| Matrix of DTSC-Regulated Sites2 in California Using Common Vapor Treatment Technologies and Possible Alternatives | ||||||
| Click on the links below to move directly to the section containing the treatment technologies of interest use scroll bar between links | ||||||
| Traditional Treatment Technologies | Potential Alternative Treatment Technologies | |||||
| Catalytic Oxidation | Thermal/Catalytic Oxidation | Adsorption | Chemical Conversion/Destruction | |||
| Thermal Oxidation | Granular Actviated Carbon | Biological Treatment | Other | |||
| Footnotes | Permeable Membrane | Footnotes | ||||
| Technology/Site Location | Description | DREs | By Products Measured? | Dioxins Measured? | Comments | |
| Traditional Thermal, Catalytic or Granular Activitated Carbon Treatment Technologies | ||||||
| Catalytic Oxidation | ||||||
| SVE2 | SVE with catalytic oxidizer at Fire Training Area (FTA-1)2 | Not Available | Not Available | Not Available | Chemical of Concern - TCE and fuels at FTA-12 and Fuels at Bldg 13252 | |
| Castle AFB | SVE with catalytic oxidizer at Bldg 13252 | |||||
| SVE2 | Catalytic oxidation with heat exchanger at Site 10C/68, 2 | Not Available | Not Available | Not Available | Chemical of Concern - TPH, carbon tetrachloride2 | |
| Mather AFB | Catalytic oxidation with heat exchanger at Site 18/592 | Not Available | Not Available | Not Available | Chemical of Concern - TCE, 1,2-DCE, TPH2; Planned January 2000 start-up2 | |
| Catalytic oxidation with heat exchanger at Site 232 | Not Available | Not Available | Not Available | Chemical of Concern - PCE, TCE, 1,2-DCE, xylenes2; Planned February 2000 start-up2 | ||
| Catalytic oxidation with heat exchanger at Site 572 | Not Available | Not Available | Not Available | Chemical of Concern - TCE2 | ||
| SVE2 | Fixed bed, catalytic oxidizer moved from IC-1 to OU-D in 7/962 | Not Available | Not Available | Not Available | Chemical of Concern - TCE, PCE, DCE, TCA, petroleum hydrocarbons2 | |
| McClellan AFB2 | OU-D Site S, OU-C Site 19 | |||||
| Fluidized bed, catalytic oxidizer2 | Not Available | Not Available | Not Available | Chemical of Concern - TCE, DCE, fuels2 | ||
| OU-C1 | ||||||
| Catalytic oxidizer moved from IC-7.2 | Not Available | Not Available | Not Available | Chemical of Concern - TCE, PCE, DCE, fuels2 | ||
| OU-A, IC-31 | ||||||
| Dual Phase Extraction. Plumbed into IC-31 catalytic oxidizer system2 | Not Available | Not Available | Not Available | Chemical of Concern - TCE, PCE, DCE2 | ||
| OU-A, IC-29 | ||||||
| SVE2 | Catalytic oxidation2 | Not Available | Not Available | Not Available | ||
| Lockheed Beaumont2 | Chemical of Concern - TCE, DCE, DCA2 | |||||
| SVE2 | Catalytic oxidation2 | Not Available | Not Available | Not Available | ||
| Riverside County | ||||||
| SVE2 | Not Available | Not Available | Not Available | |||
| Stauffer Chemical Co.2 | Chemical of Concern - TCE, DCA2 | |||||
| SVE2 | Catalytic oxidation2 | Not Available | Not Available | Not Available | ||
| Carson (Los Angeles) | ||||||
| Catalytic oxidation2 | Not Available | Not Available | Not Available | System not installed yet2 | ||
| Landfill2 | Chemical of Concern - methane, benzene, chlorobenzene, 1,4-DCB, 1,1-DCE, 1,1-DCA, 1,2-DCA, ethylbenzene, toluene, PCE, methylene chloride, 1,1,1-TCA, TCE, vinyl chloride, xylene2 | |||||
| Gardena Valley 1&2 | ||||||
| SVE2 | Catalytic oxidation2 | Not Available | Not Available | Not Available | Chemical of Concern - Benzene2 | |
| Monsanto Chemical Co.2 | ||||||
| Carson (Los Angeles) | ||||||
| SVE2 | Catalytic oxidation2 | Not Available | Not Available | Not Available | Chemical of Concern - BTEX, PCE, TCE2 | |
| SP Taylor Yard2 | System not installed yet22 | |||||
| Los Angeles | ||||||
| SVE2 | 2 King Buck Catalytic oxidizers2 | Not Available | Not Available | Not Available | Chemical of Concern - PCE, TCE, acetone, methylene chloride, MEK, TCA, DCA, benzene, vinyl chloride2 | |
| Former McKesson Facility2 | ||||||
| Santa Fe Springs | ||||||
| SVE2 | Catalytic oxidation | Chemical of Concern - TCE, DCE, DCA, vinyl chloride2 | ||||
| Union Pacific2 | ||||||
| Sacramento Rail Yard | ||||||
| SVE2 | Catalytic oxidizers2 | Not Available | Not Available | Not Available | Chemical of Concern - TCE2 | |
| Boeing/Aerojet2 | ||||||
| Rancho Cordova | ||||||
| SVE2 | Catalytic oxidation (King Buck)2 | Not Available | Not Available | Not Available | Chemical of Concern - acetone, tetrachloroethane, cis-1,2-DCA, others2 | |
| Van Waters & Rogers2 | ||||||
| Los Angeles | ||||||
| SVE2 | Catalytic oxidation2 | Not Available | Not Available | Not Available | Chemical of Concern - PCE, TCE2 | |
| Whittaker Bermite2 | ||||||
| Santa Clarita | ||||||
| Thermal Oxidation | ||||||
| Dual Phase Extraction System2 | Thermal oxidation unit2 | Not Available | Not Available | Not Available | Chemical of Concern - TCE2 | |
| Travis AFB | IRP Site SS016, Oil Spill Area | |||||
| SVE2 | Thermal oxidation with heat exchanger2; Site 7 | Not Available | Not Available | Not Available | Chemical of Concern - TPH2 | |
| Mather AFB | Thermal oxidation with heat exchanger2; Site 11 | Not Available | Not Available | Not Available | Chemical of Concern - TPH2 | |
| Thermal oxidation without heat exchanger2; Site 37/39/54 | Not Available | Not Available | Not Available | Chemical of Concern - TPH2 | ||
| Air Stripping Tower on Groundwater Treatment Plant | Flameless Thermal Oxidation2 | Not Available | Not Available | Not Available | Chemical of Concern - TCE, PCE, DCE2 | |
| McClellan AFB2 | ||||||
| SVE2 | Flameless thermal oxidation2; Edge-QR VOC Abatement System | >98% overall27 | Tested for ROC, CO, NOx, SO2, and PM.27 | Total dioxins/ furans: | Chemical of Concern - 1,1- DCE2 | |
| McClellan AFB2 | Soil vapor is combined with natural gas, sent on through a flame arrestor, and into the burner distribution plenum within the Edge-QR Thermal oxidizer. Combustion products are controlled to 1500°F. Effluent from the oxidizer is cooled in a quench chamber to 160°F and then sent to a caustic scrubber.27 | 0.0737-0.720 ng/dscm | ||||
| OU-A, IC-23 | ||||||
| Flameless thermal oxidation2 | Not Available | Not Available | Not Available | Chemical of Concern - TCE2 | ||
| OU-G, T-44 | ||||||
| Flameless thermal oxidation2 | Not Available | Not Available | Not Available | Chemical of Concern - TCE, PCE, DCE2 | ||
| OU-A, IC-43 | Planned mid-2000 start-up2 | |||||
| SVE2 | Thermal oxidation2 | Not Available | Not Available | Not Available | Chemical of Concern - PCE, TCE, acetone, methylene chloride, MEK, TCA, DCA2 | |
| Angeles Chemical Co.2 | Pilot studies in 1999 only2 | |||||
| Santa Fe Springs | ||||||
| SVE2 | 3 Airex Thermal oxidizers2 | Not Available | Not Available | Not Available | Chemical of Concern - BTEX, PCE, TCE, DCA, vinyl chloride2 | |
| Golden Eagle Refinery2 | ||||||
| Carson (Los Angeles) | ||||||
| SVE2 | Thermal oxidation2 | Not Available | Not Available | Not Available | Chemical of Concern - benzene,xylenes, toluene, styrene2 | |
| Kaiser Steel2 | ||||||
| SVE2 | Thermtech thermal oxidizer2 | Not Available | Not Available | Not Available | Chemical of Concern - pesticides, PCBs, PAHS2 | |
| U.C. Riverside2 | Planned for March 20002 | |||||
| Agricultural Experiment Station | ||||||
| SVE2 | Thermal oxidation2 | Not Available | Not Available | Not Available | Chemical of Concern - trimethylbenzene, xylene, ethyltoluene, 1,2-dichloropropane2 | |
| FMC2 | ||||||
| Fresno | ||||||
| SVE2 | Hazardous Waste Incinerator used with SVE cleanup2 | Not Available | Not Available | Not Available | Chemical of Concern - PCE, toluene, ethylbenzene, xylenes2 | |
| Ashland Chemical2 | ||||||
| Commerce | ||||||
| Granular Activated Carbon | ||||||
| SVE2 | Granular Activated Carbon | Not Available | Not Available | Not Available | Thermal treatment is typical for regeneration of carbon | |
| McClellan AFB2 | OU-B, IC-7 | Chemical of Concern - TCE, PCE, DCE2 | ||||
| Granular activated carbon | Not Available | Not Available | Not Available | Chemical of Concern - TCE, PCE, DCE2 | ||
| OU-A, IC-35 | ||||||
| formerly fixed bed, catalytic oxidizer now GAC.2 | Not Available | Not Available | Not Available | Chemical of Concern - TCE, PCE, freon2 | ||
| OU-B, IC-1 | ||||||
| Combined Thermal and Catalytic Oxidation | ||||||
| SVE/Air Sparging System2 | 500 scfm thermal catalytic oxidizer at OU-1, Site 11 - Bldg. 17242 | Not Available | Not Available | Chemical of Concern - Jet Fuel (JP-4) at Site 112 | ||
| Edwards AFB | 500 scfm thermal catalytic oxidizer at OU-1, Site 17 - Bldg. 1425 & 16002 | Petroleum products at Site 172 | ||||
| Dual Phase Extraction System2 | 2000 scfm thermal/catalytic oxidizer at OU-1, Site 16 - Bldg. 18202 | Not Available | Not Available | Dioxin at Site 16: | Chemical of Concern - Jet Fuel (JP-4) and TCE2 | |
| Edwards AFB | 1500 scfm thermal/catalytic oxidizer at OU-1, Sites 5 & 152 | 6.6-9.6 pg/dscm18 | ||||
| SVE2 | Thermal and catalytic oxidation with heat exchange2 | Not Available | Not Available | Not Available | Chemical of Concern - TPH2 | |
| Mather AFB | Site 29 | |||||
| Thermal and catalytic oxidation with heat exchange2 | Not Available | Not Available | Not Available | Chemical of Concern - TPH2 | ||
| Site 35/36 | ||||||
| Potential Alternative Technologies for Vapor Treatment | ||||||
| Adsorption | ||||||
| Resin removal | VOCs removed using polymeric adsorbents. VOCs are desorbed from the resin using three dimensional microwaves.1 | Not Available | Not Available | Not Available | ||
| Ameripure1 - (now American Purification, Inc.) | ||||||
| Elastomeric Polymer Filter12 - (PetroLOKÔ PL22) | Blend of PetroLOKÔ PL22 and activated carbon12,17 | 0% without carbon17 | did not work17 | Not Available | only carbon portion could remove contamination17 | |
| Radian Corporation | VOCs are adsorbed onto the activated carbon from the vapor phase. For water applications, the PetroLOKÔ PL22 absorbs the VOCs from the water and chemically binds them to the PetroLOKÔ PL22.12 | |||||
| Fluidized Bed Recovery7 | Resin/Chiller17 - VOCs are removed from the vapor stream in the adsorption chamber and adsorbed onto the FB material. The FB material is transferred to a continuous flow non-contact heating chamber and desorbed form the FB material. The VOC-laden gas is routed to a two-staged chiller where the VOCs are condensed into two liquid waste streams while the FB material is returned to the adsorption chamber.7 | 91% recovered for TCE17,26 | Not tested26 | Not tested26 | According to the SERDP/NETTS summary, AmbersorbÔ 600 used as the FB material, cohered which caused clogging within the transfer system and prevented the bed from maintaining a fluidized condition. The cohesion was due to a buildup of long-chained hydrocarbons on the AmbersorbÔ 600 which could not be effectively desorbed by the unit.7 | |
| Harding Lawson Associates | 3-43% Freon 11326 | |||||
| 24-67% TVH26 | ||||||
| 85% TCV26 | ||||||
| Microwave Regenerable Granular Activated Carbon (GAC) Treatment6 | GAC regenerated using microwaves and a palladium catalyst | 82% overall25 | At scrubber25: | Low DREs may be associated with the GAC regeneration rate in the micorwave regeneration reactor.25 | ||
| CHA Corporation | GAC is used to remove VOCs and other pollutants from an SVE off-gas stream. VOCs are removed from the saturated GAC using microwaves. The VOCs that are removed are carried to a destruction chamber by a nitrogen purge gas. In the destruction chamber, VOCs are treated using microwaves which induce oxidation reactions on the surface of a palladium catalyst.6 | Nox - 0.0618lb/ day | Conc. below reporting limits for dioxins & furans25 | |||
| CO - 0.0384 lb/day | ||||||
| HF - 0.085 grams/hr | ||||||
| HCl - 0.129 grams/hr | ||||||
| Cl2 - 1.588 grams/day | ||||||
| On-site resin "PADRE"17 - Purus Adsorption Desorption Remediation Equipment (PADRE)15 | The PADRE system consists of two sets of identical resin beds, the active bed and the inactive beds. The resin in the active beds adsorbs VOCs from the off-gas. When the resin is saturated or "full" of VOCs, then the vapor is diverted to the inactive beds. The "full" bed is purged with a hot gas, such as nitrogen, to release the VOCs from the resin. The purge gas containing the VOCs leaves the bed and is cooled in a condenser. The VOCs are removed from the purge gas in the condensed liquid formed.15 | overall 95%17 | Not Available | Not Available | Corrosion problems observed for components that were in contact with the liquid condensate15,17 | |
| Thermatrix, Inc. (formerly PURUS, Inc.) | 70->99.6 contam.17 | 50% water/50%organic17 | ||||
| 101 Metro Drive, Suite 248 | ||||||
| San Jose, CA 95110 | ||||||
| Biological Treatment | ||||||
| Biofilters | Biological decomposition in aqueous phase | 1st stage 43-73%17 | Not tested30 | Not tested30 | with bio upsets, no removal occurred17 | |
| Envirogen, Inc. | 2 stage system: a fixed-film biofilter with continuously stirred reaction tank (CSTR) using cometabolic processes for treating chlorinated VOCs11 | 2nd stage max 15%17 overall 51-74%17 | ||||
| Biological Destruction11 | ||||||
| Phytoremediation23 | Uptake by plants | Not Available | Not Available | Not Available | Technology in demonstration phase | |
| Phytokinetics, Inc. | Treatment of contaminated soils , sediments, and groundwater with plants. Uses several biological mechanisms: (1) the plant’s ability to enhance bacterial and fungal degradation, (2) the nutrients, metabolites, and enzymes excreted by the roots to stimulate microbial activity, and high population of active microbes in the soil near the plant’s roots. 23 | |||||
| Phytovolatilization | Developed four plant species that are capable of removing mercury from the soil and release it as a vapor into the air. Process is called phytovolatilization. Phytovolatilization has been documented to occur when some plants are exposed to certain volatile organic compounds.22 | Not Available | Not Available | Not Available | Technology in demonstration phase | |
| Phytoworks1 | ||||||
| 1400 Mill Creek Rosa | ||||||
| Gladwyne, PA 19035 | ||||||
| Chemical Conversion/Destruction | ||||||
| Advanced Photolytic Destruction3 | Fluidized Bed (FB) concentration/UV | in progress17 | Not Available | Not Available | Cost effective only for high VOC concentrations16 | |
| Process Technologies, Inc. | ||||||
| Photocatalysis - Air 20001 | Ultra Violet (UV) oxidation with catalyst | NA | NA | NA | Product information not listed on Trojan Technologies’ website as of 5-3-01. | |
| Trojan Technologies Inc. | "Volatile organic compounds (VOCs) treated by passing contaminated air through a proprietary catalyst bed that is illuminated with ultraviolet light. | |||||
| 3020 Gore Road | Process operates at ambient temperature." 1 | |||||
| Electrochemical reaction | Electrochemical reaction with cerium oxide in nitric acid | Not Available | Not Available | Not Available | Designed to treat liquids. Not applicable to gas flows at this time, would require design change. | |
| CerOx | temperature 90-99oC | High-energy requirements. | ||||
| Thermochemical Reaction | High temperature cracking and oxidation | 99.9999% PCBs19 | THC (avg)19: 1.53-15.5 ppmv | Dioxin: 0.156-0.368 ng/dscm19 | Information listed for DRE, DE, by products, and dioxins is based on field test data performed using-PCB-contaminated wastewater, waste-oil, and soil. | |
| Eli Eco Logic1 143 Dennis Street | Process uses a gas-phase reduction reaction of hydrogen with organic and chlorinated organic compounds at elevated temperatures to produce a hydrocarbon rich gas product. The gas phase reduction takes place within a specially designed reactor at 850°F.1 | DE: 99.99% PCE19 | CO (avg)19: 2.3-23.3 ppmv | Furans: 0.007-0.011 ng/dscm 19 | ||
| Rockwood, Ontario, Canada | 80-96%benzene19 | PAHs (avg)19: 24.0-28.6 µg/dscm | ||||