Disclosed is a chemical wastewater treatment and reuse system, which corresponds to a raw water tank and includes a regulation tank pretreatment system, an A/A/O biological treatment system, an MBR treatment system and an electrical control system. The regulation tank pretreatment system includes a grating tank, a primary sedimentation tank and a regulation tank that sequentially communicate with the raw water tank. The A/A/O biological treatment system includes an anaerobic tank group and an aerobic tank group that sequentially communicate with the regulation tank. The MBR treatment system includes a separation tank and a membrane tank that sequentially communicate with the aerobic tank group, the membrane tank communicates with a clarification tank, and the membrane tank and the clarification tank jointly communicate with the sedimentation tank. The sedimentation tank sequentially communicates with a clear water tank, a discharge tank, an advanced treatment tank and a reused water tank.

An aerated wetland system used for wastewater treatment is disclosed. The system includes a main frame with an entrance and an output opening. The wastewater is entered into the system with maximum velocity via the entrance and via a racetrack. The racetrack comprises an agitated flow pattern with a plurality of baffles along the longitudinal axis of the racetrack to deflect the wastewater and create turbulent flow into the wastewater. The racetrack further includes at least four intersecting sections. The at least two intersecting sections include washed soils and an aeration system and other two intersecting sections include washed soils and a plurality of wetland plants respectively, thereby subjecting the influent wastewater to anaerobic and aerobic conditions respectively, along the racetrack to effectively purify and treat volatile compounds in the influent wastewater. The outlet opening directs out effluent wastewater from the aerated wetland system via the effluent device.

An aerated wetland system used for wastewater treatment is disclosed. The system includes a main frame with an entrance and an output opening. The wastewater is entered into the system with maximum velocity via the entrance and via a racetrack. The racetrack comprises an agitated flow pattern with a plurality of baffles along the longitudinal axis of the racetrack to deflect the wastewater and create turbulent flow into the wastewater. The racetrack further includes at least four intersecting sections. The at least two intersecting sections include washed soils and an aeration system and other two intersecting sections include washed soils and a plurality of wetland plants respectively, thereby subjecting the influent wastewater to anaerobic and aerobic conditions respectively, along the racetrack to effectively purify and treat volatile compounds in the influent wastewater. The outlet opening directs out effluent wastewater from the aerated wetland system via the effluent device.

A liquid waste treatment system includes: a baffle tank subsystem for particle settling; a preprocess tank subsystem downstream of the baffle tank subsystem; a process tank subsystem downstream of the preprocess tank subsystem; and a storage tank subsystem downstream of the process tank subsystem for the storage of treated liquid. A Microbial Fuel Cell (MFC) processing module may be included and may be inserted into the preprocess tank subsystem or implemented in a second process tank downstream of the process tank subsystem. A faster disinfection may occur in the process tank subsystem, and a slower disinfection may occur in the second process tank according to distinct respective kill curves. An electrochemical cell may be operated in a pulse mode in liquid waste in a pulsed mode.

An inclined plate baffled A2O reactor with high oxygen transfer efficiency is proposed. The inclined plate baffled A2O reactor with high oxygen transfer includes a reactor body and a secondary sedimentation tank. The reactor body includes an anaerobic zone, an anoxic zone and a deep oxic zone which are arranged sequentially from top to bottom. An anaerobic-anoxic inclined plate is arranged between the anaerobic zone and the anoxic zone. An anoxic-oxic inclined plate is arranged between the anoxic zone and the deep oxic zone. The oxic zone communicates with the secondary sedimentation tank through a gravity pipeline. Microporous aerators are arranged at a bottom of the deep oxic zone.

A plant for the anaerobic purification of waste and/or process water comprising: i) a reactor tank with at least one feed line for supplying waste and/or process water into tank and with at least one outflow line for draining a mixture of microorganisms, waste and/or process water and gas from the tank, ii) a first separation apparatus outside and downstream of the tank for separating at least a part of the microorganisms from the mixture from the tank, wherein the first separation apparatus comprises at least one separation stage, an inlet line connected with at least one of the outflow line(s), at least one discharge line and at least one outlet line, and iii) a return line for returning the separated sludge separated into the reactor tank, wherein the return line connects with at least one of the at least one outlet line of the first separation apparatus.

Disclosed is a chemical wastewater treatment and reuse system, which corresponds to a raw water tank and includes a regulation tank pretreatment system, an A/A/O biological treatment system, an MBR treatment system and an electrical control system. The regulation tank pretreatment system includes a grating tank, a primary sedimentation tank and a regulation tank that sequentially communicate with the raw water tank. The A/A/O biological treatment system includes an anaerobic tank group and an aerobic tank group that sequentially communicate with the regulation tank. The MBR treatment system includes a separation tank and a membrane tank that sequentially communicate with the aerobic tank group, the membrane tank communicates with a clarification tank, and the membrane tank and the clarification tank jointly communicate with the sedimentation tank. The sedimentation tank sequentially communicates with a clear water tank, a discharge tank, an advanced treatment tank and a reused water tank.

An inclined plate baffled A2O reactor with high oxygen transfer efficiency is proposed. The inclined plate baffled A2O reactor with high oxygen transfer includes a reactor body and a secondary sedimentation tank. The reactor body includes an anaerobic zone, an anoxic zone and a deep oxic zone which are arranged sequentially from top to bottom. An anaerobic-anoxic inclined plate is arranged between the anaerobic zone and the anoxic zone. An anoxic-oxic inclined plate is arranged between the anoxic zone and the deep oxic zone. The oxic zone communicates with the secondary sedimentation tank through a gravity pipeline. Microporous aerators are arranged at a bottom of the deep oxic zone.