United States
Environmental Protection
Agency
Industrial Environmental Research
Laboratory
Research Triangle Park NC 27711
Research and Development
EPA-600/S7-81-037  July 1981
Project Summary
Fabric  Filter  System  Study
Second  Annual  Report

K. L. Ladd, R. L. Chambers, 0. C. Plunk, and S. L. Kunka
  This report describes second year
activities of a comprehensive EPA-
funded study of a commercial fabric
filter on a 360 MW low sulfur coal-
fired unit at Southwestern Public
Service Company's Harrington Station
near Amarillo, Texas. Special tests
were performed to characterize gas-
eous and particulate emissions, to
evaluate fabric performance, and to
optimize the fabric filter system's
performance. Tests will continue dur-
ing the third year of study.
  This report is submitted in fulfillment
of Contract No. 68-02-2659 by South-
western Public Service Company
under the sponsorship of the U.S.
Environmental Protection Agency.
This report covers the period  October
1,1978 to October 1,1979.
  This Project Summary was developed
by EPA's Industrial Environmental
Research Laboratory. Research Trian-
gle Park. NC. to announce key find-
ings of the research project that is fully
documented in a separate report of the
same title (see Project Report  ordering
information at back).

Introduction
  In order to  assess the feasibility of
utilizing fabric filters for air quality
control, the U.S. Environmental Protec-
tion Agency (EPA) executed a  contract
with Southwestern Public Service Corn-
pa ny (SPS) in  1977 to make a compre-
hensive study of a fabric filter system
used for particulate collection on a large
electrical generating unit that burns low
sulfur Western coal. The plant site
selected was  Harrington Station (Unit
2), Southwestern's first coal-fired facility.
When constructed, the baghouse was
the first and largest to be used on a new
utility boiler.  It remains  one of the
largest baghouses currently in operation.
  The baghouse being  studied at
Harrington Station is a Wheelabrator-
Frye, Inc. structural baghouse with
deflate/shake cleaning. It first went on
line in June, 1978. The baghouse con-
sists of 28 compartments with 204 bags
per  compartment for a total of 5,712
bags; each bag is 11V4 inches in diam-
eter and 30 feet, 8 inches long. The
baghouse was specified at 1,650,000
acfm of flue gas at 313°F, thus yielding
a design air-to-cloth ratio  of 3.15 to 1
(gross) or 3.4 to 1 (net).
  Unit 2, on which the baghouse is
installed, has a 360 MW turbine with a
tangentially-fired steam generator. The
boiler utilizes pulverized, low sulfur
Western coal  to produce 2,688,000
Ibs/hr of steam. The fly ash-laden flue
gas  from the boiler flows  through the
preheater directly through the fabric
filter system and then out the  stack.
  The study objectives set out in the
EPA/Southwestern contract are de-
scribed below. These objectives were
formulated to help utilities and  other
coal burning facilities obtain information
for evaluating air control alternatives.
SPS especially hopes to aid those burn-
ing low-sulfur Western coal.
  1. Determine operating and mainte-
    nance costs of an operating fabric
    filter system over an extended
    period of time in order to give other
    utilities  data on the economic
    feasibility of baghouses.

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  2. Characterize performance of the
     unit by looking at specific param-
     eters which include (a) an assess-
     ment of the effect of pressure drop
     versus time;  (b) removal efficiency
     to be determined by special manual
     testing; (c)  continuous opacity
     monitoring; (d) an investigation of
     the long-term reliability of the sys-
     tems; and (e) determination of
     optimum operating conditions.
  3. Bag performance and bag life will
     be studied by (a) periodic removal
     of test bags for analysis by an
     independent consultant; (b) analy-
     sis of  pressure drop and through-
     put on an individual compartment
     basis; (c) and other special fabric
     studies.
  Progress during the first year of study
is discussed in the First Annual Report
(EPA-600/7-79-183, August, 1979).
This report describes project activities
during the second year of study, which
progressed from the first year's organi-
zational stage to actual testing and
evaluation. The first set of special tests
was conducted, a fabric assessment
program was implemented, and a wide
range  of operation and maintenance
tasks were completed. In  addition,  a
data acquisition system was established
and certain study areas were given
special consideration.
  The original work plan for the second
year of study entailed a number of tests
and programs which could not be con-
ducted during  an abnormal start-up
phase typical of  first-year operation.
However, project activities provided
valuable information about parameters
neither the utility nor the vendors had
expected. These circumstances allowed
for trouble-shooting to bring the bag-
house up to an expected level of per-
formance.

Summary of Project Activities
   1. To characterize gaseous and
      particulate  emissions from the
      boiler/baghouse system, South-
      western conducted  a series of
      special tests during December,
      1978. Results of particulate test-
      ing confirmed  that  Unit 2 can
      operate in compliance with  the
      existing New Source Performance
      Standard (NSPS) of .1 lb/108Btu.
      However, problems in the testing
      with  the  heated probe caused
      particulate  results to be biased
      (high).  Concentrations of NO*
      were determined to be consistent
      at all five sampling locations. As
      a result. Southwestern and EPA
      concluded the testing program
      could be better managed by ex-
      cluding NO, from future  testing.
      Test results from the stack loca-
      tion indicated the  unit can meet
      existing NSPS standards  for S02
      and results correlated  well with
      stoichiometric calculations. S02
      measurements at  inlet locations
      were erratic due to high negative
      duct pressure. Table I  shows
      results of particulate, NOX and
      S02 testing.
    2. GCA Corporation conducted ex-
      tensive  tests from February 9,
      1979 through February 15,1979.
      (See Table II, GCA Data Summary.)
      Mass emissions of particulate
      were conducted at the stack loca-
      tion with five sampling runs.
      Mass emissions  ranged  from
      .007 lbs./106 Btuto.034lbs./106
      Btu. Average particulate collec-
Table I.    Results of Particulate Testing
tion efficiency was determined to
be approximately 99.3%.
  Particulate size distributions
were made utilizing Anderson
impactors. The mean particle
diameter was determined to be
5.4 microns at the stack exit. The
mean particle diameter for the
east  and west  inlet was deter-
mined to be 3.8 and 2.6 microns,
respectively. Due to erratic data
scatter, further testing by impac-
tor is recommended.
  Sulfur dioxide emissions were
within NSPS of 1.2 lb/10«  Btu.
However, the results were erratic,
probably due to high negative
stack pressure. Oxides of nitrogen
emission were consistent across
the entire baghouse.
  Results of sulfur trioxide testing
ranged from 0.3 to 3 ppm. To
obtain a better measurement and
to better understand  S03 con-
centrations and their relationship
Run
n
East
Inlet
gr/SCF
West
Inlet
gr/SCF "
Theoretical
Inlet +
gr/SCF
Stack***
gr/SCF lb/106 Btu
    1*         2.28         2.74         2.09         .053         .106
    2*         2.04         2.26         1.96         .050         .097
    3**        1.67         1.63         2.27         .033         .061
  ^Assumes 70% Fly ash, 30% bottom ash and economizer ash; no consideration for
   sootblowing.
  *Sootblowing continuously.
 **Not sootblowing.
 **The concentrations of particulate obtained from the stack are biased high because
   a reaction took place in the unheated Inconel probe liner.

                           Results of /VO, Testing
Run
#
/
2
3
East
Inlet
Method 7
.68
.71
.67
East
Outlet
Method 7
.64
.68
.71
West
Inlet
Method 7
.61
.59
.62
West
Outlet
Method 7
.62
.62
.62
Stack
Method 7
.63
.66
.64
                           Results of SOz Testing
t
Run
#
2
3
East Inlet*
Method 6
lb/106 Btu
.53
.59
.62
West Inlet*
Method 6
lb/106 Btu
.36
.32
.20
Stoichiometric**
lb/106 Btu
.76
.84
.88
Stack
Method 6
lb/106 Btu
.73
.78
.84
 *These concentrations are suspected of being low because of the high negative
  pressure pulling the absorbing solutions forward, thereby resulting in the
  absorbed SO? not being analyzed.                                           t
**Assumes alt sulfur is converted to SOa.                                      '

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Table II.    GCA Data Summary

                 Results of Paniculate Testing EPA Method 5
Run
#
1
2
3
4
5
6
East
Inlet
gr/SCF
1.03
0.99
1.34
2.21
1.53
1.36
West
Inlet
gr/SCF
1.57
1.68
1.20
1.36
1.02
2.36
East
Outlet
gr/SCF
0.011
0.007
0.004
0.004
0.001
0.005
West
Outlet
gr/SCF
0.019
0.005
0.008
0.007
0.002
0.042
Stack
gr/SCF
#
0.009
0.008
0.012
0.004
0.017
Stack
lb/106 Btu
*
o.o/s
0.076
0.024
0.007
0.034
                    Results of SO* Testing EPA Method 6
Run
#
2
4
6
East
Inlet
lb/106 Btu
#
0.98
1.10
West
Inlet
lb/106 Btu
0.91
0.80
0.61
East
Outlet
lb/106 Btu
0.82
0.94
0.68
West
Outlet
lb/106 Btu
0.95
*
0.64
Stack
lb/106 Btu
1.10
#
0.74
                    Results of /VOx Testing EPA Method 7
Run
tt
2
4
6
East
Inlet
lb/106 Btu
ft
0.55
0.63
West
Inlet
lb/106 Btu
*
0.50
0.53
East
Outlet
lb/106 Btu
0.60
0.52
0.48
West
Outlet
lb/106 Btu
0.69
0.53
0.55
Stack
lb/106 Btu
*
0.51
0.47
                    Results of 503 Testing EPA Method 8
Run
#
2
4
6
East
Inlet
ppm
0.27
2.07
2.56
West
Inlet
ppm
0.79
0.67
1.96
East
Outlet
ppm
0.99
0.60
1.81
West
Outlet
ppm
0.72
0.82
1.67
Stack
ppm
1.10
«
1.86
 *No data this run.
**Average based on three samples only.

      to acid dew point, a Goksoyr Ross
      test will be performed during the
      next series of tests.
        Difficulties encountered during
      organic emission sampling pre-
      vented  a conclusive  analysis  of
      this data during the second year
      of study. GCA's  final report will
      deal with this parameter in a
      more complete manner.
   3.  During the second year of study,
      Southwestern implemented a
      fabric assessment program  in
      which individual bags  were re-
      moved from compartments  at
      random and sent to an  indepen-
      dent testing firm for  evaluation.
      This phase of study will continue
      in the third year to determine if
      such tests are useful in evaluating
      bag performance and bag life.
Another special study was initi-
ated between Southwestern and
Wheelabrator-Frye, Inc. This study
was designed to determine distri-
bution of ash on bags in a given
compartment and differences in
particle size distribution in the
compartment and along the fab-
ric. Preliminary results of these
tests show that the bags receive
equal dust loading regardless of
position in the compartment.
Furthermore, indications are that
both dust loading  and particle
size do not change significantly
along the length of the bag.
An additional fabric assessment
program was conducted by Acurex
Corporation utilizing a small mo-
bile baghouse. Recommendations
made to Southwestern following
  this study were that Southwes-
  tern should evaluate the perfor-
  mance of an Acid Flex coating
  and performance characteristics
  of higher deflation pressures
  with ringed bags. Acurex also
  recommended higher shake fre-
  quencies, confirming results of
  previous tests performed by
  Southwestern.
6. Southwestern developed a tech-
  nique for analyzing individual
  compartment  performance by
  measuring relative flow.  This
  technique allows data taken at
  any flow condition to be compared
  with data taken at any other set of
  flow conditions. Results to date
  have indicated this technique to
  be a reliable  and  sufficiently
  accurate method for measuring
  compartment performance.
7. Improved performance was ob-
  tained during the second year of
  study by optimizing deflation
  pressure drop and shaker speed.
  As a result, deflation pressures
  were attenuated from the initial
  0.5-inch w.g.  to 0.1-inch w.g.
  Excellent  results were obtained
  by increasing rapidity of shake in
  several experiments. Studies are
  in  progress to determine the
  effect of increased shake on bag
  life. Preliminary results to date
  indicate that there is no drastically
  detrimental effect on bag life.
8. Originally,  pressure drop in the
  baghouse was excessive.  Since
  rebagging with different bags,
  optimizing deflation control, and
  increasing shake speed, baghouse
  performance has been greatly
  improved.
9. A data collection and assessment
  program was initiated during the
  second  year of study. However,
  due to a  faulty magnetic  tape
  system, appropriate data  proc-
  essing has not been possible so
  that data can be easily reduced
  and analyzed. An intense  effort
  will be made in the third year of
  study to manually reduce much
  of this data. In addition, a new
  magnetic tape system will be
  installed. Due to concern about
  high pressure drop problems,
  much of the pressure drop data
  was manually processed to give
  monthly values for the full load
  pressure drop.  Plots of full load
  pressure drop  for each month

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      have proven to be an invaluable
      tool in assessing trends in bag-
      house performance. (See Figures
      1 and 2).
  10. A special study area of the EPA/
      Southwestern project includes
      corrosion testing, electrostatics,
      and quality assurance (QA). Cor-
      rosion coupons were  installed
      and then removed for  analyses
      during the second year of study.
      Results indicate that corrosion in
      the Harrington baghouse at this
      point  is minimal. Cage voltage
      measurements made by Acurex
      during the mobile baghouse study
      led to a decision by EPA to initiate
      a program with Research Trian-
      gle Institute to study electrostatics
      and its relationship to pressure
      drop problems.
                                               East Side
                                                 West Side
   14.0


   12.0


   10.0
A/>

H*°8.0\


    6.0


    4.0


    2.0
Before Rebagging
        Sept.   Nov.  Jan.  Mar.  May
            Oct.   Dec.   Feb.  Apr.
                    Month
*Air to cloth ratio of 3.4

Figure  1.
    Monthly full load pressure
    drop, original fabric.
                                CD

                               "• 7
                                I
                                (0
                               I
                               .C
                               0.
                               < 5
                                                                                        OAt V = 3.4 ft./min.
                                                                                        X At V = 3.0 ft./min.
                                   July
          Aug.     Sept.

              1979
Oct.
July    Aug.     Sept.

            1979
Oct.
                               Figure 2.    Monthly full load pressure drop., new fabric.
K. L Ladd, R. L Chambers, O. C. Plunk, and S. L Kunka are with the Southwest-
  ern Public Service Company, Amarillo, TX 79170.
Dale L Harmon is the EPA Project Officer (see below).
The complete report,  entitled "Fabric Filter System Study: Second Annual
  Report," (Order No. PB 81-185 670; Cost: $17.00, subject to change) will be
  available only from:
        National Technical Information Service
        5285 Port Royal Road
        Springfield, VA  22161
        Telephone: 703-487-4650
The EPA  Project Officer can be contacted at:
        Industrial Environmental Research Laboratory
        U.S.  Environmental Protection Agency
        Research Triangle Park,  NC 27711
                                                                                    » U.S. GOVERNMENT PRINTING OFFICE 1»1 -757-01Z/7H9

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