US2008000819A1PendingUtilityA1

Water decontamination systems

Assignee: LIQUID SEPARATION TECHNOLOGIESPriority: Feb 15, 2006Filed: Feb 14, 2007Published: Jan 3, 2008
Est. expiryFeb 15, 2026(expired)· nominal 20-yr term from priority
B01D 46/2411B01D 46/02C02F 2101/322B01D 17/047B03D 1/1412C02F 1/20B01D 1/16B03D 1/028B03D 1/26
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Claims

Abstract

Water decontamination systems including one or more of an aerator module, a separator tower, and a contamination gas treatment system are described herein. Such systems are capable of removing contaminants, including volatile organic compounds, from the water. Certain volatile organic contaminants can be removed at high efficiencies. The systems may be automated to remove the contaminants and produce cleaned water on a continuous basis.

Claims

exact text as granted — not AI-modified
1 . A system comprising: 
 an aerator module configured to convert one or more contaminants in a contaminated liquid into gas phase contaminants;    a separator tower configured to convert the contaminated liquid into a contaminated gas phase and a liquid with reduced levels of the one or more contaminants; and    a contaminated gas treatment system configured to receive the contaminated gas phase and the gas phase contaminants;    wherein the contaminated gas treatment system reduces the levels of contaminants in the contaminated gas phase and the gas phase contaminants.    
     
     
         2 . The system of  claim 1 , wherein the aerator module comprises a plurality of nozzles, wherein the nozzles are configured to deliver gas bubbles to the contaminated liquid.  
     
     
         3 . The system of  claim 1 , wherein the aerator module operates under a static or dynamic vacuum.  
     
     
         4 . The system of  claim 1 , wherein the separator tower comprises a high vacuum environment.  
     
     
         5 . The system of  claim 1 , wherein the separator tower comprises a plurality of nozzles which receive the contaminated liquid and are configured to convert the contaminated liquid into an atomized contaminated mist.  
     
     
         6 . The system of  claim 5 , wherein the contaminated mist is converted into the contaminated gas phase and the liquid with reduced levels of the one or more contaminants.  
     
     
         7 . The system of  claim 1 , wherein the liquid with reduced levels of one or more contaminants comprises less than about 5% of the contaminants in the contaminated liquid.  
     
     
         8 . The system of  claim 1 , wherein the liquid with reduced levels of one or more contaminants comprises less than about 1% of the contaminants in the contaminated liquid.  
     
     
         9 . The system of  claim 1 , wherein the liquid with reduced levels of one or more contaminants comprises less than about 0.5% of the contaminants in the contaminated liquid.  
     
     
         10 . The system of  claim 1 , wherein the liquid with reduced levels of one or more contaminants comprises less than about 0.1% of the contaminants in the contaminated liquid.  
     
     
         11 . The system of  claim 1 , wherein the one or more contaminants are volatile organic compounds.  
     
     
         12 . The system of  claim 1 , wherein the contaminated gas treatment system reduces the levels of contaminants by one or more processes selected from the group consisting of adsorption, oxidation, and condensation of the contaminants.  
     
     
         13 . The system of  claim 1 , wherein the aerator module, the separator tower, and the contaminated gas treatment system is in communication with a controller.  
     
     
         14 . The system of  claim 13 , wherein the controller is capable of activating or deactivating of one or more aerator module, the separator tower, the contaminated gas treatment system.  
     
     
         15 . The system of  claim 13 , wherein the controller is capable of regulating one or more of the aerator module, the separator tower, and the contaminated gas treatment system.  
     
     
         16 . The system of  claim 13 , wherein the controller is capable of regulating the influent or effluent transfer of water into or from one or more of the aerator module or the separator tower.  
     
     
         17 . The system of  claim 13 , wherein the controller is capable of regulating flow of the contaminated gas from one or more of the aerator module and separator tower.  
     
     
         18 . The system of  claim 1 , wherein the system is configured to extract and treat a contaminated gas from soil, wherein the contaminated gas does not comprise a contaminated liquid.  
     
     
         19 . A system comprising: 
 an aerator module configured to convert one or more contaminants in a contaminated liquid into gas phase contaminants;    a contaminated gas treatment system configured to receive the gas phase contaminants;    wherein the contaminated gas treatment system reduces the levels of contaminants in the gas phase contaminants.    
     
     
         20 . A system comprising: 
 a separator tower configured to convert a contaminated liquid into a contaminated gas phase and a liquid with reduced levels of the one or more contaminants; and    a contaminated gas treatment system configured to receive the contaminated gas phase;    wherein the contaminated gas treatment system reduces the levels of contaminants in the contaminated gas phase.    
     
     
         21 . The system of  claim 20 , wherein the liquid with reduced levels of the one or more contaminants is substantially free of contaminants.  
     
     
         22 . The system of  claim 20 , wherein the separator tower receives a dilution air.  
     
     
         23 . The system of  claim 22 , wherein the dilution air mixes with the contaminated gas phase in the separator tower.  
     
     
         24 . The system of  claim 22 , wherein the contaminated gas phase treatment system is configured to control an amount of the dilution air.  
     
     
         25 . The system of  claim 20 , wherein the contaminated liquid is contaminated water.

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