EPA -660/2-73-005
September 1973
                         Environmental  Protection Technology Series
 Batch  Disinfection of Treated  Wastewater
                                            o
 With  Chlorine At  Less Than 1   C

                                   National Environmental Research Center
                                   Office of Research and Development

                                   U.S. Environmental Protection Agency

                                   Corvallis, Oregon 97330

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            RESEARCH REPORTING SERIES
Research reports of the  Office  of  Research  and
Monitoring,  Environmental Protection Agency, have
been grouped into five series.  These  five  broad
categories  were established to facilitate further
development  and  application   of   environmental
technology.   Elimination  of traditional grouping
was  consciously  planned  to  foster   technology
transfer   and  a  maximum  interface  in  related
fields.  The five series are:

   1.  Environmental Health Effects Research
   2.  Environmental Protection Technology
   3.  Ecological Research
   U.  Environmental Monitoring
   5.  Socioeconomic Environmental Studies

This report has been assigned to the ENVIRONMENTAL
PROTECTION   TECHNOLOGY   series.    This   series
describes   research   performed  to  develop  and
demonstrate   instrumentation,    equipment    and
methodology  to  repair  or  prevent environmental
degradation from point and  non-point  sources  of
pollution.  This work provides the new or improved
technology  required for the control and treatment
of pollution sources to meet environmental quality
standards.

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                                                 EPA-660/2-73-005
                                                 September 1973
         BATCH  DISINFECTION OF TREATED WASTEWATER

              WITH CHLORINE AT LESS THAN 1°C
                              by

                      Ronald  C.  Gordon
                   Charlotte  V.  Davenport
         Arctic Environmental  Research Laboratory
                  Fairbanks,  Alaska  99701
                      Project  16100 GKG
                   Program  Element 1BB044
For sale by the Superintendent of Documents, U .S. Government Printing Office, Washington, B.C. 20402 - Price 65 ceats
           NATIONAL ENVIRONMENTAL RESEARCH  CENTER
              OFFICE OF  RESEARCH AND MONITORING
            U.S. ENVIRONMENTAL PROTECTION AGENCY
                  CORVALLIS,  OREGON  97330

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                            ABSTRACT

A laboratory study was conducted in which the batch treatment techni-
que was used to gain some insight into chlorine disinfection of waste
treatment system effluents at less than 1°C.   One primary and three
secondary effluents were examined at the low temperature with parallel
control samples at 25°C.  Effluent disinfection was considered mini-
mally effective if, after one hour contact time in the presence of 1
mg/1 total chlorine residual, there were no more than 1000 total  and
200 fecal coliforms/100 ml.

The results indicated that both chlorine demand and the rate or ex-
tent of coliform reduction were decreased at the low temperature.
The disinfecting ability of chlorine varied significantly at less than
1°C when all four effluents were compared.  These effects did not in
themselves negate the effectiveness of chlorine as a disinfectant at
low temperature because the previously stated minimums were easily met
in effluents from all sources.   However, batch treatment is not plagued
with short-circuiting as are most operating contact chambers, so a
higher bacterial quality could be expected after the contact period.

The only real measure of satisfactory disinfection is the number of
enteric bacteria being discharged into the receiving water.  An arbi-
trary chlorine residual after a predetermined contact time cannot be
considered prima facie evidence of satisfactory disinfection because
of the variable disinfecting ability of chlorine.  The chlorine resid-
ual:contact time relationship must be established for each effluent
at the lowest temperature encountered in the system.
                                ii

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                            CONTENTS
                                                                    Page
Abstract                                                             ii
List of Tables                                                       iv
Acknowledgments                                                       v
Sections
   I  Conclusions                                                     1
  II  Recommendations                                                 2
 III  Introduction                                                    3
  IV  Experimental Methods and Materials                              5
   V  Experimental Results                                           11
  VI  Discussion                                                     23
 VII  References                                                     26
VIII  Glossary                                                       29
                                 iii

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                             TABLES
No.                                                                Page
 1  Effluent Chemical and Physical  Characteristics                  12
 2  Chlorinated and Unchlorinated Disinfection Controls at 25°C     14
 3  Primary Sedimentation Effluent  Disinfection at Less Than 1°C    15
 4  Aerated Lagoon Effluent Disinfection at Less Than 1°C           17
 5  Extended Aeration (Submerged Aerator) Effluent Disinfection
    at Less Than 1°C                                                18
 6  Extended Aeration (Surface Aerator) Effluent Disinfection
    at Less Than 1°C                                                20
                                iv

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                         ACKNOWLEDGMENTS

The support of the Arctic Environmental Research Laboratory personnel is
acknowledged with sincere thanks, especially Ms. Candace George for doing
the chlorine determinations throughout the study.

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                            SECTION I

                           CONCLUSIONS

Low temperature caused a definite reduction in chlorine demand with the
percent reduction essentially independent of effluent source.

Low temperature caused a marked reduction in the disinfecting  ability
of chlorine which varied significantly with effluents from different
sources.

Temperature did not appreciably affect the relative rate of fecal  and
total coliform reduction in a particular effluent.  In all cases,  a
lower chlorine residual and shorter contact time were required to  meet
the minimum fecal coliform criteria for effective disinfection than
were required for minimum total coliform criteria.

Low temperature did not prevent minimally effective disinfection (1000
total and 200 fecal coliforms/100 ml) from being attained in effluents
from all sources when batch disinfection was used.

To achieve satisfactory disinfection at low temperatures, the  chlorine
residual:contact time relationship must be determined for each effluent
at the lowest temperature encountered in the system rather than use an
arbitrary relationship as prima facie evidence of satisfactory disin-
fection.

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                           SECTION II

                         RECOMMENDATIONS

Chlorine disinfection in flow through contact chambers must be studied
at less than 1°C to determine the extent to which the enteric bacteria
reduction:chlorine residual relationship is changed from that found in
batch treatment.

The source and significance of "non-fecal" coliforms (those not giving
a positive elevated temperature test) found in waste treatment systems
during the winter should be determined.

Both total and fecal coliform criteria should continue to be used for
establishing effective disinfection if receiving water quality is to
be effectively maintained or enhanced.

Guideline criteria for attaining effective disinfection in low temper-
ature effluents must be developed.

Evaluation of disinfectants, other than chlorine, for possible appli-
cation in effluents having low temperatures should be accelerated.

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                           SECTION III

                          INTRODUCTION

Chlorine is the disinfectant which has attained wide acceptance for
use in treated wastewater disinfection, but the role of effluent tem-
perature in the process has received insufficient emphasis.  This pres-
entation is limited to the low temperature aspects, and a more com-
plete discussion of chlorine disinfection can be found in several re-
cent publications (2, 6, 29).  In addition to chlorine, there are sev-
eral other disinfectants which have potential application in treated
wastewater disinfection (2) and, some day, may also be widely accepted.

In 1936, Heathman et aj_. (16) studied the ability of chlorine and
chloramine to kill pure cultures of enteric bacteria in tap water.
Among other things, they compared this ability at room temperature and
at the temperature of iced water.  They concluded that, "The time
required for chloramine and chlorine in some instances to kill strains
of £. typhosa and members of the coli-aerogenes group is appreciably
greater at low temperature than at room temperature."  Subsequent work
in the 1940's, 50's and 60's (see references 6 and 7) followed the
lead of Heathman and co-workers and showed that low temperature hin-
dered chlorine disinfection in pure culture:pure water systems.
Chambers (6) recently reviewed chlorination of waste treatment plant
effluents and pointed out the reason why disinfection studies had been
conducted in this manner.  He stated that, "Wastewater effluents con-
tain many compounds and materials that interfere with the germicidal
activity of chlorine, some of which completely neutralize it.  Because
of the many interferences in wastewater, it  has been necessary to es-
tablish the inherent disinfecting characteristics of chlorine in highly
purified water under the most carefully controlled and interference-
free conditions  possible."

Another study was also  conducted  in  1936 in  which Rudolfs and Gehm  (25)
made a  rather extensive study of  sewage chlorination.  They concluded
that,  "Within the limits  of  5°  and  37°C, neither bacterial reduction
nor  chlorine demand  was appreciably affected by temperature in fresh
or  stale  sewage."  Since  this early study,  little attention has  been
given  to  directly studying disinfection in  treated wastewater.

The need  to study chlorine disinfection of  treated wastewaters con-
 taining the inherent interferences  was pointed out by Marais et  al.
 in  1967 (21) when they  stated that,  "To date there have been no  re-
 liable  laboratory studies  on the  efficiency  of chlorine as a disin-
fectant in  polluted  waters,  such  as  secondary sewage effluents which
contain varying  amounts of nitrogenous compounds and ammonia."   Sub-
sequently,  there has  been  some  study of wastewater disinfection  (8,
19), but  little  effort  has been directed toward temperature effect.

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Chambers (6) pointed out that low water temperature severely limits
the effectiveness of chlorine.   This limitation poses a particularly
serious problem in regions such as the Arctic and Subarctic where tem-
peratures in some waste treatment systems, effluents from these sys-
tems and receiving waters are at or near 0°C during several months each
winter.  Thus, at low water temperatures, treated wastewater may con-
tain more bacteria of fecal origin (9, 26).  After entering the receiv-
ing water, the fecal indicator bacteria survive for longer periods at
0°C (14) than at warmer temperatures (3).  The decreasing effective-
ness of chlorine as a disinfectant and the higher number of fecal bac-
teria suggest that effluent disinfection may be more difficult to
achieve at low temperatures.  In addition, greater survival in cold re-
ceiving waters may mean requiring the discharge of fewer bacteria than
is acceptable at warmer temperatures.

After considering the wide use of chlorine, the problems involved in
low temperature treated wastewater disinfection and the research needs
stated by Chambers and Berg (7), this study was designed to determine
if effective disinfection could be attained in treated wastewater at '
less than 1°C (<1°C).  The disinfection criteria developed by the
Environmental Protection Agency, Region X (10) were used as the basis
for establishing minimum effective disinfection.  Briefly, these cri-
teria are:  [1] that effluents from chlorine contact chambers shall
average less than 1000 total coliforms and 200 fecal coliforms/100 ml
when the effluent is discharged into recreational waters; and [2] that
the total chlorine residual shall not be less than 1 mg/1 after 60 min-
utes of contact time when conclusive coliform data are not available.

Discussion of enteric parasites and viruses has been omitted because
these groups of organisms are more resistant to chlorine than are bac-
teria of the coliform group [see the review by Chambers (6), for refer-
ences and discussion].

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                           SECTION IV

               EXPERIMENTAL METHODS AND MATERIALS

EFFLUENT SOURCES AND SAMPLING

Effluents from one primary sedimentation and three secondary biologi-
cal  waste treatment systems were examined during the winter of 1971-
1972.   The biological treatment systems were a 15 day detention time
aerated lagoon and two extended aeration systems.  One extended aera-
tion system had submerged aeration and the other had surface aeration
(oxidation ditch).  Numerous extended aeration system (submerged aera-
tor) effluent samples were used to develop the procedures followed
throughout the remainder of the study.  Both grab and 24-hour composite
effluent samples were examined with no appreciable differences in coli-
form numbers or chlorine demand attributable to the sampling method.
Samples were also examined in parallel at less than 1°C (<1°C) and at
25°C to determine what temperature effect could be expected.  Disin-
fection results obtained at 25°C were consistent and compared favorably
with other studies regardless of how the results varied at <1°C.  Fol-
lowing this developmental work, only grab samples of the other three
effluents were used, and the number of 25°C controls was kept to a min-
imum because of the timing problems encountered when extra samples were
examined during the disinfection runs.  One effluent sample was exam-
ined each week and each source was studied for three weeks.

PROCEDURES FOR EFFLUENT PROCESSING

To obtain the necessary degree of experimental control, the following
three day schedule was required for complete effluent analysis:

Day One:

     A.   Effluent collected  in five gallon, polyethylene carboys be-
          tween  7:00  and  9:00 a.m., and  transported  to the laboratory
          without  delay.

     B.   Effluent temperature measured  immediately  after arrival in
          the laboratory.

      C.   Effluent transferred to  a five gallon,  glass carboy and stir-
          red while  being  cooled  to 0.0-0.5°C  in  a -10°C refrigerated
          water  bath.

      D.   Effluent transferred to  a 0°C  room and  stirred continuously un-
          til  Day  Two.

     E.   Sample withdrawn  for preliminary coliform  enumeration.

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Day Two:

     A. Preliminary coliform enumeration completed.

     B.  An immediate and one hour total chlorine demand  established
         for the effluent at <1°C, and the amount of chlorine necessary
         to provide approximately 1 mg/1 total  chlorine residual  after
         one hour contact time determined.

     C.  Effluent temperature was measured and  samples were withdrawn
         for initial time coliform enumeration  and physical  and chemi-
         cal parameter determinations.

     D.  For the disinfection run at <1°C, four effluent  volumes  of two
         or three liters each were set up as shown in Figures 1  and 2,
         and immersed in a refrigerated water bath set to maintain ap-
         proximately 0°C in the bottles.

     E.  Chlorine dosing for the disinfection run at 0°C:  [1] unchlo-
         rinated control, [2] sufficient chlorine injected into each
         of the other three bottles to provide  approximately 0.5, 1.0
         and 1.5 mg/1 residual after one hour contact time.

     F.  Approximately four liters of effluent  were warmed rapidly to
         25°C, the pH determined and a sample withdrawn for initial
         coliform enumeration.  For the disinfection run  at 25°C, bot-
         tles containing one liter of effluent for the unchlorinated
         control and two liters to be dosed with the same amount of
         chlorine that should have given approximately 1.0 mg/1  resid-
         ual at 0°C after one hour contact time were set  up on the labo-
         atory bench as shown in Figure 1.

     G.  The <1°C and 25°C set-ups were completed concurrently and the
         contact period started as each bottle  was dosed  with chlorine.
         Total chlorine residual determination  and coliform enumeration
         were conducted at predetermined intervals.   At the end of the
         contact period, pH and temperature were measured in each bottle.

Day Three:

     A. Coliform enumeration completed.

GLASSWARE PREPARATION

All glassware used during this study was made chlorine demand free (1)
with the exception of the five gallon carboys.   The glassware for use
at <1°C was allowed to equilibrate at 0°C.

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  WASTE
 RECEPTACLE
2 OR 4  LITER
GLASS CARBOY-
                         STIRRING  BAR
                                              SUBMERSIBLE
                                              MAGNETIC
                                              STIRRER
     Figure 1.   Schematic  of  batch treatment reactor vessel for chlorine
                disinfection  studies

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Figure 2.   Reactor vessel  set-up for chlorine disinfection studies
           at less than 1°C
                                 E

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WATER PREPARATION

Distilled water from the building supply was filtered through a
Barnstead Organic Removal cartridge followed by a Corning Ultra-High-
Capacity demineralizer cartridge and then distilled in an all glass
apparatus.  Sufficient glass distilled water was prepared each week
so that all water used in a disinfection run was from the same supply.
The water for use at <1°C was allowed to equilibrate at 0°C.

CHLORINATION METHOD

A chlorine stock solution containing approximately 500 mg/1 total chlo-
rine was freshly prepared from household bleach (Purex brand) and glass
distilled water the day it was to be used.  This solution was standard-
ized by the iodometric method (1) and was then used for all chlorine
dosages.

Effluent examination early in the study indicated that immediately after
dosing, there was essentially no free available chlorine present as
measured by the orthotolidine-arsenite (OTA) method (1).  Therefore, all
chlorine residual determinations were done in triplicate using the or-
thotolidine (OT) method (1) for measuring total chlorine residual.  A
Bausch and Lomb Spectronic 20 was used to measure the color intensity.
All values were rounded to the nearest 0.1 mg/1 for reporting in this
study.

A pi pet was used to deliver the chlorine stock solution when making
temporary  standards in distilled water.  A syringe fitted with a 14
gauge cannula was used to add chlorine stock solution to all effluent
samples so the  total volume could be delivered rapidly.  All stock so-
lution  additions were delivered directly into the vortex created by stir-
ring with  a magnetic stirrer.

COLIFORM  ENUMERATION

The membrane  filter method  (11) was used for both total and fecal coli-
form enumeration.  M-Coliform Broth  (BBL) and M-FC Broth (Difco) were
the media used  for total  and fecal coliforms respectively.  Each time
the M-FC  Broth  was prepared, the  pH was checked and adjusted to 7.4 as
necessary.

All effluent  samples  for coliform enumeration were collected in sterile,
220 ml, polypropylene containers  (Falcon Plastics) which contained 0.5
ml  of  a 10 percent sodium thiosulfate solution.

PHYSICAL  AND  CHEMICAL PARAMETER MEASUREMENT

Chemical  oxygen demand  (COD), total solids  (TS), total suspended solids
(TSS),  volatile suspended solids  (VSS), total dissolved solids (TDS),

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volatile dissolved solids (VDS), and total  volatile solids (TVS) were
determined by the methods described in Standard Methods for the Examina-
tion of Water and Wastewater, 13th Edition  (1).  Ammonia nitrogen (NH3-N)
was determined with Technicon AutoAnalyzer  Methodology (27).  The pH me-
ters were fitted with combination electrodes and automatic temperature
compensators.
                                10

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                            SECTION V

                      EXPERIMENTAL RESULTS

GENERAL

Physical and chemical parameters for all effluents examined are presented
in Table 1.  Some of these parameters have been considered among the most
important in affecting chlorine demand and bactericidal activity in
treated wastewater (5, 6, 23, 24).  They appeared to be fairly consistent
in samples from each source with the exception of COD, which varied over
a wide range in both extended aeration systems.  Although differences be-
tween systems were quite pronounced, only total suspended (TSS) and vol-
atile suspended (VSS) solids could be related to the type of treatment
(primary vs. secondary).  The full range of solids data was not collected
until after the extended aeration system (submerged aerator) effluent
study had been completed.  However, solids data from other work being
conducted during the same time period suggested consistent results from
the extended aeration system.

Effluents from systems operating at or near 0°C were not readily avail-
able in the Fairbanks area.  Therefore, it was necessary to use efflu-
ents which arrived in the laboratory with temperatures ranging from
4.8-12.3°C (Table 1) and cool them to less than 1°C (<1°C).  Since the
ambient air temperature was low and the travel time was short, these
were essentially the system operating temperatures when the samples
were taken.

It has  been pointed out that non-coliform bacteria and turbidity in
chlorinated wastewater may interfere with coliform enumeration by the
membrane filter method  (1).  Non-coliform bacteria caused little prob-
lem with fecal coliform enumeration, but occasionally did interfere
with total coliform  enumeration when there were more than 1000 total
coliforms/100 ml.  Since  the minimum bacterial quality for effective
disinfection was  set at  1000 total and  200 fecal coliforms/100 ml of
chlorinated effluent,  sample volumes for filtration were generally se-
 lected so  that  1000  total  coliforms/100 ml was the maximum countable
 number thus minimizing the non-coliform interference.  Under these con-
 ditions,  total  coliform  numbers greater than 1000/100 ml were reported
 as  Too Numerous To  Count  (TNTC).   The  sample volume that could be fil-
 tered  was  limited by suspended material which  plugged the filter and/or
 built  up  on  the surface  obscuring  the  coliform colonies.  To avoid
 these  problems, the  maximum  effluent volume filtered was 8-12 ml with.
 the  result that many coliform counts were less than 20 per filter after
disinfection.  The validity  of these low counts per filter may be ques-
tionable  (1), but this was partially offset by filtering all effluent
volumes in triplicate  and  reporting the average coliform number.  For
example, if a 10  ml  sample was filtered and there were no colonies on
any of  the filters,  the count/100 ml could only be reported as less than
                                11

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Parameter
Temperature When Received (°C)
At Start of Contact Time
TS (mg/1)
TSS (mg/1)
VSS (mg/1)
TDS (mg/1)
VDS (mg/1)
TVS (mg/1)
COD (mg/1)
NH3-H W/l)
In 0°C Contact Chambers
Initial Temperature (°C)
Final Temperature ("C)
Initial pH
Final pH
In 25°C Contact Chambers
Initial Temperature (°C)
Final Temperature (8C)
Initial pH
Final pH
Effluent Source
Primary Sedimentation*
2/10/72 2/17/72 3/2/72
10.2 9.7 9.8

530 490
92 96 89
65 71 69
350 350 350
140 150 150
340 230 270
31 1 284 270
21 22 23

0.2 0.0 1.6
-0.2-+0.1 0.2-0.4 0.2-0.4
6.9 6.9 6.8
7.2-7.3 6.9-7.1 6.8-6.9

25.0
25.0
6.9
6.9-7.1
Aerated Lagoon*
4/6/72 4/13/72 4/20/72*
4.8 12.3 7.1

320 400 400
27 33 43
21 29 35
270 380 320
150 140 190
140 160 240
203 226 152
20 21 21

1.3 1.0 0.6
0.0-0.1 0.1-0.2 14.9-15.4*
7.0 6.8 7.1
7.1-7.3 6.9-7.0 7.2-7.3

25.0
25.0
7.2
7.2-7.5
Extended Aeration
Surface Aerator#
3/9/72 3/23/72
7.9 11.6

730 820
37 44
30 35
680 740
210 150
263 230
461 148
19 22

2.2 0.5
-O.l-t-0.2 -0.1-0.0
7.1 7.1
7.2-7.4 7.2-7.4

___** ___**
Extended Aeration
Submerged Aerator
12/2/71# 12/9/7W 12/16/7W
9.2 8.9 8.0

35 43 37
114 120 618
15 20 22

0.4-0.6 0.3-0.5 0.9-1.0
7.4 7.2 7.9
7.5-7.6 7.3-7.4 8.0-8.3

25.0
25.5-25.6
7.5
7.6-7.8
        * Temperature control  lost during the hour contact time at 0°C.
       ** No 25°C  data for the oxidation ditch.
        i Grab sample.
       ## 24 hour  composite sample.

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10/100 (<10/100 ml).  If the average count was five when 10 ml  was
filtered, the count was reported as 50/100 ml and footnoted as  being
based on an average of less than 20 colonies per filter.

Since this study was completed, Lin (20) has evaluated Most Probable
Number (MPN) and membrane filter methods for total and fecal coliform
enumeration in chlorinated effluents.   His results indicated possible
supression of both total and fecal coliform numbers when the membrane
filter method was used with chlorinated effluents.  Thus, the coliforms
enumerated in chlorinated effluent during this study may have repre-
sented as little as two thirds of the actual number present.

The chlorine residual and bacterial results obtained at 25°C are shown
in Table 2.  It should be noted that the extended aeration results in
this table are for the submerged aerator system only.  Results from
the surface aerator system have been omitted because the effluent was
considered atypical at the time the 25°C work was scheduled.  The ef-
fluent was black, anaerobic and contained 1000 mg/1 total suspended
solids (TSS).  Time did not permit scheduling another run to include
the 25°C portion.

At 25°C, all effluents had a high immediate chlorine demand followed by
a much lower continuous demand throughout the contact period and a sharp
decline in coliform numbers during the first 30 minutes of contact time.
This was in close agreement with recent work conducted by Kott  (19) at
20°C.  The primary effluent had up to an order of magnitude greater
total and fecal coliform numbers than did the other effluents and about
twice the chlorine dosage was required to provide a similar residual
after 30 and 60 minutes contact time.  The  25°C results  indicated:  [1]
the minimum bacterial quality for effective disinfection was met with
ease  in all effluents after 30 minutes of contact time;  [2] both total
and fecal coliforms  had essentially disappeared after 60 minutes in the
presence of Q.3-0.6 mg/1 total chlorine residual; and [3] no apparent
effect on final  bacterial quality  could be  attributed to effluent source
when  similar chlorine residuals were maintained.  Previously, correspond-
ing observations  have been made in operating treatment systems  (18).

PRIMARY SEDIMENTATION  EFFLUENT

The  results  in Table 3  were obtained at <1°C with effluents from a pri-
mary  sedimentation system examined during three consecutive weeks.  This
 system  appeared to produce a  consistent effluent as  indicated by the
 solids  and  ammonia nitrogen concentrations  (Table 1), and chlorine demand,
Three effluent batches  were dosed  with chlorine during each run to en-
 sure approximately a 1  mg/1 total  chlorine  residual after one hour con-
tact  time.   The required chlorine  dosage was very close  to 4.5 mg/1 each
week.   The  results indicated  that  the minimum effluent bacterial qual-
ity of  1000  total  and 200 fecal coliforms/100 ml was easily attained
                                13

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Effluent
Source tt
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within the hour contact time when the total  chlorine residual  concentra-
tion was as low as 0.5 mg/1  and in no case was more than 1  mg/1  required.
In two of the three runs, coliform numbers well below the minimum qual-
ity were achieved in no more than 30 minutes with less than 1  mg/1 total
chlorine residual.  Coliforms were enumerated at five minute intervals
from 15-30 minutes during the third run and the results indicated that
more than 15 but less than 30 minutes contact time were required to re-
duce the total coliform count sufficiently to meet minimum effluent
quality, while less than 15 minutes were required for fecal coliforms.
Comparison of the 25°C results (Table 2) with the <1°C counterparts sug-
gested that temperature effect on disinfection was minimal  but there
was a significant effect on chlorine demand in effluent from this source.

AERATED LAGOON EFFLUENT

Aerated lagoon effluent was examined for three consecutive weeks during
which the solids and ammonia nitrogen (Table 1), and chlorine demand re-
mained fairly constant.  The major differences between this effluent and
the primary effluent were that some components of the solids and COD ap->
peared to be significantly higher in the primary effluent.   When aerated
lagoon effluent was first examined, it was assumed that disinfection
would proceed at least as rapidly as primary effluent disinfection.
However, this effluent was considerably more difficult to disinfect at
<1°C than the primary effluent (Table 3).  It was possible to disinfect
the aerated lagoon effluent (Table 4) to a total and fecal  coliform den-
sity which easily met the minimum bacterial quality after one hour con-
tact time in the presence of approximately 1 mg/1 total chlorine resi-
dual, but a contact time of at least 50 minutes was consistently re-
quired.  When the final residual was appreciably greater than 1  mg/1,
the contact time required to achieve minimum total coliform quality was
shortened but variable from greater than 20 to greater than 40 minutes.
Minimum total coliform quality was not reached during the hour when the
final residual was appreciably less than 1 mg/1.  Fecal coliforms were
reduced to fewer than 200/100 ml in less than 30 minutes at all  chlorine
residual concentrations and possibly in less than 15 minutes in some
cases.  During the third run, temperature control was lost with a sub-
sequent temperature rise from <1°C to 15°C.  The probable effect of this
temperature rise was an increased bacterial reduction and increased chlo-
rine demand.  When the 25°C results for this effluent (Table 2)  were com-
pared with the <1°C results, it was apparent that disinfection and chlo-
rine demand were affected by temperature.

EXTENDED AERATION EFFLUENT (SUBMERGED AERATOR)

During the three consecutive weeks in which extended aeration system
(submerged aerator) effluent was examined, both grab and composite sam-
ples were studied at <1°C.  Little or no effect on the disinfection
process could be attributed to the sampling method so it was assumed
that the results presented in Table 5 were directly comparable.   The
physical and chemical parameters from this system suggested a fairly

                                16

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            § No  coliform colonies on any filter when triplicate filters were examined.

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-------
consistent effluent as did the chlorine dosage required to provide ap-
proximately 1 mg/1  total chlorine residual after one hour contact time.

With this effluent, more than 30 minutes were required to meet the min-
imum total coliform quality for effective disinfection, but it was met
without difficulty during the one hour contact period in two of the
three runs when approximately 1 mg/1 total chlorine residual remained.
When the residual was appreciably less than 1 mg/1, the minimum quality
was not achieved during the hour.  Fecal coliform results were available
for one of these two runs and the minimum quality was surpassed with
ease in less than 30 minutes in the presence of approximately 0.5 mg/1
total chlorine residual.  Results from the third run were entirely dif-
ferent because minimum quality for neither total nor fecal coliforms
was met after an hour contact period with a total chlorine residual of
2.1 mg/1.  There may be some question as to when the minimum fecal coli-
form quality was attained during this run, but it appeared to require
approximately 2 hours and 1.5-1.8 mg/1 chlorine residual.  The contact
time was approaching 4 hours before minimum total coliform quality was
achieved in the presence of a 1.8 mg/1 residual.

The reason why effluent from this source should occasionally have been so
difficult to disinfect is not clear but the results did suggest that some
factors other than the measured parameters played a role.  One point in
which all three runs showed agreement was that coliform numbers continued
to decrease after the first hour, but the rate was much lower than dur-
ing the first hour of contact time.

Again, as with the aerated lagoon effluent (Table 4), this extended aera-
tion effluent proved to be more difficult to disinfect than the primary
effluent (Table 3) even though the chemical and physical parameters
(Table 1) and the initial coliform numbers suggested that the primary ef-
fluent was of lower quality.  It should also be noted that both chlorine
demand and disinfection were significantly affected by increasing the
temperature to 25°C (Table 2).

EXTENDED AERATION EFFLUENT (SURFACE AERATOR)

For three consecutive weeks, extended aeration system (surface aerator)
effluent was examined in the same manner as effluents from other sources.
As stated previously, the effluent was atypical during one week and there
was not sufficient time for an extra run, so results from two runs are
presented in Table 6.  The chemical and physical parameters (Table 1) sug-
gested that this was a fairly consistent effluent when the system was op-
erating properly.  There was sufficient spread between the chlorine dos-
ages required to produce approximately a 1 mg/1 total chlorine residual
in the two runs that it could not be considered a consistent dosage.

Less than 30 minutes were required to meet the minimum bacterial quality


                                19

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-------
for effective disinfection in both runs when approximately 1  mg/1  total
chlorine residual remained after one hour of contact time, and as  little
as 0.5 mg/1 residual was necessary to reduce the total coliforms to well
below the minimum quality in less than 60 minutes contact time.  The fe-
cal coliforms had essentially disappeared in less than 30 minutes  when
the final total chlorine residual was approximately 1 mg/1.  When  the
coliforms were enumerated at five minute intervals, the results suggested
that the minimum fecal coliform quality was attained in less  than  15 min-
utes and that the total coliform reduction required at least  25 minutes
when the final total chlorine residual was approximately 1 mg/1.  Of
course, the rather large difference in the initial total and  fecal coli-
form counts probably accentuated any differences in the results between
the two runs.

COMPARATIVE RESULTS

When results from the two extended aeration systems were compared, it was
apparent that disinfection proceeded more rapidly in effluent from the
surface aerator system (Table 6) than in the submerged aerator system
(Table 5) at <1°C.  Recorded physical and chemical parameter  differences
between these systems were not sufficiently pronounced to provide an ex-
planation for these results.  Even though disinfection did proceed more
rapidly in the surface aerator system, the results were still not equal
to those obtained with primary effluent (Table 3).

Primary effluents have been considered more difficult to disinfect to a
predetermined coliform content than secondary effluents (6).   This was
borne out to the extent that greater chlorine dosages were required in
the primary effluent  (Tables 2 and 3} than in the secondary effluents
(Tables 2, 4, 5 and 6) in order to satisfy the immediate chlorine de-
mand and to provide the desired total chlorine residual.  The consis-
tently higher suspended solids concentration in the primary effluent
(Table 1) may have accounted for the greater chlorine demand.  However,
a chlorine dosage of approximately 4.5 mg/1 to provide 1 mg/1 residual
after one hour contact time in the primary effluent was not excessive
when compared to the 2.4-4.0 mg/1 dosages required in the secondary
effluents.

When all chlorine dosages and all effluents were considered,  it appeared
that most of the one hour chlorine demand was satisfied in the first 1
to 2 minutes of contact time at <1°C and 25°C, with a much lower demand
continuing throughout the hour.  The portion of the one hour demand which
was satisfied between dosing and first residual measurement was in excess
of 80 percent in all except one aerated lagoon sample at <1°C and the
primary effluent sample at 25°C.  These were 72 and 73 percent of the one
hour demand respectively.

Direct comparison of the 25°C results with the <1°C counterparts which
received the same chlorine dosage showed that a much lower chlorine

                                21

-------
residual remained after one hour contact time at 25°C and  suggested  that
temperature had a rather pronounced effect on chlorine demand.   Because
of the greater demand at 25°C,  the primary effluent one hour  chlorine
demand at <1°C was 80 percent of the corresponding 25°C demand,  the
aerated lagoon effluent demand was 86 percent and the extended aeration
system (submerged aerator) effluent demand was 81 percent.
                                22

-------
                           SECTION VI

                           DISCUSSION

The objective of this study was to determine if effective treated waste-
water disinfection could be attained with chlorine at less than 1°C
(<1°C).  Results obtained with effluents from four waste treatment sys-
tems indicated that there were definite temperature effects.  The most
consistent of these effects was on chlorine demand, which was lower at
<1°C than at 25°C by nearly the same percentage in effluents examined
at both temperatures.  The rate and/or extent of coliform reduction
during the contact period was also lower at <1°C than at 25°C but the
temperature effect ranged from no apparent effect in the primary efflu-
ent to a pronounced effect in the extended aeration system (submerged
aerator) effluent.  These temperature effects did not in themselves ne-
gate the effectiveness of chlorine as a disinfectant at temperatures as
Tow as 0°C because the minimum criteria for effective disinfection were
met with ease in effluents from all sources.  The single exception to
meeting the minimum quality was in one sample of extended aeration sys-
tem (submerged aerator) effluent.

Extended aeration system (submerged aerator) and aerated lagoon effluents
were the most difficult to disinfect at <1°C.  Both of these systems were
pilot plant operations located on a large military installation and, as
a result, may have received waste containing some "atypical" components
which interfered with the disinfection process.  Although military waste
may contain some components not normally found in "typical" civilian do-
mestic waste, such a waste is not atypical in Alaska where a large num-
ber of military installations are located.

Batch treatment is essentially analogous to plug flow which does not
simulate the course of events in most operating disinfection contact
chambers.  Batch treatment with continuous mixing and rapid chlorine
injection, as used in this study, had several advantages over most op-
erating contact chambers.  The following were among these advantages:
[1] chlorine was thoroughly and rapidly mixed with the effluent; [2]
chamber configuration ensured that all effluent remained in contact
with the chlorine throughout the contact period; and [3] theoretical
and actual contact time were the same.  In addition, the effluent chlo-
rine demand was determined immediately prior to treatment.  Thus, higher
bacterial quality could be expected after the contact period in this
system than in most operating systems which are plagued with short-cir-
cuiting problems and are usually designed for average rather than max-
imum flow contact time.

During the winter months, climatic conditions in interior Alaska effec-
tively seal all exposed soil  and water surfaces, making it unlikely that
coliform bacteria enter waste treatment systems from other than sewered
                                23

-------
locations.  The source of coliforms can probably be further restricted
because there are no industries in the area which contribute unusually
large coliform numbers in the wastes they produce.  Thus, coliforms ap-
parently come almost entirely from domestic wastes, suggesting that a
large portion of the total coliform population should give a positive
elevated temperature fecal coliform test.  Throughout this study, the
fecal coliforms consistently represented a smaller portion of the total
coliform population than could have been expected if no alterations oc-
curred (12).  There are at least three possible explanations for an al-
tered coliform population.  Although there is no supporting evidence,
one possible explanation is that the coliform population in the human
intestinal tract is modified when living in a cold environment.  The
other two explanations are related to the warm temperature encountered
in the sewage collection and treatment systems during this study.  One
of these is differential die-off of fecal and non-fecal coliforms with
the fecal coliform viability being reduced more rapidly.  The other pos-
sible explanation was derived from observations during a study currently
in progress which suggested some differential growth enhancement at the
8-10°C temperatures in the collection and treatment systems with some
portion of the non-fecal coliform population increasing in numbers while
the fecal coliform numbers remained nearly constant (15).  Similar ob-
servations suggesting enteric bacteria growth in 5-10°C river water were
made by Hendricks and Morrison (17).

Geldreich (12) presented a very comprehensive discussion in which he
pointed out the significance of the fecal coliform portion of the total
coliform population.  He showed that the portion of the total coliform
population which did not give a positive fecal coliform test had only a
small chance of originating in warm blooded animal feces, whereas coli-
forms which gave a positive test had very little chance of being from any
other source.  Because of this and a more recent compilation of water
quality criteria (22), there is a current effort to place more emphasis
on fecal coliform numbers and de-emphasize or possibly not use total coli-
form numbers when determining the bacterial quality of treated waste-
water and surface water (13).  This effort could possibly have the effect
of permitting an increased discharge of non-fecal coliforms to the re-
ceiving water, since the results obtained in this study indicated that
the minimum fecal coliform quality of 200/100 ml was consistently met
with a lower chlorine residual and in a shorter contact time than was the
1000/100 ml minimum total coliform quality at <1°C.  The fact that the
fecal coliforms were present in 1-2 orders of magnitude lower numbers
than total coliforms may have accounted for the differences.  However,
the results did suggest that the fecal coliforms may have been somewhat
more susceptable to chlorfne disinfection than was the non-fecal portion
of the total coliform population.

When chlorinated effluents from several sources were compared, it be-
came evident that the disinfecting ability of chlorine varied signifi-

                                  24

-------
cantly at <1°C.  Thus, an arbitrary chlorine residual  after a predeter-
mined contact time cannot be considered prima facie evidence of satis-
factory disinfection, and the chlorine residual:contact time relation-
ship must be established for each effluent to be disinfected (6) at the
lowest effluent temperature encountered.  In any event, the only real
measure of satisfactory disinfection is the number of enteric bacteria
being discharged into the receiving water.  In batch treatment, the
theoretical and actual contact times are the same.  This is not true in
many operating contact chambers.  Because of short-circuiting problems,
theoretical contact time has very little meaning and inadequately dis-
infected effluent may be discharged into a receiving water.  The result-
ing public health hazards have been well documented (22).  These hazards
acquire greatly increased significance in low temperature receiving waters
because of enhanced enteric bacteria survival (14, 28), and because
many people consume surface water without benefit of any form of treat-
ment in Alaska.

Residual chlorine toxicity to aquatic life in receiving waters is beyond
the scope of this discussion.  There is a considerable body of litera-
ture from temperate climates indicating that very low levels of chlo-
rine and compounds containing chlorine are toxic to aquatic life (4).
However, there has been no determination of toxic effects in receiving
waters approaching 0°C, and under the additional stress of severely de-
pleted dissolved oxygen.  Therefore, it is essential that extreme cau-
tion be exercised in maintaining chlorine residuals no higher and pos-
ibly lower than those established as being non-toxic in warmer receiving
waters until low temperature bioassay studies have been conducted under
Arctic and Subarctic conditions.
                                  25

-------
                            SECTION VII

                            REFERENCES

 1.   American Public Health Association.   Standard Methods for the Ex-
     amination of Water and Wastewater.   13th Edition.   New York, Ameri-
     can Public Health Association, 1971.   874 p.

 2.   American Society of Civil  Engineers.   Proceedings  of the National
     Specialty Conference on Disinfection.  New York, American Society
     of Civil Engineers, 1970.   705 p.

 3.   Ballentine, R.  K., and F.  W.  Kittrell.   Observations of Fecal Coli-
     forms in Several Recent Stream Pollution Studies.   In:  Proceed-
     ings of the Symposium on Fecal Coliform Bacteria in Water and Waste-
     water.  Bureau  of Sanitary Engineering, California State Department
     of Public Health, 1968.  p.  80-126.

 4.   Brungs, W. A,  Effects of Residual  Chlorine on Aquatic Life: Liter-
     ature Review.  Journal Water Pollution Control Federation.  In Press.

 5.   Burns, R. W., and 0. J. Sproul.  Virucidal Effects of Chlorine in
     Wastewater.  Journal Water Pollution Control  Federation.  39:1834-
     1849, November  1967.

 6.   Chambers, C. W.  Chlorination for Control of Bacteria and Viruses
     in Treatment Plant Effluents.  Journal  Water Pollution Control Fed-
     eration.  43_:228-241, February 1971.

 7.   Chambers, C., and G. Berg.  Disinfection and Temperature Influences.
     In:  International Symposium on Water Pollution Control  in Cold Cli-
     mates, Murphy,  R. S., and D.  Nyquist (eds.).   Environmental  Protec-
     tion Agency, Fairbanks, Ak.   Publication Number 16100 EXH 11/71.
     November 1971.   p. 312-328.

 8.   Collins, H. F., R. E. Selleck, and  G. C. White. Problems in Obtain-
     ing Adequate Sewage Disinfection.  In:   Proceedings of the National
     Specialty Conference on Disinfection.  New York, American Society  of
     Civil Engineers, 1970.  p. 137-161.

 9.   Coutts, H. J.,  and C. Christiansen.   Extended Aeration in Cold Re-
     gions.  Environmental Protection Agency, Fairbanks, Ak.   In  Prepar-
     ation.  1973.

10.   Environmental Protection Agency, Region X.  Disinfection Criteria
     and Design Guidelines.  Environmental Protection Agency, Seattle,
     Wa.  December 1970.  6 p.

11.   Federal Water Pollution Control Administration. Current Practices
     in Water Microbiology.  Federal Water Pollution Control  Administra-
     tion, Cincinnati, Ohio.  February 1970.
                                 26

-------
12.  Geldreich, E. E.  Sanitary Significance of Fecal Coliforms in the
     Environment.   Federal  Water Pollution Control Administration, Cin-
     cinnati, Ohio.  Publication Number WP-20-3.  November 1966.  122 p.

13.  Geldreich, E. E.  Personal Communication.  Environmental Protection
     Agency, Cincinnati, Ohio.  1973.

14.  Gordon, R. C.  Winter Survival of Fecal Indicator Bacteria in a
     Subarctic Alaskan River.  Environmental Protection Agency, Fairbanks,
     Ak.  Publication Number EPA-R2-72-013.  August 1972.  41 p.

15.  Gordon, R. C., C. V. Davenport, and B. H. Reid.  Unpublished Data.
     Environmental Protection Agency, Fairbanks, Ak.  1973.

16.  Heathman, L.  S., B. S. Pierce, and P. Kabler.  Resistance of Var-
     ious Strains  of E.. typhi and Coli Aerogenes to Chlorine and Chlora-
     mine.  Public Health Reports.  51_: 1367-1387, October 1936.

17.  Hendricks, C. W., and S. M. Morrison.  Multiplication and Growth
     of Selected Enteric Bacteria in Clear Mountain Stream Water.  Water
     Research (Oxford).  1:567-576, August/September 1967.

18.  Heukelekian,  H., and S. D. Faust.  Compatibility of Wastewater Dis-
     infection by Chlorination.  Journal Water Pollution Control Federa-
     tion.  33_:932-942, September 1961.

19.  Kott, Y.  Chlorination Dynamics in Wastewater Effluents.  In:  Pro-
     ceedings of the National Specialty Conference on Disinfection.  New
     York, American Society of Civil Engineers, 1970.  p. 585-608.

20.  Lin, S.  Evaluation of Coliform Tests for Chlorinated Secondary Ef-
     fluents.  Journal Water Pollution Control Federation.  45:498-506,
     March 1973.

21.  Marias, A. F., E. M. Nupen, G. J. Stander, and J. R. H. Hoffman.
     A Comparison of the Inactivation of Escherichia coli I and Polio
     Virus in Polluted and Unpolluted Waters by Chlorination.  In:  In-
     ternational Conference on Water for Peace.  1967.  p. 670-689.

22.  Mechalas, B.  J., K. K. Hekimian, L. A. Schinazi, and R. H. Dudley.
     Water Quality Criteria Data Book, Vol. 4, An Investigation into Rec-
     reational Water Quality.  Environmental Protection Agency, Washing-
     ton, D. C.  Publication Number 18040 DAZ 04/72.  April 1972.  256 p.

23.  Monroe, D. W., and D. C. Phillips.  Chlorine Disinfection in Final
     Settling Basins.  In:  Proceedings of the National Specialty Con-
     ference on Disinfection.  New York, American Society of Civil Engi-
     neers, 1970.   p. 163-177.
                                  27

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24.  Rhines, C. E.  Fundamental  Principles of Sewage Chlorination.   In:
     Proceedings, 20th Industrial  Waste Conference.   Lafayette, Purdue
     University, 1965.  p.  673-678.

25.  Rudolfs, W., and H. W.  Gehm.   Sewage Chlorination Studies.  Bulle-
     tin 601.  New Jersey Agricultural  Experiment Station.   March 1936.
     72 p.

26.  Slanetz, L. W., C. H.  Bartley, T.  6. Metcalf, and R. Nesman.  Sur-
     vival of Enteric Bacteria and Viruses in Municipal Sewage Lagoons.
     In:  2nd International  Symposium for Waste Treatment Lagoons,
     McKinney, R. E. (ed.).   Meseraull  Printing, Inc., 1970.  p.  132-141

27.  Technicon Corp.  Ammonia in Water and Waste Water.  Industrial
     Method IND-18-69W, Technicon  AutoAnalyzer Methodology.   Technicon
     Corp., Tarrytown, N. Y., 1969.

28.  VanDonsel, D., R. C.  Gordon, and C. V.  Davenport.  Unpublished
     Data.  Environmental Protection Agency,  Fairbanks, Ak.   1973.

29.  White, G. C.  Handbook of Chlorination.   New York, Van  Nostrand
     Rheinhold Co., 1972.  744 p.
                                 28

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                          SECTION  VIII
                            GLOSSARY
Anaerobic - Condition  under which  no  free  oxygen  is  present.
Arctic - Area north  of the 10°C isotherm for  the  warmest month  and  the
-10°C isotherm for the coldest month  of the year.
Bactericidal - Killing or  having the  power to kill bacteria.
Batch Treatment - A  quantity of effluent disinfected in such  a  manner
that all portions receive  the same exposure to the disinfectant.
Chloramine - Any compound  containing  an ammonia molecule  in which one
or more chlorine atoms has replaced hydrogen  atoms in the  ammonia por-
tion of the compound.
Chlorine Demand - The  difference between the  amount  of chlorine added to
an effluent and the  amount measured as  total  chlorine after a specified
contact time.
Chlorine Residual -  The amount of  chlorine remaining in an effluent and
measurable as total  chlorine after a  specified contact time.
COD (Chemical Oxygen Demand) - Measure  of  the oxygen equivalent of  that
portion of the organic matter in an effluent  sample  that  is susceptible
to oxidation by a strong chemical  oxidant.
Composite Sample - Equal effluent  volumes  collected  at selected time in-
tervals and pooled throughout a predetermined time span to provide  the
final  sample for analysis.
Contact Chamber - A  chamber in which  the effluent and chlorine are  con-
tinuously mixed for  a  specified length  of  time to achieve  disinfection.
Contact Time (Period)  - The length of time effluent  and chlorine are
held in the contact  chamber.
Disinfectant - An agent which destroys  harmful bacteria.
Disinfection - The act or  process  of  destroying harmful bacteria.
Domestic Waste - Water carried waste  which is mostly from kitchen,  bath-
room,  lavatory, toilet and laundry.
Effluent - Liquid portion  of the waste  which  is discharged from a waste
treatment system or  contact chamber.
                                29

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Enteric Bacteria - Bacteria which inhabit the lower intestinal  tract of
humans or other warm-blooded animals.

Fecal Conform - A total  coliform bacteria subgroup which is specifi-
cally found in the feces of humans and other warm-blooded animals.

Germicidal - See disinfectant definition.

Grab Sample - Effluent sample taken for analysis at one point in time as
opposed to composite sample.

Parameter - A determination which defines the condition of the system
relative to that determination.

Plug Flow - Ideal continuous flow in which all of the effluent has  the
same residence time.

Primary Waste Treatment - The removal  of settleable organic and inor-
ganic solids by the process of sedimentation.

Pure Culture - A single strain or species of bacteria free from other
bacteria.

Receiving Water - Body of water into which the liquid portion of the
treated wastewater is discharged.

Secondary Waste Treatment - Treatment of sewage by biological methods
following primary treatment.

Short-Clrcuiting - The extent to which portions of the effluent enter-
ing the contact chamber at the same time receive less than theoretical
contact time.,

Solids - Residue remaining after various treatments of the effluent, i.e.
evaporation of water.

Subarctic - Areas where the mean temperature is higher than 10°C for less
than four months of the year and the mean temperature for the coldest
month is less than 0°C.

Survival (Bacterial) - Continuation of viability under adverse conditions,

Temperate Climate - Any area north of the Tropic of Cancer not pre-
viously defined as Arctic or Subarctic.

Theoretical Contact Time - The length of time that a volume of effluent
and chlorine are in the contact chamber if no short-circuiting occurs.
                                30

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Total Coliform - Heterogenous group of bacteria which meet certain mor-
phological and biochemical  criteria, and are found in feces of human and
other warm-blooded animals, as well as in other environmental  situations.

Unit Process - Distinct operations which are employed to produce an ef-
fluent of the desired quality.

Viability - The capacity of bacterial cells to grow and reproduce if ap-
propriate conditions are present.
                                 31

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                            Subject Field & Group
                                05D
                                           SELECTED WATER RESOURCES ABSTRACTS
                                                 INPUT TRANSACTION  FORM
     Organization
      U.S.  Environmental Protection Agency, NERC-Corvallis, Arctic  Environmental  Research
      Laboratory, College, Alaska  99701
     Title
      Batch Disinfection of Treated Wastewater with Chlorine at  Less  Than  1°C
|Q Authotfs)
Gordon, Ronald C. and
Davenport, Charlotte V.
16

21

Project Designation
Project 16100 GKG
Note
Environmental Protection
EPA-660/2-73-005
Technology Series
 22
     Citation
 23
Descriptors (Starred Fitst)

 *Disinfection, *Wastewater,  *8ioindicators,  *Coliforms, *Chlorine, *Winter,
 Alaska, Bacteria
 25
Identifiers (Starred First)

 *Total Coliforms, *Fecal  Coliforms,  *Batch  Disinfection,  *Low Temperature
 27  Absltact   A laboratory study was conducted, using  batch  treatment technique, to gain
some insight into chlorine disinfection of waste treatment  system effluents at less than 1°C.
One primary and three secondary effluents were examined  at  the  low temperature with parallel
control samples at 25°C.  Effluent disinfection was considered  minimally effective if, after
one hour contact time in the presence of 1 mg/1 total  chlorine  residual, there were no more
than 1000 total and 200 fecal coliforms/100 ml.
     The results indicated that both chlorine demand  and the  rate or extent of coliform reduc-
tion were decreased at the low temperature.  The disinfecting ability of chlorine varied sig-
nificantly at less than 1°C, among the four effluents  studied.   These effects did not in them-
selves negate the effectiveness of chlorine as a disinfectant at low temperature because the
previously stated minimums were easily met in effluent from all  sources.  However, higher
bacterial quality can be expected from batch treatment than is  found in most short-circuit
plagued operating contact chambers.
     The only real measure of satisfactory disinfection  is  the  number of enteric bacteria
being discharged into the receiving water.  An arbitrary chlorine residual  after a predeter-
mined contact time cannot be considered prima facie evidence  of satisfactory disinfection be-
cause of the variable disinfecting ability of chlorine.   The  chlorine residual:contact time
relationship must be established for each effluent at the lowest temperature encountered in
the system.
Abstractor
                              Institution
  f»R:
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