Systems and methods for treating water containing PFAS are disclosed. A bioreactor and a supercritical water oxidation (SCWO) system may be implemented to provide a complete chain of separation and destruction of PFAS to treat contaminated water. Adsorption media may be added to facilitate the removal of PFAS from water.

A MBR system for removing PFAS from a flow of wastewater and/or landfill leachate includes an MBR which receives the flow of wastewater and/or landfill leachate having PFAS therein. An impregnation subsystem receives a flow of mixed liquor from the MBR and a predetermined amount PAC to maintain a predetermined ratio of PAC to biomass in the MBR and blends the biomass with the PAC to form PAC-impregnated biological flocs. An outlet coupled to impregnation subsystem outputs a flow of PAC-impregnated biological flocs to the MBR such that the PAC-impregnated biological flocs in the MBR adsorb to and remove a majority of the PFAS from the flow of wastewater and/or landfill leachate and the MBR outputs a flow of treated wastewater and/or landfill leachate having a majority of the PFAS removed.

Systems and methods for producing ultrapure water (UPW) for use in semiconductor fabrication include an ABA module that performs an advanced oxidation process (AOP) pre-treatment step, a bioremediation step, and an advanced oxidation process post-treatment step. Raw water flows through the ABA module, which is part of a water treatment system for producing ultrapure water. The ultrapure water is then used in a semiconductor fabrication process.

A method of treating wastewater includes removing BOD and ammonium from the wastewater. The wastewater is directed into a tank where it is mixed with mixed liquor or activated sludge from an activated sludge wastewater treatment system. The mixture of wastewater and mixed liquor or activated sludge forms a mixed liquor stream. The mixed liquor stream is directed to a ballasted flocculation system where suspended solids is removed from the wastewater. This produces a clarified effluent that is directed to a zeolite tank. Clarified wastewater from the ballasted flocculation system is directed into the zeolite tank and mixed with zeolite. Zeolite is effective to remove ammonium from the wastewater. Thus, the process as a whole is effective in removing suspended solids, soluble BOD as a result of mixing the mixed liquor or activated sludge with the wastewater, and ammonium.

A flow through aerobic granular sludge (AGS) system includes a flow through reactor. The flow through reactor includes a first adsorption zone and first and second unaerated and aerated zones and may include a wastewater distribution system and a selector zone. The first adsorption zone includes AGS granules and may include a mixing device. The first and second unaerated zones are under anaerobic, anoxic, or both anaerobic and anoxic conditions and each may include a mixing device. The first and second aerated zones are under aerobic conditions and each may include an aeration device. The flow through reactor is configured such that the wastewater and AGS granules in the first adsorption zone flow continuously from the first adsorption zone through the first unaerated zone, the first aerated zone, the second unaerated zone, the second aerated zone, and optionally to the selector zone and out of the flow through reactor.

Provided herein is a process for the removal of micropollutants and/or other pollutants from water, involving subjecting the water to a consecutive combination of biological adsorbent filtration (BAF) followed by oxidation treatment (OT), preferably ozone treatment. In a preferred embodiment, an adjustable amount of the OT effluent, preferably an adjustable amount ranging between 10-100%, more preferably 20-90%, more preferably 20-80%, most preferably 20-50% of the OT effluent, is recirculated to the BAF. The process may involve monitoring the formation of oxidation products at the end of the OT, and/or for measuring TOC, DOC, SUVA, ammonium and/or specifically targeted pollutants in or at the end of the BAF, and controlling the amount of BAF-OT treated water which is recirculated to the consecutive steps of BAF and OT based on the output of the monitoring step.

A system for decontamination of ground water containing one or more per- and polyfluoroalkyl substances (PFAS) at water treatment plants includes a powder activated carbon (PAC) module in fluid communication with a source of water containing the PFAS, wherein the PAC module comprises at least one bag filter pre-filled with the powder activated carbon, and a filter ripening module positioned downstream of the PAC module and configured to capture excess color and turbidity, wherein the powder activated carbon has a particle size of at least about 1 micron.

A granular activated carbon (GAC) reactivation waste product enhanced activated sludge system for removing PFAS from a flow of wastewater and/or landfill includes at least one bioreactor including biomass to receive the flow wastewater and/or landfill leachate and to promote growth of biological flocs and an impregnation subsystem to receive a flow of biomass and a predetermined amount of GAC reactivation waste product and to blend the biomass with the GAC reactivation waste product to form GAC reactivation waste product-impregnated biological flocs. The at least one impregnation subsystem outputs a flow of GAC reactivation waste product-impregnated biological flocs to the bioreactor such that the GAC reactivation waste product-impregnated biological flocs in the bioreactor adsorb to and remove a majority of the PFAS from the flow of wastewater and/or landfill leachate and the bioreactor outputs a flow of GAC reactivation waste product-impregnated biological flocs having a majority of the PFAS adsorbed thereto and wastewater and/or landfill leachate having a majority of the PFAS removed. The system also includes at least one secondary clarifier coupled to the bioreactor which separates the GAC reactivation waste product-impregnated biological flocs having a majority of the PFAS adsorbed thereto from the wastewater and/or landfill leachate having a majority of the PFAS removed and produces a flow the treated wastewater and/or landfill leachate having a majority of the PFAS removed.

A system and method for decontamination of surface water containing one or more per- and polyfluoroalkyl substances (PFAS) at water treatment plants is provided. The system includes a flocculation module, at least one solids removal module, and a powder activated carbon (PAC) module positioned downstream from the flocculation module and upstream of the at least one solid removal module. The PAC module including a metering device configured to continuously dose a powder activated carbon to water treatment plant process water.

A flow through aerobic granular sludge (AGS) system includes a flow through reactor. The flow through reactor includes a first adsorption zone, first and second unaerated and aerated zones, and a wastewater distribution system. The first adsorption zone includes AGS granules introduced to a top of the first adsorption zone. The first and second unaerated zones are under anaerobic, anoxic, or both anaerobic and anoxic conditions. The first and second aerated zones are under aerobic conditions. The wastewater distribution system includes a distribution grid of piping or an underdrain system at a bottom of the adsorption zone. The flow through reactor is configured such that, in operation, the wastewater and AGS granules flow continuously from the first adsorption zone through the first unaerated zone, the first aerated zone, the second unaerated zone, and the second aerated zone.