v°/EPA
                                   United States
                                   Environmental Protection
                                   Agency
                EPA/540/M5-91/002
                August 1991
                                  SUPERFUND INNOVATIVE
                                  TECHNOLOGY  EVALUATION
                                     Demonstration  Bulletin

                                           AquaDetoj^/SVE System

                                           AWD Technologies, Inc.
 Technology Description: The AWD technology simultaneously
 treats groundwater and soil-gas  contaminated with volatile or-
 ganic compounds (VOC),  such as trichloroethylene (TCE) and
 tetrachloroethylene (PCE). This technology integrates two pro-
 cesses: (1) AquaDetox®, a moderate vacuum (pressure about 50
 mm  Hg or greater) stream stripping tower that treats contami-
 nated groundwater, and (2) a soil  vapor extraction (SVE) system
 that  removes contaminated soil-gas for  subsequent treatment
 with  granular activated carbon (GAG) beds. The two technologies
 are integrated into a closed-loop system, providing simultaneous
 remediation of contaminated groundwater and soil-gas with no air
 emissions. The major components of the integrated AquaDetox®/
 SVE system are shown in Figure 1.

 AquaDetox® is a high-efficiency,  countercurrent stripping tech-
 nology developed by Dow Chemical Company. Stripping is com-
 monly defined as a process that removes dissolved volatile com-
 pounds from water.  A carrier gas, such as air  or steam, is
 purged through the contaminated water, with the volatile compo-
 nents being transferred from the water into the gas phase. Ac-
 cording to the developer,  the AquaDetox® technology can be
 used to remove a wide variety of volatile compounds, as well as
 many compounds that are normally considered "non-strippable"
 (i.e.,  those with boiling points in excess of 200°C).

 SVE is a technology commonly applied for the in-situ removal of
 VOCs from soil. A vacuum is applied to vadose zone extraction
 wells to induce air flow within the soil toward the wells. The air
 acts  as a stripping medium that volatilizes the VOCs in the soil.
 Soil-gas from the extraction wells is typically treated in GAC beds
 before release to the atmosphere/Alternatively, the treated soil-
 gas can be reinjected in the soil to control the direction of air flow
 in the soil.

The  AquaDetox® and SVE systems are connected in a closed
 loop. Non-condensable vapors from the AquaDetox® system are
combined  with vapors  from the SVE compressor and treated
using two GAC beds in series. The  GAC  beds are regenerated
periodically using steam. The regeneration steam removes the
adsorbed contamination from the GAC as it  moves upward through
the bed. ft is then condensed and sent to the AquaDetox® tower
for treatment.

Recovered organics are collected in an on-site storage tank and
are periodically trucked to an off-site facility for recycling.
Waste Applicability: The  AWD technology is designed to
treat groundwater and soil contaminated with volatile and semi-
volatile  organic compounds.  Desirable  soil  characteristics for
successful soil vapor extraction are high permeability, large grain
size, and a low moisture content.  However, for soils with even
moderate permeability (permeability range about 1Q-3 to 10* cm/
sec), sufficient air flow for removal  of contaminants is possible.


Demonstration Results: The AWD technology was demon-
strated over a 2-week period in September 1990 at the Lockheed
Aeronautical Systems,  Inc. facility in  Burbank, California. The
testing plan consisted of 21 test runs performed under varying
operating conditions. The test runs were grouped into six phases.
Phase 1 test  runs were performed at AWD-specified operating
conditions (tower pressure at  105 mm Hg, steam flow rate at
3,800 Ib/hr, and groundwater flow rate at 900 gpm). The steam
flow rate was  varied in Phase  2 test runs. Steam flow rates and
tower pressures were varied simultaneously in Phases 3  and 4.
The groundwater flow  rate was varied  in Phase  5 test runs.
Phase 6 involved the SVE system in which the GAC bed  regen-
eration frequency was varied.

Based on the  analytical results and observations from the AWD
SITEE demonstration, the following conclusions were made about
the technology's effectiveness  and cost.

•  The AWD technology can successfully treat groundwater and
  soil-gas contaminated with VOCs.
•  The efficiencies were  in the  99.92 to 99.99 percent range for
  removal of VOCs from contaminated groundwater. VOC removal
  efficiencies for soil-gas ranged from 98.0 to 99.9 percent when the
  GAC beds were regenerated according to the SWD-specified
  frequency (8-hourshifts). VOC removal efficiencies dropped to as
  low as 93.4 percent when the GAC beds were regenerated less
  frequently.

•  The AWD technology produced effluent groundwater that com-
  plied with regulatory discharge requirements for TCE and PCE (5
  (xg/L for each compound ) at  the Lockheed site throughout the
  SITE demonstration. In addition, routine sampling by Lockheed
  has shown that the effluent groundwater has been in compliance
  with the regulator requirements throughout the 2-year operation
  of the system with no reported violations.

•  The GAC beds effectively removed VOCs from contaminated
  soil-gas even after 24 hours of continuous  operation without
  steam regeneration

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• The AquaDetox® system  proved highly effective in removing
 VOCs such as TCE and PCE (boiling points up to about 120°C)
 from  contaminated groundwater. The  system should also be
 effectiveforlessvolatileorganics (boiling points in excess of 200°C
 according to the developer).  However, because higher boiling
 point organlcs were not present in the groundwatertreated during
 the AWD SITE demonstration, the system's effectiveness  in re-
 moving this type of contamination could not be evaluated. Water
 containing such organics should be subjected to a treatability
 study.

• The system's steam consumption dropped with decreasing tower
 pressures. During the demonstration, the  system proved  more
 efficient at lower operating tower pressures.

•The system has been operating successfullyfor over2 years at the
 Lockheed site. During this time period, the system  has  been
 operational for 95 percent of the time, with 5 percent down time due
 to scheduled or non-scheduled repairs.
                                   respectively. The total annual operation and maintenance costs
                                   are approximately $410,000, $630,000, and $1,500,000 for the
                                   500-, 1,000-, and 3,000-gpm systems, respectively.

                                  A Technology Evaluation Report and an Applications Analysis
                                  Report describing the complete demonstration will be available in
                                  the Summer of 1991.
                                  For Further Information:

                                  EPA Project Managers:
                                  Gordon Evans (513-569-7684 or FTS 684-7684)
                                  Norma Lewis (513-569-7665 or FTS 684-7665)
                                  Risk Reduction Engineering Laboratory
                                  Office of Research and Development
                                  U.S. Environmental Protection Agency
                                  26 West Martin Luther King Drive
                                  Cincinnati, OH 45268
• The AWD system is estimated to cost approximately $3.2, $4.3,
 and $5.8 million for the 500-, 1,000-, and 3,000-gpm systems,
                                         Rerun Water
                                               Tank
                              Control Room
                              Granular Activated
                                  Carbon Beds
                               Containment
                                    Berm
                                           Vacuum Pump

                                         Gravity Separator

                                Note:SourGO of Steam Not Shown
                                                                                  Aquadetox
                                                                                  Stripping Tower
                                                         Solvent
                                                         Storage Tank
                                                                                        Condenser
                                                  Heat Exchanger
United States
Environmental Protection
Agency
Figure 1. Isometric View of the AWD Integrated AquaDeto,


              Center for Environmental
              Research Information
              Cincinnati, OH 45268
                                                                                  'stem.
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 EPA/540/M5-91/002

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