Bioconversion processes are disclosed in which two or more biocatalysts including microorganisms or isolated enzymes that are substantially irreversibly retained in the interior of an open, porous, highly hydrophilic polymer are used in a common aqueous medium. In one exemplary embodiment, one biocatalyst produces a chemical product that is a substrate to at least one other biocatalyst. In another exemplary embodiment, the feed includes two or more substrates and one biocatalyst bioconverts at least one substrate and another biocatalyst bioconverts at least one other substrate. This aspect is particularly useful for treating water including disparate contaminants by metabolic degradation in a bioreaction zone including multiple types of biocatalysts.

An electrocoagulation unit that may include an outer shell, and a set of electrodes disposed within the inner housing. Each electrode is separated from an adjacent electrode by an electrode gap spacing. The outer shell may further include a fluid inlet; a fluid outlet; a first busbar opening with a first busbar gland associated therewith.

An apparatus and method are provided for removing nitrogen pollution from a body of water. The apparatus includes a platform configured to be released into and float on the body of water, the platform including a confinement area. A pump is connected to the platform, with the pump being configured to pump water into the confinement area during a first period, and the pump being configured to not pump water into the confinement area during a second period. A drain is positioned in the platform configured to intermittently release water out of the confinement area. A substrate is provided in the confinement area, with the substrate being configured to allow for the formation of a biofilm on the substrate. The pump and drain are configured such that during the first period, water is moved into the confinement area by the pump and out of the confinement area through the drain, and the formed biofilm performs nitrification to convert at least one of ammonia and ammonium in the water into nitrite and nitrate. The pump and the drawing are also configured such that during the second period, water is stagnant in the confinement area and the formed biofilm converts the nitrite and nitrate into gaseous nitrogen.

Exemplary embodiments are directed to pool cleaners that remove debris from water using a plurality of cyclonic flows, or that include a removable impeller subassembly, a check valve for a debris canister, a particle separator assembly having a handle that locks to the pool cleaner, a modular roller drive gear box, or a roller latch that secures a roller to the pool cleaner. Exemplary embodiments are also directed to the check valve and the roller latch themselves. Exemplary embodiments are directed to a filter medium for pool cleaners that includes embossments providing flow channels for water, and to roller assemblies for pool cleaners. Exemplary embodiments are directed to pool cleaners including alternative pump motor engagements. Exemplary embodiments are directed to pool cleaners power supplies that include a potted and contoured power board assembly, and to kickstands therefor. Exemplary embodiments are directed to a pool cleaner caddy, and removable wheels therefor.

Described herein is a water treatment system for simultaneously removing ammonia and nitrates from a liquid. The water treatment system comprises a floating platform, at least one columnar unit connected with the floating platform, where each columnar unit includes a bounding surface possessing multiple apertures. An air diffuser is connected with each columnar unit for supplying an air flow volume within the columnar unit.

The present invention provides a cage particle distribution system for wastewater treatment comprising contactors. Said contactors include shells and the interior of said shells is a hollow cavity. At least one of the side walls, the upper surface and the lower surface of said shells are equipped with through-holes. Particles are loaded inside said shells and said particles can carry some microorganisms on their surfaces at least. Said cage systems are placed in the water of a wastewater system or a wastewater treatment system and one or multiple said cage systems can be placed. Separate aeration and/or liquid distribution into each individual cage system disperse particles in the system by the gas and/or liquid, which improves the efficiency of wastewater treatment.

The present disclosure provides a container-type apparatus for wastewater treatment with a suspended particle system, including one or multiple biological reaction zones. Said biological reaction zones can be facultative, anaerobic, anoxic, and aerobic and at least one of said biological reaction zones is a suspended particle system. Particles in said suspended particle system act as the carrier of microbiota and offer better conditions for them to grow. The apparatus adopts a box structure, such as a container type, which is convenient to move, flexible to assemble, and can be used for multiple times. Based on actual requirements, this apparatus can also be a structure type. The suspended particle system disclosed herein applied in wastewater treatment can increase the concentration of microorganisms significantly, improve the ability to bear impact load, produce less sludge, and without sludge expansion. Meanwhile, the means to suspend particles by gas and liquid is able to reduce energy consumption to a larger extent. Therefore, this system features high efficiency and low energy consumption.

The disclosure describes an algal system for improving water quality through the use of algae. In example embodiments, the algal system comprises an elongate device including algae enclosed therein and capable of reducing at least the levels of nitrates and phosphates in water directed through the device. The algae may be capable of also reducing E. coli bacteria, other bacteria, and viruses in the water. Preferably, the algae comprises a filamentous green algae, including without limitation, Spirogyra grevilleana algae. In one example embodiment, the algal system comprises an elongate device and an elongate cartridge that is pre-configured to treat certain chemical compounds, bacteria, and viruses, and certain other characteristics of water. The cartridge is delivered to the site where the water is to be treated and installed in the field, possibly replacing an existing cartridge. After use, algae may be processed into biofuel.

Membrane bioreactor (2) for treating of sewage that includes a first and second bioreaction vessel (4, 6). The first bioreaction vessel (4) includes a first vessel wall (14) for enclosing an internal first vessel space. The second bioreaction vessel (6) includes a second vessel wall (26) for enclosing an internal second vessel space. The first vessel wall (14) includes a convex first peripheral vessel wall part and a first inner vessel wall part (22). The second vessel wall (26) includes a convex second peripheral vessel wall part and a second inner vessel wall part (30). The first vessel wall (14) and the second vessel wall (26) are mechanically connected to each other by means of a vessel connection structure (90). The vessel connection structure (90) positions the first and second peripheral vessel wall parts relative to each other during the treating of sewage.

A system is described herein which provides an ozonated liquid. The system comprises a liquid inlet arranged to continuously accept a liquid into the system at a desired flow rate; a liquid outlet to dispense ozonated liquid out of the system, the ozonated liquid having an oxidation-reduction potential of at least 450 mV due solely to ozone dissolved in the liquid, the liquid outlet being in fluid communication with the liquid inlet and arranged to dispense the ozonated liquid out of the system at the desired flow rate. The system has a tank-less ozonation flow path between the liquid inlet and the liquid outlet, the flow path adapted to ozonate the accepted liquid, producing the ozonated liquid to be dispensed out of the system. The accepted liquid has a fluid residence time in the ozonation flow path of less than 5 minutes prior to being dispensed as the ozonated liquid.