US2021269338A1PendingUtilityA1

Method of Treating High Strength Wastewater by Anaerobic Bio Reactor

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Assignee: AQUATECH INT LLCPriority: Oct 21, 2016Filed: May 18, 2021Published: Sep 2, 2021
Est. expiryOct 21, 2036(~10.3 yrs left)· nominal 20-yr term from priority
B01D 71/024H01M 8/16C02F 2303/12C02F 3/2853B01D 2321/168B01D 2311/2688B01D 65/02B01D 2311/10B01D 61/14C02F 3/005C02F 2303/16B01D 2321/2041B01D 61/18B01D 2315/06B01D 2315/10H01M 4/96B01D 2321/04Y02E60/50
60
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Claims

Abstract

We provide methods, systems, and apparatus for treatment of high chemical oxygen demand wastewater using anaerobic treatment with ceramic membranes. We also provide post-treatment using microbial fuel cells.

Claims

exact text as granted — not AI-modified
1 . A method of treating waste water including biodegradable compounds, comprising:
 feeding wastewater to an anaerobic reactor;   operating the anaerobic reactor at a substantially constant temperature range to produce a mixed liquor including suspended solids and wastewater;   feeding the mixed liquor to at least one ceramic membrane to separate suspended solids and wastewater, thereby producing a purified water stream.   
     
     
         2 . The method of  claim 1 , further comprising continuously stirring the anaerobic reactor during the step of feeding wastewater. 
     
     
         3 . The method of  claim 1 , wherein the substantially constant temperature range is between 20° C. and 45° C. 
     
     
         4 . The method of  claim 3 , wherein the substantially constant temperature range is between 36° C. and 38° C. 
     
     
         5 . The method of  claim 1 , wherein the substantially constant temperature range is between 56° C. and 58° C. 
     
     
         6 . The method of  claim 2 , wherein the continuous stirring is conducted through a hydraulic mixer. 
     
     
         7 . The method of  claim 6 , wherein a hydraulic mixer nozzle accommodates a high velocity of up to 14 m/sec. 
     
     
         8 . The method of  claim 1 , wherein the at least one ceramic membrane is selected from the group consisting of an ultrafiltration ceramic membrane and a microfiltration ceramic membrane. 
     
     
         9 . The method of  claim 1 , wherein the ceramic membrane is operated at a cross flow velocity of 1.5-4.0 m/sec 
     
     
         10 . The method of  claim 1 , wherein the ceramic membrane is operated at flux between 15 to 100 lmh. 
     
     
         11 . The method of  claim 1 , further comprising cleaning the ceramic membrane using backwash to retain flux at the substantially constant temperature range. 
     
     
         12 . The method of  claim 1 , further comprising chemical cleaning the ceramic membrane by circulating a solution of sodium hypochlorite, sodium hydroxide, hydrochloric acid and citric acid through the ceramic membrane. 
     
     
         13 . A method for post-treatment conditioning of wastewater conditioned by an anaerobic process, comprising:
 feeding product water from an anaerobic membrane bioreactor to a microbial fuel cell, wherein the microbial fuel cell comprises graphite electrodes and a heterogeneous cation exchange membrane.   
     
     
         14 . The method of  claim 13 , wherein the microbial fuel cell includes both a high oxidation-reduction potential zone and a low oxidation-reduction potential zone separated by heterogeneous cation exchange membrane. 
     
     
         15 . The method of  claim 14 , wherein an anaerobic outlet of the anaerobic membrane bioreactor feeds to the low oxidation-reduction potential zone of the microbial fuel cell. 
     
     
         16 . The method of  claim 14 , wherein an air and water mixture is fed to the high oxidation-reduction potential zone. 
     
     
         17 . The method of  claim 16  further comprising generating voltage due to a potential difference between high oxidation-reduction potential zone and a low oxidation-reduction potential zone in the microbial fuel cell following degradation of chemical oxygen demand in the low oxidation-reduction potential zone. 
     
     
         18 . A method of treating waste water including biodegradable compounds, comprising:
 feeding wastewater to an anaerobic reactor; and   feeding the wastewater to at least one ceramic membrane to separate suspended solids and wastewater, thereby producing a purified water stream.   
     
     
         19 . An apparatus carrying out a method of  claim 1 .

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