United States      Prevention, Pesticides     EPA712-C-98-298
          Environmental Protection    and Toxic Substances     January 1998
          Agency        (7101)
&EPA    Fate, Transport and
          Transformation Test
          Guidelines
          OPPTS 835.1110
          Activated Sludge
          Sorption Isotherm

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                           INTRODUCTION
     This guideline is one  of a  series  of test  guidelines that have been
developed by the Office of Prevention, Pesticides and Toxic Substances,
United States Environmental  Protection Agency for use  in the testing of
pesticides and toxic substances, and the  development of test data that must
be submitted to the Agency  for review under Federal regulations.

     The Office of Prevention, Pesticides and Toxic Substances (OPPTS)
has  developed this guideline through  a process of harmonization that
blended the testing  guidance  and requirements that  existed in the Office
of Pollution Prevention and  Toxics  (OPPT) and appeared in Title  40,
Chapter I,  Subchapter R of the Code of Federal Regulations  (CFR),  the
Office of Pesticide Programs (OPP) which appeared in publications of the
National Technical  Information Service (NTIS) and the guidelines pub-
lished by the Organization  for Economic Cooperation and Development
(OECD).

     The purpose of harmonizing these  guidelines  into a single set of
OPPTS  guidelines is to minimize variations among the testing procedures
that must be performed to meet the data  requirements of the U. S. Environ-
mental Protection Agency  under the Toxic  Substances  Control Act  (15
U.S.C. 2601) and the Federal Insecticide, Fungicide and Rodenticide Act
(7U.S.C. I36,etseq.).

     Final  Guideline Release: This guideline  is available from the U.S.
Government Printing Office, Washington, DC 20402 on The Federal Bul-
letin  Board.   By  modem  dial   202-512-1387,  telnet   and   ftp:
fedbbs.access.gpo.gov  (IP 162.140.64.19), or  call 202-512-0132 for disks
or paper copies.  This  guideline is also available electronically in ASCII
and PDF (portable document format) from EPA's World Wide Web  site
(http://www.epa.gov/epahome/research.htm) under the heading "Research-
ers and  Scientists/Test Methods and Guidelines/OPPTS  Harmonized Test
Guidelines."

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OPPTS 835.1110  Activated sludge sorption isotherm.
     (a) Scope—(1) Applicability. This guideline is intended to meet test-
ing  requirements  of  both  the Federal  Insecticide,  Fungicide,  and
Rodenticide Act (FIFRA) (7 U.S.C. 136, et seq.} and the Toxic Substances
Control Act (TSCA) (15 U.S.C. 2601).

     (2) Background.  The source material used in developing this har-
monized OPPTS test guideline are the articles referenced under paragraphs
(f)(l) through (f)(10) of this guideline.

     (b) Introduction.  The sorption  of chemical compounds to activated
sludge  biomass in biological wastewater treatment systems is an important
process that affects the  distribution of the compounds between solid, aque-
ous,  and vapor phases. If a chemical compound is sorbed to sludge bio-
mass, it may be removed from the system along with other solids by clari-
fication. If a compound is not sorbed, it will remain in the aqueous phase
where  it is subject to removal via biodegradation, chemical interactions,
and/or   volatilization.  A  nonsorbing, nonbiodegradable, noninteracting,
nonvolatile compound will pass through a biological treatment system un-
affected. Information on sorption potential is needed to assess the possibil-
ity for  the removal of chemical compounds in biological wastewater treat-
ment systems.  This test guideline describes a procedure for the determina-
tion  of the sorption potential of activated  sludge  solids for removal of
specific chemical compounds.

     (c) Discussion. (1) This guideline  describes a procedure for measur-
ing the extent to  which  a chemical  compound distributes itself between
activated sludge as the sorbent  and water  as the  solvent.  The equation
describing  that relationship is called a sorption isotherm.  The chemical
compound  solubilized  at a constant  concentration in  the solvent  is con-
tacted with a measured quantity of the sorbent for a time period sufficient
to attain sorption  equilibrium. Data  are obtained for various sorbent dos-
ages. The amount of compound remaining in solution is determined analyt-
ically and the  amount of compound sorbed is calculated for each  sorbent
dosage. A range of sorbent dosages is selected to achieve optimal spread
of the  data and to reflect biomass concentrations in an actual wastewater
treatment system.

     (2) There are several common  models for describing a sorption iso-
therm.  Historically,  each model has been based on either an empirical or
a theoretical equation. The three most common models are the Freundlich,
the  Langmuir, and the  Brunauer, Emmett,  and Teller  (BET).  The
Freundlich model is most widely  used to  describe  sorption in dilute
wastewater systems and is employed in this test guideline.

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     (i) The basic form of the Freundlich equation is as follows:

                           X/M = K • Ce1/n

where

     Co = initial concentration of the chemical compound in solution ex-
pressed in grams per liter

     Ce = final concentration of the chemical compound in solution ex-
pressed in grams per liter

     X = amount of test compound sorbed =

              [(Co x solution volume (L)) - (Ce x solution volume (L))]

     M = mass of sorbent expressed in grams

     K = Freundlich sorption coefficient

     1/n = exponent where n is a constant

     (ii) K and 1/n are the sorption constants and are unique for each iso-
therm.  In order to determine K and  1/n graphically, the Freundlich equa-
tion  is plotted on a log-log scale to yield a linear relationship.  X/M is
plotted along  the Y-axis and Ce along  the X-axis. The  data will fit the
logarithmic form of the Freundlich equation, as follows:

                    log X/M = log K + 1/n log Ce

     (iii) K is the X/M intercept when Ce = 1, and  1/n is  the slope of
the line when plotted.  The logarithmic plot of the  equation is termed the
isotherm plot.

     (3) In order to assess the  potential for relative sorptive removal of
the chemical compound, the values K and 1/n are  compared with the val-
ues for other  chemicals whose behavior  in activated sludge treatment sys-
tems is documented.

     (4) A sorption isotherm is dependent on the conditions  under which
it is  determined. Sorption can be greatly affected by changes in tempera-
ture,  pH, and test chemical concentration. Therefore, each of these param-
eters must be held constant during a sorption isotherm test.

     (d)  Sorption  isotherm test—(1)   General, (i)  The  papers  by
Aharonson and Kafkafi  (1975), Goring  and Hamaker  (1972),  Harvey
(1974), Lieberman (1986),  Murray (1975), Saltzman  (1972),  Weber
(1971), and Wu  (1975),  under paragraphs  (f)(l)  through  (f)(8) of this
guideline, served as the basis for this test guideline. For  additional infor-
mation on conducting sorption isotherm experiments, the reader is  referred
to OPPTS  835.1220, Sediment  and Soil Adsorption/Desorption Isotherm.
The  soil  and  colloid chemistry  literature and the analytical  chemistry lit-

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erature  substantiate the experimental conditions and procedures specified
in this guideline as accepted, standard procedures. These procedures have
been modified slightly to allow the use of activated sludge solids.

     (ii) Any procedure designed to determine the  sorption potential of
activated sludge for the test compound should use lyophilized, desiccated
sludge  solids as  the sorbent. Lyophilization freeze-dries the microorga-
nisms in sludge and allows the sorption potential to  be measured without
interference by biodegradation of the test compound. After lyophilization
many of the microorganisms are still  viable, but desiccation (drying in
an oven) should inactivate the remaining microorganisms. The flocculation
and  settling properties of lyophilized, desiccated sludge resemble those of
active sludge biomass upon rehydration. Photomicrographs of this material
reveal  the  presence of structurally intact  microorganisms (see the report
referenced in paragraph (f)(9) of this guideline). Furthermore, sludge sub-
jected to this treatment has been shown to have a sorption capacity similar
to that  of  viable sludge  solids (see paragraph (f)(10) of this  guideline).

     (iii) Lyophilization is an expensive process with a significant capital
investment. For the purpose of this test guideline, it is assumed that the
lyophilization process  will be contracted to a qualified vendor, for which
cost should be less significant (less than $500 for several grams of sludge).

     (2) Activated  sludge collection and preparation, (i)  The activated
sludge  to be used  as  a sorbent should be collected from  the most con-
centrated source  available within an activated sludge treatment process;
i.e.,  the return activated sludge (RAS)  line.  If the solids concentration of
the sludge  to be collected and the amount of sorbent required for the iso-
therm test are known, the  volume  of sludge that needs to be collected
can  be  determined. About 2 to 3x the volume calculated  should  be  col-
lected  as a safety measure.  The  shelf life of lyophilized sludge has not
been determined systematically,  but  based on empirical  observation  it
should  be  approximately 6 mo. As a  result, excess sludge  may  be  col-
lected,  prepared,  and held for future testing as outlined under paragraphs
(d)(2)(ii) through (d)(2)(v) of this guideline.

     (ii) The sludge solids to be lyophilized need to be separated from
the wastewater present in the sludge.  In the first step  collected sludge is
allowed to settle for 15 to 30 min before the supernatant is  decanted. Care
must be taken to remove only the supernatant and leave the solids.

     (iii) Further mechanical separation (e.g. centrifugation)  of the solids
from the water  is required  in order  to achieve a sludge suitable for
lyophilization. To accomplish this, settled  solids are placed  in a centrifuge
vessel  and centrifuged for 5 min. After centrifugation the supernatant is
decanted and the sludge solids remain in the centrifuge vessel.

     (iv) Washing of the  solids is recommended to  remove  any color or
matrix  materials. Washing can  be accomplished  by  filling the centrifuge

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vessel with laboratory-grade water and suspending the sludge solids in the
water,  followed by centrifugation and decantation  of the supernatant.
Sludge  solids should be washed and centrifuged 3 times. They can be
stored  at 4  °C until lyophilization can be undertaken by  a vendor,  but
sludge  should not be held  for  longer  than  24 hr  prior  to  starting
lyophilization because  changes in the sludge are likely to occur after this
even when the sludge is held at 4 °C.

     (v) After the lyophilization process  is complete, the  solids  will be
in the form  of a dry cake.  This cake  should be  broken into a  dry powder
by gently passing  it through a mesh screen. The  powder should  be  des-
iccated at 103 °C for 3  h or more prior to use as a sorbent.

     (3) Procedure—(i) Test  conditions. (A)  The isotherm  test should
be run at constant temperature and pH. Temperature control can be accom-
plished using a bath or  constant temperature room. pH should be controlled
using buffers. Preliminary  tests should be run to assure that there are no
interactions between test compound and buffer (such as complexation with
the buffer) that  could  affect sorption of  the test  compound.  This test is
accomplished by dosing the test compound into a mixture  of buffer and
clean water  at the  isotherm test's target concentration. The  dosed mixture
should be mixed for  a time period equal to the  anticipated  duration of
the isotherm  test.  Analytical  tests and  visual observation  of the  test
compound in the buffered  mixture  should be performed to  verify that no
chemical interactions or buffer-catalyzed degradation of the test compound
has occurred.

     (B) A sorption isotherm plot can be generated with two sorbent  dos-
ages. However, the accuracy of the  isotherm plot is increased if more  data
points are generated. Generally, six to eight points are needed to produce
an accurate plot.

     (C) Normal  quality  assurance/quality control  practices  (QA/QC)
should be employed when  conducting the isotherm test in order to assure
that valid data are generated. A test solution control and a sorbent control
should be included as  part of the isotherm test. The test solution control
consists of a sample of the test compound dosed at the target concentration
into buffered water with no sorbent present. This control is  used to verify
the initial concentration of test compound for  each  reaction vessel and
to indicate if any degradation or  interaction  of the test compound with
buffer occurs during the test period. The sorbent control consists of a sam-
ple of the sorbent in buffered water  without test  compound.  Analysis of
this sample  will indicate if any color or matrix  interferences were caused
by the sorbent.

     (ii) Equilibration. (A) Weigh  sludge solids into  six to eight individ-
ual isotherm reaction vessels to yield final concentrations of sludge solids
that will achieve varying degrees of  sorption of the test compound.  Test

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vessel volume is not specified in this test guideline because it is not critical
as long as the vessel is large enough to allow for good mixing. The vessels
should be of a constant and known volume.

     (B) Place a stirring bar or other mixing device in each reaction vessel.
Contents of test vessels must not be mixed by bubbling gas through them
because this could remove test compound by stripping.

     (C) If necessary, bring the  buffered test substance/solids mixtures in
the reaction  vessels up to the correct  volume  with measured  quantities
of laboratory-grade water and buffer.

     (D)  Stir mixtures in the reaction  vessels  for  0.5 h. Stirring should
be vigorous  enough to keep the sorbent  in suspension without being  so
vigorous as to break it up.

     (E) Measure the pH and temperature of the contents  of each reaction
vessel while stirring to verify the target conditions for the test.

     (F) Dose each  reaction vessel and the test  solution control while stir-
ring by pipeting in a calculated volume of test  compound. This will  bring
the solution in the vessel up to a final specified  volume and test compound
concentration. The dosing process should be completed quickly and with
precision, in order to achieve a uniform starting time for  all reaction ves-
sels.

     (G)  Stir the test  solutions until  sludge  and  test compound  have
reached equilibrium. How long  this takes may have to be determined by
trial and error.

     (iii) Centrifugation. (A) At the end of the stirring period, transfer
a representative sample of the mixture from each reaction vessel into a
clean centrifuge tube.  The volume of mixture  that needs to be collected
is determined by the analytical  method employed to detect and quantify
the test compound.  Contents of the reaction vessels should be stirred con-
tinuously while samples are being collected.

     (B)  Centrifuge the contents of each  tube  at 2,000 x g for 5 min in
order to provide adequate separation of solid and liquid phases for subse-
quent analysis.

     (4) Analysis for test  compound,  (i) After centrifugation,  remove a
volume  of the  supernatant sufficient for analysis from each tube, pass it
through a  0.45 (im pore-size  filter  previously  shown  not to  sorb test
compound, and place the filtrate in a clean sample bottle.

     (ii) Analyze the aqueous phase for the presence and amount of test
compound using an  appropriate analytical method. QA/QC procedures
should be employed for verification of analytical precision.

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     (iii) If the analysis for test compound must be delayed for any reason
after the samples have been filtered, store samples at 0 to  4 °C. Samples
should not be stored for more than 24 h before analysis.

     (5) Analysis of test  data, (i) After the isotherm test has been per-
formed and analysis for test compound is complete, tabulate the data gen-
erated  using the following format, representative of a Freundlich model:
                         Data Collection Format
M
Activated sludge







Ce
Test chemical
n/l
y/L





X
Test chemical sorbed
(Ce x sol'n volume in L)]
mass in grams





X/M

Grams test chemical
sorbed per gram sludge






     (ii) Plot X/M vs. Ce on log-log paper, and calculate the line of best
fit to yield the factors K and 1/n for the isotherm.

     (e) Reporting. Report the following information:

     (1) Test conditions: Temperature and pH at which the test was con-
ducted.

     (2) Detailed description of the analytical techniques used in the recov-
ery and quantitative analysis for test compound.

     (3) Amount of test compound dosed (Co x solution volume), and the
amount recovered in each reaction vessel (Ce x solution volume).

     (4) Volume of each reaction vessel and  total volume of the sorbent/
sorbate mixture.

     (5) QA/QC data such as duplicate analyses, background interferences,
spikes, matrix spikes, etc.

     (6) Graphical plots of log X/M  as a function of log Ce, and the values
of K and 1/n determined from the plots.

     (7) Sludge solids  information:  Sampling location, observations, cal-
culations for volume sampled, lyophilization  vendor, sample custody, de-
scription of the lyophilized sludge, desiccation time.

     (8) Any unusual observations made during the experiments.

                                  6

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     (f) References. The following references should be consulted for ad-
ditional background material on this test guideline.

     (1) Aharonson, N. and U. Kafkafi. Adsorption, mobility and persist-
ence  of thiabendazole and  methyl-2-benzimidazole carbamate in soils.
Journal of Agricultural and Food Chemistry 23:720-724 (1975).

     (2) Goring, C.A. and J.W. Hamaker, Eds. Organic chemicals  in the
soil environment, vol. I and II. Marcel Dekker, NY (1972).

     (3) Harvey, R.G. et al. Soil adsorption and volatility of dinitroaniline
herbicides. Weed Science 22:120-124 (1974).

     (4) Lieberman, R.J. Technical status report for adsorption of azo dyes
onto activated sludge solids. Report prepared under EPA contract no. 68-
03-3183. USEPA Risk Reduction Engineering Laboratory, Cincinnati, OH
(1986).

     (5) Murray, D.S. et al. Comparative  adsorption, desorption, and mo-
bility of dipropetryn and prometryn in soil. Journal of Agricultural and
Food Chemistry 23:578-581 (1973).

     (6) Saltzman, S.L. et al. Adsorption, desorption of parathion  as af-
fected by soil organic matter. Journal of Agricultural and Food Chemistry
20:1224-1226(1972).

     (7) Weber, J.B.  Model soil system, herbicide leaching, and sorption.
Weed Science 19:145-160 (1971).

     (8) Wu, C.H. et al. Napropamide adsorption, desorption, and move-
ment in soils. Weed Science 23:454-457 (1975).

     (9) USEPA. Prediction of the Fate of Organic Chemicals in Activated
Sludge Wastewater Treatment Processes. EPA/600/2-85-102 (1985).

     (10) Hopkins, B.T. et al. Activated  sludge adsorption methodology:
effect of biomass inactivation and incubation conditions. Presented at the
Society of Environmental  Chemistry and Toxicology (SETAC) 13th An-
nual Meeting, November  8-12,  Cincinnati, OH.  Abstract no. WA4A18
(1992).

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