table 3-15: projects exsitu physical/chemical for ground water

<body stylesrc="table3_15_nfr.html" background="tile007.jpg" bgcolor="#FFFFFF">  <noscript><iframe src="//www.googletagmanager.com/ns.html?id=GTM-L8ZB" height="0" width="0" style="display:none;visibility:hidden"></iframe></noscript> <script>(function(w,d,s,l,i){w[l]=w[l]||[];w[l].push({"gtm.start": new Date().getTime(),event:"gtm.js"});var f=d.getElementsByTagName(s)[0], j=d.createElement(s),dl=l!="dataLayer"?"&l="+l:"";j.async=true;j.src= "//www.googletagmanager.com/gtm.js?id="+i+dl;f.parentNode.insertBefore(j,f); })(window,document,"script","dataLayer","GTM-L8ZB");</script>   <h1 align="center"><font size="5">TABLE 3-15 COMPLETED PROJECTS: EX SITU PHYSICAL/CHEMICAL TREATMENT FOR GROUND WATER, SURFACE WATER, AND LEACHATE</font></h1> <hr> <p align="center"><MAP NAME="FrontPageMap"><AREA SHAPE="RECT" COORDS="490, 0, 582, 55" HREF="3_13.html"><AREA SHAPE="RECT" COORDS="394, 0, 491, 55" HREF="../appd_f/synonym.html"><AREA SHAPE="RECT" COORDS="298, 1, 395, 55" HREF="../section1/toc.html"><AREA SHAPE="RECT" COORDS="201, 0, 299, 55" HREF="table3_2.pdf"><AREA SHAPE="RECT" COORDS="106, 0, 203, 55" HREF="../top_page.html"><AREA SHAPE="RECT" COORDS="22, 0, 108, 55" HREF="3_12.html"></MAP><a href="../../_vti_bin/shtml.exe/matrix2/section3/table3_15_fr.html/map"><img src="head4.gif" border="0" width="605" height="56" ismap usemap="#FrontPageMap"></a></p> <hr> <div align="center"><center> <table border="1" width="80%" bgcolor="#FFFFFF"> <tr> <th><font size="1">Site Name/<br> Contact</font></th> <th><font size="1">Technology/<br> Vendor</font></th> <th><font size="1">Media Treated</font></th> <th><font size="1">Contaminants Treated</font></th> <th><font size="1">Operating<br> Parameters</font></th> <th><font size="1">Materials Handling</font></th> <th><font size="1">Residuals Management</font></th> <th><font size="1">Comments</font></th> </tr> <tr> <td valign="top"><a name="national"></a><font size="1"><b>EPA Demo</b><br> National Lead Industry, NJ<br> 10/93<br> Carolyn Esposito<br> (908) 906-6895<br> Gary Vaccaro,<br> SAIC (201)489-5200</font></td> <td valign="top"><a href="../section4/4_49.html"><font size="1">FORAGERŽ sponge</font></a></td> <td valign="top"><font size="1">Waters</font></td> <td valign="top"><font size="1">Heavy metals<br> 90% removal</font><p><font size="1">Sponge can scavenge metals at ppm or ppb in industrial discharges</font></p> </td> <td valign="top"><font size="1">1 bed volume/minute control pH, temp, total ionic content</font></td> <td valign="top"><font size="1">Open-celled cellulose sponge</font></td> <td valign="top"><font size="1">Regeneration or incineration of the metals-saturated sponge</font></td> <td valign="top"><font size="1">In situ directly inserted into well or ex situ. Sponge can scavenge metals in concentrated levels of ppm and ppb from industrial discharges. $340 per 1000 gallons</font></td> </tr> <tr> <td valign="top"><a name="pease"></a><font size="1">Pease Air Force Base, Newington, NH</font><p><font size="1">Ronald Turner (513) 569-7775</font></p> </td> <td valign="top"><a href="../section4/4_49.html"><font size="1">Adsorption (AmbersorbŽ 563 adsorbent)</font></a></td> <td valign="top"><font size="1">Ground water</font></td> <td valign="top"><font size="1">Vinyl Chloride, 1,1-Dichloro- ethene, Trichloroethene</font></td> <td valign="top"> </td> <td valign="top"> </td> <td valign="top"><font size="1">Condensed con taminants are recovered through phase separation</font></td> <td valign="top"><font size="1">Ambersorb 563 adsorbent has 5 to 10 times the capa city of granular activated carbon (GAC) for low concentrations of volatile organic com-pounds (VOC).</font></td> </tr> <tr> <th><font size="1">Site Name/<br> Contact</font></th> <th><font size="1">Technology/<br> Vendor</font></th> <th><font size="1">Media Treated</font></th> <th><font size="1">Contaminants Treated</font></th> <th><font size="1">Operating<br> Parameters</font></th> <th><font size="1">Materials Handling</font></th> <th><font size="1">Residuals Management</font></th> <th><font size="1">Comments</font></th> </tr> <tr> <td valign="top"><a name="western"></a><font size="1"><strong>Superfund Site</strong>: Western Processing, WA (near Seattle)</font><p><font size="1">Mark Benjamin, University of Washington, Seattle, WA 98195, (206) 543-7645</font></p> </td> <td valign="top"><a href="../section4/4_49.html"><font size="1">Adsorption (Adsorptive Filtration)</font></a></td> <td valign="top"><font size="1">Ground water</font></td> <td valign="top"><font size="1">Soluble and particulate Zinc</font></td> <td valign="top"> </td> <td valign="top"> </td> <td valign="top"> </td> <td valign="top"><font size="1">Adsorptive filtration removes inorganic contaminants (metals) from aqueous waste streams.</font></td> </tr> <tr> <td valign="top"><a name="rma"></a><font size="1"><strong>Superfund Site</strong>: The Rocky Mountain Arsenal, Operable Unit 17, Comerse City, CO</font></td> <td valign="top"><font size="1">Sequence of unit processes uncluding precipitation, filtration, UV/chemical oxidation, GAC, air stripping and </font><a href="../section4/4_49.html"><font size="1">Adsorption (Activated Alumina)</font></a></td> <td valign="top"><font size="1">Wastewater</font></td> <td valign="top"><font size="1">VOCs: benzene, toluene, TCE, PCE;<br> Metals: arsenic, chromium, lead.</font></td> <td valign="top"> </td> <td valign="top"> </td> <td valign="top"><font size="1">Discharge of treated effluent to the sanitary sewer and offsite disposal of sludge and residuals.</font></td> <td valign="top"><font size="1">Treatment goals meet Colorado Basic Standards for Ground Water (CBSG) and the state MCLS.</font></td> </tr> <tr> <th><font size="1">Site Name/<br> Contact</font></th> <th><font size="1">Technology/<br> Vendor</font></th> <th><font size="1">Media Treated</font></th> <th><font size="1">Contaminants Treated</font></th> <th><font size="1">Operating<br> Parameters</font></th> <th><font size="1">Materials Handling</font></th> <th><font size="1">Residuals Management</font></th> <th><font size="1">Comments</font></th> </tr> <tr> <td valign="top"><a name="valley"></a><font size="1"><strong>Superfund Site</strong>: Valley Wood Preserving, Inc., Turlock, CA</font></td> <td valign="top"><font size="1">Excavation and cement-based fixation for contaminated soil.<br> Chemical treatment followed by </font><a href="../section4/4_49.html"><font size="1">Adsorption (Activated Alumina)</font></a></td> <td valign="top"><font size="1">Soil and ground water</font></td> <td valign="top"><font size="1">Chromium and arsenic.</font></td> <td valign="top"> </td> <td valign="top"> </td> <td valign="top"><font size="1">Backfilling excavated area with treated soil.<br> Treated water is reinjected to ground water and/or discharged to percolation ponds.</font></td> <td valign="top"><font size="1">Total estimated cost for this remedial action is $3,850,000 with annual O&M cost of $224,000.</font></td> </tr> <tr> <td valign="top"><a name="motor"></a><font size="1"><strong>Superfund Site</strong>: Motor Wheel, Lansing TWP, MI</font></td> <td valign="top"><font size="1">Backfilling, capping, and slurry wall containment for contaminated soil.<br> Aeration, separation, air stripping, and </font><a href="../section4/4_49.html"><font size="1">Adsorption (Activated Alumina)</font></a><font size="1"> for ground water.</font></td> <td valign="top"><font size="1">Soil and groundwater</font></td> <td valign="top"><font size="1">VOCs: benzene, PCE, TCE, toluene, and xylenes;<br> Organics: PAHs, PCBs, and pesticides;<br> Metals: arsenic, chromium, and lead</font></td> <td valign="top"> </td> <td valign="top"> </td> <td valign="top"> </td> <td valign="top"><font size="1">Activated alumina adsorption process removes fluoride from ground water.</font></td> </tr> <tr> <td valign="top"><a name="perham"></a><font size="1"><strong>Superfund Site</strong>: Perham Arsenic, Perham, MN</font></td> <td valign="top"><font size="1">Filtration and </font><a href="../section4/4_49.html"><font size="1">Adsorption (Activated Alumina)</font></a><font size="1"> for ground water on site</font></td> <td valign="top"><font size="1">Ground water</font></td> <td valign="top"><font size="1">Arsenic cleanup goal of 50 ppb from up to 1260 ppb in plume.</font></td> <td valign="top"> </td> <td valign="top"> </td> <td valign="top"><font size="1">Discharge of treated effluent to the aquifer; <br> Disposal of alumina filter media and filtered solids</font></td> <td valign="top"><font size="1">The overall Present Worth costs are $2,548,776, with the annual O&M costs of $217,806 (year 1 to 6)</font></td> </tr> <tr> <th><font size="1">Site Name/<br> Contact</font></th> <th><font size="1">Technology/<br> Vendor</font></th> <th><font size="1">Media Treated</font></th> <th><font size="1">Contaminants Treated</font></th> <th><font size="1">Operating<br> Parameters</font></th> <th><font size="1">Materials Handling</font></th> <th><font size="1">Residuals Management</font></th> <th><font size="1">Comments</font></th> </tr> <tr> <td valign="top"><a name="englin"></a><font size="1">Englin AFB</font><p><font size="1">Edward G. Marchand<br> HQ AFCESA/RAVW<br> Tyndall AFB,FL (904) 283-6023</font></p> </td> <td valign="top"><a href="../section4/4_50.html"><font size="1">Rotary air Stripper- high iron content</font></a></td> <td valign="top"><font size="1">Soil & Ground water</font></td> <td valign="top"><font size="1">>99% removal</font></td> <td valign="top"> </td> <td valign="top"> </td> <td valign="top"> </td> <td valign="top"> </td> </tr> <tr> <td valign="top" width="13%" bgcolor="#FFFFFF"><a name="savannah"></a><font size="1"><strong>DOE Demo</strong>- Savannah River Site, SC</font><p><font size="1">G.E. Turner, DOE Savannah R. Oper. Office Env. Rest, Aiken, SC</font></p> </td> <td valign="top" width="13%"><font size="1">Full-scale pump and treat using aboveground </font><a href="../section4/4_50.html"><font size="1">air stripping. </font></a></td> <td valign="top" width="10%" bgcolor="#FFFFFF"><font size="1">Ground water</font></td> <td valign="top" width="15%"><font size="1">Influent concentrations: up to 48 ppm for TCE, up to 12 ppm for PCE. Average VOC removal efficiencies in air stripper: >99.9%</font></td> <td valign="top" width="12%" bgcolor="#FFFFFF"><font size="1">In Situ</font></td> <td valign="top" width="12%"><font size="1">7 horizontal wells installed; only 2 wells used in field demonstration</font></td> <td valign="top" width="12%" bgcolor="#FFFFFF"> </td> <td valign="top" width="13%"><font size="1">Total Capital Cost: $4,103,000; Total Annual Operating Cost: $149,200.<br> $0.20/1,000 L ($0.75/1,000 gallons)</font></td> </tr> <tr> <th><font size="1">Site Name/<br> Contact</font></th> <th><font size="1">Technology/<br> Vendor</font></th> <th><font size="1">Media Treated</font></th> <th><font size="1">Contaminants Treated</font></th> <th><font size="1">Operating<br> Parameters</font></th> <th><font size="1">Materials Handling</font></th> <th><font size="1">Residuals Management</font></th> <th><font size="1">Comments</font></th> </tr> <tr> <td valign="top"><a name="langley"></a><font size="1">Langley AFB, VA</font><p><font size="1">Vern Bartels<br> Remedial Project Manager</font></p> </td> <td valign="top"><font size="1">Vacuum assisted well point extraction system and aboveground </font><a href="../section4/4_50.html"><font size="1">air stripping.</font></a></td> <td valign="top"><font size="1">Goundwater</font></td> <td valign="top"><font size="1">Total Recoverable Petroleum Hydrocarbons: 25 to 4,100 ppb on ground water, >100 ppm in soil.</font></td> <td valign="top"> </td> <td valign="top"> </td> <td valign="top"> </td> <td valign="top"><font size="1">Total Capital Cost: $569,739; Annual Operating Cost: $216,561</font></td> </tr> <tr> <td valign="top"><a name="mcclellan"></a><font size="1">McClellan AFB, CA</font><p><font size="1">Remedial Project Manager<br> McClellan AFB</font></p> </td> <td valign="top"><a href="../section4/4_50.html"><font size="1">Aboveground air stripping.</font></a></td> <td valign="top"><font size="1">660 million gallons of ground water</font></td> <td valign="top"><font size="1">Estimated 33,000 kg of VOCs released. Influent VOC concentration at 60 ppm</font></td> <td valign="top"> </td> <td valign="top"><font size="1">7 extraction wells were installed. 2 GAC units in series were used to polish liquid phase after stripping.</font></td> <td valign="top"><font size="1">Effluent below permitted discharge levels.</font></td> <td valign="top"><font size="1">Total Capital Cost; $4,000,000; Total Annual Operating Cost: $1,240,000.</font></td> </tr> <tr> <td valign="top"><a name="fort dix"></a><font size="1"><b>Army Demo</b><br> Fort Dix, NJ</font><p><font size="1">Steve Maloney<br> (217) 373-6740</font></p> </td> <td valign="top"><font size="1">Catalytic Decontamination and </font><a href="../section4/4_50.html"><font size="1">Air stripping</font></a></td> <td valign="top"><font size="1">Ground water</font></td> <td valign="top"><font size="1">Reduction:<br> 0% TOC<br> up to 90% VOC</font></td> <td valign="top"><font size="1">Ex situ</font></td> <td valign="top"><font size="1">Ozone injection and stripping</font></td> <td valign="top"><font size="1">Air stream - treated in catalytic unit and recycled</font></td> <td valign="top"><font size="1">Metal precipitate clogging and biofouling can occur.</font></td> </tr> <tr> <th><font size="1">Site Name/<br> Contact</font></th> <th><font size="1">Technology/<br> Vendor</font></th> <th><font size="1">Media Treated</font></th> <th><font size="1">Contaminants Treated</font></th> <th><font size="1">Operating<br> Parameters</font></th> <th><font size="1">Materials Handling</font></th> <th><font size="1">Residuals Management</font></th> <th><font size="1">Comments</font></th> </tr> <tr> <td valign="top"><a name="verona"></a><font size="1">Verona Wellfield<br> Battle Creek, MI</font></td> <td valign="top"><a href="../section4/4_51.html"><font size="1">GAC</font></a><font size="1"> as pretreatment for </font><a href="../section4/4_50.html"><font size="1">air stripper.</font></a></td> <td valign="top"><font size="1">Ground water</font></td> <td valign="top"><font size="1">12,850 ppb TVOC Attained: 11 ppb</font></td> <td valign="top"> </td> <td valign="top"> </td> <td valign="top"> </td> <td valign="top"> </td> </tr> <tr> <td valign="top"><a name="u.s.g.c."></a><font size="1">U.S. Coast Guard<br> Traverse City, MI</font></td> <td valign="top"><a href="../section4/4_51.html"><font size="1">GAC</font></a><font size="1"> used with Pump/treat </font></td> <td valign="top"><font size="1">Ground water</font></td> <td valign="top"><font size="1">10,329 ppb of Toluene. Attained: < 10 ppb</font></td> <td valign="top"> </td> <td valign="top"><font size="1">Discharge to municipal sewer.</font></td> <td valign="top"> </td> <td valign="top"> </td> </tr> <tr> <td valign="top" width="13%" bgcolor="#FFFFFF"><a name="love"></a><font size="1">Love Canal<br> Niagara Falls, NY</font></td> <td valign="top" width="13%"><a href="../section4/4_51.html"><font size="1">GAC system</font></a><font size="1"> for leachate treatment.</font></td> <td valign="top" width="10%" bgcolor="#FFFFFF"><font size="1">Ground water</font></td> <td valign="top" width="15%"><font size="1">28,000 ppb Benzene. Attained: < 10 ppb</font></td> <td valign="top" width="12%" bgcolor="#FFFFFF"> </td> <td valign="top" width="12%"> </td> <td valign="top" width="12%" bgcolor="#FFFFFF"> </td> <td valign="top" width="13%"> </td> </tr> <tr> <td valign="top" width="13%" bgcolor="#FFFFFF"><a name="fort drum"></a><font size="1">Fort Drum,<br> Watertown, NY</font><p><font size="1">Remedial Project Manager<br> Fort Drum Environmental Division</font></p> </td> <td valign="top" width="13%"><a href="../section4/4_38.html"><font size="1">Air Sparging</font></a><font size="1">, </font><a href="../section4/4_41.html"><font size="1">Dual Phase Extraction</font></a><font size="1"> and </font><a href="../section4/4_51.html"><font size="1">GAC </font></a></td> <td valign="top" width="10%" bgcolor="#FFFFFF"><font size="1">Ground water</font></td> <td valign="top" width="15%"><font size="1">Benzene, Toluene, Ethylbenzene, and Xylenes (BTEX)</font></td> <td valign="top" width="12%" bgcolor="#FFFFFF"><font size="1">Full-scale remediation to recover free-phase petroleum product using ground water extraction and air stripping and GAC</font></td> <td valign="top" width="12%"><font size="1">2 recovery wells were installed and 2 GAC drums were used in series. </font></td> <td valign="top" width="12%" bgcolor="#FFFFFF"> </td> <td valign="top" width="13%"><font size="1">Total Capital Cost: $958,780; Total annual Operating Cost: $129,440.</font></td> </tr> <tr> <td valign="top"><a name="milan"></a><font size="1">Milan AAP<br> Milan, TN</font><p><font size="1">USAEC ETD<br> (410) 671-2054</font></p> </td> <td valign="top"><a href="../section4/4_51.html"><font size="1">GAC</font></a><font size="1"> for explosives contaminated ground water.</font></td> <td valign="top"><font size="1">Ground water</font></td> <td valign="top"><font size="1">1.0 - 2.0 mg/L total explosive. Attained: ND (< 10 ppb) for all explosives</font></td> <td valign="top"> </td> <td valign="top"> </td> <td valign="top"> </td> <td valign="top"> </td> </tr> <tr> <th><font size="1">Site Name/<br> Contact</font></th> <th><font size="1">Technology/<br> Vendor</font></th> <th><font size="1">Media Treated</font></th> <th><font size="1">Contaminants Treated</font></th> <th><font size="1">Operating<br> Parameters</font></th> <th><font size="1">Materials Handling</font></th> <th><font size="1">Residuals Management</font></th> <th><font size="1">Comments</font></th> </tr> <tr> <td valign="top"><a name="amoco"></a><font size="1">Amoco Petroleum Pipeline<br> Constantine, MI</font></td> <td valign="top"><a href="../section4/4_38.html"><font size="1">Air Sparging</font></a><font size="1">, </font><a href="../section4/4_41.html"><font size="1">Dual Phase Extraction</font></a><font size="1"> and </font><a href="../section4/4_51.html"><font size="1">GAC</font></a><font size="1"> to recover free product and treat ground water. </font></td> <td valign="top"><font size="1">775 million gallons of ground water</font></td> <td valign="top"><font size="1">300,000 to 2 million gallons of gasoline, fuel oil, and kerosene </font></td> <td valign="top"><font size="1">In situ air sparging was subsequently added to treat the saturated zone. 4 extraction wells and 30 air sparging wells were installed. 2 GAC vessels in series</font></td> <td valign="top"><font size="1">118,000 gallons of free product recovered</font></td> <td valign="top"> </td> <td valign="top"><font size="1">Capital Cost: $297,000 for ground water recovery and treatment, $375,000 for air sparging.<br> Annual Operating Cost: $475,000<br> $3 per 1,000 gallons of ground water treated.</font></td> </tr> <tr> <td valign="top"><a name="commencement"></a><font size="1">Commencement Bay South Tacoma Channel,<br> Tacoma, WA</font><p><font size="1">Kevin Rochlin<br> Remedial Project Manager<br> U.S. EPA </font></p> </td> <td valign="top"><a href="../section4/4_51.html"><font size="1">2 liquid-phase GAC </font></a></td> <td valign="top"><font size="1">281,700,000 gallons of ground water</font></td> <td valign="top"><font size="1">Specific VOCs at influent: 13 to 2,000 ľg/L.<br> DCE up to 100 ppb, PCA up to 300 ppb, PCE up to 5.4 ppb, TCE up to 130 ppb. Attained: Specific VOCs at effluent: 1 to 13 ľg/L.</font></td> <td valign="top"><font size="1">Full-scale application of ground water extraction followed by GAC treatment in conjunction with an SVE system. 7 ground water extraction wells were installed and 2 liquid-phase GAC containers were operated in parallel. </font></td> <td valign="top"> </td> <td valign="top"> </td> <td valign="top"><font size="1">Total cost: $1,343,701</font></td> </tr> <tr> <th><font size="1">Site Name/<br> Contact</font></th> <th><font size="1">Technology/<br> Vendor</font></th> <th><font size="1">Media Treated</font></th> <th><font size="1">Contaminants Treated</font></th> <th><font size="1">Operating<br> Parameters</font></th> <th><font size="1">Materials Handling</font></th> <th><font size="1">Residuals Management</font></th> <th><font size="1">Comments</font></th> </tr> <tr> <td valign="top"><a name="kerr"></a><font size="1"><b>EPA Demo</b><br> Kerr-McGee Chemical Corp., WI</font><p><font size="1">1993</font></p> <p><font size="1">Douglas Grosse<br> (513) 569-7844</font></p> </td> <td valign="top"><a href="../section4/4_52.html"><font size="1">Ion Exchange:</font></a><font size="1"> Electrochemical reduction & immobilization</font></td> <td valign="top"><font size="1">Ground water</font></td> <td valign="top"><font size="1">Hexavalent chromium and other heavy metals</font></td> <td valign="top"><font size="1">In situ requires excess ferrous ions - maintain pH</font></td> <td valign="top"><font size="1">Electrochemical reactions generate ions for removal of hexavalent chromium</font></td> <td valign="top"><font size="1">Clean water is reinjected into ground</font></td> <td valign="top"><font size="1">Ex situ can be used to maximize rate and removal.</font></td> </tr> <tr> <td valign="top"><a name="usace"></a><font size="1"><b>Army Demo</b><br> USACE-WES, MS</font><p><font size="1">Mark Bricka<br> (601) 634-3700</font></p> </td> <td valign="top"><a href="../section4/4_52.html"><font size="1">Ion exchange:</font></a><font size="1"> Xanthate treatment</font></td> <td valign="top"><font size="1">Ground water & wastewater</font></td> <td valign="top"><font size="1">Heavy metals</font></td> <td valign="top"><font size="1">Ion exchange with xanthated material</font></td> <td valign="top"><font size="1">Precipitation, sedimentation, and filtration</font></td> <td valign="top"><font size="1">Concentrated metal sludge</font></td> <td valign="top"><font size="1">Offers many advantages over hydroxide precipitation.</font></td> </tr> <tr> <th><font size="1">Site Name/<br> Contact</font></th> <th><font size="1">Technology/<br> Vendor</font></th> <th><font size="1">Media Treated</font></th> <th><font size="1">Contaminants Treated</font></th> <th><font size="1">Operating<br> Parameters</font></th> <th><font size="1">Materials Handling</font></th> <th><font size="1">Residuals Management</font></th> <th><font size="1">Comments</font></th> </tr> <tr> <td valign="top"><a name="palangana"></a><font size="1"><b>EPA Demo</b> <br> Palangana Uranium Mine Site, TX</font><p><font size="1">7/93</font></p> <p><font size="1">Annette Gatchett<br> (513) 569-7697</font></p> </td> <td valign="top"><a href="../section4/4_53.html"><font size="1">Precipitation/ Filtration</font></a></td> <td valign="top"><font size="1">Ground water</font></td> <td valign="top"><font size="1">Low-moderate levels of NORM (uranium, radium-226, thorium-230)</font></td> <td valign="top"><font size="1">Complexing, adsorption, and absorption</font></td> <td valign="top"><font size="1">URAL complexing agent</font></td> <td valign="top"><font size="1">Treated water to holding pond</font></td> <td valign="top"><pre><font size="1"> </font></pre> </td> </tr> <tr> <td valign="top"><a name="coakley"></a><font size="1">Coakley Landfill<br> New Hampshire</font></td> <td valign="top"><a href="../section4/4_53.html"><font size="1">Precipitation: Pretreatment of ground water by hydroxide precipitation with lime, </font></a></td> <td valign="top"><font size="1">Ground water</font></td> <td valign="top"><font size="1">Cr - 330 ppb<br> Ni - 122-200 ppb<br> As - 10-90 ppb Attained: <br> Cr - 50 ppb<br> Ni - 100 ppb<br> As - 50 ppb</font></td> <td valign="top"> </td> <td valign="top"><font size="1">Used air stripping for removal of VOCs</font></td> <td valign="top"> </td> <td valign="top"> </td> </tr> <tr> <td valign="top"><a name="stringfellow"></a><font size="1">Stringfellow Acid Pit Site California</font></td> <td valign="top"><a href="../section4/4_53.html"><font size="1">Precipitation.</font></a></td> <td valign="top"><font size="1">Water</font></td> <td valign="top"><font size="1">Cr - 1.5-270 ppm<br> Cd - 0.32-9.3 ppm<br> Zn - 2.2-300 ppm<br> Cu - 1.7-20 ppm<br> Attained:<br> Cr - 0.5 ppm<br> Cd - 0.11 ppm<br> Zn - 2.61 ppm<br> Cu - 2 ppm</font></td> <td valign="top"><font size="1">Pretreatment for the removal of metals and organics, then POTW</font></td> <td valign="top"> </td> <td valign="top"> </td> <td valign="top"> </td> </tr> <tr> <th><font size="1">Site Name/<br> Contact</font></th> <th><font size="1">Technology/<br> Vendor</font></th> <th><font size="1">Media Treated</font></th> <th><font size="1">Contaminants Treated</font></th> <th><font size="1">Operating<br> Parameters</font></th> <th><font size="1">Materials Handling</font></th> <th><font size="1">Residuals Management</font></th> <th><font size="1">Comments</font></th> </tr> <tr> <td valign="top"><a name="winthrop"></a><font size="1">Winthrop Landfill<br> Winthrop, ME</font></td> <td valign="top"><a href="../section4/4_53.html"><font size="1">Precipitation</font></a></td> <td valign="top"><font size="1">Ground water</font></td> <td valign="top"><font size="1">As - 0.1-0.8 ppm<br> Ni - 0.04 ppm<br> Zn - 0.2-0.6 ppm<br> Attained:<br> As - 0.05 ppm<br> Ni - 0.04 ppm<br> Zn - 0.18 ppm</font></td> <td valign="top"><font size="1">Pilot test of metals from the ground water by precipitation</font></td> <td valign="top"> </td> <td valign="top"> </td> <td valign="top"> </td> </tr> <tr> <td valign="top"><a name="crown"></a><font size="1">EPA Removal Action<br> Crown Plating, MO</font><p><font size="1">10/1/89 to 12/31/89 (Removal)</font></p> <p><font size="1">Mark Roberts<br> (913) 236-3881</font></p> </td> <td valign="top"><a href="../section4/4_53.html"><font size="1">Dechlorination using the KPEG process/EPA removal contractor</font></a></td> <td valign="top"><font size="1">Liquid (5 gallons)</font></td> <td valign="top"><font size="1">Criteria:</font><p><font size="1">Dioxin: <1 ppbInput:<br> Silvex - 10,000 ppm <br> Dioxin equivalents - 24.18 ppb</font></p> <p><font size="1">Output:<br> Silvex - 32 ppb<br> Dioxin equivalents - 0.068 ppb</font></p> </td> <td valign="top"><font size="1">Batch operation</font><p><font size="1">Retention time - 36 hours (including time of equipment breakdown)</font></p> <p><font size="1">Temperature - 72 °C</font></p> <p><font size="1">pH - 13</font></p> <p><font size="1">Moisture content - 100%</font></p> </td> <td valign="top"><font size="1">Ground water extraction</font></td> <td valign="top"><font size="1">Built an on-site vacuum for emissions control</font><p><font size="1">Contaminated residual oil incinerated off-site</font></p> </td> <td valign="top"><font size="1">Three mobile units currently available. Electroplating site.</font></td> </tr> <tr> <th><font size="1">Site Name/<br> Contact</font></th> <th><font size="1">Technology/<br> Vendor</font></th> <th><font size="1">Media Treated</font></th> <th><font size="1">Contaminants Treated</font></th> <th><font size="1">Operating<br> Parameters</font></th> <th><font size="1">Materials Handling</font></th> <th><font size="1">Residuals Management</font></th> <th><font size="1">Comments</font></th> </tr> <tr> <td valign="top"><a name="wastewater"></a><font size="1">Wastewater Technology Center</font><p><font size="1">John Martin<br> U.S. EPA NRMRL (513)569-7676</font></p> </td> <td valign="top"><a href="../section4/4_54.html"><font size="1">Separation</font></a></td> <td valign="top"><font size="1">Ground water</font></td> <td valign="top"><font size="1">VOCs. 99% Removal efficiency</font></td> <td valign="top"> </td> <td valign="top"> </td> <td valign="top"> </td> <td valign="top"> </td> </tr> <tr> <td valign="top"><a name="rocky"></a><font size="1"><b>EPA & DOE Demo</b><br> Rocky Flats Facility, CO</font><p><font size="1">7/90</font></p> <p><font size="1">Annette Gatchett<br> (513) 569-7697</font></p> </td> <td valign="top"><a href="../section4/4_54.html"><font size="1">Separation: Filtration</font></a></td> <td valign="top"><font size="1">Ground water 58-95% removal of uranium</font></td> <td valign="top"><font size="1">"Polishing" filtration process for heavy metals and non-tritium radio-nuclides (NORM, LLRW, TRU). Uranium in ground water influent at filtration system concentration 40-100 mg/L</font></td> <td valign="top"><font size="1">Specific control - water chemistry, water flux, and bed volume</font></td> <td valign="top"><font size="1">Sorption, chemical complexing, and hydroxide precipitation</font></td> <td valign="top"><font size="1">Concentrated waste sludge</font></td> <td valign="top"><font size="1">Capital - $150K</font><p><font size="1">Operation - $0.40 to $0.53/1,000 L $1.50-$2.00/1,000 gallons treated.</font></p> <p><font size="1">Colloid sorption filter for metals and nontritium radionuclides commercial scale SITE demo.</font></p> </td> </tr> <tr> <th><font size="1">Site Name/<br> Contact</font></th> <th><font size="1">Technology/<br> Vendor</font></th> <th><font size="1">Media Treated</font></th> <th><font size="1">Contaminants Treated</font></th> <th><font size="1">Operating<br> Parameters</font></th> <th><font size="1">Materials Handling</font></th> <th><font size="1">Residuals Management</font></th> <th><font size="1">Comments</font></th> </tr> <tr> <td valign="top"><a name="creosota"></a><font size="1"><b>EPA Demo</b><br> American Creosote Works, FL<br> 1991</font><p><font size="1">Kim Lisa Kreiton (513)569-7328 EPA RREL<br> John Martin<br> (513) 569-7758</font></p> </td> <td valign="top"><a href="../section4/4_54.html"><font size="1">Membrane Separation</font></a></td> <td valign="top"><font size="1">Ground water </font></td> <td valign="top"><font size="1">PAHs, smaller phenolics <br> Removal:<br> 90% PAH<br> 80% creosote<br> 25-30% smaller phenolics</font></td> <td valign="top"><pre><font size="1"> </font></pre> </td> <td valign="top"><font size="1">Positive pressure membrane hyperfiltration unit</font></td> <td valign="top"><font size="1">Clean H<sub>2</sub>O to POTW, concentrated contaminants to holding tanks</font></td> <td valign="top"><font size="1">$228-$1,739/1,000 gallons treated. $500K - $1.2M annual</font></td> </tr> <tr> <td valign="top"><a name="birmingham"></a><font size="1"><b>DOI Demo</b><br> Birmingham, AL Manassas, VA</font><p><font size="1">1992</font></p> <p><font size="1">Ronald H. Church<br> (205) 759-9446</font></p> </td> <td valign="top"><a href="../section4/4_54.html"><font size="1">Solid/liquid separation</font></a></td> <td valign="top"><font size="1">Wastewater</font></td> <td valign="top"><font size="1">Solids and fine particulate matter in mining wastes</font></td> <td valign="top"><font size="1">Feed flow rate in field test unit was 50-175 gpm. Freed material is usually a degradable polyacrylamide</font></td> <td valign="top"><font size="1">Pipe delivery system used as mixing system to minimize quantity of feed used. Waste should be in slurry form</font></td> <td valign="top"><font size="1">The "clean" water can be discharged. Flocculated material becomes solid waste for a landfill</font></td> <td valign="top"><font size="1">Polymer costs are $0.50-0.60 per ton of dry solids produced when polymer is bought in bulk.</font></td> </tr> <tr> <th><font size="1">Site Name/<br> Contact</font></th> <th><font size="1">Technology/<br> Vendor</font></th> <th><font size="1">Media Treated</font></th> <th><font size="1">Contaminants Treated</font></th> <th><font size="1">Operating<br> Parameters</font></th> <th><font size="1">Materials Handling</font></th> <th><font size="1">Residuals Management</font></th> <th><font size="1">Comments</font></th> </tr> <tr> <td valign="top"><a name="bureau"></a><font size="1"><b>DOI Demo</b> <br> Bureau of Mines and USAEC (Cooperative effort) Buffalo, NY</font><p><font size="1">Ronald H. Church<br> (205) 759-9446</font></p> </td> <td valign="top"><a href="../section4/4_54.html"><font size="1">Solid/liquid separation</font></a></td> <td valign="top"><font size="1">Wastewater</font></td> <td valign="top"><font size="1">Suspended particulates from dredging wastes</font></td> <td valign="top"><font size="1">Waste pumped through a 4-inch line to 1,000-gallon fiberglass mixing tank. 6-inch- by-2-inch static mixer.</font></td> <td valign="top"><font size="1">Polymer used for flocculation is pumped through a 1-inch line to the mixing tank.</font></td> <td valign="top"><font size="1">NTU values of the discharge water ranged from 12 to 17, with the underflow discharge containing about 31% solids</font></td> <td valign="top"><font size="1">Polymer costs: <br> $0.50/lb when bought in bulk. Focus of DOI/USACE test is removal of suspended particulates from dredging of sediments.</font></td> </tr> <tr> <td valign="top"><a name="selma"></a><font size="1"><strong>EPA SITE Demo</strong><br> Selma Pressure Treating Selma, CA</font><p><font size="1">11/90</font></p> <p><font size="1">Edward Bates<br> (513) 569-7774</font></p> </td> <td valign="top"><a href="../section4/4_54.html"><font size="1">Pretreatment separation/ </font></a><font size="1">Solidification/ Stabilization with silicate compounds</font></td> <td valign="top"><font size="1">Ground water, soil, sludge</font></td> <td valign="top"><font size="1">Organics and inorganics</font></td> <td valign="top"><font size="1">Silicate compounds</font></td> <td valign="top"><font size="1">Pretreatment separation of coarse and fine materials</font></td> <td valign="top"><font size="1">PCP leachate concentrations reduced up to 97%. As, Cr, Cu immobilized</font></td> <td valign="top"><font size="1">Applied to a wide variety of hazardous soils, sludges, and wastewaters.</font></td> </tr> <tr> <td valign="top"><a name="integrated"></a><font size="1"><b>DOE Integrated Demo</b>,<br> 4 DOE sites: <br> (1) Hanford <br> (2) Fernald, ID<br> (3) Oak Ridge<br> (4) Savannah River</font><p><font size="1">2/91</font></p> <p><font size="1">Roger Gilchrist<br> (509) 376-5310</font></p> </td> <td valign="top"><a href="../section4/4_54.html"><font size="1">Separation: </font></a><font size="1">USTs, emphasizing the single-shell storage tanks located at the Hanford site</font></td> <td valign="top"><font size="1">Ground water, soil</font></td> <td valign="top"><font size="1">Tank waste constituents ranging from Na-nitrates to transuranics, in 3 forms: supernatant (liquid), sludges, and saltcake (which can be as hard as cement) </font></td> <td valign="top"><font size="1">UST-ID is pursuing technologies in two general areas: characterization/ retrieval and separations of low-level waste</font></td> <td valign="top"><font size="1">Parameters vary among technologies</font></td> <td valign="top"><font size="1">Parameters vary among technologies</font></td> <td valign="top"><font size="1">The UST-ID program will be used at Hanford, Fernald, Idaho, Oak Ridge, and Savannah River. Most UST waste was generated by processes used to separate nuclear fuels from other components.</font></td> </tr> <tr> <th><font size="1">Site Name/<br> Contact</font></th> <th><font size="1">Technology/<br> Vendor</font></th> <th><font size="1">Media Treated</font></th> <th><font size="1">Contaminants Treated</font></th> <th><font size="1">Operating<br> Parameters</font></th> <th><font size="1">Materials Handling</font></th> <th><font size="1">Residuals Management</font></th> <th><font size="1">Comments</font></th> </tr> <tr> <td valign="top"><a name="saginaw"></a><font size="1"><b>DOI, Army, EPA Demo</b><br> Saginaw Bay Confined Disposal Facility, MI; Toronto, Canada</font><p><font size="1">10/91 to 6/92</font></p> <p><font size="1">S. Jackson Hubbard<br> (513) 569-7507</font></p> </td> <td valign="top"><a href="../section4/4_54.html"><font size="1">Particle Separation Process</font></a></td> <td valign="top"><font size="1">Sediments (30 ydł day)</font></td> <td valign="top"><font size="1">PCBs, heavy metals, radionuclides</font></td> <td valign="top"><font size="1">Contaminant and grain size analysis</font></td> <td valign="top"><font size="1">Screening, water and chemicals added, attrition scrubbing, particle separation</font></td> <td valign="top"><font size="1">Output soil, silts, clays, and waste-water</font></td> <td valign="top"><font size="1">Demo was part of the Assessment and Remediation of Contaminated Sediments (ARCs) Program.</font></td> </tr> <tr> <td valign="top"><a name="palmerton"></a><font size="1"><b>EPA Demo</b><br> Palmerton Zinc Superfund Site, PA</font><p><font size="1">1990</font></p> <p><font size="1">John Martin<br> (513) 569-7758</font></p> </td> <td valign="top"><a href="../section4/4_54.html"><font size="1">Membrane microfiltration</font></a></td> <td valign="top"><font size="1">Liquid wastes</font></td> <td valign="top"><font size="1">Solid particles in liquid wastes-removal averaged 99.95% for Zn & TSS</font></td> <td valign="top"><font size="1">Filter press 45 psi</font><p><font size="1">Shallow aquifer with dissolved heavy metals</font></p> </td> <td valign="top"><font size="1">Tyvek (T-980) spun-bound olefin filter</font></td> <td valign="top"><font size="1">Filter cake 40-60% solids</font></td> <td valign="top"><font size="1">Best for treating waste less than 5,000 ppm.</font><p><font size="1">$213K - $549K annual</font></p> </td> </tr> <tr> <th><font size="1">Site Name/<br> Contact</font></th> <th><font size="1">Technology/<br> Vendor</font></th> <th><font size="1">Media Treated</font></th> <th><font size="1">Contaminants Treated</font></th> <th><font size="1">Operating<br> Parameters</font></th> <th><font size="1">Materials Handling</font></th> <th><font size="1">Residuals Management</font></th> <th><font size="1">Comments</font></th> </tr> <tr> <td valign="top"><a name="north island"></a><font size="1">Naval Air Station North Island, San Diego, CA</font><p><font size="1">Ronald Turner (513) 569-7775</font></p> </td> <td valign="top"><a href="../section4/4_54.html"><font size="1">Separation (Cross-Flow Pervaporation System)</font></a></td> <td valign="top"><font size="1">Ground water</font></td> <td valign="top"><font size="1">Organics, primarily TCE - 98% reduction</font></td> <td valign="top"><font size="1">TCE influent concentrations - 250 ppm, flow rate - 10 gpm</font></td> <td valign="top"> </td> <td valign="top"> </td> <td valign="top"><font size="1">The ZENON Environmental Inc. cross-flow pervaporation technology is a membrane-based process that removes VOC from aqueous matrices.</font></td> </tr> <tr> <td valign="top"><a name="harris"></a><font size="1">Harris County</font><p><font size="1">John Blount (713) 956-3000</font></p> </td> <td valign="top"><a href="../section4/4_55.html"><font size="1">Trickling Filter (Sprinkler Irrigation)</font></a></td> <td valign="top"><font size="1">Wastewater</font></td> <td valign="top"><font size="1">BOD, TSS</font></td> <td valign="top"><font size="1">BOD load rate - 45 lbs./day/1000 sq. ft.. Hydraulic load rate - 235 gallons/day/sq. ft..</font></td> <td valign="top"> </td> <td valign="top"><font size="1">Effluents are chlorinated and stored in a pump tank. They are distributed to lawns through an automatic irrigation system.</font></td> <td valign="top"> </td> </tr> <tr> <th><font size="1">Site Name/<br> Contact</font></th> <th><font size="1">Technology/<br> Vendor</font></th> <th><font size="1">Media Treated</font></th> <th><font size="1">Contaminants Treated</font></th> <th><font size="1">Operating<br> Parameters</font></th> <th><font size="1">Materials Handling</font></th> <th><font size="1">Residuals Management</font></th> <th><font size="1">Comments</font></th> </tr> <tr> <td valign="top"><a name="tracey"></a><font size="1">Tracey, CA 1992</font><p><font size="1">National Risk Management Research Laboratory (513) 569-7697</font></p> </td> <td valign="top"><a href="../section4/4_56.html"><font size="1">Photochemical</font></a></td> <td valign="top"><font size="1">Ground water</font></td> <td valign="top"><font size="1">TCE, PCE, DCA</font></td> <td valign="top"> </td> <td valign="top"> </td> <td valign="top"> </td> <td valign="top"> </td> </tr> <tr> <td valign="top"><a name="lawerance"></a><font size="1">Lawrence Livermore Site 300, CA 1992</font><p><font size="1">Vulcan Peroxidation Systems, Inc. (602)790-8383 National Risk Management Research Laboratory (513) 569-7697</font></p> </td> <td valign="top"><a href="../section4/4_56.html"><font size="1">Chemical Oxidation</font></a></td> <td valign="top"><font size="1">Ground water</font></td> <td valign="top"><font size="1">VOCs</font></td> <td valign="top"> </td> <td valign="top"> </td> <td valign="top"> </td> <td valign="top"> </td> </tr> <tr> <th><font size="1">Site Name/<br> Contact</font></th> <th><font size="1">Technology/<br> Vendor</font></th> <th><font size="1">Media Treated</font></th> <th><font size="1">Contaminants Treated</font></th> <th><font size="1">Operating<br> Parameters</font></th> <th><font size="1">Materials Handling</font></th> <th><font size="1">Residuals Management</font></th> <th><font size="1">Comments</font></th> </tr> <tr> <td valign="top"><a name="coleman"></a><font size="1"><b>EPA Demo</b><br> Coleman-Evans Site, FL</font><p><font size="1">Norma Lewis<br> (513) 569-7665</font></p> </td> <td valign="top"><font size="1">Soil washing/</font><a href="../section4/4_56.html"><font size="1">catalytic ozone oxidation</font></a></td> <td valign="top"><font size="1">Soil, sludge, & ground water</font></td> <td valign="top"><font size="1">Organics - 1-20,000 ppm</font></td> <td valign="top"><font size="1">Soil washing enhanced by ultrasound followed by oxidation</font></td> <td valign="top"><font size="1">Soil particles larger than 1 inch are crushed</font></td> <td valign="top"><font size="1">Carbon filter for off-gas</font></td> <td valign="top"><font size="1">Excalibur technology.</font></td> </tr> <tr> <td valign="top"><a name="bangor"></a><font size="1"><b>Navy Demo</b><br> Bangor SUBASE, WA</font><p><font size="1">Spring 1993</font></p> <p><font size="1">Carmen LeBron<br> (805) 982-1616</font></p> </td> <td valign="top"><a href="../section4/4_56.html"><font size="1">Advanced Oxidation Process. </font></a><font size="1">Bench-scale TNT and RDX treatability test. Recirculating UV/ozone reactor. 30-minute retention.</font></td> <td valign="top"><font size="1">Ground water</font></td> <td valign="top"><font size="1">Beginning levels: 7 ppm TNT; 600 ppb RDX <br> Ordnance - treated to 2.9 ppb TNT and 0.8 ppb RDX</font></td> <td valign="top"><font size="1">Maintain pH.</font></td> <td valign="top"><font size="1">UV oxidation, H<sub>2</sub>0<sub>2</sub> to generate hydroxyl radicals</font></td> <td valign="top"><font size="1">Possible toxic byproducts</font></td> <td valign="top"><font size="1">Full scale system being designed.</font></td> </tr> <tr> <td valign="top"><a name="navy site"></a><font size="1"><b>Navy Demo</b><br> U.S. Navy Site, NJ</font><p><font size="1">1991</font></p> <p><font size="1">Andy Law<br> (805) 982-1650</font></p> </td> <td valign="top"><a href="../section4/4_56.html"><font size="1">Advanced Oxidation Process</font></a></td> <td valign="top"><font size="1">Ground water</font></td> <td valign="top"><font size="1">Organics - TOC 50-100 ppm</font></td> <td valign="top"><font size="1">Maintain pH</font></td> <td valign="top"><font size="1">UV oxidation, H<sub>2</sub>0<sub>2</sub> to generate hydroxyl radicals</font></td> <td valign="top"><font size="1">Contaminant destruction</font></td> <td valign="top"><pre><font size="1"> </font></pre> </td> </tr> <tr> <th><font size="1">Site Name/<br> Contact</font></th> <th><font size="1">Technology/<br> Vendor</font></th> <th><font size="1">Media Treated</font></th> <th><font size="1">Contaminants Treated</font></th> <th><font size="1">Operating<br> Parameters</font></th> <th><font size="1">Materials Handling</font></th> <th><font size="1">Residuals Management</font></th> <th><font size="1">Comments</font></th> </tr> <tr> <td valign="top"><a name="winthrop2"></a><font size="1">Winthrop Superfund Site, ME</font><p><font size="1">Dr. Raymond Machacek<br> Arthur D. Little, Inc.<br> (617) 498-5580</font></p> </td> <td valign="top"><a href="../section4/4_56.html"><font size="1">UV/oxidation</font></a></td> <td valign="top"><font size="1">Ground water</font></td> <td valign="top"><font size="1">Pretreat for iron, then UV/oxidation solvents. 5 ppm DMF. Attained: < 5 ppb</font></td> <td valign="top"> </td> <td valign="top"> </td> <td valign="top"> </td> <td valign="top"> </td> </tr> <tr> <td valign="top"><a name="milan2"></a><font size="1">Milan AAP<br> Milan, TN</font><p><font size="1">USAEC ETD<br> (410) 671-2054</font></p> </td> <td valign="top"><a href="../section4/4_56.html"><font size="1">UV/oxidation</font></a></td> <td valign="top"><font size="1">Ground water</font></td> <td valign="top"><font size="1">Explosives: 20.0 ppm total explosives</font><p><font size="1">Attained: ND (10 ppb) for all explosives</font></p> </td> <td valign="top"> </td> <td valign="top"> </td> <td valign="top"> </td> <td valign="top"> </td> </tr> <tr> <td valign="top"><a name="edwards"></a><font size="1"><b>Air Force & EPA Demo</b><br> Edwards AFB, CA</font><p><font size="1">3/93</font></p> <p><font size="1">Richard Eilers<br> (513) 569-7809</font></p> </td> <td valign="top"><a href="../section4/4_56.html"><font size="1">UV/oxidation: CAV-OXŽ Process</font></a></td> <td valign="top"><font size="1">Ground water & wastewater</font></td> <td valign="top"><font size="1">Organics - 96-100% reduction</font></td> <td valign="top"><font size="1">H<sub>2</sub>O<sub>2</sub> and metal catalysts added if needed</font></td> <td valign="top"><font size="1">Hydrodynamic cavitation and UV oxidation</font></td> <td valign="top"><font size="1">Contaminant destruction</font></td> <td valign="top"><font size="1">Cannot handle free product or highly turbid streams.</font></td> </tr> <tr> <th><font size="1">Site Name/<br> Contact</font></th> <th><font size="1">Technology/<br> Vendor</font></th> <th><font size="1">Media Treated</font></th> <th><font size="1">Contaminants Treated</font></th> <th><font size="1">Operating<br> Parameters</font></th> <th><font size="1">Materials Handling</font></th> <th><font size="1">Residuals Management</font></th> <th><font size="1">Comments</font></th> </tr> <tr> <td valign="top"><a name="lake charles"></a><font size="1"><b>EPA Demo</b><br> Lake Charles Treatment Center, LA</font><p><font size="1">Randy Parker<br> (513) 569-7271</font></p> </td> <td valign="top"><a href="../section4/4_56.html"><font size="1">PO*WW*ER<sup>TM</sup> evaporation & catalytic oxidation</font></a></td> <td valign="top"><font size="1">Ground water & wastewaters</font></td> <td valign="top"><font size="1">Volatile & non-volatile organic compounds, salts, metals, volatile inorganics</font></td> <td valign="top"><font size="1">0.25 gpm pilot-plant</font></td> <td valign="top"><font size="1">Evaporation & oxidation</font></td> <td valign="top"><font size="1">Concentrated contaminant solution disposed of or treated further</font></td> <td valign="top"><font size="1">$110/1,000 gallons treated.</font></td> </tr> <tr> <td valign="top"><a name="san jose"></a><font size="1"><b>EPA Demo</b><br> San Jose, CA</font><p><font size="1">3/89</font></p> <p><font size="1">Norma Lewis<br> (513) 569-7665</font></p> </td> <td valign="top"><a href="../section4/4_56.html"><font size="1">Ultraviolet radiation & oxidation</font></a></td> <td valign="top"><font size="1">Ground water</font></td> <td valign="top"><font size="1">Halogenated hydrocarbons, VOCs, pesticides, PCBs - 99% TCE, 58% 1,1-DCA, 85% 1,1,1-TCA removal</font></td> <td valign="top"><font size="1">UV,H<sub>2</sub>0<sub>2</sub> destruction</font></td> <td valign="top"><font size="1">Tank with air compressor, O<sub>3</sub> generator, and H<sub>2</sub>0<sub>2</sub> feed</font></td> <td valign="top"><font size="1">Offgas to ozone destruction</font></td> <td valign="top"><font size="1">20 commercial systems installed.</font></td> </tr> <tr> <td valign="top"><a name="kansas"></a><font size="1"><b>DOE Demo</b><br> Kansas City Plant, MO</font><p><font size="1">Sidney B. Garland II<br> (615) 579-8581</font></p> </td> <td valign="top"><a href="../section4/4_56.html"><font size="1">Ultraviolet radiation, hydrogen peroxide, and ozone</font></a></td> <td valign="top"><font size="1">Ground water</font></td> <td valign="top"><font size="1">TCE concentration above 10,000 ľg/L in ground water. >99.5% VOCs were destroyed.</font></td> <td valign="top"><font size="1">30% downtime for maintenance and repair</font></td> <td valign="top"><font size="1">Flow rate has averaged 15% of design rate</font></td> <td valign="top"><pre><font size="1"> </font></pre> </td> <td valign="top"><font size="1">Total Capital Cost: $1,383,400; Annual Operating Cost: $355,200.</font></td> </tr> </table> </center></div> <p>Sources: <i>Innovative Treatment Technologies: Annual Status Report (EPA, Eighth Edition, Nov. 1996). Completed North American Innovative Remediation Technology Demonstration Projects (EPA, Aug.1996)</i></p> <hr> <p align="center"><MAP NAME="FrontPageMap1"><AREA SHAPE="RECT" COORDS="490, 0, 582, 55" HREF="3_13.html"><AREA SHAPE="RECT" COORDS="394, 0, 491, 55" HREF="../appd_f/synonym.html"><AREA SHAPE="RECT" COORDS="298, 1, 395, 55" HREF="../section1/toc.html"><AREA SHAPE="RECT" COORDS="201, 0, 299, 55" HREF="table3_2.pdf"><AREA SHAPE="RECT" COORDS="106, 0, 203, 55" HREF="../top_page.html"><AREA SHAPE="RECT" COORDS="22, 0, 108, 55" HREF="3_12.html"></MAP><a href="../../_vti_bin/shtml.exe/matrix2/section3/table3_15_fr.html/map1"><img src="head4.gif" border="0" width="605" height="56" ismap usemap="#FrontPageMap1"></a></p> <hr>  </body>