United States
                                     Environmental Protection
                                     Agency
                                   EPA/540/MR-94/510
                                   April 1994
                                    SUPERFUND INNOVATIVE
                                    TECHNOLOGY  EVALUATION
                                     Demonstration  Bulletin

                           In Situ Steam Enhanced Recovery Process

                                   Hughes Environmental Systems, Inc.
Technology Description:  The Steam  Enhanced Recovery
Process (SERP) is designed to remove volatile compounds such
as halogenated solvents and petroleum hydrocarbons, and semi-
volatile compounds from contaminated soils in situ.  The vapor
pressures of most contaminants will increase by the addition of
steam, causing them to become more volatile and mobile.  The
technology operates through wells drilled  in the contaminated
soil.  Injection wells deliver high pressure steam (15 psig) to the
soil,  while extraction  wells draw a vacuum on  the soil.  The
pressure gradient drives the steam, water, and vaporized con-
taminants to the extraction wells where they can be removed for
disposal or recycling.  Figure 1 illustrates  the operation of  the
process beneath the soil surface.

A site to be treated with in situ SERP must have predominantly
medium to high permeability soils.  A geological confining layer
below the treatment depth and a confining layer above the treat-
ment zone help  to contain  the flow of steam.  Injection  and
extraction wells are arranged on the site in a pattern designed to
promote  even  distribution of the  steam.  Site-specific  factors
determine the number of wells used, their  arrangement  on  the
site, their construction, and the above-ground process equipment
to be used.

A full-scale SERP system with 35  injection  wells  and 38  extrac-
tion wells was used to treat a 2.3-acre area of soil up to 40 feet
dee.p at the Rainbow Disposal site in  Huntington Beach, Califor-
nia.  This site was contaminated with  diesel fuel'compounds.
Water for steam generation was pumped from an on-site deep
water well, treated by ion exchange and the addition of  chemi-
                                 Extractlon of Vapors
                                    And Liquids
                                (to treatment systems)


                         EXTRACTION*
                           WELL
                       DEPTH
                     INTERVAL OF
                     TREATMENT
                  cals, and heated in one of two natural gas-fired steam boilers.
                  High pressure steam was delivered to all the injection wells using
                  a manifold system.  Air-lift pumps were used to remove accumu-
                  lated oily water from the extraction wells, and a vacuum pump
                  maintained a negative pressure on the soil  and removed the
                  vapors from each extraction well.

                  The  heated  liquid (condensate) from  the extraction wells was
                  routed to a heat exchanger used to pre-heat the boiler feedwater,
                  and then treated in a gravimetric oil/water separator. The diesel
                  phase from the separator was collected in a storage tank. The
                  remaining  water phase was then treated further using filtration
                  and  activated carbon before being discharged directly to  an
                  underground storm sewer.   Liquids and particulates entrained in
                  the extracted vapor were removed using a knock-out drum. The
                  vapor stream was then treated in a thermal oxidizer unit which
                  used electrical heating to oxidize the vapor before discharging it
                  through a stack to the atmosphere.

                  The full-scale SERP system used at the Rainbow Disposal site
                  was  operated for  approximately two  years.   The system was
                  operated for 16 hours a  day, 5 days a week for the first year. A
                  24-hour  cycle of operation, 6  days a week was used for the
                  remaining  year.  During most of the treatment, steam injection
                  and vacuum extraction were used simultaneously. Vacuum ex-
                  traction alone was used when the boilers were  inoperable, during
                  interim soil sampling activities, and at the end of the remediation.
                  Vacuum extraction used alone after steam injection is expected
                  to  dry and cool the soil and  remove  contaminants from lower
                  permeability soils.

                       !            Injection of High Quality Steam
                       ;                 (from boilers)
                                                INJECTION
                                                  WELL
                                                                      Steam Front (moving
                                                                        through soil)
Vapor, Water and Contaminants
                                                                                            INJECTION
                                                                                            INTERVAL
                                                 CONFINING LAYER (e.g., day layer)
Figure 1. Conceptual operation of the SERP process beneath the soil surface.
                                                                                               Printed on Recycled Paper

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Demonstration Approach: The U.S. EPA Superfund Innova-
tive Technology Evaluation (SITE) program became involved with
th« la situ SERP technology developer after  the system was
Installed at the Rainbow  Disposal site.  Pre-treatment soil sam-
pling and analyses occurred prior to full SITE program participa-
tion.  Therefore, the focus of the  Demonstration was on  the
condition of the soil after treatment to determine if the technology
met the she-specific cleanup criterion of 1,000 mg/kg  (ppm) of
total petroleum hydrocarbons (TPH, diesel).  An economic analy-
sis of the system was also a primary objective for the Demonstra-
tion.

Before treatment, one to four samples from each of twelve bore-
holes within the defined perimeter of contamination were sampled
by the technology developer and analyzed for TPH and benzene,
toluene, ©thyfoenzene, and xylenes (BTEX).  The pre-treatment
results will be used by the SITE Program in a non-critical evalua-
tion of the removal efficiency of the treatment.

The SITE program (EPA) performed post-treatment soil sampling
and  analyses,  Including  sampling  from boreholes adjacent to
(within four feet)  and at the same depths as those sampled before
treatment.  Additional samples at other depths were collected in
most of these boreholes.  Twelve additional boreholes were also
sampled, including six outside the defined perimeter of contami-
nation for a total of 24 boreholes. Samples collected after treat-
ment were analyzed for TPH, BTEX, and total  recoverable
petroleum hydrocarbons (TRPH). Six sets of triplicate samples
were  collected at randomly determined sampling  locations to
assess soil contaminant spatial variability. The data collected from
post-treatment sampling and  analysis  has been  used in a
geostatistteal model to determine the likely distribution of contami-
nation remaining in the soil and the statistical significance of the
results.

A detailed economic analysis of this full-scale technology applica-
tion will be performed utilizing monitoring data (i.e., water, chemi-
cal, and gas usage; waste generation; and maintenance needs).
This data was collected by  the developer with oversight by the
SITE program during the course of operation. This analysis will
focus on the actual costs of the full-scale remediation as well as
theoretical costs at another site.

Preliminary Results:  Preliminary evaluation of the post-treat-
ment data suggests the following conclusions:
  • The geostatistical weighted average soil TPH concentration in
    the treatment area after treatment was 2,290 mg/kg. The 90
    percent confidence interval for this average concentration is
    996 mg/kg to 3,570 mg/kg, which shows that there is a high
    probability that the technology did not meet the cleanup crite-
    rion. Seven percent of soil samples had TPH concentrations in
    excess of 10,000 mg/kg.

  • The geostatistical weighted average soil TRPH concentration
    was 1,680 mg/kg with a 90 percent confidence interval of 676
    mg/kg to 2,680 mg/kg.  Levels of BTEX were below the
    detection limit (6 ug/kg) in post-treatment soil samples; BTEX
    was detected at low mg/kg levels in a few pre-treatment soil
    samples.

  • Analysis of triplicate samples showed marked variability in soil
    contaminant concentration over short  distances.  Analogous
    results for TPH and TRPH triplicate samples suggest that the
    contaminant concentration variability exists within the site soil
    matrix and  is not the result of analytical techniques.  This
    inhomogeneity is the reason that confidence intervals for the
    average concentrations are so large.

  • The  data suggests that lateral or downward migration  of
    contaminants did not occur during treatment.

Key findings from the demonstration, including complete analyti-
cal results and  the economic analysis, will be published in an
Innovative Technology Evaluation Report.  This report will be
used to evaluate the in situ SERP technology as an alternative
for cleaning up similar sites across the country.  Results will also
be presented in a SITE Technology Capsule and a videotape.

For Further Information:

EPA Project Manager:
Paul dePercin
U.S. EPA Risk Reduction Engineering Laboratory
Office of Research and Development
26 West Martin  Luther King Drive
Cincinnati, OH 45268
(513) 569-7797
                      " 'US. Governmant Printing Office: 1994 — 560-067/80252
    United States
    Environmental Protection Agency
    Center for Environmental Research Information
    Cincinnati, OH 45268

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