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Description | Synonyms | Applicability | Limitations | Site Information | Points of Contact | |
Data Needs | Performance | Cost | References | Vendor Info. | Health & Safety |
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Description: Figure 4-56:Typical Membrane Separation Diagram A high pressure membrane separation system has been designed by DOE to treat feedstreams that contain dilute concentrations of VOCs. The organic vapor/air separation technology involves the preferential transport of organic vapors through a nonporous gas separation membrane (a diffusion process analogous to pumping saline water through a reverse osmosis membrane). In this system, the feedstream is compressed and sent to a condenser where the liquid solvent is recovered. The condenser bleed stream, which contains approximately 5,000 ppm of the VOC, is then sent to the membrane module. The membrane module is comprised of spiral-wound modules of thin film membranes separated by plastic mesh spacers. The membrane and the spacers are wound spirally around a central collection pipe. In the membrane module the stream is further concentrated to 3% VOC. The concentrated stream is then returned to the compressor for further recovery in the condenser. |
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Synonyms: NA |
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Applicability: The targeted contaminants are VOCs, carbon tetrachloride, and chloroform in gas streams. |
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Limitations: Limitations of this technology are:
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Data Needs: A detailed discussion of these data elements is provided in Subsection 2.2.3. (Data Requirements for Air Emissions/Off-Gases). |
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Performance Data: This technology is being tested at a Hanford site where VOCs will be obtained by vacuum extraction. Carbon tetrachloride and chloroform will preferentially be removed from the gas stream. Based upon a VOC effluent concentration of 1,000 ppm, there is a 95% removal efficiency. The remaining 5% is polished using carbon adsorption. Future work involves sizing the pilot plant to handle fluctuations in the VOC concentrations and fouling of the membrane with other constituents. |
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Cost: Capital equipment (7,000 scfm) is $2.5 million; O&M is $6,000 (replacement every 3 years). Information on life-cycle will be available upon completion of testing, and emissions treatment is $2,000 to $5,000 per pound of VOC recovered. |
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References: DOE, 1994. Technology Catalogue, First Edition. February.DOE-RL, 1993. Technical Name: VOC Offgas Membrane Separation, Technology Information Profile (Rev. 3), DOE ProTech Database, TTP Reference No.: RL-9740. EPA, 1992. SBP Technologies Membrane Filtration, EPA RREL, Demonstration Bulletin, EPA/540/MR-92/014; and Applications Analysis, EPA/540/AR-92/014. EPA, 1994. Membrane Technology and Research, Inc. - Volatile Organic Compound Removal from Air Streams by Membrane Separations, EPA RREL, Emergency Technology Bulletin, EPA/540/F-94/503. EPA, 1994. Volatile Organic Compound Removal from Air Streams by Membrane Separation, EPA RREL, Emerging Technology Bulletin, EPA/540/F-94/503. |
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Site Information:
Points of Contact:
Technology Specific Web Sites:
Vendor Information:
A list of vendors offering Air Emission/Off-Gas Treatment is available from EPA REACH IT which combines information from three established EPA databases, the Vendor Information System for Innovative Treatment Technologies (VISITT), the Vendor Field Analytical and Characterization Technologies System (Vendor FACTS), and the Innovative Treatment Technologies (ITT), to give users access to comprehensive information about treatment and characterization technologies and their applications. Health and Safety:
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Notice | |
Foreword | |
Report Documentation Page | |
Acknowledgement | |
Objectives | |
Background | |
How to use this document | |
Natural Resources | |
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Online Survey |
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Nonhalogenated VOCs | |
Halogenated VOCs | |
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Inorganics | |
Radionuclides | |
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Soil,Sed.,Bedrock & Sludge | |
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In Situ Thermal | |
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Other Treatment | |
Ground,Surf. H2O,Leachate | |
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Ex Situ Phys/Chem | |
Containment | |
Off Gas & Air Emissions | |
Biofiltration | |
High Energy Destruction | |
Membrane Separation | |
Oxidation | |
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Carbon Adsorption |
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Soil,Sed.,Bedrock & Sludge | |
Gr. & Surf. H2O, Leachate | |
Air Emissions/Off-Gases |
Properties & Behavior | |
Techs for Soil | |
Techs for H2O | |
Techs for Air Emissions | |
Treatment Train |
Properties & Behavior | |
Techs for Soil | |
Techs for H2O | |
Techs for Air Emissions | |
Treatment Train |
Properties & Behavior | |
Techs for Soil | |
Techs for H2O | |
Techs for Air Emissions | |
Treatment Train |
Properties & Behavior | |
Techs for Soil | |
Techs for H2O | |
Treatment Train |
Properties & Behavior | |
Techs for Soil | |
Techs for H2O | |
Treatment Train |
Properties & Behavior | |
Techs for Soil | |
Techs for H2O | |
Treatment Train |
Properties & Behavior | |
Techs for Soil | |
Techs for H2O | |
Treatment Train |
Properties & Behavior | |
Techs for Soil | |
Biological Techs | |
Thermal Techs | |
Other Techs | |
Common Techs | |
Treatment Train |
Bioventing | |
Enhanced Bioremediation | |
Phytoremediation |
Chemical Oxidation | |
Electrokinetic Sep. | |
Fracturing | |
Soil Flushing | |
Soil Vapor Extraction | |
Solidification/Stabilization |
Thermal Treatment |
Biopiles | |
Composting | |
Landfarming | |
Slurry Phase |
Chemical Extraction | |
Chemical RedOx | |
Dehalogenation | |
Separation | |
Soil Washing | |
Solidification/Stabilization |
Hot Gas Decon. | |
Incineration | |
OB/OD | |
Pyrolysis | |
Thermal Desorption |
Landfill Cap | |
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Natural Attenuation | |
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Chemical Oxidation | |
Directional Wells | |
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Thermal Treatment | |
Hydrofracturing | |
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Treatment Walls |
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Constructed Wetlands |
Adsorption/Absorption | |
Adv. Oxidation Processes | |
Air Stripping | |
GAC | |
Ground Water Pumping | |
Ion Exchange | |
Prec./Coag./Flocc. | |
Separation | |
Sprinkler Irrigation |
Physical Barriers | |
Deep Well Injection |