Electrode, fuel cell and water treatment device
US-2017309942-A1 · Oct 26, 2017 · US
US10640401B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10640401-B2 |
| Application number | US-201715589219-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 8, 2017 |
| Priority date | May 18, 2016 |
| Publication date | May 5, 2020 |
| Grant date | May 5, 2020 |
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A system and method for algal harvesting and destabilization are provided. The system includes a multifunctional reactive electrochemical membrane (REM). The application of an electrical current generates reactive species at the REM surface and oxidizes algae and soluble organic compounds. This novel type of membrane filtration avoids the use of harmful chemical additives. In addition, it provides the benefits of avoiding polymer aging, membrane fouling, and high costs caused by high transmembrane pressures and frequent membrane cleaning. Traditional membrane separation that significantly suffers from membrane fouling due to either the formation of a cake layer of algal cells, or more commonly due to organic matter adsorption onto the membrane surface is significantly avoided.
Opening claim text (preview).
What is claimed is: 1. An electrochemical membrane filtration system for water purification and biomass separation, comprising: a multifunctional reactive electrochemical membrane having a porous substance and a filtration reactive electrochemical membrane surface, the membrane acting as an electrode and disposed in a filtration tank; an electrically conductive mesh having a mesh surface and surrounding the membrane and performing as a counter electrode to the membrane; and a power source connected to the membrane and the mesh wherein an electrical current generates reactive species at the reactive electrochemical membrane surface and oxidizes algae and soluble organic compounds; and wherein the power source is an AC power source, and surface radicals are generated by applying an AC current at an intermittent rate and at a radio frequency of 100 to 500 MHz to polarize the reactive electrochemical membrane surface or the mesh surface or both the membrane and the mesh surfaces for inducing oxidant or radical production and electrostatic repulsion against potential foulants. 2. The electrochemical membrane filtration system in claim 1 , wherein the membrane is made of a ceramic material. 3. The electrochemical membrane filtration system in claim 2 , wherein the ceramic is Ti 4 O 7 . 4. The electrochemical membrane filtration system in claim 1 , wherein the membrane is made of a conductive material in the form of a tube or a flat membrane. 5. The electrochemical membrane filtration system in claim 1 , wherein the mesh is a stainless steel mesh. 6. The electrochemical membrane filtration system in claim 1 , wherein the mesh completely surrounds the membrane. 7. The electrochemical membrane filtration system in claim 1 , wherein the power source is used to polarize the membrane surface or the mesh surface to generate radicals for organic compound degradation and removal and repulsion of surface foulants. 8. The electrochemical membrane filtration system in claim 7 , wherein surface radicals are generated by applying an electric current density from 50 A·m −2 to 250 A·m −2 or approximately 10 to 22 V of voltage. 9. The electrochemical membrane filtration system in claim 1 , further including a baffle settling tank in communication with the filtration tank, wherein the baffle settling tank is used for a pre-settling process to concentrate biomass. 10. An electrochemical membrane filtration system for water purification and biomass separation, comprising: a multifunctional reactive electrochemical membrane having a porous Ti 4 O 7 substance and a filtration reactive electrochemical membrane surface, the membrane acting as an electrode and disposed in a filtration tank; a stainless steel mesh having a mesh surface and surrounding the membrane inside the filtration tank, wherein the mesh is a counter electrode to the membrane; a baffle settling tank for receiving a biomass feed and concentrating algal biomass, the baffle settling tank in communication with the filtration tank; a receiving tank in communication with the membrane and containing filtered water from the filtration tank; a power source connected to the membrane and the mesh wherein an electrical current generates reactive species at the reactive electrochemical membrane surface and oxidizes algae and soluble organic compounds; and wherein the power source is an AC power source, and surface radicals are generated by applying an AC current at an intermittent rate and at a radio frequency of 100 to 500 MHz to polarize the reactive electrochemical membrane surface or the mesh surface or both the membrane and the mesh surfaces for inducing oxidant or radical production and electrostatic repulsion against potential foulants. 11. The electrochemical membrane filtration system in claim 10 , further including a three-way valve disposed between the membrane and reeving tank, wherein the thee-way valve switches between a permeate discharge position and a backwash water position to withdraw water from the receiving tank. 12. The electrochemical membrane filtration system in claim 10 , wherein the receiving tank further includes a water level sensor or an absorption sensor. 13. The electrochemical membrane filtration system in claim 12 , further including a controller in communication with the water level sensor or absorption sensor, wherein the controller receives at least one process parameter, and adjusts operation of the system based upon processing of the at least one process parameter. 14. The electrochemical membrane filtration system in claim 13 , further including a flow meter disposed between the membrane and the receiving tank. 15. The electrochemical membrane filtration system in claim 14 , wherein surface fouling or pore clogging on the membrane is indicated by the changes of a permeate flux measured by the flow meter or the water level sensor, and backwash is performed together with AC polarization when the permeate flux declines.
Combined electrochemical biological processes (aeration by electrolytically produced oxygen bubbles C02F3/202) · CPC title
Liquid flow rate · CPC title
by electrooxydation · CPC title
Regeneration of sorbents, filters · CPC title
use of algae · CPC title
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