US2021269338A1PendingUtilityA1
Method of Treating High Strength Wastewater by Anaerobic Bio Reactor
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
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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-modified1 . 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 .Cited by (0)
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