Systems and methods for disposing of blackwater are disclosed. A first vessel contains a screw running through the vessel from a first end to a second end. The screw is surrounded radially by a filter. The first vessel has a blackwater inlet adjacent the first end. An extrusion plate is adjacent the second end of the first vessel. A combustor vessel is configured to receive a solids component from the extrusion plate. A blackwater stream, consisting of a liquid component and the solids component, is passed through the blackwater inlet into the first vessel, is conveyed by the screw from the first end to the second end, and is pressurized against the extrusion plate. The liquid component is thereby forced from the blackwater stream through the filter and the solids component is forced through the extrusion plate into the combustor. The combustor is configured to combust the solids component.

A system includes a first separator configured to receive waste water, retain a first portion of the waste water, and separate the first portion of the waste water into a first vapor and a first solid material; and a second separator in fluid communication with the first separator, the second separator being configured to receive a second portion of the waste water from the first separator and to separate the second portion of the waste water into a second vapor and a second solid material, the second separator including a first condenser, a heating element, and a first electrocoagulation unit. Related apparatus, systems, techniques and articles are also described.

A facility-based domestic wastewater treatment system equipped with modified toilets and a hypochlorous acid machine, neutralizing coliform bacteria from bodily excretions at the source. The treated batch content in the toilet is flushed to a secondary process tank equipped with a grinding pump, hypochlorous acid dispensing nozzles and solenoid valves. Toilet and other facility utilities wastewater are treated and discharged to a filtration system to be separated. The filtration system is capable of separating bacteria and other particulates up to or equal to a fineness of 0.01 microns. Separate storage tanks are used to store recovered and reclaimed water in conjunction with a slurry waste collection tank for solid waste disposal. A facility-based wastewater reclamation system utilizing Reverse Osmosis process to remove unwanted contaminants and dissolved solids producing potable water, some of which is further processed with UV, and Ozone treatment to be used as drinking and cooking water.

A Septic Aid system includes at least tablet containing dissolvable septic treatment so constituted as to supply a septic system with replacement bacteria and/or enzymes. The at least one tablet is configured to slowly release the septic treatment into toilet water. The at least one tablet may also have a dissolvable color indicator configured to run out at approximately the same time as the dissolvable septic treatment is depleted. An attachment may be provided in the form of an adhesive disc, suction cup, or hangar. An applicator may be used to apply the at least one tablet to an interior surface of the toilet.

A waste treatment includes a package with compartments. A surfactant, an oxidizing agent, and, optionally, a liquid may be disposed within the compartments. The oxidizing agent is within a compartment that does not contain the surfactant or the liquid. A bursting force may unseal a sealed end of each compartment. The liquid flushes the surfactant and the oxidizing agent out of the package into a non-contact agitating toilet. A dual compartment package made with a fluidly disintegrable material may separate the surfactant from the oxidizing agent where the liquid may not be provided. The waste treatment may be mixed with a waste deposited within the non-contact agitating toilet. The package may disintegrate in the presence of the liquid to allow the reactive components to mix. A plurality of waste treatments may be connected. A perforated barrier may separate a first waste treatment from a second waste treatment.

A wastewater spray distribution apparatus is operative to distribute wastewater produced by a sewage treatment system (10) onto a ground level (22) through operation of sprayers (118, 260). The exemplary sprayers include a manifold (142, 262) that includes outlet nozzles (158, 264) that can be readily removed and replaced. The exemplary manifold further includes interior areas bounded by surfaces that slope continuously downward from the outlet nozzles to the manifold inlet to assure the draining of water therefrom. Each of the nozzles include a base (140) which includes brake (207). A brake is provided in each nozzle and is adjustable to provide brake force to limit rotational movement produced by the thrust of water passing from the outlet nozzles to assure that the sprayer operates at the appropriate rotational speed. Alternative arrangements include manifolds including fixed or adjustable flaps and radially outwardly adjustable arms to adjust rotational properties.

Various implementations include a combustor system including an inner wall, a fuel grate, an ash grinder, an igniter, and a fan. The inner wall defines a combustion chamber and has a longitudinal axis and first and second ends. The inner wall defines primary and secondary air inlets. The primary air inlets are defined closer than the secondary air inlets to the first end. The fuel grate is disposed within the combustion chamber between the primary and secondary air inlets and is configured to support fuel disposed within the combustion chamber. The ash grinder is disposed between the fuel grate and the secondary air inlets and is rotatable about the longitudinal axis relative to the fuel grate. The igniter provides energy to the combustion chamber. The fan is configured to cause air to flow from the primary and secondary air inlets through the second end of the combustion chamber.

Methods for electrochemically oxidizing organic compounds in aqueous solution. The methods include contacting an aqueous solution comprising organic compounds with a first anode and electrochemically oxidizing at least a portion of the organic compounds to provide a first aqueous solution comprising oxidation products; and contacting the first aqueous solution comprising oxidation products with a first cathode and electrochemically reducing at least a portion of the oxidation products to provide a first aqueous solution comprising reduced products and residual oxidizable organic compounds. The first aqueous solution can be further treated to electrochemically oxidize at least a portion of the residual oxidizable organic compounds to provide a second aqueous solution comprising oxidation products, and the second aqueous solution can be further treated to electrochemically reduce at least a portion of the oxidation products to provide a third aqueous solution comprising reduced products and residual oxidizable organic compounds. Systems for electrochemically oxidizing organic compounds and effectively carrying out the methods are also provided.

A sewage treatment device includes a fluidized bed body, a reflux device and a chemical feeding device. The fluidized bed body is sequentially provided with a sedimentation zone, a transition zone and a fluidization zone from top to bottom. The reflux device is connected to the fluidized bed body through a reflux pipe. The reflux pipe extends into the fluidized bed body from the sedimentation zone, and the granularity of a crystal product can be controlled by changing the height of a reflux inlet at the bottom end of the reflux pipe in the fluidized bed body. By controlling the position of the reflux inlet of the reflux pipe in the fluidized bed body, combining product granularity requirements, and adjusting an insertion depth of the reflux pipe, the granularity of a final product can be flexibly regulated and controlled, and meanwhile, a product recovery rate is improved.

The wastewater treatment apparatus of present invention has an electro-coagulation unit for removing contaminants with at least one anode and at least one cathode and an electro-oxidation unit for oxidizing contaminants with at least one anode and at least one cathode wherein oxidants are electrochemically generated. Based on the type of wastewater, the apparatus can have an electro-flotation unit between the electrocoagulation unit and the electro-oxidation unit. The apparatus also has an oxidant removal unit which can have a metal ion-liberating electrode for reacting with and removing residual oxidants. In some cases, portions of effluent from the oxidant removal unit can be recirculated to the electro-coagulation unit for increased efficiency.