A three-dimensional electrode-ozone oxidation-electrocatalytic membrane coupled wastewater treatment device, including a circulating fluidized bed reactor. The circulating fluidized bed reactor includes a funnel-shaped internal, a truncated cone, a fiber ball filter, a gas-liquid distribution plate, an inner cylinder, an intermediate cylinder and an outer cylinder. The inner cylinder, the intermediate cylinder and the outer cylinder are coaxial. The inner cylinder is an electrocatalytic membrane assembly; the intermediate cylinder is a gas diffusion electrode; and the outer cylinder is a stainless-steel mesh. A particle electrode is filled between the intermediate cylinder and the outer cylinder, and between the intermediate cylinder and the inner cylinder. The intermediate cylinder is connected to a negative electrode. The inner cylinder and the outer cylinder are connected to a positive electrode. A wastewater treatment method using the device is also provided herein.

An embodiment of this disclosure provides a liquid treatment device, provided at a carbon block used for post-treating a liquid treated by the carbon block. The liquid treatment device includes: a housing; a cover; a sealing portion; a lower treatment unit; and an upper treatment unit. The liquid treatment device and the carbon block may be detachably mounted mutually, thereby enabling the liquid treatment device to be replaced independent of the carbon block. Furthermore, the liquid treatment device includes an upper treatment unit and a lower treatment unit, and a liquid inlet is provided in the housing of the liquid treatment device, thereby making distribution of the liquid flow in the carbon block more uniform.

A chemical solution supply system including: a first tank that stores a first chemical solution; a first pipe that is connected to the first tank and conveys the first chemical solution; a first filter unit that is connected to the first pipe and has a first filter through which the first chemical solution is filtered; a first valve that is provided in the first pipe between the first tank and the first filter unit; a second tank that stores a second chemical solution; and a second pipe that is connected to the second tank and the first pipe between the first filter unit and the first valve.

A system, a cartridge and a dispensing valve for eliminating a drift or sag in BCDMH output from an inline dispensing valve containing a dispensing cartridge mountable within the inline dispensing valve with the dispensing cartridge containing a batch of water erodible cluster inhibiting BCDMH particles to provide a linear output flow of BCDMH which is responsive to flow of water though a cartridge in the dispensing valve and a method of obtaining a linear output in a dispensing system by increasing the size of particles in a dispensing cartridge in the system.

A system, a cartridge and a dispensing valve for eliminating a drift or sag in BCDMH output from an inline dispensing valve containing a dispensing cartridge mountable within the inline dispensing valve with the dispensing cartridge containing a batch of water erodible cluster inhibiting BCDMH particles to provide a linear output flow of BCDMH which is responsive to flow of water though a cartridge in the dispensing valve and a method of obtaining a linear output in a dispensing system by increasing the size of particles in a dispensing cartridge in the system.

Provided is a cartridge filter using nanofiber composite fiber yarn, the cartridge filter including: a core having a plurality of holes through which a liquid passes; and a filter medium wound around the core to collect an object to be filtered contained in the liquid, wherein the filter medium comprises composite fiber yarn in which a nanofiber web which is produced by accumulating nanofibers produced by an electrospinning method is laminated to a porous nonwoven fabric, to thus provide excellent durability and improved filtration performance.

The present up-flow water filtration system is made up of three or more layers. In the example of three layers, each layer is individually rigid and capable of supporting loads above it, and each serves a separate function. These layers include the inlet layer on the bottom of the system, the outlet layer at the top of the system, and the central layer in between which contains the filter media. Additionally, the system includes one or more vertical ports that are open above ground and that extend into the central layer and provide access to the central media containment layer for maintenance. There are also several layers of textiles which form the flexible outer casing, as well as internal membranes to separate the different layers and components of the system. Some systems may include inlet and outlet pipes, but other inlet and outlet configurations are possible.

The present up-flow water filtration system is made up of three or more layers. In the example of three layers, each layer is individually rigid and capable of supporting loads above it, and each serves a separate function. These layers include the inlet layer on the bottom of the system, the outlet layer at the top of the system, and the central layer in between which contains the filter media. Additionally, the system includes one or more vertical ports that are open above ground and that extend into the central layer and provide access to the central media containment layer for maintenance. There are also several layers of textiles which form the flexible outer casing, as well as internal membranes to separate the different layers and components of the system. Some systems may include inlet and outlet pipes, but other inlet and outlet configurations are possible.

Provided is a process comprising receiving overflow of wastewater influent from a clarifier basin in a clarifier effluent collection trough; receiving inflow of wastewater influent from the clarifier effluent collection trough in a filter influent flow inlet distribution channel; maintaining substantially constant liquid level in the filter influent inlet distribution channel; applying hydrostatic pressure to push wastewater influent from the filter influent flow inlet distribution channel into an upflow backwash filter contusing denitrifying biomass or deammonification biomass; backwashing the backwash filter with a gas lift backwash flow; returning filter reject backwash wastewater from rejection compartment of the filter through denitrifying bacteria or deammonification biomass recycle return line to a location upstream of the filter; and recycling denitrifying bacteria or deammonification biomass from denitrifying bacteria or deammonification biomass recycle return line to at least one of the clarifier effluent collection trough, filter influent flocculation tank, or filter influent flow distribution channel.

Disclosed are devices, systems and methods for treatment or pre-treatment of stormwater which can provide a high-rate stormwater filtration that is suitable for sites with high particulates (total suspended solid (TSS)) loading.