
INT.
STD.
INT.
STD.
LJLJt
FIGURE 544. Acid extract prof I les for Contactor D and
pilot contactor. Phase 3-1, runday 58.
544
-------
CD
INT.
STD.
FIGURE 54S Acid extract profiles for Contactor D and
pilot contactor/ Phase 3-1., runday 78.
545
-------
FIGURE S46. Acid extroct profiles for Contactor D and
pilot contactor, Phase 3-1., runday 106.
546
-------
•gj Aopunj '2-£ »soiy 'jop
puo (] Jopo^uoQ joj. se] i j.ojd }
__ . -TTv-~ , ., ,-.
— .— . — ^i-yr
f t
( I
1
"CIS
UNI
T . r
r
D}UOO ]0\ }d
ooj^xe pjoy ^W 3an3Id
— • -f — • — ^">v,^ »1
i?nrA:\1
'• 'f^
i ^
^V
»»•'
>
'
' s
'
^\
t \
t '
}'
~ «5 f
'OlS
'INI
* i •
"OiS
'INI
•o
5
en
m
u
to
-------
Lrt
•<
tnti
V*
••I,
lit
i 1
,,[*>,. . ,(
•wii'1 ; i — • — •< "i -
INT.
STD.
t
Jl
CD
VJ
tl ,!
,v
INT.
STD.
FIGURE 548. Acid extract profiles for Contactor D and
pi lot contactor, Phase 3-2, runday 43.
548
-------
FIGURE 54a Acfd extract profiles for Contactor D and
pilot contactor, Phase 3-2, runday 71.
549
-------
LO
if
Q_
00
MM
INT.
STD.
5, ?, .....? F
^-^_.IJLJL " " ' L
INT.
STD.
FIGURE 5581 Acid «xtroct prof I Us for Contactor D and
pi lot contactorf Phase 3-2, runday
550
-------
fa
UJ
LO
uf
O.
CO
INT.
STD.
INT.
STD.
INT.
STD.
IL
•1- .i-^L-
( J\-r •- 'i * r— ^ J • • {
INT.
STD.
•
FIGURE 551. Acfd extract profiles for Contactor D and
pilot contactor, Phase 3-2, runday 127.
551
------- |