A sewage uniform distribution treatment device for an aerobic granular sludge system and a use method therefor, the device comprising a reactor tank body (1), a water inlet device (2), and a water outlet device (3). The water inlet device (2) comprises a water inlet inner channel (4), a water inlet weir (5), a water inlet outer channel (6), a vertical water inlet branch pipe (7), and vertical bell mouths (8); the water outlet device (3) comprises a water outlet main pipe (9), a water outlet channel (10), a water outlet weir (11), an outer baffle plate (12), and an inner baffle plate (13); the water outlet channel is connected to the water outlet main pipe; the outer baffle plate is a vertical baffle plate; the inner baffle plate is located at the bottom of the water outlet channel and is connected to the water outlet channel.

A process for the treatment of wastewater is disclosed, which comprises (a) contacting the wastewater with fast settling sludge from step (c) in an anaerobic zone, obtaining a mixture of wastewater and sludge; (b) subjecting the mixture from step (a) and slow settling sludge from step (c) to an aerobic zone, obtaining a water and sludge mixture; (c) subjecting a first part of the mixture from step (b) to a sludge selection step, wherein sludge is selected based on settling velocity and a first portion containing slow settling sludge and a second portion containing fast settling sludge are collected, wherein average settling velocity of the fast settling sludge is greater than that of the slow settling sludge, and wherein the first portion is returned to step (b) and the second portion is returned to step (a); and (d) separating sludge from a second part of the mixture from step (b).

A wastewater treatment system includes a first sub-system having a biological treatment unit and a second sub-system having a dissolved air flotation unit. A method of treating wastewater includes directing a first stream of wastewater to a biological treatment unit and directing an overflow stream of wastewater to a dissolved air flotation unit. A method of facilitating treatment of overflow wastewater in a biological treatment system includes connecting an overflow treatment system in a parallel configuration with the biological treatment system, the overflow treatment system having a dissolved air flotation unit, and directing a fraction of activated sludge from the biological treatment system to the overflow treatment system.

A wastewater treatment system includes a biological treatment plant and an auxiliary, non-biological treatment plant. The auxiliary plant receives overflow, which can be sanitary sewer overflow, combined sewer overflow or strictly storm overflow. Treatment is by coagulation and membrane separation, removing most bacteria. Following treatment the outflow can be discharged to streams.

The mobile water treatment cartridge is connectable into a water treatment circuit and includes fluid connectors and power and data connection ports. The cartridge includes an outer shell having an upper opening that can be hermetically sealed by a lid, and an inner shell having an opening at the top and delimiting an internal volume of the cartridge, in which all the technical equipment for operation of the cartridge is placed. The inner shell is secured to at least one structure that can be inserted into the interior volume through the opening. There is a device for handling the cartridge secured to the outer shell and a device for rendering the cartridge mobile.

Provided is a sewage treatment system capable of maintaining a positive dissolved oxygen concentration of sewage flowing down through a sewer conduit downstream of a relay pump station, and changing a microbial state on an inner wall of the sewer conduit to prevent corrosion of the sewer conduit. The sewage treatment system comprises: dehydration means connected to an initial sedimentation pond and/or a final sedimentation pond of a sewage treatment facility and configured to receive surplus sludge from the initial sedimentation pond and/or return sludge from the final sedimentation pond and dehydrate the received surplus sludge and/or the received return sludge; a microbial material production device configured to supply oxygen to the dehydrated sludge received from the dehydration means while maintaining a temperature of the dehydrated sludge within the range of 60 C. to 110 C., to subject the dehydrated sludge to aerobic fermentation using Gram-positive aerobic microbes in the hydrated sludge, thereby producing a microbial material in which Gram-negative anaerobic and facultative anaerobic microbes in the hydrated sludge are decomposed and extinguished and which contains aerobic microbial spores produced after the aerobic fermentation; water feeding means configured to feed water from any part of the sewage treatment system to the after-mentioned microbe activation device; a microbe activation device configured to receive the microbial material from the microbial material production device, and supply the water from the water feeding means to the received microbial material, while maintaining a temperature and an oxygen concentration of the water, respectively, within the range of 10 C. to 40 C., and within the range of 1 to 10 mg/L, thereby germinating the spores of the microbial material to activate the microbial material; and oxygen supply means configured to supply oxygen to the sewage at any position of the relay pump station; wherein the sewage including the activated microbial material and the oxygen supplied from the oxygen supply means is sent from the relay pimp station to the sewage treatment facility.

A wastewater treatment system consisting of a single tank extended aeration activated sludge process with a continuously operating clarifier skimming device which is capable of producing a clear odorless effluent which meets applicable state discharge standards.

A septic tank system includes a multiple compartmented (or chambered) supplemental tank. The supplemental tank has a cover/lid with a plurality of strategically situated access holes (both small and large ports) for servicing the various chambers from above ground.

The present invention relates to a testing method for testing a state of an aeration tank in a wastewater treatment facility that uses activated sludge. The testing method comprises obtaining a difference between: a sedimentation amount when a given period of time has elapsed after an activated sludge mixed liquid collected from the aeration tank and water having a higher dissolved oxygen concentration than the activated sludge mixed liquid are poured into the same container and mixed together; and a sedimentation amount when a period of time equal to the given period of time has elapsed after the activated sludge mixed liquid collected from the aeration tank and water having a lower dissolved oxygen concentration than the activated sludge mixed liquid are poured into the same container and mixed together.

The disclosure herein relates to a helical bed biofilm reactor for wastewater treatment, and belongs to the fields of environment engineering and chemical engineering. The helical bed biofilm reactor comprises a reaction vessel, a draft tube, helical screen meshes, carriers, a carrier passage, a gas distributor, a gas inlet, a gas outlet, a water inlet, a water outlet and a sludge outlet. By improving the arrangement structure of the carriers and the structure of the helical passage, the helical bed biofilm reactor improves the oxygen transfer rate, the oxygen transfer efficiency and the biological reaction efficiency of a biological treatment process of wastewater, and helps to control the thickness of the biofilm and reduce energy consumption in wastewater treatment.