&EPA
            United States
            Environmental Protection
            Agency
           Office of Solid Waste and
           Emergency Response
           Washington DC 20460
Office of Research and
Development
Washington DC 20460
            Superfund
                       EPA/540/5-88/001 Feb 1988
The Superfund
Innovative Technology
Evaluation Program:

Progress and
Accomplishments

A Report to Congress
SUPERFUND INNOVATIVE
TECHNOLOGY EVALUATION

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                                                  EPA/540/5-88/001
                                                     February 1988
      THE SUPERFUND INNOVATIVE
TECHNOLOGY EVALUATION PROGRAM

       PROGRESS AND ACCOMPLISHMENTS
                    A Report to Congress
               U.S. Environmental Protection Agency
                Office of Research and Development
            Office of Solid Waste and Emergency Response
                      401 M Street, S.W.
                     Washington, DC 20460

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                            TABLE OF CONTENTS
EXECUTIVE SUMMARY  	  v
I.      Introduction  	  1-1
       A.   Statutory Authority  	  1-1
       B.   Historical Perspective 	  1-2
       C.   SITE Program Components 	  1-3
II.     The SITE Demonstration Program  	  2-1

       A.   Selection of Technologies  	  2-1
       B.   Selection of Demonstration Sites  	  2-3
       C.   Negotiation of Cooperative Agreements 	  2-5
       D.   Community Relations Activities  	  2-5
       E.   Demonstration Planning Process  	  2-6
       F.   Program Outputs 	  2-7

III.     First Year Progress and Accomplishments  	  3-1
       A.   Demonstration Program-Project Descriptions	  3-1
       B.   Measurement and Monitoring Techniques Development  	  3-19
       C.   Technology Transfer/Clearinghouse  	  3-20
IV.     Planned 1988 Activities 	  4-1
       A.   Demonstration Program	  4-1
       B.   Emerging Technologies Program  	  4-1
       C.   Measurement and Monitoring Techniques Development  	  4-2
       D.   Innovative Development and Evaluation Program  	  4-3
       E.   Technology Transfer/Clearinghouse  	  4-5
                                            in

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                          EXECUTIVE SUMMARY
   The  Superfund  Amendments   and
Reauthorization Act of 1986 (SARA) (Section
209(b)) amends Title III of the Comprehensive
Environmental  Response, Compensation and
Liability Act of 1980 (CERCLA) by adding
Section 311 which directs the Environmental
Protection Agency to establish an "Alternative
or Innovative Treatment Technology Research
and Demonstration Program." Section 311(e)
requires EPA to submit a report to Congress
annually on the progress and results of this
program. This report presents the program's
accomplishments during Fiscal Year 1987 and
through January 30,1988.

   In response  to SARA, EPA created the
Superfund Innovative Technology Evaluation
(SITE) Program. The SITE Program is intended
to 1) accelerate the development, demonstration
and use of new or innovative treatment
technologies and 2) demonstrate  and  evaluate
new, innovative measurement and monitoring
technologies.

   During  FY 1987, the SITE Program estab-
lished a Demonstration Program,  Measurement
and Monitoring Techniques Development
Program, and a Technology Transfer Program.

   Demonstration Program. The demonstration
and evaluation of technologies developed by
private industry  have been the primary
activities of the SITE Program in  FY 1987. The
major objective of the demonstration program is
to develop reliable  performance  and cost
information of the technologies selected so that
they can be adequately considered in Superfund
decision making. Demonstrations take place at
Superfund sites or under conditions that either
duplicate or closely  simulate wastes  and
conditions found at  Superfund sites.  At the
close of FY 1987, 20 developers had been selected
to participate in the program, ten in each of two
solicitation cycles.

   Measurement and Monitoring Techniques
Development  Program. The Environmental
Monitoring Systems Laboratory in Las Vegas,
Nevada, has been supporting the development of
two monitoring/measurement techniques under
the SITE  Program: immunoassays for  toxic
substances and fiber optic sensing for in situ
analysis at Superfund sites.

   Technology   Transfer   Program/
Clearinghouse. SARA requires  that  an
information  dissemination program  be
established in  conjunction  with the SITE
Program.  During FY 1987, EPA designed a
Clearinghouse for  information on the SITE
Program and other related information on
alternative  hazardous  waste  treatment
technologies.  The Clearinghouse includes a
hotline,   an    electronic     bulletin
board/computerized data network, and a
reference library of relevant reports, books, and
articles.

   In FY 1988, the SITE Program will continue
the programs described above, and will expand
to several new  areas. An Emerging Technologies
Program  will be initiated  to  support
technologies  that are  not yet ready for
demonstration but show  high potential for
successful transition  from  conceptual to
demonstration stage. The solicitation for this
program has  already been announced  and
developers will be  selected by Spring 1988.
Another new initiative in FY 1988 will be the
Innovative Development and  Evaluation
Program which will accelerate the development
of alternative  technologies developed by EPA's
Office of Research and Development.

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                              I.  INTRODUCTION
 STATUTORY AUTHORITY

   The  Superfund  Amendments  and
Reauthorization Act of 1986 (SARA)  (Section
209 (b)) amends Title HI of the Comprehensive
Environmental Response, Compensation and
Liability Act of 1980 (CERCLA) by adding
Section 311 which directs the Environmental
Protection Agency to establish an "Alternative
or Innovative Treatment Technology Research
and Demonstration Program" and to submit a
report to Congress annually on the progress and
results of this program. As required in Section
311(e), this report presents the program's
accomplishments during Fiscal Year 1987 and
through January 30,1988.

   In response to SARA, EPA has established a
formal program  to 1)  accelerate the
development, demonstration and use of new or
innovative treatment technologies,  and  2)
demonstrate  and evaluate new, innovative
measurement and monitoring technologies. This
program  is called the Superfund Innovative
Technology Evaluation (SITE) Program.

   The overall goal of this program is to "carry
out a program of research, evaluation, testing,
development, and  demonstration of alternative
or innovative treatment technologies .  . . which
may be utilized in response actions to  achieve
more permanent protection of human health and
welfare and the environment." SARA defines
"alternative   technologies"  as   "those
technologies, including proprietary or  patented
methods, which  permanently alter the
composition  of hazardous waste through
chemical, biological, or physical means so as to
significantly reduce the toxicity, mobility,  or
volume (or any combination  thereof) of the
hazardous waste  or contaminated materials
being  treated. The term also  includes
technologies that characterize or assess the
extent of contamination, the chemical and
physical character of the contaminants, and the
stresses  imposed by the contaminants  on
complex ecosystems at sites." Under the SITE
Program,  alternative  technologies are
categorized by  their development status  as
follows:

 • Available  Alternative  Technology.
   Technologies, such as incineration,  that
   are fully proven and in routine commercial
   or private use.

 • Innovative Alternative Technology.  Any
   fully-developed technology for which cost
   or performance information is incomplete,
   thus hindering routine use at hazardous
   waste sites  An innovative  alternative
   technology requires full-scale field testing
   before it is considered proven and available
   for routine use.

 • Emerging Alternative Technology.  An
   emerging technology is one in an earlier
   stage of development; the research has not
   yet successfully passed laboratory- or pilot-
   scale testing.

   The SITE  Program  assists technology
developers in the development and evaluation of
new and innovative treatment technologies, and
thus  enhances the commercial  availability and
use of these  technologies at Superfund sites as
alternatives to land-based  containment systems
presently in use. The program consists of the
following major initiatives:

 • Conduct  and monitor  demonstrations of
   promising  innovative technologies to
   provide reliable  performance  and  cost
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   information    for    future    site
   characterization and  cleanup decision
   making.

 • Identify  and  remove informational
   impediments to the use of alternative
   technologies.

 • Develop procedures and policies  that
   encourage the use of alternative treatment
   remedies at Superfund sites.

 • Encourage the development of emerging
   technologies.

 Section 121(b) of SARA states a preference for
treatment technologies that permanently reduce
the volume, toxicity or mobility of the hazardous
waste. Section 209(b) of SARA authorizes EPA
to use hazardous waste from or representative of
Superfund  sites for alternative technology
research and demonstrations.

 The SITE  Program  also supports the testing
and development of improved monitoring and
measurement  technologies to be  used  at
Superfund sites. This component of the program
is intended to  improve capabilities in  site
assessment,  measuring  the  extent  of
contamination,  as well  as  measuring the
effectiveness of a selected remedy.

   Recognizing that access  to  accurate,
pertinent information is essential to the
acceptance of alternative technologies, Section
311(b)(8) also directs EPA to ". .  conduct a
technology transfer program including the
development,   collection,   evaluation,
coordination,  and dissemination of information
relating  to the utilization of alternative  or
innovative treatment technologies for response
actions.  . ." The statute requires the Agency to
establish and maintain a central reference
library for such  information As described later
in this  report, EPA has  established a
clearinghouse to ensure that program findings,
as well as other  treatability data,  will  be
available to the  Agency and other interested
parties.
    This report documents the progress made
prior to the enactment of SARA during Fiscal
Year 1987 and during the first quarter of Fiscal
Year 1988. It also summarizes activities planned
for  the remainder of Fiscal Year 1988. The
report includes the following:

  •  An overview of the development  of the
    program and its components.

  •  A description of the process used for the
    technology demonstration program.

  •  A description of progress  made by the
    program to date.

  •  An outline of activities for 1988.

 HISTORICAL PERSPECTIVE

    Prior to the enactment of SARA, concern had
been growing among the scientific community,
citizens, and government officials over the
effectiveness and cost of conventional methods
for  handling hazardous wastes at Superfund
sites.  Over the past few years,  it has become
evident that  land  disposal is not the  best
solution for much of the hazardous waste present
at these sites. The need for long-term, reliable,
low cost treatment solutions  has been  stressed
by studies and legislation:

  •  The  Hazardous  and  Solid  Waste
    Amendments of 1984 (reauthorization of
    the Resources Conservation and Recovery
    Act) imposed prohibitions on land disposal
    of certain hazardous wastes. These
    restrictions will require treatment of many
    Superfund wastes that previously may
    have been placed untreated into land
    disposal units.

  •  A 1985 report by the U.S. Congress, Office
    of  Technology  Assessment  (OTA)
    highlighted concerns with lamd disposal of
    hazardous wastes. It concluded that while
    land disposal is a proven technology for
    nonhazardous wastes, it is not a long-term
    solution to our hazardous waste problems,
    and that the long-term costs of land
    disposal may be quite high when the costs
    of monitoring, operation and maintenance,
    and possible future cleanup action are
    considered.

    The scientific and engineering communities
recognized that the demand for treatment often
outstripped the availability  and capability of
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existing technologies. OTA concluded in its
report that  research,  development,  and
demonstration (RD&D) devoted to innovative
cleanup technologies were inadequate.  The
Science Advisory  Board also recommended
embarking  on a  comprehensive  research
program to identify more effective, permanent
solutions.  However, the Comprehensive
Environmental Response, Compensation  and
Liability Act  of 1980 (CERCLA) directed  that
Superfund resources  be used  only to support
activities directly related to site cleanups, and
prohibited the use of funds for R&D.

   In response to these growing concerns, EPA
moved ahead in  early  1986 to develop a
technology demonstration program within the
existing statutory and  budgetary authority
provided by the Hazardous and Solid Waste
Amendments of 1984. A strategy was  developed
to lay  out the  problems, impediments,  and
possible solutions relative to the increased use of
innovative treatment technologies at Superfund
sites. EPA convened a review group composed of
experts from large  and  small companies,
academia, State governments, environmental
groups, and consulting  engineering firms  to
review and help develop this strategy.  The
review group provided  much of the rationale for
developing  a technology  demonstration
program,  citing the  need for an objective
evaluation of new technologies being marketed
to the  EPA  Regional Offices and States  for
cleanup efforts.

   EPA advertised its  first  solicitation  for
innovative treatment technology demonstration
proposals in the Commerce Business Daily on
February 13, 1986. This solicitation attracted 20
proposals  ranging from containerization  to
incineration  to robotics. In  addition,  EPA
invited developers of promising technologies
that were  already involved in hazardous
waste/Superfund demonstrations or cleanup
activities to participate in the program. EPA
staff also evaluated unsolicited proposals that
were submitted to EPA during the Spring and
Summer of 1986.

   As  a  result of this initial work on the
program, when SARA was enacted in October
1986, EPA was able to respond with a program
that was  already in the planning stages,
although funding had not been available.
SITE PROGRAM COMPONENTS
   There are a number of obstacles inhibiting
the  acceptance  and  use  of alternative
technologies for the treatment  of  hazardous
wastes at Superfund sites. These  technologies
often have not had the opportunity to be proven
effective on a commercial scale or have not been
used for specific applications at hazardous waste
sites. As  a result, it is difficult to assure
potentially responsible parties, site owners, and
the affected community that technologies which
have not undergone  full-scale  demonstration
will  be effective in remediating a site. A key
component of the SITE Program is the removal
of these informational  impediments,  by
supporting demonstrations that  will provide
reliable performance and cost data.

   To foster this comprehensive program for the
development  and acceptance of new  and
improved technologies,  the SITE Program
includes several components These include the
following:

  • Demonstration   Program.     The
   demonstration  and evaluation   of
   technologies developed by private industry
   have been the primary activities in  the
   first year of the  program  (Fiscal Year
   1987). As part  of a cooperative agreement
   between the technology developers and
   EPA, the developers provide and operate
   the  technology, and  EPA  conducts
   sampling  and analysis.  Evaluations
   normally take  place at a  Superfund site,
   EPA Test and  Evaluation facility, or  the
   developer's site.

  • Emerging Technologies Program. In Fiscal
   Year 1988 EPA will assist private industry
   in  the  development  of  emerging
   technologies from the conceptual stage to
   pilot-scale demonstration through cost-
   sharing agreements. It is anticipated  that
   these projects will  take place at the
   developer's facility or at an EPA Test and
   Evaluation Facility.
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• Innovative Development and Evaluation.
  EPA R&D staff have been active in the
  development of new technologies which
  show potential  for  application  at
  Superfund sites but where  the  private
  sector is not actively  pursuing these
  applications. This program will accelerate
  the development and demonstration of
  these technologies by quickly moving them
  to the field demonstration stage.

• Measurement and Monitoring Techniques
  Development.  EPA laboratories are
  exploring technologies that will permit
  improved assessment  of the extent of
  contamination, characterization of
  contaminants, and evaluation of
   remedial/ removal activities at hazardous
   waste sites.
 • Technology    Transfer   Program.
   Dissemination   of    data    from
   demonstrations conducted under the SITE
   Program is the key to increasing the use of
   alternative technologies at Superfund
   sites. EPA has designed and  will be
   implementing  a  clearinghouse  for
   information relevant to the SITE Program.

   The SITE  demonstration program is the
major objective of SITE and  the first
component to be fully implemented. The other
components will be fully implemented in 1988
and 1989.
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             II. THE SITE DEMONSTRATION PROGRAM
   Based  on  the  emphasis placed  on
demonstrations in Section 31 Kb) of CERCLA,
the demonstration program  has been the
primary focus of the SITE Program. The major
objective of the demonstration program is to
develop reliable  performance  and cost
information on innovative  alternative
technologies so that they  can  be adequately
considered in Superfund decision making. The
demonstrations  are designed to  provide
sufficient information to enable potential users
to make sound judgments as to the applicability
of the  technology for a specific site and to
compare the technology's effectiveness and cost
to other alternatives. The  results of the
demonstrations identify the limitations of the
technology, the potential need for pre- and post-
processing of wastes, the types of wastes and
media to which the process can be applied, the
potential  operating  problems,  and  the
approximate capital and operating costs. The
demonstrations also permit evaluation of long-
term operating and maintenance costs and long-
term risks. Demonstrations take place at
Superfund sites  or under conditions that
duplicate or closely simulate actual wastes and
conditions found at Superfund sites to assure the
reliability of the information collected and
acceptability of the data by users.


   EPA has developed implementation
procedures to ensure that the  demonstration
program facilitates developer participation,
gathers required data, and provides adequate
safeguards  for  human  health  and  the
environment. This implementation process
includes the following major steps:

  • Selection of technologies and developers
   for participation.
 • Selection of sites for the demonstrations.

 • Development of cooperative agreements
   with developers.

 • Development and  implementation of
   community relations activities.

 • Preparation of detailed plans  for  the
   demonstration.

 • Conduct of the demonstration.

 • Preparation  of  reports  on   the
   demonstration results.

   The procedures developed and the activities
that have been performed under each of  these
steps are discussed in the following sections.

SELECTION OF TECHNOLOGIES
   The solicitation and  selection processes
developed by  EPA for the SITE Program are
designed to ensure that all technologies that are
potentially  useful for cleaning up Superfund
sites are identified and screened, that those with
the  most   potential  are   selected  for
demonstration,  and that  all developers  have
access to the program.

   The primary method used by EPA to identify
privately-developed technologies for  potential
demonstration is advertisement of the annual
solicitation in the Commerce Business Daily. In
response to the solicitation, technology
developers submit proposals to EPA addressing
the following selection criteria:
 • Technology  Factors: description of  the
   technology and its history; identification of
   effective  operating range; application to
   hazardous waste site cleanup; mobility of
   equipment; capital  and operating costs;
   advantages over existing  comparable
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   technologies; and identification of health,
   safety, and environmental problems.

 • Capability of the Developer'  development
   of other technologies; completion of field
   tests; experience, credentials, and
   assignment of personnel; and capability to
   commercialize and market technology.

 • Approach to Testing:  operations plan;
   materials and equipment; range of testing;
   health and safety plan; monitoring plan;
   quality assurance plan; assignment of
   responsibilities; backup treatment system
   plan; and regulatory compliance plans.

   Two solicitation cycles have been completed.
These have been titled SITE 001 and SITE 002.
Selection of Site 001 Demonstration
Projects

   In response  to the first solicitation in the
Commerce Business Daily in February 1986,
EPA received approximately 450 requests  for
the SITE Program Request for Proposal (RFP).
The RFP was made available on March 15th and
the deadline for responses was April 25th. EPA
reviewed a total of 20 proposals by May. None of
the proposals  was considered fully acceptable.
The proposals  were categorized as "conditionally
acceptable," "rewrite," or  "not  acceptable "
Those  that were considered "conditionally
acceptable"   had   either  technical  or
administrative issues that needed to  be
addressed by the technology developer. The
"rewrites" required more extensive revision
Those  that were "not  acceptable"  offered
unproven containment technologies, failed to
submit sufficient technical data, or provided
only bench-scale data.
   In  early  July  1986,  EPA  notified the
developers  of their  proposal  status.
Conditionally  acceptable  and  rewritten
proposals were due for resubmission in August.
After reviewing the responses, the following six
vendors were considered acceptable:

  • American Combustion, Inc. (PYRETRON
   Oxygen-Air-Fuel Burner)
 • Hazcon, Inc.
   (Solidification/ Stabilization Process)

 • Shirco Infrared Systems, Inc.
   (Infrared Thermal Destruction)

 • Terra Vac, Inc.
   (In situ Vacuum Extraction)

 • Waste-Tech Services, Inc.
   (Fluidized Bed Combustion)

 • Westinghouse Electric Corporation
   (Electric   Pyrolyzer   System  and
   Pyroplasma System)

   A second method used  by  EPA to identify
SITE Program  participants  focused on
conducting evaluations  of alternative
technologies that  were  in  current use  at
Superfund sites during routine response actions
associated  with  both removal and remedial
activities.  Several projects  were identified
through this method, including:

 • The Haztech, Inc -owned Shirco Infrared
   Systems Unit at the Peak Oil  Superfund
   site in Brandon, Florida

 • Resources Conservation Company's Basic
   Extraction    Sludge    Technology
   demonstration at the  General Refining
   Superfund site in Savannah, Georgia.

 • New  York  State   Department  of
   Environmental Conservation Plasma Arc
   Unit demonstration at  Love Canal, New
   York.

 • Ogden    Environmental   Services
   Circulating Fluidized Bed Combustor on
   waste from  California Superfund sites.
 • International Waste Technology In Situ
   Stabilization/Solidification Process at the
   General Electric site in Hialeah, Florida.

 • Detox  Industries,   Inc.  Biological
   Degradation Process at a Texas site.

   In July, 1987,  Waste-Tech Services,  Inc.,
notified EPA that they were withdrawing  from
the program due to indemnification issues. At a
future date,  Waste-Tech  may decide  to
participate further in the SITE  Program.
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Selection of Site 002 Demonstration
Projects
    On  January  15,  1987,  EPA   sent
approximately 400 Requests for Proposal (RFP)
for the SITE 002 cycle to private developers who
expressed an interest in becoming involved with
the program. The SITE 002 solicitation differed
from  the SITE 001 program in that the 002
program included  requests  for  pilot-scale
technologies as well as those at demonstration
scale. Responses  to the RFP were due by  March
13,  1987. Twenty-nine proposals  were received
and were reviewed by a panel  of EPA experts.
The review panel determined that:

  • Twelve were not acceptable.

  • Three were incomplete because they did
    not specifically address the RFP and its
   criteria. They were  asked to  submit  a
   complete proposal.

  • Two were asked to rewrite their proposals

  • Twelve were considered  conditionally
   acceptable and were asked to clarify issues
   or submit additional information.

   On June 12, 1987, a letter was sent to all 29
developers notifying them of the results of the
review.  All  but the  12 "not  acceptable"
applicants were asked  to address specific
questions or provide information pertaining to
their technologies.

   The twelve proposals that were rejected
involved technologies that were already proven
as a viable alternative, or technologies that did
not meet the definition of an "alternative
technology."

   As a result of this process,  the  following
developers were selected for participation in the
SITE Program and notified in September 1987:
Thermal Technology

  •Retech, Inc

Extraction Technology

  •C.F. Systems Corporation
Solidification/Stabilization Technology

  •Soliditech, Inc.
  •Chemfix Technologies, Inc.

  •Waste Chem Corporation

  •Battelle Pacific Northwest Laboratory
Ion Exchange Technology

  •Sanitech, Inc.

Biological Technology

  •Air Products and Chemicals, Inc.

  •Zimpro Environmental Control Systems

  •MoTec, Inc.


SELECTION OF
DEMONSTRATION SITES
   Once EPA has evaluated the  technology
proposals  and  notified the developers of their
acceptance into the SITE Program,  the
demonstration site selection process is initiated.
Potential SITE demonstration locations include
Federal  and State Superfund  removal and
remedial sites, EPA research facilities, sites
from other Federal  agencies, and  developers'
sites.

   The criteria  used to screen  and select
candidate  sites for target  demonstrations
include the following:

•Compatibility of waste with technology

•Volume of waste

•Variability of waste

•Availability of data characterizing waste

•Accessibility of waste (i.e., degree of excavation
 required)

•Applicability  of demonstration to site cleanup
 efforts

•Availability of required utilities (i.e., power
 and water sources, sewers)

•Support of community, State  and  local
 governments, and potentially responsible
 parties

•Potential for  adverse effects to  public health
 and the environment.
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    In October  1986,  each of EPA's Regional
Offices  nominated Superfund sites for the
demonstration of the  following  SITE  001
demonstration projects that were brought  into
the program through the solicitation process:

  • Shirco Infrared Systems, Inc.'s Infrared
    Thermal Destruction

  • Hazcon, Inc.'s Solidification/Stabilization

  • Westinghouse  Electric  Corporation's
    Electric Pyrolysis System and Pyroplasma
    System

  • Terra Vac's In situ Vacuum Extraction

    A site was not requested for American
Combustion, Inc. since EPA's Combustion
Research  Facility  was  selected  for  the
demonstration of its PYRETRON burner

    The  Regional Offices submitted information
on the type of waste(s) for which the technology
is appropriate  and additional  desirable  site
characteristics, as provided by the developers
They also included a statement explaining why
the site was chosen.

    Nineteen Superfund sites were nominated
for consideration by the EPA Regional Offices.
The sites  were characterized  by  EPA
Headquarters in terms of a general description,
contaminants and  media  present, status  of
Superfund remediation,  presence  of  utilities,
and access  considerations  The strengths and
weaknesses of each site were compiled based on
considerations and preferences provided by the
developer and  four principal program goals.
These goals include:
• Production of the most useful information on
  each technology's capabilities

•Expeditious implementation.

•Production  of information relevant  to the
  specific site cleanup efforts.

•Involvement  of as  many EPA  Regions as
  possible in the SITE Program.

    EPA staff worked  extensively with the
technology  developers to obtain additional
information needed to match potential sites with
the technologies. EPA also coordinated with the
Department of Energy to identify possible  sites
for technologies for which no Superfund site was
nominated  During the Spring of 1987, as sites
were tentatively selected, a series of kick-off
meetings were held for each project to acquaint
the technology developer with appropriate EPA
and State officials. Visits were made  to inspect
and confirm site access,  physical layout, and
other factors. The  site selections that resulted
from this process,  or from  current cleanup or
research activities, are listed  below and are
described in further detail in Chapter III.

  •  American  Combustion, Inc. -- The  EPA
    Combustion Research Facility in Jefferson,
    Arkansas  is treating contaminated soil
    from the Stringfellow Acid Pit Superfund
    site in California.

  •  Detox Industries, Inc. -- A Superfund site
    in Conroe, Texas is being negotiated.
  •  Hazcon, Inc. -- Douglassville Disposal
    Superfund  site  in Union Township, Berks
    County, near Douglassville, Pennsylvania.
  •  Haztech, Inc./Shirco Infrared Systems, Inc.
    -- Peak Oil Superfund site in Brandon,
    Florida.
  •  International Waste  Technologies --
    General Electric site in Hialeah, Florida
  •  New   York  State  Department  of
    Environmental  Conservation  -- Love
    Canal in New York.
  •  Ogden  Environmental Services -- Ogden
    facility in San Diego, California will  treat
    wastes  from the  Stringfellow Superfund
    site and the McColl Superfund site in
    Fullerton, California.
  •  Resources Conservation Company — no site
    selected yet.
  •  Shirco  Infrared Systems,  Inc.  -- Rose
    Township-Demode Road Superfund site in
    Michigan.
    Terra  Vac, Inc  -
    Superfund    site
    Massachusetts.
Groveland  Wells
      Groveland,
in
  • Westinghouse Electric Corporation  -- no
    sites selected yet.
    EPA is in the process of selecting sites for
SITE 002 demonstration projects
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NEGOTIATION OF COOPERATIVE
AGREEMENTS
    In  order  to  implement  the  SITE
demonstration program, SARA has authorized
the Agency to enter into grants, contracts and
cooperative agreements.  Applicants whose
technologies are  selected  through  the
solicitation process negotiate with the Agency to
determine the degree of cost sharing, if any, and
the conditions of the agreement.
    Usually,  the  developer  bears  the
demonstration costs of building, locating on-site,
operating, and dismantling cleanup equipment.
EPA assists the  developer with permit
acquisition and  pays the costs associated with
sampling and analysis, quality assurance and
control, evaluating the data, and preparing
summary reports. Thus, the EPA contribution
reduces the actual cost of a demonstration
project to the developer.
   Section 311(b)(5) permits EPA to fund up to
50% of the developer's  cost  of   a  SITE
demonstration project, if the developer  shows
that it cannot  obtain appropriate  private
financing on reasonable terms sufficient to carry
out the project without Federal assistance. EPA
can provide no more than $3 million total for any
single project and no more than $10 million total
in any one year for such assistance. EPA's
guidelines  for financial assistance were
announced in January 1988  in the SITE 003
solicitation. Developers selected for the SITE
Program that desire assistance will be required
to show that a good faith effort has been made to
obtain  financing and that a financial  need
exists.

COMMUNITY RELATIONS
ACTIVITIES
   A well-planned community relations effort is
an integral  part of the  Superfund program,
including the SITE demonstration program. In
fact,  Section   311(b)(5)   requires   the
establishment of a public  notice and  comment
period prior to  the final selection of a SITE
demonstration  site.  The objective of this
community relations  program is to  actively
encourage two-way communication between
communities affected by releases  of hazardous
substances  and  government  agencies
responsible for cleanup action.  The program
enables local citizens to have input to decisions
regarding cleanup actions so that planning
reflects public concerns. At the same time, the
community relations program ensures that the
community is  provided  accurate  and timely
information about cleanup plans and progress.

   In designing a community relations program
for a particular SITE demonstration,  EPA
focuses  on the  special concerns of  the
community. The Agency has noted that the
amount  of  information available on  the
operation of each technology affects the degree
and nature of public concern. For example, some
communities  are  concerned  with  the
developmental,  unproven aspect of  the
technology and may oppose the demonstration.
Other  communities   may   support   a
demonstration irrespective of  limited data
because of their belief that the demonstration
represents progress in cleaning up the site. Some
communities may be concerned with potential
increased health risks posed by possible failure
of the technology demonstration.

   To address these  and other concerns,
community relations activities occur during all
phases of the SITE Program. Activities  began
during the first site selection process and have
continued through actual demonstrations. EPA
has prepared  and distributed  site-specific
technology fact sheets, published notices in local
newspapers, and held public meetings. Each
Regional  Community Relations Office has been
encouraged to hold at least one informational
briefing or public meeting in the community.
Public meetings have been held in Brandon,
Florida;   Rose   Township,    Michigan;
Douglassville, Pennsylvania;  Groveland,
Massachusetts; and Love Canal,  New  York.
Public reaction at these meetings has generally
been supportive of the proposed demonstrations.
   Communication with the  community
continues during the actual demonstrations.  It
may  include site tours, workshops, an  on-scene
information office,  community meetings,  and
status reports. A summary of the demonstration
results and the final report are made available
to the community.
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   Specific activities have varied  for each
demonstration. A more detailed description of
community relations activities  associated with
each demonstration  project  is included  in
Chapter III.

DEMONSTRATION PLANNING
PROCESS
   After technologies and sites  are selected, the
next step in the process is development of a
detailed design of the technology demonstration,
testing, and evaluation program. The design
includes specifications for all activities needed to
ensure that the  information objectives of the
program are met. For each demonstration, the
following must be addressed by the developer
and EPA.
  • Evaluation program  duration and
   schedule. The duration of the  testing
   program   needed  to   sufficiently
   demonstrate  and evaluate the technology,
   including estimates of the  time required
   for  test preparation, performance,
   equipment  dismantling, and  technical
   evaluation preparation.
  • Site requirements.  Utilities, certain types
   of test materials (i.e., contaminated
   liquids, soils, or sludges);  land area for
   setup; legal access to the land; proximity to
   support facilities  (i.e., machine  shops);
   geographical or geological restrictions;
   personnel support,  security provisions; and
   personnel safety provisions.
  • Detailed evaluation design.  Operating
   conditions  outside of and within the
   expected operating range; all  operating
   and control variables and their full range
   of settings; the expected influence on the
   performance  of each variable, including  a
   sensitivity analysis for each variable;
   measurements  to be taken during the
   experiment;  calibration of  all  measuring
   equipment, exclusive of sampling points
   with samples of calibration curves from
   previous activities; proposed information
   for nonmeasurement-related operating
   conditions;   data   from  previous
   experiments; detailed operating log sheets
   that  identify operating problems, system
   weaknesses, safety problems, and other
  pertinent operating information; all
  logistics and support requirements,
  including the number and training levels
  of operating  personnel, specific  utility
  requirements,   and  other  support
  information as given in the site logistics
  requirements identified above.
• Sampling and analytical program. To
  provide data  adequate to support  the
  claims for the proposed technology and to
  evaluate its effectiveness.
• Quality assurance/ quality control (QA/QC)
  program. QA/QC is  a critical element of
  each SITE demonstration because  QA/QC
  procedures ensure that data are of known
  and acceptable quality for their intended
  use. There  are  three  separate  tasks
  pertaining to the QA/QC activities:
  •   QA/QC  Audit  of the  Proposed
      Technology Testing Facility. A  QA/QC
      audit of the technology testing  facility
      is performed by EPA.  Where  the
      developer's  facility  is  used,  the
      developer makes the facility available
      to be audited by  EPA and/or EPA
      contractor(s) and provides appropriate
      assistance to them. The developer
      agrees to upgrade the testing facility
      as necessary based upon the outcome of
      the audit. A QA/QC audit is performed
      when sampling is implemented at the
      site as  well as an audit at  the
      laboratory when the samples  are
      analyzed.
  •   Preparation of a QA/QC Program Plan.
      EPA prepares a QA/QC program plan
      covering general QA/QC  goals for all
      evaluation projects. This plan serves as
      a  coordinating and format guide
      document for  the  specific QA/QC
      project  plans  prepared for each
      technology evaluation project.
  •   Preparation and Implementation  of a
      Written QA/QC Project Plan. Preparing
      and implementing  a QA/QC project
      plan is the responsibility of EPA with
      assistance from the developer.  This
      plan identifies QA/QC goals specific to
      the  evaluation of the  developer's
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       technology and is in accordance with
       EPA established requirements and
       procedures for all QA/QC activities.
^Health and safety requirements. A coordinated
 health and safety plan contains the following
 elements:
    •   Provisions for  medical  monitoring of
       operating and management personnel,
       if necessary.
    •   Safety training for personnel who will
       be in restricted zone
    •   Level   of   worker    protection
       (classification of outergarments as a
       function of the type of exposure).
    •   Establishment of zones of safety;
       "clean  area" establishment  and
       movement restrictions in various
       zones.
    •   Decontamination of personnel outer-
       garments and equipment.
    •   Emergency procedures.
    •   Supervision responsibilities.
    Seven demonstration  plans  have been
completed.

PROGRAM OUTPUTS
    There are  two  major  outputs  for each
demonstration. The  first is  a technical report
documenting the performance data  resulting
from the demonstration. The  report includes
testing procedures, data collected, and QA/QC
conducted. It summarizes the results in terms of
performance (effectiveness and reliability) and
cost. The report also addresses issues such as
applicability,  pre- and  post-treatment
requirements, and  advantages/disadvantages
compared to available technologies. EPA is
responsible for distribution  of the  report
following review and approval. The first such
report, from Haztech, Inc.'s demonstration of the
Shirco Infrared System at the  Peak Oil site in
Brandon, Florida, is scheduled to be completed
in Spring, 1988.
    Successful demonstration of a technology at
one Superfund site does not, by itself, imply that
the technology will be  adopted for full-scale use
at other  Superfund sites.  To  enable and
encourage  the  general  use of demonstrated
technologies, EPA prepares a second report that
evaluates the applicability of each technology to
other sites and wastes, and  provides cost
estimates for these  applications. This
information will  then be  disseminated to
potential users  in the form of an Applications
Analysis Report. The Applications  Analysis
Report for  each technology will be  available
approximately two  months after  the  first
performance data report.
    The development and reporting of cost data
for  the demonstrated technologies is a difficult
issue. Specific  site and waste characteristics
have a significant impact on costs. In some cases,
the SITE demonstration period comprises only a
portion of the time a process is in operation at a
site. For purposes of the two reports  described
above,  a  protocol for evaluating  SITE
demonstration costs has been developed and will
be applied to all projects  The SITE cost protocol
makes use  of both the raw variable  cost data
collected during the demonstration, as well as
the developer's  specific baseline cost data.  By
allowing the developer to specify his underlying
cost structure, the Agency  precludes  the
possibility of  misrepresenting  the cost to
potential customers. A balance  is provided by
critically analyzing the developer's costs in light
of the demonstration experience. These costs can
then be placed  within a competitive range of
similar processes. The reader will then be able to
draw  a more complete picture of the  potential
costs given a particular sites' characteristics.
    The dissemination of information  on the
performance of  technology demonstrations and
applications of the technologies is crucial once
results from  demonstration projects  are
available. If alternative  technologies  are to be
applied more broadly at Superfund sites, Agency
personnel,  engineers, and  others  must have
access to reliable technical  information. Thus,
the  technology transfer/ clearinghouse
component  of the SITE Program is intended to
provide technical  information from  the
SITEdemonstrations to interested parties in a
timely manner.  Details on the overall approach
to technology transfer in the SITE Program are
given in Chapter III
                                            2-7

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   III.  FIRST YEAR PROGRESS AND ACCOMPLISHMENTS
    During the first year of the SITE Program
(Fiscal Year 1987), EPA focused on establishing
the processes  and procedures  needed  to
implement the program and initiate activity in
several program components. Specifically, the
following were accomplished in FY 1987:

Demonstration Program

 •  SITE  001 - Twelve technologies were
    selected for  demonstrations; sites have
    been selected for nine of the technologies;
    three  demonstrations  have   been
    completed; and two more are underway.

 •  SITE 002 -  Ten developers have been
    selected to conduct  alternative technology
    demonstrations and  the site  selection
    process is underway.

Measurement and Monitoring Techniques
Development

    Support was provided to the development of
the  following two technologies:

 •  Immunoassays for toxic substances

 •  Fiber optic sensing for in situ analysis

Technology Transfer/Clearinghouse

    A long-term technology  transfer strategy
was developed and  a clearinghouse was
established that  included:

 •  A hotline

 •  An electronic bulletin board

 •  A collection  of reports, journals and other
    pertinent documents
   Progress and accomplishments in each of
these three areas are described in the sections
that follow.

DEMONSTRATION PROGRAM

   During the first year of the SITE  Program,
the demonstration program followed the process
outlined in the previous chapter. While it took
time to establish the new process, the developers
and EPA have made considerable progress. In
addition, the experience  of the first  year has
contributed  lessons  that will enable EPA to
move more rapidly in subsequent years of the
program.  Descriptions of each of the  SITE 001
and SITE 002 demonstration projects follows.

Site 001 Demonstration Project
 Descriptions

Shirco Infrared Systems, Inc.

Technology
   The Shirco Infrared  Thermal Destruction
System is a  transportable thermal treatment
unit (See Figure 1). The Shirco process  uses rows
of electrically-powered silicon carbide rods to
bring the  waste to combustion temperatures.
Remaining combustibles are destroyed in an
afterburner.

   The full-scale four-component system can
process from 100 to 250 tons  of waste per day,
depending on the waste characteristics. The first
component, the primary furnace, is lined with
layers  of lightweight ceramic fiber blanket
insulation. The furnace generates temperatures
up to 1850°F using infrared radiant  heat
provided by horizontal rows of silicon carbide
rods (located above the conveyor belt). Waste
moves through the primary furnace on a woven
                                          3-1

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Figure 1.   Transportable Infrared Thermal Unit

wire mesh belt. The second component, an
infrared or gas-fired secondary combustion
chamber, is capable of reaching temperatures up
to 2300°F. The secondary chamber destroys
gaseous volatiles from the primary furnace. The
third component consists of an emissions control
system which removes particulates in a venturi
scrubber.  Acid vapors are neutralized in a
packed tower scrubber, and an induced draft
blower draws cleaned gases from the scrubber
into the exhaust stack. The fourth component
consists  of  a process  management  and
monitoring control center.
Progress and Accomplishments
   Shirco  Infrared   Systems,
participating in two demonstrations.
Inc.,
       is
Demonstration One. Full-Scale System

   Site Selection   EPA contracted  with
Haztech, Inc , of Atlanta, Georgia, to incinerate
approximately 7,000  cubic yards of waste oil
sludge contaminated with  polychlorinated
biphenyls (PCBs) and lead. In November  1986,
Haztech began setting up a full-scale, mobile
thermal processing system, owned by Haztech
but manufactured by  Shirco Infrared Systems,
Inc. In early 1987, the SITE Program sought to
include this technology in the demonstration
program and to  monitor and  evaluate the
performance of this system during the cleanup
operation.

   Community  Relations.   As part  of
community relations activities for the removal
action, EPA distributed a notice to the local
community of the  upcoming action and held an
openhouse  at  the  town hall.  The  public
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expressed little interest in the planned removal
activities.

   Demonstration  Status.   The  first SITE
demonstration involving Haztech, Inc.'s Shirco
Infrared System was conducted at the Peak Oil
Superfund site in Brandon, Florida, on July 31
through  August 5, 1987, during a removal
operation by EPA Region IV

   In February 1987, SITE contractors began
preparing a demonstration plan, which included
the test and quality assurance plans. The  main
components  of the demonstration were to
evaluate the reliability of the performance of the
unit for the destruction of PCBs and validate the
manufacturer's claim that the  lead compounds
could be converted from a soluble to an insoluble
form by the Shirco process  In addition to the
standard trial burn tests, the  demonstration
would attempt to establish a material balance
for the unit,  identify products of incomplete
combustion (PICs), and  assess reliability and
operational factors.

   By June, the  unit was  operating  at
approximately 100 tons per day and was ready
for  performance testing.  The  on-site
demonstration and testing of the  infrared
system began on July 31 and continued through
August 5, 1987. EPA SITE staff and contractors
were present to observe and collect data  During
the week, the SITE project team conducted a
trial burn (three 8-hour  runs), and extensive
sampling, including solid waste feed, stack gas,
furnace ash, scrubber  liquid  effluent, scrubber
water influent, scrubber effluent  solids, and
ambient air. All operating conditions during the
runs were  documented. By  mid-October, the
phase of the removal action involving the use of
the infrared system was completed  A total of
7,000 cubic yards of waste material had  been
processed.

   In addition to the  sampling data described
above, the report on  the demonstration will
document the entire mechanical  operating
history  of the  system and  the  problems
encountered in operating this type  of full-scale
system.  This  documentation should  be
particularly useful to other users of innovative
technologies.  A final  technical report on the
demonstration is scheduled to be completed in
Spring, 1988.

Demonstration Two. Pilot-Scale System

   Site Selection.  The pilot-scale infrared
destruction system is a portable one-ton per day
version of the system described above, housed in
one trailer. The site identified for the evaluation
of the portable pilot-scale  Shirco unit was the
Rose Township - Demode Road Superfund site in
Michigan. The Rose Township dump site is a 20-
acre  site  used to  bury and dump drums of
various solvents and paint sludges. The  drums
were removed in 1980, but the contaminated soil
contains high concentrations of organics, PCBs,
and metals, principally lead. EPA chose the Rose
Township site for the following reasons:

  • Successful destruction  of PCB-containing
   waste provides a  good indication  of
   thermal destruction efficiency

  • The Michigan Department of Natural
   Resources, which has the  lead for  site
   cleanup, is interested in determining the
   fate of metals in  thermal  treatment
   systems

  • The draft feasibility study identified
   thermal treatment as a potential remedy;
   therefore, the  demonstration will have
   direct application to the  final cleanup
   remedy selection. (The Record of Decision
   has since selected thermal destruction).

   In addition, it is  anticipated that this
demonstration was intended  to  determine
whether the treatment will fuse the lead in the
waste to the ash, thus reducing the potential for
lead  leaching out of the ash over time and the
potential for lead emissions in the stack gas.

   During   the   development  of   the
demonstration plan, EPA  worked  with the
Michigan Department of Natural Resources
(DNR) to identify all regulatory requirements
that apply to this demonstration. The Michigan
Air Pollution Control Commission issued a
permit to  Shirco  Infrared Systems,  Inc. to
proceed  with  the test program  for the Shirco
unit. The Michigan  DNR   waived  the
requirement for hazardous waste construction
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and operating permits based, in part,  on the
short duration of the test.

   Community Relations. On June 30 and July
1,  1987, the  State of Michigan held an  open
house, followed by a public meeting on both the
planned demonstration and the draft feasibility
study for the Superfund cleanup. Approximately
30 townspeople attended and expressed general
support for  the demonstration.  The  public
comment period ended on July 29, 1987, with no
serious issues raised. EPA  performed  an
environmental review and the State of Michigan
reviewed   the   project   through   the
intergovernmental  review. Thus,  EPA and the
Michigan  Department of Natural Resources
decided to  proceed  with  the  planned
demonstration in the  Fall of 1987.  Public
visitors' days were held on October  31  and
November 4, 1987.

   Demonstration  Status.  The demonstration
took place November 2-13, 1987. The pilot-scale
infrared thermal destruction  unit treated about
ten cubic yards of contaminated soil The project
utilized a  blend of the most highly  PCB- and
lead-contaminated  soils at the site. During the
first  three days of testing, EPA conducted
detailed sampling of solid waste feed, stack gas,
primary furnace off-gas, furnace ash, scrubber
liquid effluent,  scrubber  water  influent,
scrubber effluent solids, and  ambient  air
During the  remaining six days  of operation,
Shirco varied several operating parameters, and
EPA sampled furnace  ash, furnace off-gas,
scrubber effluent, and stack emissions  In
particular, the test investigated the effect of
varied operating conditions on the fate of lead in
the system.  The stack discharge from the  unit
was  monitored closely  to determine  the
effectiveness of the technology and to ensure the
health and safety of individuals in and  around
the project area. A final technical report on the
demonstration is scheduled to be completed in
June 1988.

American Combustion, Inc.

Technology

   American Combustion, Inc. (ACI),  has
developed the PYRETRON, an oxygen-  air-fuel
burner, which  can be  fitted onto   any
conventional combustion  unit for burning
liquids or solids and sludges (See Figure 2).

   Pure  oxygen in combination with air and
natural gas is combusted in a proprietary burner
to destroy liquid hazardous waste. Solids and
sludges can be coincinerated when the burners
are used  in conjunction with a rotary kiln or
similar equipment. The use of oxygen allows a
higher burning  temperature (up to  4500°F as
compared  to  a maximum of 2400°F in  a
conventional burner)  without the addition of
excess air. Using less air is advantageous
because the nitrogen in air takes away heat,
puts a greater load on the air pollution control
equipment, and requires a longer retention time
in the combustor  before the waste is fully
incinerated. The higher temperatures also
ensure more complete incineration of the wastes,
thereby increasing the destruction and removal
efficiency and reducing stack gas emissions. The
rate of waste through-put is also increased, thus
reducing unit costs.

   The PYRETRON burner is a proprietary
design which employs advanced fuel injection
and mixing  concepts to provide faster ignition
and more thorough burning of wastes. Burner
operation is computer controlled to automati-
cally adjust the amount of oxygen according to
sudden changes in  the heating value of the
waste

Progress and Accomplishments

   Site Selection.   Prior to the initial SITE
solicitation, the American Combustion, Inc.,
PYRETRON burner was selected for research at
EPA's bench-scale facility at Research Triangle
Park. The proposal from American Combustion
was subsequently accepted and a demonstration
at the larger-scale  EPA Combustion Research
Facility (CRF)  in  Jefferson,  Arkansas, was
planned.
   Contaminated soil from the Stringfellow
Acid Pit  Superfund  site in California is being
burned during the demonstration at the CRF.
The Stringfellow site is a 17-acre remedial  site
in a California canyon that was used as a dump
for industrial wastes from World War II to the
early 1980s. The site contained about 20 unlined
ponds into which were dumped waste acids
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Figure 2.   Pyretron ™ Oxygen Enhanced Burner

containing metals and organics. In addition to
some five dozen organic compounds, a large
amount of sulfuric acid was deposited at the site.
The  surface liquids  have been removed,  but
contaminated soils and rock remain. Chemicals
from the site have leached into the  drinking
water supplies of the nearby town, Glen Avon.
Wells  have been installed  at the site for
pumping water to an on-site treatment plant
California has the lead in cleaning up the site
and is considering thermal treatment; thus the
demonstration will have direct application to the
feasibility study the State is preparing

   Community Relations. EPA and the State of
California have developed and distributed
information to the community to introduce the
SITE Program. At a Stringfellow public meeting
held in July 1987, EPA addressed the excavation
of wastes for the demonstration and the  role of
the SITE  project in  the overall remediation
process. A public  visitors' day was  held on
November 20, 1987
   Demonstration Status. The demonstration of
the PYRETRON  burner began November 16,
1987, and is scheduled to be completed by the
end  of January  1988  The objective of the
demonstration tests is to  provide  data to
evaluate three ACI claims:
1)  The PYRETRON System  reduces  the
   magnitude of the transient high levels of
   organic emissions, carbon monoxide,  and
   soot ("puffs") that occur with repeated batch
   charging of waste to the rotary kiln.
2)  The PYRETRON  System  is capable of
   acheiving  the RCRA-mandated 99.99
   percent destruction and removal efficiency
   (DRE) of principal organic  hazardous
   constituents in  wastes  incinerated  at a
   higher waste feedrate than for conventional
   air-only incineration.
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Figure 3.    Hazcon's Truck-Mounted Solidification/Stabilization System
3)  The PYRETRON system is more economical
    than conventional incineration.

    It is anticipated a final technical report on
the  demonstration  will  be completed in
July/August 1988.


Hazcon, Inc.

Technology

    The Hazcon solidification/stabilization
process uses a patented nontoxic chemical blend
which  Hazcon  claims encapsulates organic
molecules  and renders  them ineffective in
retarding or inhibiting solidification. The wastes
are then mixed with pozzolans (such as fly ash,
kiln dust, or portland cement) and  water to
immobilize  and bind the  contaminants into a
hardened concrete-like mass. The encapsulated
material attains compressive strengths between
1000 and 5000 psi. It is nearly impermeable,
denser than concrete, and only slightly porous.
The Hazcon  process utilizes  mobile field
blending units. These units, mounted on trucks
or trailers (See Figure 3), consist of soil and
cement holding bins, a chloranan feed tank, and
a blending auger  to mix all of the components.
Water is added as necessary,  and the resultant
slurry is transferred to molds.

Progress and Accomplishments

    Site Selection.  The Douglassville  Disposal
Superfund site located in Union Township,
Berks   County,   near   Douglassville,
Pennsylvania, was chosen as the demonstration
site for the Hazcon technology. The 50-acre site
is  an abandoned  oil recovery facility on the
floodplain  of the Schuylkill  River.  The  site
includes two large lagoons once filled with waste
oil  sludges and  subsequently  drained  and
backfilled with soil, an oily filter cake disposal
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area, an oil drum storage area, and an area
where waste oil sludge was land-farmed into the
soil. More  than 250,000 cubic yards of soil may
be contaminated with a wide variety  of
constituents including volatile organics,  PCBs,
and lead. A Record of Decision  was signed in
1985 approving capping and diking of a portion
of the  site.  However, additional engineering
work is ongoing  to consider the possibility of
treatment.

   EPA chose the Douglassville site for the
Hazcon demonstration for the following reasons:

  • It is relevant to the remedial analysis of
   the site.

  • The developer requested a site containing
   oily wastes.

  • It provides an opportunity to demonstrate
   fixation of both high concentration organic
   and metal-bearing wastes

   Community Relations.  A public  notice and
comment period was held during August with a
public  meeting held on September 9, 1987. An
environmental review was performed and the
State of Pennsylvania was given an opportunity
to comment on  the  project  during its
intergovernmental review The public comment
period ended  with no significant comments
raised. A public visitors' day was held on
October 14,1987
   Demonstration Status.  The  demonstration
took place October 13-16, 1987. The primary
objectives of the demonstration were to evaluate
reduced contaminant  mobility and the integrity
of the solidified soil mass. Wastes from six areas
of the site were  chosen for the  demonstration
Five cubic yards of each of the  six feedstocks
were processed, two to three feedstocks each day,
with the  last day being  an  extended run
processing 25-30 cubic yards.  Samples  were
taken from the untreated soil feedstocks and
from the blended slurry for analysis after seven
days of curing. The solidified blocks were buried
and core samples were taken  after 28 days of
curing. The samples were analyzed  for soil
characteristics, teachability,  permeability,
unconfined    compressive     strength,
microstructure  changes, and  contaminant
levels. A final technical report is scheduled to be
completed in May 1988.

Terra Vac, Inc.

Technology

   Terra Vac, Inc., has developed a process for
the in situ vacuum extraction of volatile organic
compounds (VOCs) from soils and groundwater.
The major functional parts of the system are a
subsurface extraction well and a vacuum pump.
The capacity of the vacuum pump and the depth
of wells used at a site are dependent on  the
subsurface  conditions  (i.e.,  soil   type,
stratigraphy, groundwater depth) and the
chemical characteristics of the contaminants
(i.e., vapor  pressure, solubility). The vacuum
induces a negative pressure gradient in the well,
which propagates laterally (10 feet to more than
100  feet depending on soil conditions),
volatilizing  liquid and adsorbed VOCs (See
Figure 4). The gases migrate through the  soil to
the area of lowest pressure (the well), where
they  are extracted and  pulled through
separation tanks and  an air emission control
technology apparatus before being discharged to
the atmosphere. Various air emission control
technologies include  activated carbon
adsorption,  thermal oxidizers,  catalytic
oxidizers, or simple dispersion stacks.

   The process has been applied to a wide range
of volatile compounds  such  as chlorinated
organic solvents  The process is capable of
removing volatile contaminants from the vadose
zone, the layer of soil below the surface and
above  the  water table.  Terra Vac can use
existing monitoring wells,  if they are properly
constructed, and Terra Vac's process can also be
used for groundwater recovery and treatment, if
necessary.

Progress and Accomplishments

   Site Selection.  The site chosen for this
demonstration is the  Groveland Wells
Superfund site, Groveland, Massachusetts. This
site contains two municipal wells along with the
surface water and groundwater that supply
them. Vall'ey Manufactured Products Company,
Inc., a  machine shop at the site, is one of three
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Figure 4.    Terra Vac, Inc.'s In-Situ Vacuum Extraction Process
potential sources  of soil and  groundwater
contamination  resulting from  surface and
subsurface disposal  of solvents and cutting oils
A two-acre area containing 2000  to 3000 cubic
yards of soil  is contaminated  with volatile
organic  compounds, principally trichloro-
ethylene, with lesser concentrations of 1,2-trans-
dichloroethylene and tetrachloroethylene

    EPA chose the Groveland site for the Terra
Vac, Inc., demonstration because of the desirable
depth of the watertable and relevance to  the
ongoing feasibility study. For example, most of
the contamination at the facility  occurs above
the water table and beneath a concrete slab
which is being used  as a  storage platform. Thus,
as  part of the feasibility study, EPA  is
considering in situ treatments such as soil-
flushing and  vacuum extraction because
excavation of soil beneath the facility would be
difficult due to space constraints,  the proximity
of local residents to the site, and the potential for
health and safety incidents. The demonstration
is expected to provide data on the feasibility and
cost effectiveness of in situ vacuum extraction as
a possible alternative treatment of VOCs at the
Groveland site

   Community Relations.  On July 16, 1987,
EPA  Region I  issued a  public notice  of the
proposed demonstration and announced a public
meeting for July 29.  Fifteen citizens and local,
State, and Federal officials  attended;  the
reaction  was generally supportive  of  the
demonstration.  An environmental review was
performed and both the State of Massachusetts
and Puerto Rico reviewed the project during the
intergovernmental review. A public visitors' day
was held January 15, 1988.


   Demonstration Status. The demonstration
plan has been completed. The demonstration site
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                                                                               STAGE
Figure 5.   Circulating Bed Combustor Unit

preparation began November 30 and continued
until December 18,  1987. Field work resumed
January 4, 1988. The demonstration officially
began January 8,  1988, and is expected to last
through April. The demonstration is to provide
data to evaluate in  situ vacuum  extraction of
VOCs in the soil beneath a building at the site.
The test  will  measure the ability  of the
technology to reduce the level of contaminant
concentration in the soil. Four extraction wells
have been  drilled at  the edge  of the
contamination zone;  three of the wells are acting
as barrier wells and intercept  VOCs that would
normally be drawn to the main extraction  well.
The vacuum  extraction system  is operating
continuously  (24 hours per day). Samples
collected  and  analyzed daily  include: soil gas;
process gas  (from  various  locations  of the
vacuum system unit); activated carbon, liquid
from the vapor/liquid  separator; and stack gas
emissions.
                                             COOLING
                                             WATER
Ogden Environmental Services, Inc.

Technology

   Ogden Environmental Services, Inc., has
developed a circulating bed combustor (CBC), an
improvement over traditional fluidized bed
combustion because  it yields  improved
performance and simpler operation (See Figure
5). The improvements arise in part from an
increased  fluidization of  the bed  in the
combustion chamber  (greater turbulence) and
the reinjection  of solids removed from the
combustion gas.  Stated advantages over other
types  of thermal  units  include  lower
temperature of operation, reduced NOx and CO
generation, simplicity of solid/liquid/auxiliary
fuel feed, and better  contaminant  removal.  In
particular, the system has achieved very high
destruction  and removal  efficiencies  for
halogenated organics and other acid-containing
wastes.
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    In the Ogden system, waste  material and
limestone,  a neutralize!", are fed into  a
combustion chamber  along  with  recirculating
bed material from a hot cyclone. The materials
travel at a high speed through the combustion
chamber  to the cyclone,  where  solids are
separated from the hot gases,  which pass
through a convective  cooler  and baghouse filter
before being exhausted to the atmosphere.

Progress and Accomplishments

    Site Selection.  Wastes from two California
Superfund sites, Stringfellow and McColl, were
originally scheduled to be  taken  to Ogden's
facility in San Diego for the  demonstration. The
Stringfellow  site has already been described.
(See American Combustion, Inc.,  Technology
description.) The McColl site, in Fullerton,
California, covers 9.5 acres,  bordering both the
Los Coyotes  National Park  and a golf course
Pits at  the  McColl site  were used to dump
asphalt, tars, and drilling muds from oil
production and refining from 1942 to 1962. The
resulting wastes are a mixture of very oily,
odorous substances and  soils containing high
levels of organics and  sulfur.  The original
Record of Decision signed in  1983 recommended
off-site  disposal  but the  State  and EPA are
reevaluating the remedy options.

    The State was already considering using the
Ogden  combustor to  run  treatability tests on
these wastes as part of their  feasibility study, so
EPA offered to evaluate these tests under  the
SITE Program. Both of these wastes have a high
sulfur content. This acidic  characteristic will
test the circulating bed combustor's ability to
neutralize waste, thus minimizing corrosion and
extending the unit's operating life. Wastes from
both sites have been excavated and are awaiting
shipment to the Ogden facility pending the
issuance of a local use permit from San Diego

    Community Relations.   Public comment
periods and hearings were held prior to issuance
of Federal, State and local permits. EPA and the
State of California developed and distributed in-
formation to the communities surrounding the
two Superfund sites to  introduce the  SITE
Program and address the role of the SITE project
in the overall remediation process.
   At the McColl site, the EPA Regional office
meets periodically  with a community action
group. At a May  1987  meeting, the Regional
staff discussed burning McColl waste during the
Ogden demonstration Once the local use permit
is issued to Ogden, the Region intends to develop
a fact sheet on the demonstration for  the
community.

   Demonstration Status  On March 30, 1987,
EPA  Region IX issued an RD&D permit to
Ogden to operate the  CBC. The California
Department of Health Services has also issued a
hazardous waste facility operating permit to
Ogden  Environmental Services, Inc.  On
December 8, 1987, the San Diego City Council
voted 7 to 2 to deny the issuance of a local
conditional use permit to Ogden. As a result, the
Ogden transportable CBC will be used for an on-
site demonstration at  a Superfund  site   Site
selection is presently underway

Resources Conservation Company

Technology

   BEST (Basic Extraction Sludge Technology)
is a patented solvent extraction-type process for
dewatering and deoiling hazardous sludges and
contaminated soils (See  Figure 6). BEST
employs  the  unusual inverse miscibility
properties of aliphatic amines (soluble in water
below room temperature and insoluble above) to
break difficult-to-handle emulsions  and
suspensions. Sludges  that resist physical/
mechanical concentration are easily separated
by  BEST  into three distinct  fractions:
dischargeable water, reusable oil/organics, and
dry, oil-free solids. Heavy metals are isolated by
conversion to hydrated oxides, which precipitate
out and exit the process with the solids fraction.

Progress and Accomplishments

   Site Selection. During early  1987, the BEST
system was in use as part of a removal action at
the General Refining  Superfund site near
Savannah, Georgia. EPA recognized this as an
opportunity  to evaluate the performance  and
reliability of the technology under the SITE
Program. Unfortunately, the removal operation
was completed in early March 1987, before funds
were available  for  the SITE evaluation
contractor.  The  developer  is currently
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Figure 6.    Basic Extraction Sludge Technology Field Equipment Program
negotiating the use of BEST for a remediation
action at another Superfund site which could
provide  an opportunity  for  a technology
demonstration.

Community Relations. The BEST demonstration
has not reached the level of planning to warrant
community relations activities as  no site has
been selected

    Demonstration Status.  On November 19,
1987, more data from the remediation action at
the General Refining  Site near Savannah,
Georgia, were received. Based on the evaluation
of these data, Resources Conservation Company
was officially accepted into the SITE Program on
December 2, 1987

International Waste Technologies

Technology

    International  Waste Technology's (IWT) in
situ stabilization/solidification  process  utilizes
proprietary chemicals and a unique soil mixing
technology which precludes the need  for soil
excavation.  IWT  claims  that the process
generates a complex crystalline connective
network of organic polymers in a two-step
reaction. The first reaction is reported to produce
chemical bonding between the IWT chemicals
and the ions and neutral organics present in the
soil. The  second reaction involves building
macromolecules which are generated over a long
period of time

   The method for injecting the chemical into
the soil involves a  widely  used Japanese
technology which utilizes a hollow drill with
helical blades  containing injection ports  (See
Figure 7)  The drill is advanced into the ground
to the desired  depth. The chemical  additive is
then  injected at low  pressure  to  prevent
excessive spreading and is blended with the soil
as the drill rotates The treated soil forms a solid
vertical column  Soil columns overlap to ensure
all the  soil is adequately treated The  soil
surface is then covered with a layer of asphalt to
protect the solidified mass from rain and water
erosion.

Progress and Accomplishments

    Site Selection. IWT's in-situ stabilization/
solidification  process  demonstration  is
tentatively scheduled to occur during  a test of
the process at  the General Electric (GE) site in
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Figure 7.    International Waste Technologies' In-Situ Stabilization/Solidification Process
Hialeah, Florida. About 7000 cubic yards of soil
are contaminated with  PCBs  which  were
disposed of on-site.  Because this is not a
Superfund site, but a private developer site, the
demonstration is currently awaiting a decision
by GE to proceed with the cleanup.


   Community Relations.  There  have been no
  EPA-sponsored  community  relations
  activities for this SITE demonstration as this
  is a private clean-up at a non-Superfund site.


   Demonstration Status.  Both EPA and  IWT
  are  fully  prepared   to   conduct  the
  demonstration. A delay has been encountered
  because General Electric has  not committed to
  a project start date. The general objectives of
  the demonstation will  be  to evaluate the
  ability of the method to immobilize PCBs and
  the uniformity and integrity of the in situ
  solidified soil mass

Detox Industries, Inc.

Technology

    Detox Industries, Inc., has developed  a
biological process for the degradation of targeted
organic contaminants in a water/sludge/soil
matrix through the application of proprietary
naturally occurring nonpathogenic organisms.
The process involves the accelerated growth of
these microorganisms and eventual inoculation
into the soil or other matrix in which the waste
is contained Nutrients and catalysts are added
to the matrix to enhance the microbial activity.
Subsequent inoculations of microorganisms,
nutrients, and catalysts are added over time on
an  as-needed basis. The  result  is a systematic
biodegradation  of the  contaminants over  a
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Figure 8.   Detox Industries Process Treatment Tank with Waste Being Treated
relatively short period of time (usually two to
four months). Detox claims that the process can
be applied on-site in soil or sludge as well as in
open tanks where depth of contamination makes
in situ treatment impractical (See Figure 8)

    Byproducts of metabolic consumption are
carbon dioxide, water, and cell protoplasm. Once
the contaminants have been biodegraded, the
microorganisms die due to the lack of adapted
food source,  leaving nonhazardous cell
protoplasm behind, which in turn acts as  a food
source for  the  indigenous  microorganisms
present in the matrix.

Progress and Accomplishments

    Site Selection.  EPA selected the United
Creosote  Superfund site, a wood  preservation
facility in Conroe, Texas, for the technology
demonstration. The company  used  a pressurized
treating process employing pentachlorophenol
(PCP) and creosote. Creosote was produced on
the site from the distillation of coal tar and is a
sticky substance consisting mainly of polycyclic
aromatic hydrocarbons (PAHs). The PCP was
not produced on-site but was stored in above-
ground tanks. The total site comprises 100 acres
and contains two large waste ponds which were
used to treat or dispose of the creosote  wastes.
Leaching from ponds is  causing a plume of
contaminated groundwater. The pond area has a
temporary soil cover installed by EPA to divert
runoff. There are approximately 85,000 cubic
yards of soil contaminated with PCPs, PAHs,
dibenzofurans, and chlorinated dioxins.  The
wood preserving facility was demolished in 1975
and the property was  sold, half for business
development  and  half for  residential
development.

   EPA  Region VI is coordinating with the
Texas Water Commission on a nine-month study
to explore  treatment technologies that may
permanently clean up the  site Biodegradation
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and contaminant desorption (soil washing) are
two possible alternatives.

   The contamination at the  sites consists
entirely of organic chemicals which potentially
can  be destroyed  by the  biodegradation
technique.  It  is  anticipated  that this
demonstration  will provide EPA and the State
with useful and timely information for the site
cleanup.

   Community Relations.  The surrounding
community will be  given the opportunity  to
comment on the proposed demonstration in the
near future.

   Demonstration Status.  The  treatability
study plan is  undergoing final review. The
revised demonstration plan is scheduled to  be
completed by the end of January 1988. An access
agreement for  the treatability study has been
obtained, and this study is tentatively scheduled
to begin in February 1988. The demonstration is
planned for May through September 1988


Westinghouse Electric Corporation

Technology

   Westinghouse has developed two thermal
technologies to be demonstrated  in the SITE
Program -- the Pyroplasma  System and the
Electric Pyrolyzer.

   The Pyroplasma System  is based on the
concept of pyrolyzing waste molecules using a
thermal plasma field.  The unit  has been
developed to destroy liquid organic waste  by
dissociation to its component elements. The
heart of the destruction system is a plasma torch
(See Figure 9). The system  uses 800 kW  of
electric  power across a  colinear  electrode
assembly to produce an electric arc in a medium
of dry low pressure air. The intense energy
causes  the air  stream  to become ionized,
producing a thermal plasma with temperatures
ranging from 5,000 to 15,000°C.

    Liquid waste  is injected directly into the
plasma where the  hazardous molecules are
broken down to their atomic states in an oxygen-
deficient atmosphere. The atoms then recombine
according to  chemical kinetics to produce
hydrogen, carbon monoxide, nitrogen, hydrogen
chloride, particulate carbon and small amounts
of carbon dioxide, ethylene, and acetylene. The
product gas is scrubbed with  caustic soda to
neutralize and remove acid gas  (HC1)  and to
remove particulate carbon. The scrubber fluid is
used once. The remaining gas is drawn off by an
induction fan and flared. The unit can process 2
to 3 gallons per minute.

    The entire  system is process  computer
controlled The computer updates temperature,
pressure,  flow,  fluid reserve, and other
performance parameters while providing
continuous online monitoring of the process. The
computer  is  programmed to  shut  down  the
process in the event  of deviation from  set
parameters. Onboard monitoring of bulk  gas
constituents  in the off-gas is provided. The
entire unit is contained in a 48-foot trailer.

    The Electric  Pyrolyzer is a mobile  system
designed  to  thermally destruct hazardous
organic wastes, without combustion (See Figure
10)  The  system operates  a rapid transfer of
energy to  waste materials  causing dissociation
of organic molecules into individual atoms. The
destruction of wastes is accomplished  without
oxidation and the  associated generation of
products of incomplete combustion (PIC).

    The Electric  Pyrolyzer will accept  a wide
range of waste types including both  liquid  and
solid waste. The prototype system is designed to
process 5 to  20  tons per  day of solid waste
containing up to 10% (by  weight) organics  and
up to 25% (by weight)  water. Input  materials
may range in size from fine powders and sludges
to large solids (< 4 inches in diameter).

    The Electric Pyrolyzer is designed to operate
at temperatures  up to 3250°F. Residence times
for  materials in the gaseous and liquid phases
are fully  controllable by the operator.  Thus, a
wide range of destruction  efficiencies may be
achieved,   depending   on  regulatory
requirements.  The  resultant products  are
vitrified solids and clean off-gas.


Progress and Accomplishments

    Site Selection.  No  Superfund site has yet
been selected for either demonstration.
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                                                Process Gas

                                                Heated process gas
Plasma column

Electrodes
Figure 9.  Schematic of Westinghouse Plasma Torch

   Demonstration  Status.    Currently,
Westinghouse has both units at their Waltz Mill,
Pennsylvania facility  for further modifications
and testing. Westinghouse is  also  awaiting
issuance of an RD&D permit by EPA. EPA plans
to observe  and/or collect data from  the
Westinghouse testing  Upon successful
operation of  the  units, EPA  will  select
Superfund sites for  the SITE demonstrations of
each unit, which could  occur in mid-1988 if
Westinghouse's testing indicates the  units are
operational and ready for Field demonstration.

New York State Department of
Environmental Conservation (NYSDEC)

Technology

   The New  York  State  Department of
Environmental Conservation (NYSDEC)  and
EPA established a cooperative agreement in
1982 for the construction and testing of a mobile
                 plasma arc system for the destruction of liquid
                 hazardous wastes. The project consisted of four
                 phases:

                     Phase I    Design and construction of the
                               unit by  NYSDEC's contractor,
                               Pyrolysis Systems, Inc.

                     Phase II:   Performance testing of the  unit
                               at the  Kingston, Ontario,
                               Canada test site.
                     Phase III:  Installation  of the  plasma arc
                               system   and   additional
                               performance  testing at a site  in
                               New York

                     Phase IV:  Demonstration  testing  as
                               designated by NYSDEC at a
                               New York hazardous waste site.

                     The first two phases were completed  in
                 Canada by  April  1986  Refer   to  the
                 Westinghouse Pyroplasma  System (described
                                          3-15

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Figure 10.   Side View of the Westinghouse Electric Pyrolyzer
previously) for a description of the plasma arc
system.

Progress and Accomplishments

   Site Selection. In accordance with Phase III
of the EPA/NYSDEC  agreement, New  York
State chose the  Love Canal site for testing the
unit. Perimeter drains installed around Love
Canal have been intercepting underground
water (leachate) for treatment. Oily sludges are
separated from the leachate and stored on-site.
It is these  sludges, containing 200  to 300
different chemicals, including dioxins and many
chlorinated organics, that will be destroyed in
the plasma arc unit.

   Community Relations.  Since  1982,
NYSDEC  has held  regular  public meetings
involving  Love Canal and has  discussed the
plasma arc  at  several;  one meeting was
dedicated solely to the use of the plasma arc on
Love Canal waste. In May 1986, NYSDEC held a
weekend open house where the community could
walk through the mobile plasma arc unit and
talk with  State  and  contractor  staff;
approximately 300 to 400 people attended The
NYSDEC has an office located at Love Canal,
with two  full-time employees dedicated to
community relations. One of the office functions
is to publish regular notices and a quarterly
newsletter on site activities, including the status
of the plasma arc demonstration. New York has
chosen to follow the State Environmental
Quality Review  Act which requires a public
hearing on this demonstration project.

   Demonstration Status.  In October 1986,
EPA accepted the plasma arc demonstration into
the  SITE Program. New York has the  lead in
cleaning up the site and has decided to meet all
substantive technical permit  requirements,
including complying with RCRA, the New York
State air  regulations,  the New York State
Pollution Discharge  Elimination  System
regulation, and drafting an environmental
impact statement. EPA is assisting NYSDEC in
developing these documents. Based on receiving
the approvals,  the demonstration is planned for
the Spring of 1988.

Site 002  Demonstration Project
Descriptions

   SITE  002  Projects were accepted  into the
SITE Program in September 1987, and site
selection is underway. EPA's Regional Offices
                                           3-16

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have recommended sixteen sites to be considered
as demonstration locations.


Retech,Inc.

    Retech, Inc., offers a technology that uses a
centrifugal  reactor with  plasma heat to
decompose organics  in a mixed solid and liquid
feedstock. The solid  components are melted and
cast or granulated  for  disposal. The volatile
compounds are vaporized and decomposed in an
afterburner heated by plasma heat in an oxygen-
enriched atmosphere. The  off-gases from the
afterburner are.treated for removal  of fine
particles and scrubbed.

    During the process, solid and liquid wastes
are fed steadily through a hollow trunnion  into
the spinning reactor well. A plasma torch, with
the arc transferred to a conducting spindle, adds
energy to the feedstock. The spinning  motion
spreads out the charge;  the plasma heat turns
liquids into  gas, and  solids  into  glassy or
metallic liquids.  The temperature  of the
condensing phase is so high that no combined
carbon can remain.  If the melt is metal, it may
dissolve some carbon. The  condensed phase
accumulates  in the centrifugal reactor bowl.
When removal of  the condensed phase is
desirable, the reactor is tilted by a hydraulic
mechanism and the "slag" is poured into a
cooling mold. The  scrubber water contains
enough caustics to tie up halogens in the off-gas.
Almost all the scrubber water is recycled, adding
enough makeup to keep dissolved solids below
the saturation level.


C.F. Systems

    C.F.  Systems offers a solvent extraction
technology that uses liquefied gases near their
critical conditions as solvents to remove  organic
constituents from sludge, solid, or liquid  wastes.
The proposed  solvents have lower viscosities and
higher diffusivities, allowing  more favorable
rates  of mass transfer than other solvent
extraction  processes. The patented processes
include a combination of liquefied gas extraction
with vapor recompression and conventional
distillation  to recycle  the solvents and
concentrate  the  organic constituents in an
effluent  stream. The  effluent  stream  may
require further treatment prior to land disposal.

Soliditechjnc..

   The Soliditech solidification process uses the
concept  of  microblending   and  micro-
encapsulating  hazardous  waste materials.
Microblending is used  to thoroughly  mix the
reagent, URR1CHEM, with the waste stream.
Microencapsulation occurs by cross-linking the
organic and inorganic particles during a  five-
phase cementation process, coating the large
particles with pozzolanic materials, and  by
sealing the matrix containing micropores and
spaces. The reagent formula can be modified  for
the treatment of a specific waste thus optimizing
the chemical reaction and resulting character of
the solidified waste.

Chemfix Technologies

   The Chemfix fixation/stabilization process is
based on the use of soluble silicates and silicate
setting agents. The combination and proportions
of reagents are optimized for each particular
waste requiring treatment. Three classes of
interactions can be described:

•A reaction  between  soluble silicates and
 polyvalent metal ions, producing  insoluble
 metal silicates.

•A reaction  between  soluble silicates and
 reactive components producing a  gel structure.

•Hydrolysis, hydration, and neutralization
 reactions.

   The Chemfix process may be  useful for the
reduction in toxicity of high molecular organics
(BNA and  PAHs) and the immobilization of
metals.

Waste Chem Corporation

   Waste Chem Corporation has developed a
mobile volume reduction  and solidification
system, designed to decontaminate and solidify
liquids,  sludges, or  dried  soils. The system
consists of a two-stage process:

1) A fluidized waste stream feed and an asphalt
   stream are  simultaneously  fed to  an
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    extruder-evaporator unit. The waste-asphalt
    mixture is discharged into a 55-ga!lon drum
    where solidification is allowed to take place.
    The extruder is heated indirectly causing
    constituents to volatilize.

 2) Organic volatiles are then scrubbed with a
    caustic solution and condensed  volatiles are
    stored in a tank where further  treatment is
    provided by  ozonation. Residues from the
    ozonation tank as  well  as uncondensed
    volatiles  are  filtered through carbon
    absorption filters. These filters  may need to
    be incinerated prior to land disposal.

Batelle Pacific Northwest Laboratory

    The Battelle Pacific  Northwest Laboratory
has developed an in situ vitrification technology,
a thermal  treatment process which converts
contaminated soil or sludge into a chemically
inert, stable glass and crystalline product.
Because the soil is  not electrically conductive
once the moisture  is driven off, a conductive
mixture of flaked  graphite and glass frit  is
placed among the electrodes to act as a starter
path. An electrical potential is applied  to the
electrodes establishing  an electrical current.
The graphite starter  path is  eventually
consumed  by oxidation and the  current  is
transferred to the  soil  which is  electrically
conductive in the molten state. As  the vitrified
zone grows, it incorporates nonvolatile elements
and destroys organic components by pyrolysis.
The pyrolized products migrate to the surface of
the vitrified zone where they may oxidize in the
presence of oxygen. A hood is placed over the
processing area to confine  any  combustion
products. All gases are then drawn into an off-
gas treatment  system.  This  process  was
developed primarily for vitrifying nuclear waste
at the Hanford-Department of Energy facility in
Richland, Washington.

Sanitech,Inc.

    Sanitech, Inc., has developed a technology
that uses ion-exchange-like materials to process
and selectively remove toxic heavy metals from
contaminated groundwater or surface waters.
The new materials are stronger and  more
abrasion resistant than resins. They operate
over a wide pH range,  have high absorption
capacities, and  appear unaffected by most
organic contaminants  and changes  in
temperature or pressure.

   A series of compounds, selective to one or
several similar metals, have been developed by
the substitution of electrophilic groups onto the
benzene ring of catechol-type siderophore.
Metal-contaminated water can  be  passed
through a bed of the coated  particles,  during
which time the  metal is selectively removed
from the water. A method has been developed to
chemically attach  the  compounds to silica
spheres. In all past  experiments, the selected
captured metal  ions have  been completely
recovered from the bed material by  acid
treatment.  The  bed material  has  been fully
regenerated for reuse.

Air Products and  Chemicals, Inc.,
(Formerly Dorr-Oliver)

   This technology offers a mobile biotreatment
technique for treating aqueous waste containing
hazardous and toxic organic substances.  A fixed-
film  fluidized-bed biological reactor contains
either an inert media or activated carbon as the
fluidized media. Pure oxygen is predissolved and
totally consumed  in the process thus  limiting air
stripping of  volatile organics. The  use of
activated carbon  as  the media in the Oxitron
Activated Carbon  System  improves  the
treatment capabilities of the basic Oxitron
system. Components which are   easily
biodegradable are rapidly converted to  carbon
dioxide  and water.  Organic compounds  are
adsorbed on the  carbon,  producing  an effluent
consistent with conventional activated  carbon
treatment.  Compounds  which degrade more
slowly,  however, are eventually  converted
biologically.

Zimpro Environmental Control Systems

   Zimpro Environmental  Control Systems
offers a powdered activated carbon treatment
(PACT)  process  using a biological treatment
process. In  the PACT process,  powdered
activated carbon  is added to the aeration basin
at a dosage  that varies  depending  on  the
biodegradability  and adsorptive characteristics
of the waste material. Treatment effectiveness
                                           3-18

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depends on the carbon dosage applied and other
process parameters such as the  hydraulic
retention time of the wastewater in the aeration
basin, the solids residence time of the carbon and
biomass, and the carbon concentration  in the
aeration basin.

Motec, Inc.

    MoTec, Inc., offers a three-stage aerobic
organic waste  biodegradation process.  In the
first stage, water and emulsifiers are mixed with
contaminated sludges or soils. In  the second
stage, after the organics have been  solubilized,
the mixture  is transferred to a batch digester,
where  acclimated seed bacteria are added  and
aerobic biological oxidation occurs. The third
stage  is  a  biological step where target
concentration levels of organics  are achieved.
The technology is known as liquid/solids contact
digestion. The  system uses portable tanks or
lined in situ earthen digesters.

MEASUREMENT AND MONITOR-
ING TECHNIQUES DEVELOP-
MENT
    One of the components of the SITE Program
is the demonstration and development of  new
and innovative measurement and monitoring
technologies  which will  be  applicable to
Superfund site characterization. There are  four
important  roles  for   monitoring  and
measurement technologies at Superfund sites:
(1) to assess the extent of contamination at a site
(remedial investigation and for the Hazard
Ranking System), (2)  to  supply data  and
information to determine impacts on human
health and the environment (exposure and  risk
assessment), (3) to supply  data  to select the
appropriate remedial action (feasibility study),
and (4) to monitor the success or effectiveness of
the selected remedy.
    KFA  has  been  involved  with  the
development and  evaluation  of monitoring
methodologies  practically since its inception.
EPA monitoring research has focused primarily
on the application  of existing technologies to
support its monitoring requirements. EPA has
been conducting research and development
projects concerning  geophysical instru-
mentation, monitoring well design,  sampling
strategies, site characterization, groundwater
flow and contaminant transport modelling, soil
sampling, and vadose zone monitoring, among
other areas.

    With the enactment of SARA, EPA has been
supplied with a mechanism specifically aimed at
supporting monitoring needs at Superfund sites.
The Environmental  Monitoring  Systems
Laboratory in Las Vegas, Nevada  (EMSL-LV)
has been supporting  the development of
improved measurement and monitoring
techniques in  conjunction  with the SITE
Program,  with  a focus on two  areas:
immunoassays for toxic  substances  and fiber
optic sensing for in situ  analysis at Superfund
sites.


Immunoassay Program

    EMSL-LV's  research  on immunoassays for
toxic substances actually began prior to the
enactment of SARA. Laboratory  researchers
were  initially interested  in  the  use of
biomarkers in exposure and risk assessment. In
FY 1987, two requests for information (RFI)
were published in the Commerce Business Daily
soliciting input  from industry concerning the
State  of  the  technology of biomarkers  and
immunoassays.  As a result of the  responses to
the RFIs, two meetings were  held  in FY 1987
during which industry was invited to present the
status of their research

    The application of immunoassays to
environmental monitoring  is still  in  the
developmental stage and has  received support
from the SITE Program. During the first year of
the SITE Program, EMSL-LV has  initiated
efforts in the following areas:

  • Participation in the development and
    evaluation of a monoclonal antibody-based
    immunoassay  for pentachlorophenol.
    Results of  the initial testing  of the
    monoclonal antibody assay,  although
    promising, were not  up to  expectations
    because of prevailing irreproducibility  of
    antigen binding to   commercial plates.
    Subsequent  research indicates that this
    problem can  be overcome and  will allow
                                          3 19

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   relative standard deviations of less than
   10% for repetitive analysis.

 • Submission of two requests for information
   to the Commerce Business  Daily. One
   requested information concerning general
   advancements  in    immunoassay
   technology  and  biomarkers. A number of
   innovative  approaches were  brought
   forward from the commercial sector.
   EMSL-LV has attempted to function as a
   catalyst to encourage the interaction
   necessary to advance the field, particularly
   for field screening  applications. The
   second Request  for Information was
   directed toward  advanced analytical
   methods  specifically  for  benzene,
   ethylbenzene, toluene, and phenol. As a
   result of that solicitation, a cooperative
   agreement is  being negotiated  with
   Westinghouse  to develop monoclonal
   antibody assays for these chemicals.

 • Initiation  of an interagency agreement
   with the U.S. Department of Agriculture
   to develop monoclonal antibodies and
   immunoassays  of mutual  interest for
   monitoring programs

 • Negotiation of an  interagency agreement
   with the California  Department of Food
   and Agriculture for  EMSL-LV to develop
   sample preparation  techniques for
   environmental  matrices which will  be
   compatible with   immunoassays. If
   consummated, activities will begin by mid-
   FY 1988.
 • Negotiation of  cooperative agreements
   with  scientists at  the  University of
   California,  Berkeley and Davis campuses,
   to develop monoclonal antibodies and
   immunoassays for selected compounds of
   interest to Superfund for  which the
   commercial  sector has  shown  little
   interest.

Fiber Optics Program
   EMSL-LV embarked on a program in 1982
to determine the feasibility of using fiber optic
sensing to monitor  groundwater. The program
was a fragment of the Lawrence Livermore
National Laboratory  sensor development
program, and it led to the development of
lightweight portable instrumentation, a sensor
for organic  chloride detection, a sensor for pH
and, most importantly, an abundant interest in
and new ideas for  other  fiber optic based
chemical sensors. EPA is joined in fiber optic
sensor research by the National Oceanic  and
Atmospheric Administration, National
Institutes of Health,  U.S. Geological  Survey,
Department of Defense, Department of Energy,
National  Bureau  of Standards,  National
Aeronautics and Space Administration, and the
industrial community.
   In FY  1987,  EMSL-LV  applied  SITE
resources to its fiber optic sensor program.  The
fiber optic chemical sensor  for chloroform  (the
primary tri- halomethane component) that has
been under development for about three years
has been significantly improved over the last six
months.  The latest modifications and calibration
studies  have permitted  measurement of
chloroform  concentrations in soil  gases above
contaminated groundwater with confidence that
the sensor response was linear between 2 and 12
ng/ml. The reproducibility at 6 ng/ml in the field
was + 10%, which exceeded that of the portable
gas chromatograph being used for verification in
the field. In addition, the sensor results were
obtained in only 10 to 20% of the time required
for the  chromatographic results.  The latest
modifications have resulted in a more sensitive
and rugged sensor which can be reliably loaded
with sensing  reagent in about  10 seconds.
However, the  sensor is presently limited to
making measurements in the gas phase.
TECHNOLOGY TRANSFER/
CLEARINGHOUSE
   The technology transfer program initiated in
November 1987 to support the SITE program is
composed of three major components:

  • a  hotline,  incorporated  into  the
   RCRA/CERCLA hotline

  • an electronic bulletin board, using the
   office of Solid Waste and   Emergency
   Response  (OSWER) Technology Transfer
   Bulletin Board

  • a collection of reports, journals, and other
   documents.
                                          3-20

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   The hotline provides callers with up-to-date
information on SITE projects, demonstration
schedules, and  the availability of data on
demonstration results. It also serves as a
referral source for callers, providing them with
information on other resources available in the
area of innovative hazardous waste treatment
technologies. These resources  include other
databases  on relevant topics,  such as  the
Hazardous Waste Control Technology Database
and  individuals with particular areas of
expertise.

   The information available  through  the
hotline has also been placed on the office of Solid
Waste and  Emergency Response (OSWER)
Technology Transfer Bulletin Board. Users  can
access the bulletin board through a personal
computer and obtain information on the SITE
Program and other databases.

   Finally, the EPA  Library maintains a
Hazardous Waste Collection which makes  key
documents available through the EPA library
network. This Collection contains reports, books,
EPA policy and guidance directives, legislation
and regulations, periodicals,  and a listing of
commercial  databases  containing  hazardous
waste information. The database is accessible
using a  personal computer, and provides
automated search and retrieval capability by the
following access points:  keyword or subject
heading, abstract, title, author, sponsoring
organization or office, project manager's name,
or contract number. Documents related  to
innovative treatment technologies have been
added to the collection and reports  on SITE
demonstrations will be  added as they become
available.

   A  one-page  flyer   describing  the
clearinghouse has been distributed to  potential
users at appropriate meetings and conferences.
The flyer outlines the three components of the
clearinghouse and methods of gaining access to
each.

   The  Clearinghouse  on  Alternative
Hazardous Waste  Treatment Technologies was
designed and initiated  by  an  Implementation
Committee composed of representatives from
relevant EPA Headquarters, Regional offices,
and Laboratories. This committee will continue
to oversee  the  implementation  of the
Clearinghouse and plan for its future activities.
                                           3-21

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                        IV.  PLANNED ACTIVITIES
   The goal of the SITE Program in Fiscal Year
1988 and beyond is to expand  its scope by
furthering the development of technologies that
are at  the proof of concept  stage  and require
additional developmental assistance to reach the
field demonstration stage. In addition, the
program will continue to support the evaluation
of technologies provided by private industry  at
the pilot- and full- scale. Technologies developed
by EPA also will be accelerated to  the field
demonstration stage.


DEMONSTRATION PROGRAM

   The  first  year of the SITE  Program
concentrated its efforts and resources on the
Demonstration  Program.  Since SARA
Section209(b) requires initiation of at least ten
field demonstrations per year, this component of
the program will continue  to be the primary
focus  in  the coming years. At this time, 20
developers have been accepted into the  SITE
Program in the  first two solicitation cycles, and
it is anticipated that between  10 and 15 new
ones will be added in 1988.

   In 1988, site selection and other steps will be
undertaken for SITE 002  projects,  and
demonstrations  of remaining SITE 001 projects
will occur. Reports on the performance, cost and
applicability of  these technologies will also be
published as the demonstrations are completed.
The solicitation for SITE  003 projects was
announced  in  January 1988.  Under this
solicitation, EPA will permit co-funding  of
demonstration projects  for the first time. This
provision allows up to 50% cost-sharing by EPA
of the total estimated cost of the demonstration
not to exceed a total of $10 million per year or $3
million for  any given project. To qualify,  the
developer must demonstrate that  it cannot
obtain private financing on reasonable terms
and conditions that is sufficient to carry out the
demonstration.
EMERGING
PROGRAM
TECHNOLOGIES
   In FY 1988, the first Emerging Technologies
Program solicitation was issued. It is expected
that  this solicitation, like the Demonstration
Program, will be issued annually in the future.
For 1988,  projects will be selected  that offer
solutions to critical disposal and treatment
problems at Superfund sites, have high potential
for the successful transition from conceptual to
demonstration  stage, and  show a major
commitment or capability by the developer to
commercialize the technology.

   This Emerging Technologies Program will
foster the further development of technologies or
approaches  that are not  yet  ready  for
demonstration.  The goal is to ensure that a
steady stream of more cost-effective technologies
will  be ready to be demonstrated, thereby
increasing the number of viable  alternatives
available for use in Superfund cleanups.

   The Emerging Technologies Program will
deal  with innovative technologies for recycling,
separation, detoxification, destruction, and
solidification/stabilization of  hazardous
constituents   and   material   handling
technologies. Candidate technologies must show
promise at the bench/laboratory  scale. This
program will enable technology developers to
advance from the bench/laboratory  to pilot scale
through cooperative funding with EPA.
                                           4-1

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   New candidate technologies will be added as
they become  available if they  appear to be
extremely  promising  and rank high on  a
comparative  evaluation using established
ranking criteria. Flexibility must be built into a
program such as this that deals with emerging
technologies.

   The first solicitation  for  the  program
appeared in the Commerce Business Daily on
September  17, 1987. The program  was also
advertised  in trade or professional  journals,
newsletters, and at conferences. The Request for
Proposals was available on November 15. Pre-
proposals were due on December 15, 1987. A
total of 84 were received. Those developers
selected to prepare full proposals will have until
May 16, 1988 for submission.

   The funding mechanism to be used for the
Emerging Technologies  Program  is  the
competitive  cooperative  agreement. The
maximum length of the cooperative agreements
within this  program will be two  years.
Maximum funding per project will be $300,000
total and $150,000 per year. EPA will fund part
or all  of an emerging technology project
development. The developer must show progress
after the  first year  before EPA will consider
funding for a second year.

   Proposal evaluation criteria will incorporate
both technical and cost-sharing considerations,
such as technical description of the technology,
description  of the proposed project, summary of
data results to date,  estimated  resources
(funding) needed for test project,  company and
personnel experience, and value of technology to
Superfund program.

   Thus, when proposals are technically equal,
the degree of developer cost sharing will affect
selection.

    It is anticipated that there  will be 5-10
awards in FY  1988.

MEASUREMENT AND
MONITORING TECHNIQUES
DEVELOPMENT
    Future monitoring  and measurement
technology efforts will include:
 • Development  and demonstration  of
   immunoassay  and fiber optic sensor
   technology.

 • Identification of private  entities which
   have  monitoring  technologies  to
   demonstrate, specifically for monitoring in
   the saturated and vadose zones.

 • Consideration of identified technologies
   that can be used to determine the physical
   and chemical character of contaminants.

 • Consideration of identified technologies
   that can be used to measure and  monitor
   the stresses imposed by contaminants on
   complex ecosystems at  Superfund sites.

 • Coordination with other ORD laboratories
   to identify existing and planned research
   which may be useful  for environmental
   monitoring at Superfund   sites and
   considered under the SITE Program.

 Immunoassay research  plans for  FY 1988
include:

 • Evaluation of monoclonal antibody-based
   immunoassays for benzene, ethylbenzene,
   toluene, and phenol.

 • Continuation  of the  evaluation of the
   immunoassay  for  pentachlorophenol
   initiated in FY 1987.

 • Depending on the results of the above
   evaluation,  demonstration  of the
   pentachlorophenol immunoassay  at  a
   Superfund site.

 • Compilation  of a  list of EPA priority
   compounds for potential   immunoassay
   applications.

 • Investigation  of  currently available
   standard delivery systems to determine
   potential use for Agency  monitoring
   activities.

   Plans for fiber optics research include
developing it for aqueous  phase measurements
in order to extend its application to  in  situ
groundwater  monitoring.  With adequate
improvements in sensitivity, other potential
applications for the chloroform sensor would be
monitoring trihalomethanes in drinking water.
                                           4-2

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Other FY 1988 goals include the development of
several  compound-specific sensors, for
compounds such as gasoline, aviation gasoline
(JP-4), and trichloroethylene.

   The laboratory intends to integrate its
immunoassay techniques with the ongoing fiber
optics research. Applying these tools jointly  in
Superfund site assessment will serve as a means
to cross check and validate data generated by
each method.
INNOVATIVE  DEVELOPMENT
AND EVALUATION PROGRAM

   Over the  past few  years, EPA's office  of
Research and  Development has been developing
alternative technologies for the destruction and
cleanup  of hazardous waste. These  efforts
complement the SITE program. Several of these
technologies are approaching  the  field
evaluation and  demonstration stage  and
research on these technologies has progressed to
a point where regional requests  have been
received to  apply  these technologies  to
Superfund wastes.  After the technologies are
satisfactorily demonstrated on these Superfund
wastes, it is expected that technologies will be
commercialized  and marketed by private
industry. The Technology Transfer Act of 1986
simplifies the government-industry partnership
necessary to bring these in house technologies to
market. It is expected that market risk will be
reduced and  development  accelerated by
conducting field evaluations and, in some cases,
field demonstrations under the SITE program
The  SITE Program  will  also  actively
disseminate  information concerning these
technologies.  Some of these technologies are
discussed below.

EPA Mobile Incinerator System

   The  mobile  incinerator consists  of
specialized equipment mounted on four trailers.
The first trailer contains the rotary kiln,  in
which organic  wastes  are vaporized  and
partially oxidized at approximately 1800°F with
a nominal retention time up to 60 minutes.
Incombustible treated  soil/ash is discharged
directly from the kiln. The volatile organic
compounds or gases from the primary  unit  or
first  trailer pass through the secondary
combustion chamber (SCO in the second trailer,
where oxidation is completed at a temperature of
2200-2400°F and a retention time of 2.2 seconds.
The flue gas exits from the SCC and is cooled
from 2200°F to  approximately  190°F by a
venturi quench elbow. The gases then pass into
air pollution control equipment on the third
trailer. There, submicron- sized particulates are
removed by a wet electrostatic precipitator, and
byproduct acid gases are neutralized in an
alkaline scrubber. Gases are drawn through the
system by an induced draft fan, which maintains
an overall vacuum to ensure that no toxic gases
escape from the system. The cleaned gases  are
discharged from  the system through a 40 foot
high stack. The incinerator can process 9,000
pounds of contaminated soil or 75 gallons of
liquid per hour.

    System performance  is monitored through
instruments and automatic safety shutdown
controls. Additionally, the system is manually
monitored and thus can be shut  down by an
operator.

    Upon request from EPA Region VII,  the
Mobile Incineration  System  (MIS) was
transported to the James Denney Farm site in
McDowell,  Missouri,  in 1985. The MIS
demonstrated  a  greater than 99.9999%
destruction and removal efficiency (DRE) at a
trial burn on liquids and solids contaminated
with dioxins and has been operated over the past
two years  for cleanup of dioxin-contaminated
liquids and soils at the site and from numerous
other dioxin sites  in southwest  Missouri. To
date, over 2 million pounds of solids and 18,000
gallons of liquids have been processed.

    The unit is currently processing the
remainder of the dioxin-contaminated materials
at the  Denney Farm site and may soon be
processing EPA's office of Pesticide Programs
cancelled pesticides, including  2,4,5-T/Silvex
liquids and solids.

EPA Mobile Soils Washing System

    The Mobile Soils Washing System has been
designed for the extraction of a broad range of
hazardous materials from spill-contaminated
soils using water as the extraction solvent. The
system will: 1) treat excavated contaminated
                                           4-3

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soils, 2) return the treated soil to the site and 3)
separate the extracted hazardous materials from
the washing fluid for further processing and/or
disposal. The prototype has been developed
utilizing conventional equipment  for screening,
size  reduction, washing, and dewatering of the
soils. The washing-fluid water  may contain
additives,  such as acids, alkalies, detergents,
and  selected organic solvents to enhance soil
decontamination. The nominal processing rate is
4 yd-Vhr of contaminated soil for soil particles
less  than 2 mm in size, and up to 18 yd3/hr for
soil of larger particle size.

EPA  Mobile  Carbon  Regeneration
System

   The Mobile Carbon Regeneration  System
was  designed for field use in reactivating spent
granular activated carbon used in spill or waste
site  cleanup operations. Using the process of
adsorption in  which the  molecules  of one
substance  adhere  to the surface of another, the
mobile carbon  regenerator  provides an
important means of removing dissolved  organic
hazardous  material from  water.  When
contaminated granular activated  carbon (GAC)
is  heated in the kiln, organic substances are
desorbed and volatilized. All vapors and gases
from the kiln flow through a duct into the
secondary combustion chamber where an excess
oxygen level  is maintained.  Temperature and
residence  time  are controlled  to  assure
desorption/detoxification of hazardous organic
substances, including chlorinated  hydrocarbons.
off-gases are water-quenched and  scrubbed with
an alkaline solution before being vented to the
atmosphere. Stack gases and used process water
are monitored.

KPEG Chemical Detoxification

   The KPEG process has been developed as a
method to dechlorinate toxic organochlorine
compounds, i.e., PCBs, dioxins, and furans. In
the process, potassium hydroxide reacts  with
polyethylene  glycol to form an alkoxide.  The
alkoxide in turn reacts initially with one of the
chlorine atoms  on the aryl  ring to produce an
ether and potassium chloride salt. In some
KPEG reagent formulations, dimethylsulfoxide
(DMSO) is added as a cosolvent to enhance
reaction rate kinetics.

   The mobile field equipment comprises a
2,700-gallon batch reactor mounted on a 45-foot
trailer equipped with a boiler and cooling system
and a laboratory control room area.

   The KPEG process has been used to detoxify
wastes generated at a  wood- treating site in
Butte, Montana. This waste was generated as an
oily phase of groundwater and, after separation
by decantation, contained  approximately 3%
pentachlorophenol (PCP) in a diesel-like oil. The
PCP-oil waste contained homologs of chlorinated
dibenzodioxins (CDDs)  and  chlorinated
dibenzofurans (CDFs) ranging from  147  ppb of
tetra- to 84,000 ppb of the octa-congeners. The
data indicate that after processing, all CDDs and
CDFs were destroyed to concentrations below
detection limits, which were, on the average,
less than 1 ppb.

   In another application, the equipment was
transported to  a  Superfund site in  Kent,
Washington, where it successfully processed
7,550 gallons spent solvent containing an oily
waste with a high moisture content (28%), total
chlorides of 20,700 mg/1, and a 2,3,7,8-
tetrachlorodibenzo-p-dioxin (2,3,7,8-TCDD)
content of 120 ppb. No 2,3,7,8-TCDD  was
detected at levels higher than the detection limit
of 0.3 ppb in any of the processed batches.

   More  recently, a 40-gallon  reactor  was
evaluated on PCB-contaminated liquids and
soils at the General Electric Moreau site in
Glens Falls, New York.  As a result, a 2.1 yd3
reactor was  constructed  and will be tested in
January 1988 at the U.S. Navy Public Work
Center in Guam on soil and sludge contaminated
with PCBs, ranging from 2000 to 4500 ppm. This
testing is a cooperative effort between EPA and
the U.S. Navy.  Following successful testing of
the KPEG reactor in Guam, the unit  will be
further tested and evaluated at the Wide Beach,
New York, PCB Superfundsite and  eventually
will be used  to treat PCB- contaminated oil and
soil in Butte, Montana.
                                            4-4

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TECHNOLOGY TRANSFER/
CLEARINGHOUSE

   Over the next several years, the SITE
technology transfer  program  will  move
increasingly toward immediate access to
information by telephone or computer linkage.
Users will be able to obtain answers to questions
concerning alternative technologies  by
telephone  or  via computer hookup with
EPAdatabases. The information available  will
include up-to-date status reports on individual
SITE projects and final reports on those that
have been  completed,  information on  other
alternative technologies, and  information on
relevant conferences and publications.

   A major focus of Clearinghouse activities in
1988 will be outreach to potential users. A
brochure describing the Clearinghouse will be
mailed to potential users.  In addition, EPA will
implement a feedback system to ensure that the
information provided by  the  Clearinghouse
meets users' needs, is timely, and is accurate.
                                           4-5
                                                               r US GOVERNMENT PRINTING OFFICE 1988 548-010/80018

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