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                RESEARCH REPORTING SERIES

Research reports of the Office of Research and Development. U S Environmental
Protection Agency have been grouped into nine series These nine broad cate-
gories were established to facilitate fur ner development and application of en-
vironmental technology  Elimination of traditional grouping  was  consciously
planned to foster technology transfer and a maximum interface in related fields
The nine series are

      1   Environmental Health Effects Research
      2   Environmental Protection Technology
      3   Ecological Research
      4   Environmental Monitoring
      5   Socioeconomic Environmental Studies
      6   Scientific and Technical Assessment Reports (STAR)
      7   Irteragency Energy-Environment Research and Development
      8   "Special  Reports
      9   Miscellaneous Reports

This  report has been assigned to the ENVIRONMENTAL MONITORING series
This  series describes research conducted to develop new or improved methods
and  instrumentation for the identification and quantification of  environmental
pollutants at the lowest conceivably significant concentrations It also includes
studies to determine the ambient concentrations of pollutants in the environment
and/or the variance of pollutants as a function of time or meteorological factors.
This document is available to the public through the National Technical Informa-
tion Service, Springfield, Virginia  22161

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COMPARATIVE TESTING OF  EPA METHODS 5 AND 17
       AT NONMETALLIC MINERAL  PLANTS
                       by
  William J. Mitchell  and  M.  Rodney Midgett
 Environmental Monitoring  Systems  Laboratory
     U.S. Environmental  Protection Agency
 Research Triangle Park, North  Carolina  27711

                       and

                  C. Bruffey
             PEDCo Environmental
            Cincinnati,  OH 45246
 ENVIRONMENTAL MONITORING  SYSTEMS LABORATORY
      OFFICE OF RESEARCH AND  DEVELOPMENT
     U.S. ENVIRONMENTAL PROTECTION AGENCY
      RESEARCH TRIANGLE PARK,  NC  27711
      U.S. n-.v>~r:^:-.t;-; ? K'sr.llcn A^ncy
      > \!  j i;-: ;-, ' ^
      230 Soi-;:o H:-:
      O l-i- i *-* '~* o O  ' ! • PI
      LSiiCc.^o, -ini.»..

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                                  DISCLAIMER

     This report has been reviewed by the Environmental Monitoring Systems
Laboratory, U.S. Environmental Protection Agency, and approved for publication.
Mention of trade names or commercial products does not constitute endorsement
                                                                  ^
or recommendation for use.
                   U.S. environment MOU

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                                   FOREWORD

     Measurement and monitoring research efforts are designed to anticipate
potential environmental problems, to support regulatory actions by developing
an in-depth understanding of the nature and processes that impact health and
the ecology, to provide innovative means of monitoring compliance with regula-
tions and to evaluate the means of monitoring compliance with regulations and
to evaluate the effectiveness of health and environmental protection efforts
through the monitoring of long-term trends.  The Environmental Monitoring
Systems Laboratory, Research Triangle Park, North Carolina has responsibility
for:  assessment of environmental monitoring technology and systems; implemen-
tation of agency-wide quality assurance programs for air pollution measurement
systems; and supplying technical support to other groups in the Agency including
the Office of Air, Noise and Radiation, the Office of Toxic Substances and the
Office of Enforcement.

     This study was conducted to determine if in-stack filters are suitable
substitutes for EPA Reference Method 5 when they are used to sample dry, ambient
temperature processes.
                                       m

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                                   ABSTRACT

     Comparative tests between EPA Reference Method 5 and commercially-
available in-stack filters (EPA Reference Method 17) showed that in-stack
filters can be acceptable substitutes for the Reference Method at nonmetallic
mineral plants.  These comparative tests were conducted in the exhaust stacks
from a clay calciner, a feldspar grinding mill and a limestone crusher.
Particulate concentrations encountered ranged from 30 to more than 300 mg/m  .
Laboratory studies using feldspar dust gave results identical to the field
study results.  Insignificant amounts of material were found downstream of the
in-stack filters.

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                                   CONTENTS

Foreword	iii
Abstract	iv
Figures	vi
Tables	vi

     1.   Introduction 	   1
     2.   Conclusions  	   3
     3.   Experimental 	   5
               Laboratory studies  	   5
               Field Studies	   5
     4.   Results	   9
               First field test - feldspar plant ball mill stack 	  10
               Second field test - clay plant calciner stack 	  12
               Third field test - limestone plant secondary
                    crusher stack 	   15
               Fourth field test - feldspar plant ball mill stack ....   15

References	   19
Appendices

     A.   A field evaluation of EPA Method 17 in a kraft pulp mill   ...   20
     B.   A comparative study of Method 17 with Method 5
               at a grain elevator	   45

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                                   FIGURES

Number                                                                   Page
  1   Four-train sampling arrangement showing train position 	   6
                                   TABLES
  1   Results of Laboratory Filter Evaluation  	  11
  2   Results at Feldspar Plant  	  13
  3   Results at Clay Calciner	14
  4   Results at Limestone Crushing Plant  	  16
  5   Results at Feldspar Plants 	  18
                                       vi

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                                   SECTION 1
                                 INTRODUCTION

     Method 5 was the first EPA Reference Method for measuring particulate
emissions from stacks (1).  In Method 5, the sampled gas passes through a heat-
able glass-lined probe and then through a heatable glass-fiber filter located
outside the stack.  It then passes into a series of Greenburg-Smith impingers
where moisture and other condensible material is collected.  These impingers
protect the pump and volume meter and also allow the percent moisture in the
sampled stack gas to be determined.

     Subsequently, EPA promulgated a second Reference Method for particulate
measurement, EPA Reference Method 17 (2) in which the out-of-stack (Method 5)
filter is replaced with an in-stack filter located immediately after the
sampling nozzle.  This method serves as an alternate method for Method 5 at
                                 3
kraft pulp mills, provided 9 mg/m  is added to the measured particulate concen-
tration to correct for condensible material that can pass through the in-stack
filter but would be stopped by an out-of-stack Method 5 filter.  This correction
factor was derived from comparative testing conducted at kraft pulp mills by
the National Council for Air and Stream Improvement (NCASI) and was confirmed
in a subsequent EPA study (Appendix A).

     Testers prefer Method 17 to Method 5 primarily because it is more conven-
ient to use.  For example, a filter heater box is not required.  Also, sample
recovery istsimpler and possibly more quantitative because the particulate
catch is concentrated in the nozzle and filter and not dispersed throughout a
glass sampling probe.  These features make the in-stack filter attractive for
sampling the dry, ambient temperature, baghouse-equipped stacks associated
with plants that process dry, water-insoluble, feed materials such as grains
and minerals.  At these sources, if penetration of the in-stack filter is

                                       1

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insignificant, a sampling train composed only of a nozzle, an in-stack filter
and a control  console is adequate.

     Reported below are the results of comparative tests between in-stack and
out-of-stack filters conducted in the laboratory and at three nonmetallic
mineral plants that processed feldspar, clay and limestone.  The particulate
concentration encountered at these plants ranged from 35 to 360 mg/m  and
represented the range in mineral hardness that would be encountered in sampling
the different kinds of plants that comprise the nonmetallic mineral processing
industry.  Appendix A and Appendix B describe similar studies done at a kraft
                                                                 ^
pulp mill and a grain elevator, respectively.

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                                   SECTION 2
                                  CONCLUSIONS

     If in-stack filters are properly seated and filter integrity is maintained
during sampling, very little material gets past them when they are used to
sample the dry, ambient-temperature stacks encountered in the grain and mineral
processing industries..   This conclusion is drawn from the results of this study
and a similar study conducted at a grain elevator (Appendix B).  However,
significant amounts of material can get past the in-stack filters when they are
used to sample elevated temperature stacks that can contain condensible materials
such as those encountered in kraft pulp mills (Appendix A).

     On the average at the nonmetallic mineral plants the amount of material
                                                             3
getting past the in-stack filters evaluated was only 1.3 mg/m .  This value is
                                     3
statistically similar to the 3.7 mg/m  obtained at grain elevators but statis-
                                 3
tically different from the 9 mg/m  obtained at a kraft pulp mill.

     In the first and third field tests, the in-stack filter train collected
significantly more material than the Method 5 train.  There is no clear explana-
tion for this.  Possibly it resulted from stratification of the particulate in
the stack.  Alternately, it could have been caused by non-quantitative recovery
of material from the Method 5 probe, but this seems unlikely for two reasons.
First, the probes were visually inspected after cleaning to make sure that all
particulate was recovered.  Second, the within-train precision of the Method 5
train was not significantly different from that of the in-stack filter trains.
If sample recovery was a problem we would expect both the within train variation
to be larger for the Method 5 train and some of the Method 5 trains to yield
results significantly larger than the corresponding in-stack filter trains.
Neither event occurred.

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     All in-stack filter holders evaluated to date could be improved.  The BGI
19 x 90 mm thimble holder clamp screw is easily lost and it is extremely diffi-
cult to align the clamp screw with the threaded hole.  Threading both holes
rather than just one, would prevent dropping the screw during filter assembly.
Alternately, a piece of copper wire can be slipped through the two holes and
then wire twisted to pull the clamp together.  (Private communication from
Richard H. Russell, Standard Oil of Ohio, Cleveland, OH.)  The larger thimble
holder (30 x 100 mm) is easier to assemble, but the variability in filter
diameter still makes it difficult to get a leak-free seal.

     The glass-fiber filter tends to stick to the gasket and filter support
screen of the Gelman 47 mm diameter filter holder and this makes it difficult
to completely recover the filter after use.  (The Misco Corporation 47 mm
diameter filter also suffers from these problems ~ Appendix A.)

     The NuTech Corporation 51 x 178 mm rectangular filter is cumbersome to
assemble and much heavier than the other filter holders.  It is difficult to
make leak-free and also difficult to remove the filter after use.  The portion
of the filter in contact with the viton gasket adhers strongly to the gasket
and the portion of the filter supported by the sintered metal support plate
can break free when the filter assembly is opened.  The balance of the filter
must then be scraped from the gasket.

     To prevent leaks when using these in-stack filters at stack temperatures
above 175°C, it is necessary to bring the filters to stack temperature and then
tighten them further before use.

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                                   SECTION 3
                                  EXPERIMENTAL

LABORATORY STUDIES

     Samples of feldspar dust that had been sieved through a 200-mesh screen,
were placed in the sampling nozzle and pulled into the train at an air sampling
rate of 22 1pm for 20 to 30 minutes.   The in-stack filters evaluated were
followed by a glass-lined probe, an 82-mm diameter glass-fiber filter contained
in a Method 5 filter holder and two Greenburg-Smith impingers.  The out-of-
stack filters evaluated were preceded by a glass-lined probe and followed by
two Greenburg-Smith impingers.  All impingers contained 100 ml of distilled,
deionized water.  All out-of-stack filters were supported on 200 mesh screens.

     At the conclusion of sampling each portion of the sampling train was
cleaned separately to determine the distribution of the material in the train.
Acetone was used as the wash reagent.

     The two commercially-available in-stack glass-fiber filters evaluated
extensively were the BGI TA-3, 19 x 90 mm thimble filter and the Gelman 47 mm
diameter filter.  The 82 mm diameter, glass fiber filter was the only out-of-
stack filter evaluated.  Less extensive studies were done using the NuTech
Corporation rectangular 51 x 178 mm glass-fiber filter and the Gelman 47 mm
diameter, 0.8 and 5.0 micron membrane filter.

FIELD STUDIES

     The field tests employed single-point, isokinetic sampling with the four-
train sampling assembly shown in Figure 1.  Prior to field use this assembly
was studied in a wind tunnel to confirm that the pitot tube measurement was not
affected by the four sampling nozzles.

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           8cm
                                 15cm
                                      NOZ2LE
                     4cm
                                T
                              0.5 cm
                                              ^ NOZZLE
                                            STACK GAS FLOW
                                  -(j)—   TRA.N2
                    - 2 em
              4cm
2cm
  1
1.4cm

  1
 'TYPE PITOT TUBE
                        TRAIN 4
                                            TRAIN 3
                          4cm
Figure 1.   Four-train sampling arrangement showing train  position.

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     Because this sampling assembly allows four trains to simultaneously sample
at essentially the same point in the stack, it reduces the affect of spatial
and temporal variations in the velocity and particulate profiles on the sampling
results (3).  It also permits a statistically significant number of samples to
be taken in a short amount of time.  Further, if two of the four trains are
identical, the within-train precision can be determined at the same time the
relative performance of two different trains is being compared.

     Stack testing was conducted using BGI and Gelman in-stack filters at a
feldspar grinding mill, a clay calciner and a limestone crusher.  All stacks
were at ambient temperature, contained less than two percent moisture, and
controlled their emissions using a baghouse.  Respective particulate concen-
                                       33                 3
trations encountered were:  70-160 mg/m , 35-60 mg/m , and 30-360 mg/m .

     At a minimum, each in-stack filter was backed-up by a glass-lined probe
and an out-of-stack, 82 mm diameter glass-fiber filter.  In one test this
back-up filter was followed by two Greenburg-Smith impingers containing 100 ml
of distilled, deionized water.  At the feldspar plant the out-of-stack filter
train, which served as the control, contained two Greenburg-Smith impingers in
back of the filter.  At the other two plants there was no back-up system behind
the out-of-stack filter.

     Prior to use, each probe, filter holder and back-up system was subjected
to a sample recovery wash with acetone.  Less than 1 mg was found in these pre-
test washes.

     To reduce both the time spent on sample recovery and the effect of sample
recovery errors on the results, material in a back-up system was not recovered
until at least two and sometimes three sampling runs had been completed (acetone
was the only reagent used for sample recovery of all sample-exposed surfaces).
After recovery, the weight of material found in the back-up system was distri-
buted equally among the two or three samples it represented.  Of course, waiting
several runs before recovering the back-up system meant that a broken or mis-
aligned primary filter could invalidate the back-up system results for several
samples.  Also, the back-up system results could be adversely affected if the

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penetration of the filter was a function of the participate catch and there
was a sudden, dramatic change in the stack concentration between runs.

     To further reduce total field time, to utilize field personnel more
effectively, to minimize the effect of daily variations in the particulate
concentration on sampling results, and to simplify sample identification,
three, four-train assemblies were used at each plant.  While one assembly was
sampling, the second was being recovered and the third was being reassembled
for use in the next run.  All trains were leak-checked through the nozzle
                                                       3
before and after use and no leaks in excess of 0.0008 m /min were found.
                                       8

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                                   SECTION 4
                                    RESULTS
LABORATORY TESTS
     The initial experiments determined the overall suitability of various types
of commercially-available in-stack filters for field use and familiarized field
personnel with the techniques required to quantitatively recover mineral dust
from these filter holders.  The following in-stack filter holders were evaluated
in these initial experiments.  Gelman holder with 47 mm diameter, 5.0 and 0.8
micron membrane and glass-fiber filters; BGI Corporation TA-3 with 19 x 90 mm
glass-fiber thimble; and NuTech Corporation rectangular, flat filter holder with
51 x 178 mm glass-fiber filter.

     In the preliminary tests recovery efficiencies on 20 to 100 mg quantities
of feldspar dust ranged from 80 to 98% with no correlation between recovery
efficiency and original weight of dust.  This "lost" material was not found in
the back-up system, which indicated that significant quantities of dust were not
penetrating the filters.  Careful study of these results indicated that extreme
care was necessary in assembling and disassembling the filter holders to ensure
that some of the filter was not lost.  The NuTech Corporation filter and the
Gelman glass-fiber filter tended to stick to the gasket and filter support screen,
respectively.  The BGI thimble clamp tended to cut the thimble and at times the
thimble lip would tear slightly when the thimble was slipped over the shaft.
              *
     With experience the filter handling problems of the BGI and Gelman holders
became manageable, but those of the NuTech did not, so the latter was not evalu-
ated further in field or laboratory tests.

     Extensive laboratory experiments on in-stack filters were done only with
the BGI and Gelman filter holders equipped with glass-fiber filters.  The

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out-of-stack filter (Method 5) was also evaluated in these experiments to serve
as a control.

     Results for all three filters were the same, i.e., consistent filter pene-
tration was not found and recovery efficiency did not correlate with sample
weight (Table 1).  Generally, the amount of material recovered in the front half
differed no more than ± 3 mg from the amount of material  originally placed in
the train.  Where penetration did occur, it could reflect only filter slippage
and not penetration.

FIRST FIELD TEST - FELDSPAR PLANT BALL MILL STACK

     This plant had been tested four years earlier by an EPA contractor and
                                                   o
found to have a low particulate loading (10-15 mg/m ) and a fairly uniform
distribution of particulate across the 45 cm stack.   Based on this data, the
comparative testing of the in-stack and Method 5 filters was done utilizing
three separate sampling assemblies that contained two identical trains and
two non-identical trains.  Assembly A consisted of two Method 5 trains, one
Gelman train and one BGI train; Assembly B consisted of two BGI trains, one
Gelman train and one Method 5 train; and Assembly C consisted of two Gelman
trains, one BGI train and one Method 5 train.  The BGI trains consisted of a
nozzle, a TA-3 filter holder with 19 x 90 mm glass-fiber filters and were
followed by a 50 cm glass-lined probe and an 82 mm diameter Method 5 glass-
fiber filter.   The Gelman trains consisted of a nozzle, a Gelman filter
holder with 5.0 micron, 47 mm diameter membrane filters, and a back-up system
identical to that of the BGI train.  The Method 5 train which consisted of a
nozzle, 55-65 cm glass-lined probe and a filter holder with a 82-mm diameter
glass-fiber filter did not have a back-up system.

     Unfortunately, the particulate concentration encountered was apparently
stratified and about five times larger than anticipated because several of
the baghouse bags were broken — a fact not detected until after the test
series was completed.  Because of the heavy particulate loading, some of the
membrane filters cracked (one actually ruptured) during use.  Poor quality
control during manufacture caused several of the BGI thimbles to fit loosely

                                     10

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               TABLE 1.   RESULTS OF LABORATORY  FILTER EVALUATION

Sample wt.
(nig)
Total %
recovered
% in front
section
% in back-up
section
Method 5 Filter Followed by Two Impingers
26
28
32
32
95
100
106
109
111
106
108
119
103
92
99
98
92
100
100
100
99.6
96
100
100
8.0
0.0
0.0
0.0
0.4
4.0
0.0
0.0
                               AVERAGE:
104
Gelman 47 mm Filter Followed by Method 5 Filter and One  Impinger
                                22
                                28
                                36
                                98
                               112

                               AVERAGE:
103
 83
106
 99
 97

 98
100
100
100
100
100
0.0
0.0
0.0
0.0
0.0
BGI 19 x 90 Thimble Followed by Method 5 Filter and  One  Impinger

                                25          142         100            0.0
                                32          102         100            0.0
                               104          100         100            0.0
                               110          103          99            1.0
                               AVERAGE:
112
                                       11

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over the thimble holder shaft and this made it difficult to attach the thimble
securely to the shaft with the rubber bands being used.   (The standard clamp
supplied with the BGI thimble would not slide over these thimbles easily and
it was difficult to align the clamp screw with the threaded hole under field
conditions, so they were not used.) These facts essentially invalidated the
use of the back-half catch, although the general conclusion was drawn that
where filter integrity was apparently maintained, little material was found
behind the in-stack filter.  Surprisingly, the Method 5 results were generally
lower than the Method 17 results (Table 2).  Possibly this resulted from strati-
fication in the particulate concentration caused by the broken bags.  Poor
sample recovery from the Method 5 probe may also be the cause (the, gritty
material is difficult to remove by washing) but this seems unlikely because the
probes were visually inspected after sample recovery to make certain they were
clean.

SECOND FIELD TEST - CLAY PLANT CALCINER STACK

     The second test, conducted in a 100-cm diameter stack, used sampling
trains identical to those used in the first test, except that Gelman glass-
fiber filters were substituted for the membrane filters and wire was used to
hold the BGI thimbles in place.  The statistical design was modified to better
tolerate particulate stratification and sudden shifts in the particulate con-
centration, but neither event occurred and only one sample was of questionable
validity (Table 3).

     Penetration of the in-stack filters was fairly low and consistent.  For ex-
                                                                       3
ample the average penetration of the Gelman trains was 0.7 and 3.2 mg/m  for an
                           o
overall average of 2.0 mg/m  and average penetration of the BGI trains was 1.3,
                      3                                   3
4.0, 2.2, and 3.0 mg/m  for an overall average of 2.6 mg/m .  Interestingly,
           o                                                             O
if 2.0 mg/m  is added to the average Gelman filter train catch (43.0 mg/m ),
the total (45.0 mg/m ) compares extremely well with the average catch for the
                                       3
corresponding Method 5 train (47.0 mg/m ).  Similarly, the average total catch
                                                   3
for the BGI train and its back-up system (47.4 mg/m ) compares well with the
                                       3
corresponding Method 5 train (47.9 mg/m ).
                                       12

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THIRD FIELD TEST - LIMESTONE PLANT SECONDARY CRUSHER STACK

     Testing was done in a 66 x 81 cm rectangular duct using sampling trains
and sampling assemblies identical to those used in the second field test.
Based on a previous test at the plant, a particulate concentration of about
       3
10 mg/m  was expected, but when sampling was initiated the loading was three
times higher.  The plant broke down repeatedly during the test and after the
third run was completed the opacity of the emissions increased dramatically
indicating baghouse malfunction.  Testing scheduled for that day was completed
and no further testing was attempted.  Test results are presented in Table 4.

     As in the first field test (feldspar plant), the in-stack filter trains
collected more particulate than the Method 5 trains.  However, as in the second
field test, the average penetration for the in-stack filter trains was small
                              3             3
and consistent, i.e., 1.6 mg/m  and 1.9 mg/m  for the Gelman and BGI trains,
respectively.

FOURTH FIELD TEST - FELDSPAR PLANT BALL MILL STACK

     Testing was repeated at this plant nine months after the first field test.
Just before testing was initiated the baghouse was inspected to be certain that
all bags were properly positioned and were not leaking.  Each train contained
a back-up system identical to that used in the laboratory study, i.e., all
Method 5 filters were supported on screens and were followed by two Greenburg-
Smith impingers that each contained 100 ml of distilled, deionized water.  BGI
30 x 100 mm thimbles were substituted for the 19 x 90 mm thimbles used in the
other tests.  Their larger size made it possible to securely attach the thimble
to the holder shaft using the screw clamp supplied.

     The test was designed such that day to day variations in the particulate
concentration and stratification could be statistically removed from the test
results.  During testing the baghouse again malfunctioned, but this time the
test design tolerated it.  Back-up samples were recovered after the second run.
                                      15

-------


















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-------
     Analogous to the laboratory tests with feldspar dust, no significant
penetration of the in-stack filters was found.  Penetration of the Method 5
filter trains was found in three instances but this likely resulted from the
filter slipping out of position and not an actual penetration.  (Filter slippage
occurred because the screen filter supports used did not contain a deep enough
recessed area to accommodate the glass fiber filter.  These screens were made by
hand and were used in place of the standard fritted-glass filter supports used
in the other field tests to ensure that any material penetrating the Method 5
filter would not be trapped in the filter support itself.)

     Statistical analysis of the results showed that the concentration level
increased over the four days of testing, but no correlation between concentra-
tion and between-train (Gelman versus Method 5, BGI versus Method 5) precision
or concentration and within-train (Method 5 versus Method 5, BGI versus BGI,
Gelman versus Gelman) precision was found.  Further, no significant difference
was detected between Method 5 and Gelman or Method 5 and BGI, which indicates
that the two in-stack filters would give similar results if compared directly
(Table 5).  (Some small amount of stratification was observed, based on a
position by position comparison of the sampling results for the assembly that
contained four Method 5 trains, and this difference in positions was handled
in the statistical analysis.)
                                       17

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                       TABLE  5.   RESULTS  AT  FELDSPAR  PLANTS

Sampling
assembly
A



B



C



A1



B1



C1



A"



Train
position
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
4
Type
train
Method 5
BGI
BGI
Method 5
Method 5
Method 5
Method 5
Method 5
Method 5
Gel man
Gel man
Method 5
Method 5
Method 5
Method 5
Method 5
Method 5
BGI
BGI
Method 5
Method 5
Gel man
Method 5
Gel man
Method 5
Method 5
Method 5
Method 5
Parti cul ate cone.
measured (mg/m )
First run
72.2
88.6
94.2.
74. 4b
87.3
80.5
85.7
81.7
83.7
74.4
83.5
84.3
85. 9C
87.3
92.8
82.6
120
118
123
113
131
128
122
114
127
122
142
106
Second run
78.5
89.0
85.8
74.1
90.5
72.9
77.9
72.3
83.9
95.6
79.2
95.2
131
129
120
124
.126
124
105
113
175r
170C
139
153
135C
150
136
131
Mg in
back-up
per run
0.2
0.0
0.4
2.5
0.3
0.3
0.0
0.0
0.0
0.0
1.2
0.0
6.8
0.0
0.2
0.0
0.0
0.0
0.0
0.0
0.0
7.8
0.0
0.0
8.0
0.0
0.0
0.4
Average
back-upocatch
in mg/m /train
0.1
0.0
0.1
0.8
0.1
0.1
4 0.0
0.0
0.0
0.0
0.8
0.0
6.6
0.0
0.2
0.0
0.0
0.0
0.0
0.0
0.0
4.6
0.0
0.0
7.2
0.0
0.0
0.3
aSee Figure 1 for explanation of train position.
 Filter cracked during testing.
cFilter definitely slipped out of position during testing.

                                       18

-------
                                  REFERENCES

1.   U.S. Environmental Protection Agency.   Standards of Performance for New
     Stationary Sources.  Federal Register 36(247):24876-24890, December 23,
     1971.

2.   U.S. Environmental Protection Agency.   Standards of Performance for New
     Stationary Sources.  Federal Register, 42_( 37): 7584-7596, February 23, 1978.

3.   Mitchell, W. J., and M. R. Midgett.   A Means to Evaluate the Performance of
     Stationary Source Test Methods.   Environ.  Sci.  and Technol., Kh85-88, 1976.
                                       19

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                                 APPENDIX A

          A FIELD EVALUATION OF EPA METHOD 17  IN A  KRAFT PULP MILLa
                              I. INTRODUCTION

    The proposed standard for particulate matter emissions from Kraft pulp mill recovery
furnaces is 100 milligrams/dry standard cubic meter (mg/dscm) as set forth in the Federal
Register, Part II, Volume 41, Number 187, Friday,  September 24,  1976. The specified test
method for particulate determination is EPA Method 5. EPA Method 17 may be used as an
alternative method provided that a constant value of 9 mg/dscm is added to the Method 17
results and provided that the stack temperature is no greater than 205 °C. Water is used as a
cleanup solvent instead of acetone in the sample recovery in both methods.

    A field evaluation of EPA Method 17 at a Kraft pulp mill recovery furnace to include a
comparison with EPA Method 5 was therefore considered appropriate. This report presents
the results obtained and conclusions drawn from statistical analysis of the test data.
 Report prepared by Dr. H.  F. Hamil  and  Mr.  R.  E.  Thomas of Southwest Research
 Institute, San Antonio, TX, under EPA Contract 68-02-2489 and under the direc-
 tion of Mr. Michael C. Osborne,  EPA,  Research  Triangle Park, NC.

                                         20

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                              II. TEST DESCRIPTION

     The field evaluation of Method 17 specified in the work assignment has a two-fold pur-
pose: a field comparison of EPA Methods 17 and 5 by simultaneous sampling of the same
source, and an evaluation of various commercially available Method 17 filter holders by
simultaneous sampling of the same source.

     The test plan was provided by the work assignment  monitor and is shown in Figure 1.
During the first week, six runs were to be accomplished with two Method 5 and two Method
17 trains sampling simultaneously on each run. The Method 17 filters were to be backed up
by a heated Method 5 filter and glass-lined  probe to collect any paniculate which might
pass through the in-stack filter. Nutech filter holders were to be used in the first week's test
as representative Method 17 filter assemblies.  The relative position of the trains in the
sampling assembly were to be rotated after each run to avoid any bias due to sample nozzle
location.

     During the second week, eight runs were to be accomplished with one Method 5 train
and  three Method 17 trains sampling simultaneously on each run. The  Method 17 trains

1.    All test runs will be conducted with the configuration shown in Figure 2.

2.    Runs 1-6 Characteristics

     a.   Trains 1 and 3 will be standard Method 5 trains with heated filter boxes.

     b.   Trains 2 and 4 will be Method 17 trains  with heated backup Method 5 filters.

     c.   The relative position of  trains 1,2,3,  and 4  within the sampling arrangement will be rotated
         clockwise after each run.

     d.   An additional front-half cleanup will be required following the regular cleanup of runs 1,2, and 6.

     e.   Saving and determining the back-half catch will also be required in runs 1, 2, and 6.

     f.   The Nutech filter  holders should be used to represent Method 17 unless it is observed during pilot
         calibration that these holders cause significant turbulence that changes the pilot tube coefficient.
         If such a disturbance is observed, the Misco filler holders should be used in place of the Nutech
         filter holders.

     g.   All filter holders and train components should be thoroughly leak checked before sending them
         into the field.
(continued)             _.    „  _     .
                      Figure 1.  Test plan for Kraft mill recovery furnace.

                                          21

-------
3.   Runs 7-14 Characteristics

    a.    Trains 1,2,3, and 4 should use Misco, BGI, Nutech and Method 5 filter holders, respectively.

    b.    Trains 1,2, and 3 should be operated with filters in-stack as characterized by Method 17.

    c.    Train 4 should be operated as a standard Method 5 train with the filter holders out-of-stack in a
         heated compartment.

    d.    The relative position of trains 1,2,3, and 4 within the sampling arrangement will be rotated
         clockwise after each run.

    e.    It will not be necessary to do any additional front-half cleanups or to save the ba.ck-half catch.


                                Figure 1. (continued)
were to employ one each Nutech, Misco, and BGI filter holder. No backup Method 5 filters
were to be used in the Method 17 trains during the second week of testing. The relative posi-
tion of the trains within the sampling bundle were to be rotated after each run as in the first
week of testing.

     The use of a four-train sampling system was required to accomplish the test plan. To
assure that no bias due to spatial variation in particulate loading was introduced into the
sampling, the probe bundle was assembled so the sample nozzles were situated at the cor-
ners of a square with sides of 6 cm. A single pilot tube was centrally located. The pilot tube-
sample nozzle spacings are shown schematically in Figure 2. A view of the assembled probe
bundle with a Method 5 probe and the three Method 17 probes is shown in Figure 3.

     A common thermostatically-controlled oven was fabricated to house the four Method
5 filter holders required in the first week of tesling. A view of Ihe filler holder arrangements
is shown in Figure 4. The filler holder oven was mounled on a sland in such a manner lhai
four slandard impinger irains wilh ice  balhs could be accommodaled  in  an assembly
mounted on a common base.

     This  configuration allowed Ihe  enlire sampling  syslem lo be assembled and  leak
checked. The enlire unil could ihen be moved to place Ihe sample nozzles al Ihe desired
sample poinl in Ihe slack. Single poinl  sampling wilhoul iraversing  was employed
Ihroughoul Ihe tesl. The assembled sampling syslem is shown in Figure 5.

     To avoid differences in filler media, all Melhod 5, Nulech Melhod 17, and Misco
Melhod 17 fillers were cut from Gelman lype A-E glass fiber high-volume fillers. BGI glass
fiber filters were used with the BGI filter holders.

     The sile selecied for Ihe field evaluation was Ihe recovery furnace of a Krafl pulp mill
owned and  operaied by  Ihe Arkansas  Kraft  Corporalion, Morrillon,  Arkansas.  The


                                        22

-------
                   -6
                   tea
y- ™"" 
-------
FigureS. Four probe sample bundle.
    :igure 4.  Filter holder oven

-------
   Ready for leak check.
     During sampling.




Figure 5.  Sampling system.




            25

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          East Stack
           -O-
                                   •15'
                                                        West Stack
*-68"ID-
                                                          -38'-^-
              ,,4" Port

              JL
                                                                     20"
                                                                     17"
                                                                     t
                                                                     25"
                                                                    -18'
                                                                        Roof on ESP
                                                                      ' r^l/
              Figure 6. Arkansas Kraft Corporation precipitator exits—front view.
of week one, problems were encountered with leaks in the Method 5 filter holders on trains
C and D, which were positioned nearest to the oven heating element. Presumably uneven
heating caused the metal clamps on the Method 5 filter holders to loosen. Repositioning of
the filter holders as far from the heating element as possible in conjunction with checking
the tightness of the filter holder clamps after oven heatup corrected the problem on sub-
sequent runs. Even though leaks occurred in only one of the four trains in each of the first
two runs, the data from these runs are considered invalid for the purpose of the test and are
not included in this report. However, two additional runs were made the first week, giving
the total  of six valid runs required by the test plan. A summary of the run parameters for
the fourteen valid runs is presented in Appendix A.
                                       26

-------
                                     •15'-
                                                38"
                                                Ladder
             Figure 7. Arkansas Kraft Corporation precipitator exits—top view.
     The paniculate loadings for each train within each run are presented in Table I for the
first week's test and in Table II for the second week's test. The particulate loading Cs for
the Method 17 determinations was calculated three ways for the first week of testing (Table
I).  The Cs values presented under the heading  "Method 17" were  calculated using the
actual particulate catch in the Method 17 filter and filter holder front half. The Cs values
presented under the heading "Method 17 Adjusted" were calculated  as just described
above but with a constant correction of 9 mg/dscm added according to the instructions in
the Federal Register pertaining to use of Method 17 in  Kraft pulp mills. The Cs values
presented under the  heading "Method 17 Plus  Backup" were calculated using the par-
ticulate catch from the Method 17 filter and filter holder front half, the backup probe, and
the backup Method 5 filter and filter holder front half.
    The particulate loading Cs for the Method 17 determinations for the second week of
testing is presented in Table II. Also presented in Table II are the differences, in mg/m3,
between the Method 5 train and the individual Method 17 trains.
    The actual weight of particulate caught and the location within the sample train are
given in Table III for week one and Table IV for week two. Also included in Table III is the
back-half catch for each train obtained by workup of the impinger catch. These back-half
catch values  are substantial but probably do not reflect filter inefficiency. The  residue
which was obtained upon evaporating the impinger water to dryness was not a particulate
solid but was an oily semiliquid material. It probably consists of materials volatile at the
filter oven temperature which are condensed in the impingers.
                                        27

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           TABLE I. PART1CULATE LOADING, Cs
                         mg/dscm
WEEK 1
                      Method 17a  Method 17b
Run Number Method 17  Adjusted   Plus Backup   Methods
3A
B
C
D
4A
B
C
D
5A
B
C
D
6A
B
C
D
7A
B
C
D
8A
B
C
D
Mean
18.8

20.7


40.3

46.3
46.4

47.0


44.4

37.0
60.9

53.5


61.2

54.1
44.22
27.8

29.7


49.3

55.3
55.4

56.0


53.4

46.0
69.9

62.5


70.2

63.1
53.22
34.4

34.9


53.5

55.6
60.7

62.5


54.4

46.7
70.4

62.3


73.7

63.5
56.05

35.4

34.4
49.2

57.4


58.2

52.9
51.6

56.4


71.5

70.1
63.1

73.5

56.12
a.  Actual Method 17 Cs value plus 9 mg/dscm per Kraft pulp mill
   regulations.
b.  Actual Method 17 Cs value plus the material collected in the
   glass-lined probe and the back-up Method 5 filter and filter holder.
                            28

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                 TABLE II. PARTICULATE LOADING, Cs
                         mg/dscm (Sampling Train)
WEEK 2
 Run
  No.   Methods   Nutech

         53.0(B)    35.2(A)
                         Armal Method 17a
                             11SCO
                                          BGI
                            44.7(C)    45.4(D)
         33.l(C)     20.3(D)    28.0(B)    29.l(A)

         68.9(8)     5l.8(A)    54.3(C)    25.7(D)

                              49.4(8)    54.l(Q
      68.6(A)    50.0(D)

      39.8(8)    35.0(A)    30.0(C)    29.8(D)

      3l.3(A)    27.I(D)    29.7(8)    26.6(C)

15    162.5(8)   137.7(A)   164.9(Q    138.3(D)

16    162.7(Q   196.7(D)   155.8(8)    127.5(A)    —34.0

                                         Mean       8.3
      Differences
 (Method S-Method 17)
Nutech   Misco   BGI

   17.8     8.3b   7.6

   12.8     5.1    4.0

   17.1     14.6   43.2C

   18.6     19.2   14.5

    4.8     9.8   10.0

    4.2     1.6    4.7

   24.8   —2.4   24.2

           6.9   35.2

           7.9   17.9
a. Does not include the 9 mg/dscm conversion factor. In the statistical analysis,
   9 mg/dscm was added to these values per Kraft pulp mill regulations.
b. Leak rate at conclusion of sampling four times the allowance leak rate.
c. Large paniculate deposit observed in probe indicating leakage around Filter.
   Results not deleted from analysis.
                                  29

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                                       TABLE III. PARTICULATE CATCH, mg

WEEK !

Run
3



4



5



6



7



8




Train
A
B
C
D
A
B
C
D
A
B
C
D
A
B
C
D
A
B
C
D
A
B
C
D
Method 5
Filter
12.8
29.1
13.0
31.5
52.8
10.1
59.3
6.8
8.3
55.5
11.2
52.9
53.2
7.1
58.6
7.2
9.6
79.2
6.3
75.2
71.3
11.4
84.4
6.1
Method 17
Filter
17.5
—
14.1
—
._.
47.3
„.
50.5
46.9
—
52.0
—
-__
46.1
...
41.0
78.3
—
60.9
—
	
74.7
—
65.0
Method 17 Nozzle
and Filter Holder
2.8

8.3
...
,—
1.0
—
5.0
9.1
...
3.6
...
	
6.1
...
2.9
3.8
—
8.3
—
...
3.3
—
2.6
a.  Oily residue obtained upon evaporation of water.
                                                                Method 5 Probe and        Impinger Train and Back3
                                                               Front of Filter Holder           of Filter Holder

                                                                        4.1                         46.5
                                                                        9.8                         40.0
                                                                        2.5                         43.1
                                                                        6.0                         32.4

                                                                        6.9                         30.8
                                                                        5.7                         36.9
                                                                        9.9                         30.3
                                                                        4.4                         34.8

                                                                        8.4                         34.6
                                                                        15.7                         34.2
                                                                        7.1                         34.2
                                                                        9.7                         34.0

                                                                        8.1                         61.6
                                                                        4.7                         68.3
                                                                        8.0                         60.4
                                                                        4.4                         69.9

                                                                        3.2                         42.3
                                                                        17.0                         35.4
                                                                        5.1                         43.4
                                                                        13.4                         38.4

                                                                        10.0 .                      100.9
                                                                        4.5                        106.0
                                                                        9.0                        100.8
                                                                        5.7                        106.1
                                                        30

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                                  TABLE IV. PART1CULATE CATCH, mg

         WEEK 2

                     Methods  Method 17   Nozzle, Probe,      Nozzle, M-17        Method 17 Filter
          Run  Train    Filter    Filter     M-5 Front Half      Filter Holder         Holder Type

           9    A      —      43.4         —               3.2               Nutech
                B      59.2     —          8.5
                C      —      53.0         —               5.0               Misco
                D      —      54.5         —               4.3                BG1

           10    A      —      30.2         —               3.9                BGI
                B      —      29.2         —               3.3               Misco
                C      29.9     —          9.1
                D      —      18.2         —               5.8               Nutech

           11    A      —      68.1         —                1.6               Nutech
                B      68.9     —          22.4
                C      —      63.5         —               9.0               Misco
                D      —      28.0         —               6.8                BGI

           12    A      72.4     —          18.6
                B      —      61.8         —               2.4               Misco
                C      —      66.8         —               4.3                BGI
                D      —      62.3         —               3.2               Nutech

           13    A      —      38.5         —               3.8               Nutech
                B      43.5     —          6.0
                C      —      28.9         —               8.6               Misco
                D      —      33.3         —               3.3                BGI

           14    A      29.0     —          8.1
                B      —      28.9         —               6.4               Misco
                C      —      26.5         —               5.2                BGI
                D      —      26.7         —               5.2               Nutech

           15    A      —     146.9         —               4.0               Nutech
                B     171.8     —          10.9
                C      —     167.5         —               7.2               Misco
                D      —     144.9         —               5.9                BGI

           16    A      —     113.7         —               8.7                BGI
                B      —     102.4         —              48.5               Misco
                C     142.3     —          17.1
                D      —     181.4         —               8.2               Nutech
     The particulate material recovered in the three special cleanup procedures is tabulated
in Table V. As can be seen from the values presented, the residual particulate left in a
sampling train after a properly conducted sample recovery is quite small and should not
affect the accuracy of a determination.

     Since the second week of the test was intended to compare the performance of various
commercially available Method 17 filter holders, a discussion of their relative merits will be
presented here. The statistical  evaluation of their performance with regard to particulate
determination is included in  the next section.

                                              31

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                   TABLE V. PARTICULATE RECOVERED POSTCLEANUP/CLEANUP
                                         mg

                        1A   IB   1C   ID  2A   2B   2C  2D  8A   8B   8C  8D

          Nozzle, probe, M-5
          filler front-half          1.1       4.4  2.8       0.4      1.9       2.1

          Nozzle, M-17
          filter front       1.7       1.4            1.3       2.0       1.9       3.0

          M-17 back, probe,
          M-5 front        1.9       1.4            2.3       1.5       3.1       1.3
    Three Method  17 filter holders were evaluated: Nutech, Misco and BGI. The Nutech
filter holder was quite heavy and somewhat cumbersome to assemble. The substitution of
hex-head bolts for the slotted-head bolts used in assembling the filter holder permitted the
use of a wrench instead of a screwdriver. This substitution speeded up the assembly and
provided  a  means  of more even tightening of the assembly  to prevent leaks.  Sample
recovery with the Nutech is relatively straightforward, but  care must be  exercised in
disassembly for sample recovery, since that portion of the filter in contact with the gasket
adheres to the gasket quite strongly.  The portion of the filter supported by the sintered
metal support plate breaks free, and  the balance of the filter must be scraped from the
gasket with  a spatula. With careful recovery techniques, this filter holder appears to give
good results.

    The Misco filter holder is more compact  than the Nutech and is easier to assemble.
However, two shortcomings were reported by the field crew.  Due to the relatively small
filtration area available with the Misco, the pressure drop across the filter increases more
rapidly during a run than with the other two filter holders. During the two final runs of the
test, the ESP was operating in an upset condition.  The particulate loading was high (ca.
125-200 mg/dscm), and the Misco filters blinded off to such an extent that isokinetic sampl-
ing could not be maintained for one hour. Both these runs were terminated at the point that
isokinesis  could not be maintained. The second problem involves the Teflon gaskets used in
the Misco filter holder. The three wing nuts used  to secure the assembly can  be tightened
finger-tight before a run, and the gaskets will provide a leak-free seal. However, due to the
high coefficient of thermal expansion and plastic flow characteristics of Teflon, the gaskets
deform upon heating to about 180°C (350 °F).  As  a result of this deformation, the gaskets
tend to leak upon cooling. More important than these leaks on cooling is the  fact that the
filter is subjected to fairly high pressure by the gasket due to the expansion of the gasket on
heating. The glass  fiber filter material is pressed into  the surface of the gasket and is
extremely difficult  to remove during  sample recovery.  Care must be exercised to  avoid
scraping Teflon off the face of the gasket while trying to remove the filter material with a
spatula. This problem made sample recovery from the  Misco filter holder more difficult
than for either of the other two filter holders evaluated. Use of alternative gasket materials
should be  considered when using the Misco unit at elevated temperatures.
                                        32

-------
    The BGI thimble filter holder was the lightest, easiest to clean, and easiest to assemble
of. the three units evaluated.  Since it  is only slightly larger in diameter than  a standard
Method 5 probe, it is easy to insert and withdraw through a standard four-inch sample
port. The major problem encountered with the BGI involves the thimble filter rather than
the filter holder itself. The inside diameters of the lot of thimble filters used were not
uniform. As a result, the fit of the thimble onto the thimble mounting tube of the filter
holder ranged from snug to loose. The possibility of particulate matter bypassing the filter
exists for those thimbles which do not fit tightly. During the portion of the test involved
with filter  holder  evaluation, no backup filters  were used on the Method  17  trains.
However, during sample recovery, the glass probe liners used behind the Method 17 filters
were examined  visually  for particulate matter. At the end of Run 11, Train D, equipped
with the BGI thimble, was observed to have considerable particulate material in the probe
liner. The calculated Method  17 Cs value for this run  was approximately 50 percent of the
Cs values for the other two Method 17 determinations and the Method 5 determination in
Run 11. Either some modification of the filter holder clamp or closer quality control during
filter  manufacture  to assure a leak-free fit of the  thimble into the holder should be
considered.
                                        33

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                                  III. RESULTS

    The data from the test runs were submitted to statistical evaluation. For Method 17,
9 mg/dscm were added to the observed paniculate loading as specified in the Test Methods
and Procedures section of the Federal  Register pertaining  to Kraft mills to obtain the
adjusted particulate concentration. The results from each  week of the test are treated
separately below.


A. WEEK 1

    The particulate loadings from Runs 3  through 8 were used to evaluate Method 17
(adjusted) and Method 17 plus back-half catch in comparison with Method 5 for particulate
determination. The first  two runs were not considered representative due to the problems
encountered and are not included in these analyses. The two  evaluations were treated
separately, and the results are summarized below.

7. Method 5 versus Method 17 (Adjusted)

    The sampling trains, A, B, C, and D, retained their integrity throughout the test. The
only change was made at the probe, with either only a nozzle or a combination of nozzle
and Method 17 filter attached. As such, the possibility  exists that differences might exist
between trains which could influence the results.  This possibility of train-to-train dif-
ferences is investigated using an analysis of variance (ANOVA)  with factors of runs and
trains. The run-by-train interaction is used as the error term for this ANOVA in the absence
of replicate samples. The results are summarized in Table VI.

    The between-trains factor is determined  not to be significant at the 5-percent level, and
the conclusion is that there is no need  to account for the  sample train in future analyses. In
addition to  this, a Friedman test,* a  nonparametric equivalent to the two-way ANOVA,
was run on these data to confirm the result.  The test statistic was calculated at 7.04 with 3
degrees of freedom, which is not significant when compared to a table of the chi-squared
distribution at a significance level of 5 percent.

    Since the train factor was not significant, the mean square for error from the ANOVA
was used as an estimate of sampling variability and the  differences between the Method 5
and Method 17 results investigated. A t-test was used for  this comparison, using the average
•Snedecor, G.W. and Cochran, W.G., Statistical Methods, 6th Edition Iowa State University Press, Ames., 1967.
                                         34

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                           TABLE VI. SUMMARY OF ANALYSES COMPAR-
                            ING METHOD 17 (ADJUSTED) AND METHOD 5

                          ANOVA Table

                          Source          df    SS     MS     F
Between Runs
Between Trains
Run x Train
(error)
Total
5
3

15
23
3553.97
52.78

244.50
3851.25
710.79
17.59 1.08*

16.30

                              y = MSerror
                                        Friedman Test
                                                 Train
                                               B      C
                          Rank sum       9.5    20      18     12.5

                          Test Statistic = 7.04, 3 df*

                                       Means (mg/dscm)

                               Method 5        Method 17 (adjusted)

                                 56.15              53.22

                          t statistic =1.78, 15df*

                          •Not significant at 5-percent level.

                           FQ 05(3,15) = 3.29,X^05(3) =7.81,1005(15) =2.13



values for the 12 determinations by each method. A t-statistic is calculated according to the
formula
where      *s  — average Method 5 results
            Xi 7 — average Method 17 results
            &2  — mean square for error from the ANOVA.

     The calculated t was  1.78, which is not significant at the 5-percent level. The con-
clusion is, then, that the two methods gave equivalent results with the correction factor of 9
mg/dscm added to the result obtained from the particulate catch.

     To estimate the variability associated with each method, a percent coefficient of var-
iation was calculated for each run using the ratio of the standard deviation between the two
results to the average value. The individual values obtained and the averages are shown in
                                           35

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3
4
5
6
7
8
Avg
12.97
8.07
0.76
10.60
1.96
7.57
7.99
Table VII. The average for Method 5 was 6.34 percent, while for Method 17, it was 7.99
percent.

                                TABLE VII. COMPARATIVE
                              COEFFICIENTS OF VARIATION,
                                 METHOD 17 (ADJUSTED)
                                VERSUS METHOD 5 (Percent)

                             Run  Method 17 (Adjusted)  Method 5

                                                  2.00

                                                 10.93

                                                  6.66

                                                  6.25

                                                  1.41

                                                 10.79

                                                  6.34
2. Method 5 versus Method 1 7 plus Back-Half Catch

    The paniculate loadings  for Method 17 were added to the particulate catch from the
probe wash and Method 5 backup filter to determine total particulate matter for each run.
The concentrations calculated in  this manner were analyzed in the same manner as the
Method 17 data, and the results are presented below.

    The ANOVA for investigation of a train effect is shown in Table VIII. As before, the
F-ratio for between-train variability is insignificant, and no allowance for train differences
is indicated. The Friedman test gave a test statistic of 6.40, which also is not significant, and
it is concluded that no bias existed among the four trains.

    The mean for the twelve Method 17 determinations with the back-half workup includ-
ed was 56.05, compared to the Method 5 mean of 56.15 mg/dscm. The resultant t-statistic
was calculated to be 0.05 and is clearly nonsignificant.

    The percent coefficients of variation for these runs are shown in Table IX, along with
their average value. The mean of 5.97 percent compares favorably to the Method 5 value of
6.34 percent.

B. WEEK 2

    Using the eight runs  from the second week of testing, the three types of Method 17
filters were  compared both against each other and against the Method 5 data. The first
analysis, as with the previous  data, was to determine if any  train-to-train bias existed which
could influence the test results.
                                        36

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      TABLE VIII. SUMMARY OF ANALYSES
 COMPARING METHOD 17 PLUS BACKUP CATCH
                AND METHOD 5

ANOVA Table

Source               df     SS      MS      F

Between Runs          5  3145.92   629.18
Between Trains         3     73.27    24.42    1.60*
Run x Train (error)     15   229.33     15.29

Total                23  3448.52

     52 = MSerror = 15.29

                  Friedman Test

                              Train
                    A     B       C      D
Rank Sum            11      19      19      11

Test Statistic = 6.40, 3 df*

                 Means (mg/dscm)

                          Method 17 +
      Method 5              back-half

        56.15                 56.05

t-statistic = 0.05, 15df*

•Not significant at 5-percent level.

 F0.05(3,15) = 3.29, X2} 05(3) = 7.81, to05 (15)= 2.13
    TABLE IX. COMPARATIVE COEFFICIENTS
        OF VARIATION, METHOD 17 PLUS
       BACKUP CATCH VERSUS METHOD 5
                    (Percent)
                 Method 17 +
Run
3
4
5
6
7
8
Avg
Back-Half
1.14
2.75
2.02
10.81
8.61
10.49
5.97
Method5
2.00
10.93
6.66
6.25
1.41
10.79
6.34
                     37

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     The ANOVA is summarized in Table X. The F-ratio for the between-trains component
is less than one and clearly nonsignificant.  The Friedman test for these data gave a test
statistic of 1.35, which also is not significant. As a result, no train bias can be detected., and
no allowance is made in the subsequent analyses for the sampling train used to collect the
sample.
                          TABLE X. SUMMARY OF ANALYSES ON SECOND
                                        WEEK'S DATA

                          ANOVA Table

                          Source            df    SS     MS     F
                          Between Runs        7  83,275.0811,896.44  —
                          Between Trains       3    239.98   79.99  <1*
                          Run x Train (error)    21   3,647.56   173.69

                          Total             31  87,162.62
                                     Friedman Test (train bias)

                                                   Train
                                          A     B	C	D

                          Rank Sum          18     23      21     18

                          Test Statistic = 1.35, 3 df*

                                    Friedman Test (filter type)

                                        Nutech   Misco   BG1

                          Rank Sum          16      16     16

                          Test Statistic = 0.00*

                                       Means (mg/dscm)

                             Methods     Nutech    Misco    BGI
                               77.49      78.23     78.60    68.56

                          LSD 05—13.71
                          Ho: AN + MM + MB ~ 3/*5 = °
                          Test Statistic = —1.57, 21 df*
                          *Not significant at 5-percent level.
                          F0 05 (3,21) = 3.07,\^M(3) = 7.81, t0 05 (21) = 2.08
     The first examination of the Method 17 trains was made using the Friedman test. The
factors in this analysis were the runs and the type of filter. The values for the three Method
17 trains were  ranked across each run and the rank sums computed. The rank sunn was
calculated to be 16 for each of the three trains, and no difference can be detected.
                                              38

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    A parametric approach is also used. A Least Significant Difference (LSD) is calculated
according to the formula
where
            a2 — mean square for error from the ANOVA
 and        n  =8, the number of runs used to obtain the
                 mean for each type of filter.

Substituting gave an LSD of 13.71 for these data.  The averages were 78.23, 78.60, and
68.56 mg/dscm for the Nutech, Misco, and  BGI filters, respectively. Since the range of
these means, 10.04, was less than the LSD, no difference among the filter types can be
detected.

     The Method 5 mean for these runs was 77.49 and shows good agreement with both the
Nutech and Misco average values. To test for consistency between the two methods, a con-
trast among the means is tested. The hypothesis is

                            HO:MN +MM +MB ~3MS =0

where
            MN — mean Method 17 result using Nutech filters
            MM — mean Method 17 result using Misco filters
            MB — mean Method 17 result using BGI filters
and         MS — mean Method 5 result.

     The test statistic is calculated as

                                  Xia ' Xvi ~T~ Xp — 3Xe
                              A. _ II	m.	P	  3
where
           XN	xs — sample  means  corresponding  to the /i's
               above
           Cj   — coefficient  of the  means  in the  null
               hypothesis
           n    — number of runs
and        a1   — mean square for error from the ANOVA.

Substituting gives a calculated t-statistic of -1.57. This does not exceed the tabled t-value
for 21  degrees of freedom  at the 5-percent  level, and  the results  may  be considered
equivalent.
                                      39

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                    IV. SUMMARY AND CONCLUSIONS

    The results of the statistical analysis of data from the first week of testing indicate that
Method 5  and Method  17 gave equivalent particulate results at a Kraft pulp mill recovery
furnace at the 95-percent confidence level when the correction  factor of 9 mg/dscm
specified in the Federal Register was added to the Method 17 determination. Additionally,
the Method 5 versus Method  17  plus backup filter data  indicated  that the particulate
loadings obtained on all four trains were equivalent throughout the first week of testing.
The variability of Method 5 and Method 17 (Adjusted) was good, being 6.34 percent and
7.99 percent, respectively.

    The results of the statistical analysis of data from the second week of testing indicate
that the particulate loadings determined with  all three Method 17 filter assemblies  were
equivalent at  the 95-percent confidence  level. The Method  17 (Adjusted) particulate
loadings determined during the second week of testing were also equivalent to the Method 5
result at the 95-percent confidence level.
                                        40

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       APPENDIX A
RUN PARAMETERS SUMMARY
            41

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                           APPENDIX B

             A COMPARATIVE STUDY  OF METHOD  17  WITH
                 METHOD 5 AT A GRAIN ELEVATOR3

                          H. F. Hamil
I.   INTRODUCTION

        Prior  to proposing new source performance  standards for
grain elevators, the Emissions Standards  and  Engineering Division
of the  Office of Air Quality Planning and Standards obtained source
emission  data on approximately twelve grain elevators.   This work
was  performed to characterize the emissions from  grain  elevators
and  to  determine an emission rate based upon  best available con-
trol technology.  Most, if not all, of these  source tests were
conducted using EPA Method 5.  Based upon the results of this
testing,  a particulate emission standard  of 0.023 grams per dry
standard  cubic meter was set.  This level of  particulate emissions
was  achievable by use of baghouse collectors.

        When the particulate emission standard for grain elevators
was  proposed  in the Federal Register, the reference method listed
for  determination of particulate emissions was not Method 5, but
Method  17,  an in-stack filtration method.

        The  Quality Assurance Branch, Environmental Monitoring and
Support Laboratory (QAB/EMSL) initiated a comparative study of
EPA  Methods 5 and 17 in a grain elevator  to determine their
relative  performance in collecting samples simultaneously.  This
study was conducted at a baghouse collector-equipped grain ele-
vator.  This  facility operated with particulate emissions which
were near the proposed standard.  The results of  the QAB compara-
tive testing  indicated that Method 5 collected about 20 percent
more particulates than did Method 17 when equivalent volumes of
stack gas were sampled.  It should be noted that  this relatively
large percentage difference amounted to an average difference of
only 6  milligrams between the two methods.  Such  small  variations
in mass of  particulate collected were relatively  unimportant in
the past  for  sources with higher standards.   With the lower
proposed  standards, these differences should  be resolved, since1
a review  of the data collected by the Emission Measurement Branch
for  the purpose of proposing the grain elevator standard indicated
that the  average particulate catch by Method  5 in these tests
was  50  milligrams.   Additional comparative testing at a grain
elevator  was  considered warranted.
 Report prepared by Dr. H. F. Hamil and Mr. R. E. Thomas of Southwest Research
 Institute, San Antonio, TX, under EPA Contract 68-02-2^89 and under the direc-
 tion of Mr. Michael C. Osborne, EPA, Research Triangle Park, NC.
                                 45

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II.  TEST  PLAN  AND  SITE

     A.  Test  Plan

         Week  1.  Sampling  was  accomplished with a four-probe/one-
pitot tube assembly.   The  sample  nozzles  were  at the corners of
a square array  6 centimeters on  a side.   The one pitot tube was
centrally  located between  the  four sample nozzles.   Two Method 5
trains were operated diagonally  opposite  two Method 17 trains,
as shown in Figure  1.  Glass-lined probes with new glass liners
were used  on  all four  trains,  with Method 5 filters installed
as backups on the Method 17 probe-filter  assemblies to collect
any particulate not collected  by  the  Method 17 filter.  BGI
thimbles and  holders were  used as representative Method 17 filters,

        A  complete  cleanup of  all trains  was performed prior to
the first  run.  Upon completion  of the  sample  recovery, including
retention  of  the impinger  catch  and train back-half cleanup, an
additional complete train  cleanup was performed to  insure no
particulate remained in the sample trains.   In this fashion, a
complete train  cleanup, separate  from sample recovery, preceded
each sampling run,  and an  additional  train cleanup  was performed
after the  last  run.  The wash  solutions from these  additional
cleanups were worked up to determine  residual  particulate matter
in the trains after normal sample recovery.  Six runs were made
during week 1 by this  sampling procedure.
        Week  2.  The test  plan for the  second  week  incorporated
one major modification.  This  modification consisted of moving
the Method 17 filter out-of-stack to  the  same  location in the
trains as  a Method  5 filter in order  to evaluate the performance
of both Method  5 and 17 filters  under equivalent conditions
(Figure 2).  No backup filters were used.   All other aspects
of the tests were identical to the first  week's tests described
above.  Five  runs were made the  second  week.

        During  both weeks  of the  test,  the positions of the sam-
pling probes were rotated  clockwise in  order to avoid any spatial
bias.

    B.  Test Site

        The site selected  for  this test was a  grain elevator
operated by the Cargill Company  at Reserve, Louisiana.  This
facility was  equipped  with baghouse collectors and  operated at
very low particulate emission  levels.   Pretest sampling to evalu-
ate^the site  indicated that emissions were in  the range of 1.27 x
10~  to 1.71 x  10   grams  per  dry standard cubic meter, as deter-
mined by use of EPA Method 5.  The baghouse collector selected
for the test  was located on the  conveyer  used  in unloading grain
barges.  A stack extension was installed  on the baghouse o\itlet
to bring the  exhaust gas to ground level.   This extension fed into
                               46

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a test  section  from  which the  samples were taken.   A sketch of
the site  complete  with stack extension is shown in Figure 3.

III. FIELD  TESTING

        Pretest  preparations required by the methods were carried
out and included all specified equipment calibrations.  The
pitot tube  calibration was conducted with the full four-probe
assembly  in order  to assure that no bias to the velocity head
measurements by  the  four  probes would be introduced.  The test
was conducted the  first two weeks of May 1977,  commencing on
May 2 and being  completed on May 13.  The test plan originally
called  for  five  runs each week.  The initial run on May 2 was
terminated  prematurely by a plant shutdown caused by equipment
malfunction.  An additional five valid runs were conducted the
first week,  and  five valid runs the second week.  Since the par-
ticulate  loading at  the site was quite low, it was considered
necessary to sample  for three  hours in order to obtain ca 50
milligrams  of particulate.   The first run was considered invalid
due to  a  run time  of about 1.5 hours.  Other criteria for validity
were passage of  initial and final leak checks and isokinetic
sampling within  allowable limits of variation.   During the course
of the  two-week  test period,  the facility was unloading wheat,
corn, and soybeans,  which resulted in considerable variation in
the particulate  loading at the baghouse outlet.  Specific atten-
tion by test personnel to plant operation was required, since the
unloading operations were intermittent, even though the conveyor
ran continuously.  To assure that sufficient particulate matter
was collected, sampling was conducted only when the conveyor was
loaded  and  was interrupted when the conveyor was running empty.

        Only one problem  of significance occurred with the test
equipment.   One  control console developed a leak in the pump
oiler.  This console was  replaced with a backup unit.  During
the sample  workup  in the  laboratory, two other  problems more
serious in  nature  were encountered.

        The  first  involved the Method 17 filters (BGI thimbles).
Prior to the  test, the filters were desiccated  to constant weig-ht
according to  the method (less  than 0.5 mg change on two subsequent
weighings).   Since the particulate matter is collected on the
outside of  the BGI filter,  some means of protecting the used
filter  to prevent  loss of particulate during desiccation and
weighing is  required.   Each thimble was placed  in a glassine
envelope for  this  purpose.   The thimble and envelope was desiccated
to constant  weight as  a unit.   Some difficulties were encountered
in the pretest drying  to  constant weight.   The  filter-envelope
combination  appeared  to pick up moisture fairly rapidly on the
balance pan,  even  though  the weighings were conducted in a con-
stant temperature-constant  humidity room.   However,  after several
                                47

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days the  filters  were  brought to constant weight.  When the
filters used  in field  sampling were desiccated to constant weight,
some were  found to  weigh less than the pretest tare weights.
Only one  unused Method 17 filter was available.  This filter wais
desiccated to constant weight over a period of ten days and was;
found to  weigh 37.2 mg (0.847 wt %)  less than the original tare
weight.   It appears that although in the pretest weighing of the
Method 17  filters constant weight was achieved, the filters were
not completely dry.  Subsequent investigations showed that the
problem was not due to the filter thimbles but due to the glass-
ine envelopes.  These  envelopes, intended for photographic negative
storage, have incorporated in them a certain amount of a desiccant
and will dry  to a constant weight (less than 0.5 mg change on
two subsequent weights)  while still retaining considerable moisture
Continued  desiccation  will eventually remove this water.

        Based upon  the weight change of the unused Method 17 fil-
ter, a correction factor (0.9916 x original tare weight) was used
to correct  the tare  weights of the filters.  It is realized that
this is not a particularly satisfactory solution to the problem,
but it is  the only  means available to try to salvage the data.
The Method  17 particulate catch weights are uncertain, and
quantitative  comparisons of particulate loadings by the two
methods are not possible,  as will be discussed in the next section.

        The second  problem concerned the amount of material which
passed through the  filtration system and was collected in the
back-half  (impinger  section)  of both the Method 5 and Method 17
determinations.   The particulate which passed the filter was
determined  by placing  the impinger water in a sample bottle along
with an acetone wash of  the filter holder back-half, the fritted
glass filter  support,  the impingers and connecting glassware.
Particulate mass  was determined by evaporation of this combined
acetone-water mixture  to dryness.  After evaporation to dryness,
small pieces  of glass  from the fritted glass filter support were
observed in most  of  the  samples.  As a result, the impinger resi-
due weights are somewhat inflated.

IV.  RESULTS

        The run parameters for the eleven runs are presented in
Table I.   The first  run  is of questionable value due to the short
sampling period.  For  Runs 2 through 11, the Method 17 runs are
designated  with an  asterisk.   Runs 2 through 6 were made the first
week.  In  Table I,  two particulate loadings (Cs) were calculated
for the Method 17 runs;  under the column headed Cs is the value
calculated  on the total  particulate catch  (Method 17 filter
assembly plus backup filter assembly), while the column headed
Method 17  Cs  is calculated using the particulate catch from the
Method 17  filter  assembly.   The Cs values for Method 5 are calcu-
lated in the  normal  manner.  The within-run agreement between the

                                 48

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Method  5 determinations  is  quite  good  over  the  range  of  particu-
late loadings  studied  (9-45 mg/m  ).  Unfortunately, the  Method  17
results cannot be  compared  quantitatively to  the Method  5  results
due to  the uncertainty in the  Method 17  results introduced by
the problem with the thimble tare weights.  However,  a comparison
of the  two particulate loadings calculated  for  each Method 17
run provides some  useful information.  The  difference in these
two Cs values  gives a measure  of  the amount of  particulate which
passed  through the Method 17 filter and  was collected in the back-
up Method 5 probe, filter and  filter holder.  An examination of
the data revealed  that a fairly constant amount of particulate
was collected  in the backup train over the  range of particulate
loading studied.   The mean.value  for particulate collected in the _
backup train was 3.73 mg/m  with  a standard deviation of 0.56 mg/m  ~
The lowest value was 2.52 mg/m and the  highest value was  4.17 mg/m
Since the amount of particulate remained relatively constant over
the range of particulate loading  studied, the percent error intro-
duced in a Method  17 determination would be greatest  for low
particulate loading and decrease  as the  loading increased.  This
apparent increase  in filtration efficiency  with increased  particu-
late loading may reflect the effect of a filter cake  buildup on
the filter surface which results  in more efficient particulate
retention as the run progresses.

        The results of the  second week's runs to assess  the rela-
tive performance of Method  5 and  Method  17  filters located in the
same position  in the train  {out-of-stack) are inconclusive due
to the uncertainty in the Method  17 results.

        The results of the  impinger train workup to determine the
filtration efficiency of the entire filter  assembly are  inconclu-
sive due to contamination of the  back-half  catch with glass
particles from the Method 5 filter supports.

        The additional cleanup procedures before the  first run,
between each pair of runs and  after the  last run  were performed
to assess the amount of particulate which remained in the  train
after a normal sample recovery.   A total of 48  individual  train
cleanups were performed during the course of the two-week  test.-
The mean value of particulate  recovered  from the sample  nozzle,
probe and filter holder on  these  cleanups was 4.01 mg with a
standard deviation of 1.9 mg,  indicating that very little  material
is left in the sample train if good sample  recovery procedures
are followed.

        The weights of particulate caught in each run and  the
location of the catch in the train components are presented in
Table II.   The values for impinger train residue for each  run
are presented in Table III, and the values  for  particulate  recovered
in the additional train cleanup procedures  are  presented in Table TV.
                                49

-------
V.  CONCLUSIONS

        Despite  the  fact  that  a quantitative comparison of
Methods 5  and  17  could  not  be  made,  the  data from the first week
of the test  indicate  that a significant  amount of particulate
(3.75 mg/m ) passes  through the Method  17  filter.  The amount of
particulate  passing  the filter was  relatively constant for
particulate  loadings  in the range of 10-45 mg/m .  No informa-
tion on the  amount of particulate passing  the filter at higher
loadings is  available.  It  is  possible  that the amount of parti-
culate passing the filter may  be site specific in that it could
be affected  not  only  by particulate  loading but also by the
physical and chemical properties of  the  particulate (size distri-
bution, composition,  etc.).

        The  data  from the second week of the test did not allow
an assessment of  the  relative  filtration efficiency of the two
filter assemblies operated  in  the same mode (out-of-stack).
However, review  of the  impinger train residue values for Runs 7
through 11 does  not  show  gross discrepancies in the Method 17
versus Method 5  results.  It appears possible that the Method 5
probe acts as a precollector and has an  effect on filter efficiency.

        These conclusions are  necessarily  speculative due to the
uncertainty  in the Method 17 data.   Further investigations are
needed to  confirm or  refute these tentative findings.

        One observation of  importance in the use of the BGI
thimble filters  should  be noted.  The thimbles were seated in the
filter holder merely  by friction fit.  No  securing device was
used to hold the  filters  in place.   There  was sufficient varia-
tion in the inside diameter of the  thimbles in the lot used
that the fit of the  filter  in  the filter holder varied from snug
to loose.   There  is  firm  evidence on one run (7C) that consider-
able particulate  bypassed the  filter and was collected in the
impinger train, which was very milky in  appearance at the end
of the run.  In this  run, 103  mg of  particulate was collected
by the probe and  filter and 48.2 mg  by the impingers, compared
to 174.6 mg by the probe  and filter  and  only 8.1 mg by the impingers
on Run 7A, the other  Method 17 determination in that run.  Some
means of assuring that  particulate  blow-by does not occur should
be incorporated  in the  use  of  BGI filters.
                                 50

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                                   TECHNICAL REPORT DATA
                                ead htumctions on llie reverse bciorf comnletins)
  "EPAT600/4-80-022
                             2.
                                                           3. RECIPIENT'S ACCESSION-NO.
4 TITLE A\O SLSTiTLc
 COMPARATIVE TESTING OF EPA METHODS 5 AND  17
 AT NONMETALLIC  MINERAL PLANTS
             5. REPORT DATE
               April  1980
             6. PERFORMING ORGANIZATION CODE
                                                           8. PERFORMING ORGANIZATION REPORT NO.
 William J. Mitchell,  M.  Rodney Midgett and  C.  Bruffey
9. PERFORMING ORGANIZATION NAME AND ADDRESS
 Quality Assurance  Division
 Environmental  Monitoring Systems Laboratory
 U.S. Environmental  Protection Agency
 Research  Triangle  Park,  NC  27711
             10. PROGRAM ELEMENT NO.



             11. CONTRWCT/cHANT NO.
12. SPONSORING AGENCY NAME AND ADDRESS
 Environmental Monitoring Systems Laboratory
 Office of Research  and Development
 U.S. Environmental  Protection Agency
 Research Triangle Park,  NC  27711	
             13. TYPE OF REPORT AND PERIOD COVERED

             	Final	
             14. SPONSORING AGENCY CODE
                   EPA 600/08
15. SUPPLEMENTARY NOTES
 To be published as  Environmental Monitoring  Series  report.
16. ABSTRACT
      Comparative  tests  between EPA Reference Method 5 and commercially-available
 in-stack filters  (EPA Reference Method 17)  showed  that in-stack filters  can  be
 acceptable substitutes  for the Reference Method  at nonmetallic mineral plants.
 These comparative tests were conducted in the  exhaust' stacks from a clay calciner,
 a feldspar grinding  mill  and a limestone crusher.   Particulate concentrations
 encountered ranged from 30 to more than 300 mg/m3.   Laboratory studies using
 feldspar dust gave results identical to the field  study results.  Insignificant
 amounts of material  were found downstream of the in-stack filters.  These results
 are compared to similar results obtained at a  grain elevator and a kraft pulp mill.
17.
                               KEY WORDS AND DOCUMENT ANALYSIS
                  DESCRIPTORS
                                              b.IDENTIFIERS/OPEN ENDED TERMS
                             COSATI Field/Group
 Particulate
 In-stack filter, out-of-stack filter
 EPA Method 17
 EPA Method 5
                              43F
                              68A
'.3. jljTRlsUTION STATEMENT

 Release to Public
19 SECURITY CLASS f Tins Report)

   Unclassified     	
21. NO. OF PAGES

	fin
                                              20. SECURITY CLASS (Tins page I

                                                 Unr.1 as^i f "ipH
                                                                         22. PRICE
EPA Form 2220-1 (9-73)

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