United States
                   Environmental Protection
                   Agency
 Risk Reduction
 Engineering Laboratory
 Cincinnati, OH 45268
                   Research and Development
 EPA/600/S2-89/060  Feb. 1990
SEPA         Project Summary
                   Incineration  of Creosote  and
                   Pentachlorophenol  Wood-
                   Preserving  Wastewater
                   Treatment Sludges
                   Fred D. Hall
                    Wastewater treatment  sludges
                  from two wood-preserving operations
                  were incinerated to provide data for
                  the EPA's land disposal restriction
                  regulations  under the Resource
                  Conservation  and Recovery  Act
                  (RCRA). The  untreated  wastes,
                  incinerator  ash,  and  stack  gas
                  samples were analyzed for organic
                  and metal compounds. A report was
                  prepared to document the  effective-
                  ness of the incineration tests.
                     This  Project  Summary was
                  developed by EPA's Risk Reduction
                  Engineering Laboratory,  Cincinnati,
                  OH, to announce key findings of the
                  research  project that  is  fully
                  documented in a separate  report of
                  the same title (see Project Report
                  ordering information at back).

                  Introduction
                    RCRA Waste Code K001 is defined as
                  the bottom sediment sludge  from the
                  treatment of wastewaters from wood-
                  preserving processes  that use pentachlo-
                  rophenol  (PCP) or creosote (C).
                  Pentachlorophenol is  a synthetic organic
                  compound manufactured by reacting
                  chlorine with  phenol. Creosote is  a
                  derivative of coal containing  creosols,
                  phenolic compounds,  naphthalene, and a
                  wide range of polynuclear aromatics. An
                  estimated 400 facilities  in the  United
                  States have wood-preserving processes
                  that could generate K001 wastes. Many
                  of these facilities are more than 25 years
                  old and  some  are more  than  75 years
                  old.
  The wood-preserving  process
generally  consists  of two steps: 1)
pretreatment of the wood to reduce its
natural moisture content, and 2) impreg-
nation of the wood  with preservatives.
Drippings and condensed vapors gen-
erated during treatment are  sent to an
oil/water separator, where chemicals are
recovered and recycled to the process.
The contaminated wastewater from the
separator may be collected  in surface
impoundments,  and sludges  are
periodically removed  from  these
impoundments for offsite disposal (Figure


Waste Characteristics
  The K001 used for the incineration
tests was obtained from wood-preserv-
ing facilities. Samples of each waste were
analyzed for the constituents of interest
(Table 1). Table  2 shows the selected
parameters of the test wastes that would
affect incinerator performance.

Description of Incineration
Facilities

Pentachlorophenol Test
  The  incineration system at  the
Combustion Research Center  in
Jefferson, Arkansas, consists of a primary
combustion chamber,  a transition section,
and  a fired  afterburner chamber (Figure
2). The air-pollution-control system
includes a  venturi  scrubber and a
packed-column scrubber. A carbon ad-
sorption bed and  a high-efficiency
particulate air (HEPA) filter are used to

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                                Treatment Chemicals
                              Chemicals (Creosote and/or
                                 Pentachlorophenol)
                         Wood
                                                                          Sludges
                                                                                  *• K001
                      Figure 1. Schematic of wood-preserving process.
Table 1, Analytical Results of K001 Wastes
   Waste
  Constituent
Concentration,
   percent
 K001-PCP
  K001-C
Soil
Water
Wood chips
Organics
Soli
Water
Wood chips
Naphthalene
Phenanthrene
Fluoranthene
Other organics
     40
     30
     10
     20

     100

      30
      20
      10
       4
       3.5
       2.5
      34

     100
back up the scrubbers. The rotary kiln
was operated in a temperature range of
 980° to 1102°C and  at a  feed  rate of
 about 80  Ib/h. The  afterburner  tem-
 perature range was 965° to 1108°C. (See
 Figure 2.)

 Creosote Test
   The incineration system at John Zink
 Company in Tulsa, Oklahoma (Figure 3)
 consists of a rotary kiln with continuous
 ash removal, an afterburner,  a cyclone
 separator for solids, and an  adjustable
 venturi scrubber.  A second afterburner,
 required  by the  Oklahoma  State
 Department  of Health, followed  the  air
 pollution  equipment.  The  kiln was
 operated at 923° to  1109°C, and the
 afterburner was  operated at 1056° to
 1145°C. The feed rate was 180 Ib/h.

 Conclusions
" "  Both  the K001-PCP"lncl the  KOOT-C-
 wastes were  incinerable. The incinerator
 ash from neither test contained
  detectable volatiles or semivolatiles. The
  K001-PCP test ash contained low levels
  of arsenic, lead,  chromium, copper, and
  zinc; the scrubber water contained  low
  levels of arsenic, copper, lead, and zinc.
  The  K001-C  test  ash  contained
  moderately higher levels of arsenic and
  zinc; lead and zinc were detected in the
  scrubber  water  samples.   The
  destruction/removal efficiency standard of
  99.99% was achieved  for  both  tests.
  Based on these tests, incineration was
  promulgated on August 17, 1988, as best
  demonstrated  available  technology
  (BOAT)  for the organic  constituents  of
  K001  (naphthalene,  pentachlorophenol,
  pyrene,  phenanthrene, toluene, and
  xylenes).
    The full  report  was submitted  in
  fulfillment of Contract No. 68-03-3389 by
 j>E{  Associates,   Inc._,.__.under  the_
" sponsorship of the U.S. Environmental
  Protection Agency.
                               Table 2. Parameters Affecting Incinerator Performance

                                  Waste          Parameter                Range
                                K001-PCP
                                K001-C
                               Ash
                               Heating value
                               Water
                               Pentachlorophenol

                               Ash
                               Heating value
                               Water
                               Volatile matter
                                              12 to 51%
                                          3800 to 8300 Btu/lb
                                              8 to 41%
                                           970 to 3000 ppm

                                              10 to 35%
                                         10,000 to 11,000 Btu/lb
                                              5 to 20%
                                              57 to 81%

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Sample
ID
A
B
C
D
Site
Description
Drums
Ash Bin
Venturi Scrubber
Recirculation Tank
Sample
Description
Waste Feed Before Packing
K001-PCP Ash
Scrubber Makeup
Scrubber Blowdown
                                                                           Scrubber
                                                                            Makeup
 From
 Recirculation
,Tank
                                                                                                              Blowdown to.
                                                                                                              Storage
                                                                                                              Tanks
Figure 2. CRF rotary-kiln incineration system and sampling points.
Sample
ID
A
B
C
D
E
Site
Description
Drums
Ash Bin
Solids Separator
Water Separator
Water Separator
Sample
Description
Waste Feed During Packing
Bottom Ash
Fly Ash
Scrubber Water Before Waste Feed
Scrubber Water During Waste Feed
                                                                                                           To
                                                                                                       Atmosphere
                                         Natural
                                        Gas and
                                       Combustion-
                                           Air
                                                                                                                 Blowdown
                                                                                              Effluent Recycled to
                                                                                                   Scrubber
                                                       Bottom
  Figure 3. John Zink rotary-kiln incineration system and  sampling points

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   Fred D. Hall is with PEI Associates. lnc.,Cincinnati, OH 45246.
   Ronald J.Turner is the EPA Project Officer (see below).
   The complete report, entitled Incineration  of Creosote and Pentachlorophenol
        Wood-Preserving Wastewater Treatment Sludges," (Order No. PB 90-130
        493IAS; Cost: $23.00, 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:
            Risk Reduction Engineering Laboratory
            U.S. Environmental Protection Agency
            Cincinnati, OH 45268
United States
Environmental Protection
Agency
Center for Environmental Research
Information
Cincinnati OH 45268
Official Business
Penalty for Private Use $300

EPA/600/S2-89/060


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