C02F1/4672

Disinfection system device for producing ozone water directly in water pipe system

A disinfection system device for producing ozone water directly in a water pipe system contains an electrolytic tap water ozonation generator and holder. The electrolytic tap water ozonation generator includes at least one anode sheet and at least one cathode sheet. The holder includes a base, and the base has a locking portion, an inflow orifice, an outflow orifice, a connection interface, and a damping valve. A flow switch is mounted above the base and has an intake, and a discharge orifice of the flow switch is communicated with the outflow orifice. A top of the base is connected with one of two lids, the other lid is connected with the first socket and a second socket, and the other lid accommodates a control panel. The number of the anode sheet(s) is n which is a natural number and n≥1. The number of the cathode sheets is n+1.

UNWANTED MATTER REMOVAL DEVICE, UNWANTED MATTER REMOVAL METHOD, SEPARATION DEVICE AND SEPARATION METHOD
20230121484 · 2023-04-20 ·

An unwanted matter removal device includes a removal tank 10, a pair of electrodes 31A and 31B disposed in the removal tank 10, a flow path 40 composed of the pair of electrodes 31A and 31B, a Fenton's reagent introduction portion that introduces a Fenton's reagent into the flow path, a liquid introduction portion that introduces a liquid containing an unwanted matter that should be removed into the flow path and a liquid discharge portion that discharges the liquid from the flow path, and the pair of electrodes 31A and 31B are composed of comb-like electrodes.

OZONE LAUNDRY SYSTEM
20230069797 · 2023-03-02 ·

A water ozonation system (18) that receives source water (16) from a water source (14) and converts it to ozonated water (20) for use in a washing machine (12) includes a system body (30), an ozone generator (38), a sensor assembly (21), and a controller (46). The system body (30) receives the source water (16) from the water source (14). The ozone generator (38) is configured to generate ozone. The ozone generator (38) is coupled the system body (30). The sensor assembly (21) is also coupled to the system body (30). The sensor assembly (21) is configured to sense at least one ambient environmental condition and generate at least one electronic data signal based on the sensed at least one ambient environmental condition. The controller (46) receives the at least one electronic data signal from the sensor assembly (21) and regulates a level of ozone that is generated by the ozone generator (38) based at least in part on the at least one electronic data signal.

ELECTROCHEMICAL METHOD FOR OXIDATION OF ORGANIC COMPOUNDS IN AQUEOUS SOLUTIONS AND REDUCTION OF BY-PRODUCTS
20220324729 · 2022-10-13 · ·

Methods for electrochemically oxidizing organic compounds in aqueous solution. The methods include contacting an aqueous solution comprising organic compounds with a first anode and electrochemically oxidizing at least a portion of the organic compounds to provide a first aqueous solution comprising oxidation products; and contacting the first aqueous solution comprising oxidation products with a first cathode and electrochemically reducing at least a portion of the oxidation products to provide a first aqueous solution comprising reduced products and residual oxidizable organic compounds. The first aqueous solution can be further treated to electrochemically oxidize at least a portion of the residual oxidizable organic compounds to provide a second aqueous solution comprising oxidation products, and the second aqueous solution can be further treated to electrochemically reduce at least a portion of the oxidation products to provide a third aqueous solution comprising reduced products and residual oxidizable organic compounds. Systems for electrochemically oxidizing organic compounds and effectively carrying out the methods are also provided.

Electroactive Bio-Carrier Module and Sewage Treatment Device with Same

An electroactive bio-carrier module and a sewage treatment device using same are provided, which relate to the field of bioelectrochemistry and sewage treatment. The electroactive bio-carrier module is composed of an anode module and a cathode module made of a conductive material. The anode module is formed by connecting carbon fiber brushes in series and is of a vertically ring type structure; the cathode module is formed by connecting stainless steel meshes in series; the stainless steel meshes are in a folded horizontal stacked design; the anode and cathode modules are connected through an external lead wire to form a circuit. Surfaces of the anode and cathode modules can both enrich microorganisms, biofilms are formed on the surfaces. The electrode module is arranged in an up-flow type sewage treatment device and is used as an electroactive bio-carrier, to form a hybrid sewage treatment device with a built-in electroactive bio-carrier.

METHOD AND SYSTEM FOR REMOVING CONTAMINANTS FROM SOIL

Methods, systems, and techniques for removal of PFAS contaminants from contaminated soil or sediment are provided. Example embodiments provide a water-based ex-situ method and system at a site that utilizes particle size and particle density segregation; deagglomeration, attrition, and retention time and sequential contacts with purified water; a recirculating water system with continual water treatment, and additional modules for destructive treatment of concentrated PFAS. In an example embodiment, the water treatment system of an example PFAS contaminant removal system and process includes ion exchange resin filtration component to remove PFAS effectively.

BIAS ENHANCED ELECTROLYTIC PHOTOCATALYSIS (BEEP) CLEANING SYSTEM
20230113314 · 2023-04-13 ·

Methods and systems for the purification of an aqueous solution comprising a photocatalyst employed as an anode and a cathode in communication with an electrolyte to achieve a current flow wherein a charge is applied between the cathode and the photocatalytic excited anode a corresponding increase in electron-hole pairs occurs.

System and method for removal of PFAS from waste streams

A system and method for removing and destroying PFAS from residual waste streams generated during the processing of landfill liquids prior to disposal are provided. The presently disclosed system and method can concentrate PFAS from landfill liquids into a residual waste stream so that the target compounds can be selectively removed for subsequent destruction.

FREE-STANDING POROUS CARBON FIBROUS MATS AND APPLICATIONS THEREOF
20230106325 · 2023-04-06 ·

A method of producing a porous carbon composite fibrous mats formed of a network of carbon fibers incorporated with porous carbon particles. The method includes electrospinning a polymer solution to form a porous layer of polymeric fibers and the polymeric fibers are doped with a precursor of conductive metal particles, where the polymer solution includes a polymer and the precursor of the conductive metal particles, electrospraying a metal organic framework suspension onto the porous layer of polymeric fibers, where the metal organic framework suspension includes metal organic framework particles, repeating the electrospinning and electrospraying in an alternating manner to form a porous network of polymeric fibers incorporated with the metal organic framework particles, and heating the porous network of polymeric fibers incorporated with the metal organic framework particles to form the porous carbon composite fibrous mats.

Water and Energy Recovery System

Systems and methods for wastewater treatment are described. In some embodiments, a wastewater treatment system may include a container configured to receive and store at least a portion of incoming wastewater during a digestion process that generates biogas and a biogas burner. The biogas burner may be arranged to receive and burn at least a portion of the biogas generated by the digestion process. The system may be configured to heat solids separated from the wastewater such that: (i) the solids separated from the wastewater are maintained at a temperature of at least 70° C. for at least 30 minutes; and/or (ii) a water content of the solids separated from the wastewater is less than 15% by mass.