# US 5,705,050 A · Electrolytic process and apparatus for the controlled oxidation and reduction of inorganic and organic species in aqueous solutions > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 5,705,050 A - Document ID: US5705050A - Status: Granted - Kind: A - Application number: 08/639,756 - Filed: 1996-04-29 - Granted: 1998-01-06 - Earliest claimed: 1996-04-29 - Inventors: Richard L. Sampson; Allison Hawkins Sampson - Web page: https://patentgrep.com/patent/US5705050A ## CPC - C02F 1/46114: {Electrodes in particulate form or with conductive and/or non conductive particles between them} - B01D 61/48: having one or more compartments filled with ion-exchange material {, e.g. electrodeionisation} - B01J 47/08: subjected to a direct electric current - C02F 1/4618: {for producing "ionised" acidic or basic water} - C02F 1/42: by ion-exchange (ion-exchange in general B01J) - C02F 1/4674: {with halogen or compound of halogens, e.g. chlorine, bromine} - C02F 1/4676: {by electroreduction} - C02F 2001/46138: {Electrodes comprising a substrate and a coating} - C02F 2001/46161: {Porous electrodes} - C02F 2103/023: {Water in cooling circuits} - C02F 2201/46115: Electrolytic cell with membranes or diaphragms - C02F 2201/4613: Inversing polarity - C02F 2201/46145: Fluid flow - C02F 2201/4617: DC only - C02F 2303/04: Disinfection - C02F: TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE (separation in general B01D; special arrangements on waterborne vessels of installations for treating water, waste water or sewage, e.g. for producing fresh water, B63J; adding materials to water to prevent corrosion C23F; treating radioactively-contaminated liquids G21F9/04; regeneration of reactants for recirculation into processes, see the relevant places for the processes) - B01D: SEPARATION (separating solids from solids by wet methods B03B, B03D; by pneumatic jigs or tables B03B; by other dry methods B07; magnetic or electrostatic separation of solid materials from solid materials or fluids, separation by high-voltage electric fields B03C; centrifuges, vortex apparatus B04; presses per se for squeezing-out liquid from liquid-containing material B30B9/02; treatment of water C02F, e.g. softening by ion-exchange C02F1/42; {arrangements of air intake cleaners in gas turbine plants F02C7/05} ; arrangements or mounting of filters in air-conditioning, air-humidification or ventilation F24F13/28) - B01J: CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS ## Abstract Improvements on the electrolytic reactor and process of U.S. Pat. No. 5,419,816 and copending U.S. application Ser. No. 08/400,950, filed Mar. 9, 1995, now U.S. Pat. No. 5,609,742, are disclosed for the controlled oxidation and reduction of inorganic and organic species in dilute aqueous solutions. More specifically, other physical forms and additives for the modified ion exchange material can be used in the packed bed electrolytic reactor, including powdered ion exchange materials and solid membranes containing the modified ion exchange materials. Direct contact with only one electrode, the anode for oxidation, and the cathode for reduction, is required for the modified ion exchange resin, instead of with both electrodes. Superior performance is also demonstrated for bipolar operation of the electrolytic reactor in comparison to monopolar operation. Preferably, the polarity of the electrodes is reversed every 1 to 60 minutes. Finally, other point of use applications are disclosed for the electrolytic reactor and process, including sanitization and sterilization, such as useful in the medical, dental and veterinary industries, food and animal disinfection, bacteria control and waste treatment. ## Claims ### Claim 1 An electrolytic process for oxidizing a species in a dilute aqueous solution, comprising the steps of: passing an aqueous feed solution containing said species to be oxidized through a packed bed of modified cation exchange material interposed between an anode and a cathode, with said bed of modified cation exchange material in direct contact with at least said anode; applying a direct current across the anode and cathode in a bipolar fashion; contacting said feed solution with said bed for a time to cause at least a portion of said species to be oxidized by said modified cation exchange material so that said aqueous solution contains said species in an oxidized form; and recovering the aqueous solution containing said oxidized species. ### Claim 2 (depends on 1) A process as defined in claim 1, wherein said modified cation exchange material is a particulate modified cation exchange material. ### Claim 3 (depends on 1) A process as defined in claim 1, wherein said modified cation exchange material is a powdered modified cation exchange material. ### Claim 4 (depends on 1) A process as defined in claim 1, wherein said modified cation exchange material has active semiconductor junctions formed by a cation species permanently bonded to said cation exchange material. ### Claim 5 (depends on 1) A process as defined in claim 1, wherein said modified cation exchange material includes an additive, but without substantially retarding the oxidation of said species. ### Claim 6 (depends on 1) An electrolytic process as defined in claim 1 wherein the said species to be oxidized is an inorganic or an organic species. ### Claim 7 (depends on 1) A process as defined in claim 1, wherein the step of passing said aqueous feed solution through said bed comprises passing said aqueous feed solution through at least one anode chamber, each said anode chamber containing a modified cation exchange material in contact with said anode and separated from each cathode chamber by a cation exchange membrane or diaphragm, and each said cathode chamber without any ion exchange material. ### Claim 8 (depends on 7) A process as defined in claim 7, wherein the cation exchange membrane includes modified cation exchange material. ### Claim 9 (depends on 1) A process as defined in claim 1, wherein the step of passing said aqueous feed solution through said bed comprises passing said aqueous feed solution through at least one anode chamber, each said anode chamber containing a modified cation exchange material in contact with said anode and separated from each cathode chamber by a cation exchange membrane or diaphragm, and each said cathode chamber containing ion exchange material. ### Claim 10 (depends on 9) A process as defined in claim 9, wherein said ion exchange material in said cathode chamber comprises modified ion exchange material. ### Claim 11 (depends on 9) A process as defined in claim 9, wherein the cation exchange membrane includes modified cation exchange material. ### Claim 12 An electrolytic process for reducing a species in a dilute aqueous solution, comprising the steps of: passing an aqueous feed solution containing said species to be reduced through a packed bed of modified anion exchange material interposed between an anode and a cathode, said bed of modified anion exchange material in direct contact with at least said cathode; applying a direct current across the anode and cathode in a bipolar fashion; contacting said feed solution with said bed for a time to cause at least a portion of said species to be reduced by said modified anion exchange material so that said aqueous solution contains said species in an reduced form; and recovering the aqueous solution containing said reduced species. ### Claim 13 (depends on 12) A process as defined in claim 12, wherein said modified anion exchange material is a particulate modified anion exchange material. ### Claim 14 (depends on 12) A process as defined in claim 12, wherein said modified anion exchange material is a powdered modified anion exchange material. ### Claim 15 (depends on 12) A process as defined in claim 12, wherein said modified anion exchange material has active semiconductor junctions formed by an anion species permanently bonded to said anion exchange material. ### Claim 16 (depends on 12) A process as defined in claim 12, wherein said modified anion exchange material includes an additive, but without substantially retarding the reduction of said species. ### Claim 17 (depends on 12) An electrolytic process as defined in claim 12 wherein the said species to be reduced is an organic species or an inorganic species. ### Claim 18 (depends on 12) A process as defined in claim 12, wherein the step of passing said aqueous feed solution through said bed comprises passing said aqueous feed solution through at least one cathode chamber, each said cathode chamber containing a modified anion exchange material in contact with said cathode and separated from each anode chamber by an anion exchange membrane or diaphragm, and each said anode chamber without any ion exchange material. ### Claim 19 (depends on 18) A process as defined in claim 18, wherein the anion exchange membrane includes modified anion exchange material. ### Claim 20 (depends on 12) A process as defined in claim 12, wherein the step of passing said aqueous feed solution through said bed comprises passing said aqueous feed solution through at least one cathode chamber, each said cathode chamber containing a modified anion exchange material in contact with said cathode and separated from each anode chamber by an anion exchange membrane or diaphragm, and each said anode chamber containing ion exchange material. ### Claim 21 (depends on 20) A process as defined in claim 20, wherein said ion exchange material in said anode chamber comprises modified ion exchange material. ### Claim 22 (depends on 20) A process as defined in claim 20, wherein the anion exchange membrane includes modified anion exchange material. ### Claim 23 An ion exchange membrane having a portion of the total ion-exchange sites of said membrane converted to semiconductor junctions by permanently bonding counter ions to said ion exchange sites sufficient to cause formation of a free radical under the influence of direct electrical potential in an aqueous solution. ### Claim 24 (depends on 23) An ion exchange membrane as defined in claim 23, wherein said membrane is a cation exchange membrane and the free radical formed is the hydroxyl. ### Claim 25 (depends on 23) An ion exchange membrane as defined in claim 23, wherein said membrane is an anion exchange membrane and the free radical formed is the hydrogen. ### Claim 26 An electrolytic process for oxidizing a species in a dilute aqueous solution, comprising the steps of: passing an aqueous feed solution containing said species to be oxidized through a packed bed of modified cation exchange material interposed between an anode and a cathode, said bed of modified cation exchange material in direct contact with at least said anode; applying a direct current across the anode and cathode; contacting said feed solution with said bed for a time to cause at least a portion of said species to be oxidized by said modified cation exchange material so that said aqueous solution contains said species in an oxidized form; and recovering the aqueous solution containing said oxidized species. ### Claim 27 (depends on 26) A process as defined in claim 26, wherein said modified cation exchange material has active semiconductor junctions formed by a cation species permanently bonded to said cation exchange material. ### Claim 28 A method for on-site sterilization or waste treatment of an object to be sterilized having undesirable contaminants thereon by use of a treated dilute aqueous solution which comprises adding an inorganic or organic species to at least a portion of a dilute aqueous solution, contacting said at least a portion of said dilute aqueous solution containing said inorganic or organic species with a monobed of particulate modified ion exchange material interposed between an anode and a cathode of an electrolytic reactor in which a direct current is applied across the anode and cathode, for a time to cause free radical formation in said modified ion exchange material and oxidation or reduction of at least a portion of said inorganic or organic species to a reducing or oxidizing reagent by said modified ion exchange material, applying said treated aqueous solution to said object to be sterilized to reduce or oxidize the undesirable contaminants thereon by said reducing or oxidizing reagent.