United States
                   Environmental Protection
                   Agency
 Air and Energy Engineering
 Research Laboratory
 Research Triangle Park NC 27711
                   Research and Development
 EPA/600/S7-86/030 Dec. 1986
x°/EPA         Project  Summary
                   Demonstration,  Operation,
                   and  Testing of  a  Fabric  Filter
                   on  an  Industrial  Boiler  for  an
                   Extended  Period  of Time

                   Gary P. Greiner, Jeffrey K. Smith, John M. Ross, and John D. McKenna
                     A number of fabric filters were evalu-
                   ated in baghouses controlling particu-
                   late emissions from industrial coal-fired
                   stoker boilers. Various techniques were
                   employed to achieve higher gas-to-
                   cloth (G/C) ratios and longer bag life, rt
                   was found that  off-line, high energy,
                   pulse jet cleaning was necessary for
                   long term pressure drop stability at G/C
                   ratios greater than 5/1. Cleaning energy
                   dramatically affected filter perform-
                   ance, but cleaning frequency had only a
                   minor effect. A felted fabric combina-
                   tion of Teflon and glass exhibited excel-
                   lent performance, life, and stability.
                     This Project Summary was devel-
                   oped by EPA's Air and Energy Engineer-
                   ing Research Laboratory, Research Tri-
                   angle Park, NC, to announce key
                   findings of the research project that is
                   fully documented in a separate report
                   of the same title (see Project Report or-
                   dering information at back).

                   Introduction
                     Previous pilot and full-scale programs
                   had shown that fabric filters could be
                   successfully used in  a baghouse con-
                   trolling the particulate emissions from
                   coal-fired  industrial  boilers, but that
                   gas-to-cloth (G/C) ratios and bag life
                   needed improvement. A program for
                   this purpose was instituted in March
                   1981, at Kerr Finishing Co., Travelers
                   Rest, SC, where two tandem baghouses
                   were in operation and controlling the
                   particulate from industrial coal-fired
                   boilers. These boilers produced steam
                   for a textile finishing plant where load
                   requirements fluctuated often and
 rapidly, and harsh cycling conditions of
 start-up and shutdown produced fre-
 quent dewpoint excursions in the bag-
 houses.
  One of the baghouses was a pulse jet
 dust collector with on- and  off-line
 cleaning capability. The other baghouse
 had high volume, low  pressure (10 in.
 w.g.; 2.49 kPa), reverse-flush cleaning
 which provided a cleaning energy less
 than a pulse-jet but higher than conven-
 tional reverse-air cleaned baghouses.
  This report summarizes the results of
 this program, which was terminated in
 November 1982.

 Baghouse Details
  Both baghouses contained 648 bags,
 5 in. (12.7 cm) in diameter and 104 in.
 (264.2 cm) long, providing a total filtra-
 tion area of 6800 ft2 (631.7  m2). Each
 house was divided into six cells.
  Normal operation of the pulse jet bag-
 house was to take a cell off-line during
 pulse cleaning. All fabric  in this house
 was a form of Teflon felt, with each cell
 having bags of the same material. Felts
 of varying weight and construction
 were evaluated.
  The second house was cleaned by air
 plenum pulse, rather than  pulse jet.
 Four fabric sets were evaluated in  this
 house:  three woven glass  sets with
 varying finishes, and one Nomex felt set
 with an  acid resistant finish.

 Parameters Studied
  Parameters studied as having an ef-
fect on  the gas-to-cloth ratio were:
 (1) cleaning energy—pulse jet vs. re-

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  verse air vs. combinations; (2) cleaning
  mode—on vs. off-line; (3) cleaning fre-
  quency; and (4) fabric type and style.
  Operational Stability
    The criterion for stable operation of a
  baghouse cell was the "drag," defined
  as the average tubesheet differential
  pressure (AP) during a filtering cycle, di-
  vided by the G/C of the cell. When no
  consistent upward movement in drag
  was observed over a 2 to 3 day period,
  a cell was  considered to  have short-
  term stability.
    AP across the cells was equalized, and
  the cell flows were monitored. G/C ra-
  tios, which fluctuated with steam load,
  typically varied from  5 to 8.
  Emissions Testing
    Method 5 testing for outlet paniculate
  concentrations vs. evaluation variable
  was not  done because of budget con-
  straints. Both baghouses passed stand-
  ard state compliance testing.
  Fabric Evaluation
    Fabric  properties  were evaluated by
  removing bags from the baghouses and
  testing them in the laboratory for tensile
  strength, Mullen burst strength, MIT
  flexes, loss on ignition, and permeabil-
  ity. Visual and microscopic inspections
  were also performed.
    Fabric  permeabilities determined in
  the laboratory as part of the fabric eval-
  uation program were compared on  a
  relative basis, since removal of a bag
  from the baghouse  must alter the cake
  properties on the fabric.
  Bag Conditioning
     Bags were conditioned for 4 weeks at
  G/C ratios of 1.5 to 2.5 with flow, tem-
  perature, and cell AP carefully moni-
  tored. Bags were also visually inspected
  periodically.
       Fabric Properties vs. Time
         Part of the  program involved fabric
       property tests performed on bags from
       the plenum  pulse baghouse after
       1  hour,  24 hours, 1  week, 1  month,
       3  months, 5 months,  and 7 months of
       service. The material tested was woven
       fiberglass with acid resistant Teflon B
       and an experimental Teflon finish, and
       Nomex felt with an acid resistant finish.
       These tests provided the first documen-
       tation of how rapidly strength  charac-
       teristics change with time.
       Conclusions

       High G/C Study
         Pulse  jet cleaning of felted fabric was
       necessary for long term pressure drop
       stability at G/C ratios higher than 4/1.
       There were indications that woven fab-
       rics could not operate stably above 4/1
       on a long term basis.
          Off-line pulse  jet  cleaning  was re-
       quired for stable operation at G/C ratios
       above 4-5/1.
          A new Teflon felt consisting of Teflon
       and glass fibers performed very well
       throughout the test period at G/C ratios
of 7-9 and with stable pressure drops.
This fabric exhibited the potential of op-
erating at G/C ratios 50% or more above
those in practice today. Additional long
term studies are warranted.

Effect of Cleaning on Drag
  Fabric drag was found to be a strong
function of cleaning energy.  An in-
crease of 50% in energy decreased the
drag by 30%. However, the effect of
cleaning frequency, which varied from 6
to 20 minutes, was slight.
Fabric Life
  Woven  glass bags with  either 7%
Teflon B or acid resistant finishes sur-
vived about 2 years in the low cleaning
energy baghouse. These bags were not
tested in the pulse jet house.
  Nomex bags failed within 6 months of
normal operation because of the high
sulfur trioxide.
  Teflon felt proved very durable. A cell
of original bags was still functioning af-
ter 5 years, and no major failure rates
occurred on any of the other Teflon con-
structions except for an  asymmetrical
felt construction.
          G. Greiner. J. Smith, J. Ross, and J.  McKenna are with ETS, Inc., Roamoke,
           VA 24018.
          Louis S. Hovis is the EPA Project Officer, see below.
          The complete report, entitled "Demonstration, Operation, and Testing of a Fabric
           Filter on an Industrial Boiler for an Extended Period of Time," (Order No.
           PB 87-111  134/AS;  Cost: $13.95. subject to change) will be available only
           from:
                 National Technical Information Service
                 5285 Port Royal Road
                 Springfield, VA 221611
                 Telephone: 703-487-4650
          The EPA Project Officer can be contacted at:
                 Air and Energy Engineering Research Laboratory
                 U.S.  Environmental Protection Agency
                 Research Triangle Park. NC 27711
United States
Environmental Protection
Agency
Center for Environmental Research
Information
Cincinnati OH 45268
Official Business
Penalty for Private Use $300
EPA/600/S7-86/030
       Q000329

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