The invention provides water treatment for a municipal wastewater source by removal of contaminants including nutrient contaminants, FOG, total suspended solids, pathogenic bacteria, viruses and metal contaminates. Pathogenic bacteria and viruses are removed without the use of chlorine contact, ultraviolet treatment or reverse osmosis treatment. The treatment steps may include: oxygenation by single cell algae, electrocoagulation, precipitation of solids, absorption and flocculation, de-aeration, metered amounts of an anionic or cationic flocculant added for further coagulation and precipitation of coagulated material; mixing and subsequent clarification; sand filtration; and removal of remaining contaminants by containers housing microporous media beds or ion-exchange beds. The treatment steps may be used in various combinations and sub-combinations in order to focus treatment on prevalent contaminants in the wastewater to be treated. The invention further includes embodiments of the media bed containers and a non-transitory computer-readable medium to execute a method for conducting treatment of a wastewater stream.

The invention provides water treatment for a municipal wastewater source by removal of contaminants including nutrient contaminants, FOG, total suspended solids, pathogenic bacteria, viruses and metal contaminates. Pathogenic bacteria and viruses are removed without the use of chlorine contact, ultraviolet treatment or reverse osmosis treatment. The treatment steps may include: oxygenation by single cell algae, electrocoagulation, precipitation of solids, absorption and flocculation, de-aeration, metered amounts of an anionic or cationic flocculant added for further coagulation and precipitation of coagulated material; mixing and subsequent clarification; sand filtration; and removal of remaining contaminants by containers housing microporous media beds or ion-exchange beds. The treatment steps may be used in various combinations and sub-combinations in order to focus treatment on prevalent contaminants in the wastewater to be treated. The invention further includes embodiments of the media bed containers and a non-transitory computer-readable medium to execute a method for conducting treatment of a wastewater stream.

A device for separating the liquid phase from the solid phase of a slurry, wherein such separation is obtained by a filtration process, preferably under pressure, in combination with a process of clarification and withdrawal of the clarified liquid within the filter at an adjustable height.

Dilution check valves, pumps, systems, and methods of use, useful for dilution of incoming feed into a feedwell or feed system that can be easily installed and removed on solid/liquid separation units. The feed dilution apparatuses or systems can be installed in a single location or in multiple locations around a feedwell, transferring supernatant drawn from single or multiple locations within a solid/liquid separation tank. Optionally, an in-line turbine style pump and/or downward draft configuration can be used to provide efficient pumping and accurate adjustment of volume by increasing or decreasing rotation speed. The feed dilution pumps can optionally be installed using a quick fit system that allows removal and replacement during operation without the need for mobile cranes or heavy lifting equipment.

A clarifier of a wastewater treatment system is made more efficient and cost effective with an energy dissipating inlet (EDI) that removes the need for a conventional feedwell/EDI system. A central influent pipe has wastewater outlet ports under the liquid surface, the ports being surrounded by an efficient EDI surrounding the center pipe and extending outwardly therefrom. The EDI receives influent flow and directs the sludge outwardly and generally downwardly at reduced flow velocity. Series of baffles in the EDI help slow the flow velocity and disperse the sludge. In another embodiment a faucet-type EDI has discharge openings that disperse the sludge downwardly after it has flowed through sets of baffles above. Significant cost reductions in material and installation are realized by elimination of the conventional feedwell/EDI system.

Separation device (1) includes bottomed casing (2), rotating body (3), and blade (4). Casing (2) includes outer tubular portion (5) and inner tubular portion (6). Rotating body (3) is disposed inside inner tubular portion (6) and rotates about a rotation axis along an axial direction of inner tubular portion (6). Blade (4) is disposed between inner tubular portion (6) and rotating body (3), and rotates together with rotating body (3). Inner tubular portion (6) includes inner inflow port (61) and discharge port (63). Discharge port (63) discharges a solid contained in a fluid flowing into an inside of inner tubular portion (6) through inner inflow port (61) between inner tubular portion (6) and outer tubular portion (5). Outer tubular portion (5) includes a fluid outflow port and a solid discharge portion. The fluid outflow port causes the fluid flowing out from the inside of inner tubular portion (6) and flowing into the inside of outer tubular portion (5) to flow out to the outside of outer tubular portion (5). The solid discharge portion discharges the solid discharged from discharge port (63) of inner tubular portion (6) to the outside of outer tubular portion (5).

Separation device (1) includes bottomed casing (2), rotating body (3), and blade (4). Casing (2) includes outer tubular portion (5) and inner tubular portion (6). Rotating body (3) is disposed inside inner tubular portion (6) and rotates about a rotation axis along an axial direction of inner tubular portion (6). Blade (4) is disposed between inner tubular portion (6) and rotating body (3), and rotates together with rotating body (3). Inner tubular portion (6) includes inner inflow port (61) and discharge port (63). Discharge port (63) discharges a solid contained in a fluid flowing into an inside of inner tubular portion (6) through inner inflow port (61) between inner tubular portion (6) and outer tubular portion (5). Outer tubular portion (5) includes a fluid outflow port and a solid discharge portion. The fluid outflow port causes the fluid flowing out from the inside of inner tubular portion (6) and flowing into the inside of outer tubular portion (5) to flow out to the outside of outer tubular portion (5). The solid discharge portion discharges the solid discharged from discharge port (63) of inner tubular portion (6) to the outside of outer tubular portion (5).

A feedwell design for a clarifier that may better dissipate the entrance energy of feed slurry liquid exiting the feedwell and entering the clarifier. Plates having a surface area twisted around a longitudinal axis may be provided at the bottom of the feedwell. The plates may cause a change in the flow direction of the feed, from being mostly horizontal to mostly vertical, to slow the slurry. The provision of plates at the bottom of a feedwell in a clarifier may advantageously reduce the velocity of the materials entering the clarifier, or may increase the uniformity of the flow rate of the materials while reducing or maintaining the amount of shear force, turbulence, or other forces that may have a detrimental effect on clarification. Likewise, this may improve the rate at which solids settle out of the feed slurry solution, and thus improve the clarity of the removed liquid.

One or more dilution tubes for increasing the dilution of pulp as it enters a thickener are provided. One or more pipes, referred to here as dilution tubes, can be added to sides of a feed pipe of a thickener. One end of a dilution tube can open to a tank of the thickener, and the other end can open into the feed pipe. As pulp flows through the feed pipe, low pressure suction can be created that pulls water from the tank, through the dilution tube, and into the feed pipe. The water pulled in through the dilution tube can increase the dilution of the pulp. A highly diluted pulp can contact a flocculent efficiently and lead to a high settling rate in a thickener. Accordingly, the use of dilution tubes can increase the efficiency of a thickener.

One or more dilution tubes for increasing the dilution of pulp as it enters a thickener are provided. One or more pipes, referred to here as dilution tubes, can be added to sides of a feed pipe of a thickener. One end of a dilution tube can open to a tank of the thickener, and the other end can open into the feed pipe. As pulp flows through the feed pipe, low pressure suction can be created that pulls water from the tank, through the dilution tube, and into the feed pipe. The water pulled in through the dilution tube can increase the dilution of the pulp. A highly diluted pulp can contact a flocculent efficiently and lead to a high settling rate in a thickener. Accordingly, the use of dilution tubes can increase the efficiency of a thickener.