Abstract: A defined current and aeration system for the aeration chamber of an aerobic wastewater treatment plant is disclosed. It includes the release of oxygenation gas or air into the aeration chamber through a diffuser or the like at a position such that the air injected into the tank provides the necessary amount of oxygen for aerobic bacterial digestion of the waste while creating a current or circulation pattern in the chamber that forces every portion of the fluid within the aeration chamber into circulation thus preventing the accumulation of solids as sludge in the wastewater treatment plant.

Abstract: Methods of improving anaerobic digestion by enhancing the microorganism population through the creation of a nutrient environment more favorable for microbial growth and through the addition of microbes and, more particularly, by the addition of chelating agents, chelating agents and nutrients, and methanogens. Methods for the improved production of said methanogens by the provision of controlled amount of methanol and H.sub.2 and CO.sub.2. Methods for the improved preservation of said methanogen by ultra-freezing and freeze-drying.

Abstract: An apparatus and method for treating wastewater is provided including a cylindrical tank having a top, a bottom, an outer wall and a cylindrical inner wall. The inner wall extends from the bottom of the tank to a point above a desired water level. The inner wall, the top and the bottom define an inner aerobic zone. The inner wall, the outer wall, the top and the bottom define an outer anaerobic zone. Wastewater may pass from the outer anaerobic zone to the inner aerobic zone through holes in the inner wall. An open ended conical hopper is positioned within the inner aerobic zone with its smaller end pointed toward the bottom of the tank. Several radially spaced air outlet pipes connected to a compressed air source extend downward into the inner aerobic zone where air is discharged through the open ends of the outlet pipes. An inlet line connected to the tank opens into the outer anaerobic zone of the tank. An outlet line is positioned within the clarification zone to remove purified water from the tank.

Abstract: An aquatic filter system having a rotatably mounted cylindrical filter body. The cylindrical filter body is formed by a water absorbing mass of material. Water applied to one side of the filter body unbalances the filter body which causes the filter body to rotate. As a result of the rotational movement, at least a portion of the filter body is alternately exposed to the water and the atmosphere to foster the growth of aerobic bacteria on the surfaces of the filter body.

Abstract: A process and apparatus for treating wastewater containing nitrogen compounds is disclosed. The process includes passing the wastewater to be treated through a biologically active material in one direction to treat the wastewater and passing the treated wastewater through the biologically active material in a second direction to further treat the wastewater under alternating aerobic and anoxic conditions, converting nitrogen compounds to nitrates and nitrites, and converting nitrates and nitrites to gaseous nitrogen.

Abstract: For the anaerobic fermentation of solid organic waste substances, solid waste is mixed with liquid material, particularly anaerobic slurry, and the temperature of the mixture is brought to a value between 25.degree. and 70.degree. C., preferably between 30.degree. and 40.degree. C. (mesophilic) and between 55.degree. and 65.degree. C. (thermophilic). By means of spontaneous rising of lightweight material and by means of flotation, a layer (10) of solid material floating on a methane-generating zone is formed from said mixture in a reactor. Said floating layer moves from a supply end (7) or a mixing section (2) to a discharge end (14) of the reactor, hydrolysis and acidification of solidorganic material taking place in the floating layer. The fermented floating layer is discharged via the discharge (14) end independent of the residence time of fluid and slurry in the methane-generating zone under the floating layer.

Abstract: The present invention is directed to a bioreactor system for the remediation of contaminated liquid streams. The bioreactor system is composed of at least one and often a series of sub-units referred to as bioreactor modules. The modular nature of the system allows bioreactor systems be subdivided into smaller units and transported to waste sites where they are combined to form bioreactor systems of any size. The bioreactor modules further comprises reactor fill materials in the bioreactor module that remove the contaminants from the contaminated stream. To ensure that the stream thoroughly contacts the reactor fill materials, each bioreactor module comprises means for directing the flow of the stream in a vertical direction and means for directing the flow of the stream in a horizontal direction. In a preferred embodiment, the reactor fill comprises a sulfate reducing bacteria which is particularly useful for precipitating metals from acid mine streams.

Abstract: A process of dewatering primary-treated sewage which includes mixing the sewage with a coagulant or flocculant aid, usually activated polymer. The sewage is then mixed and flocculated at conditions which involve extensive mixing turbulence of the sewage and whereby part of the sewage is recycled so as to be again subjected to such mixing and flocculating. Flocks form the solid particles in the sewage. The pH of the sewage is chemically adjusted into the basic pH range or to a higher basic pH. The sewage is applied to a sand bed whereby the flocculated solids in the sewage are separated from the liquid in the sewage, by collecting on the top of the sand bed. The flocculated solids located on the top of the sand bed are air dried. The dried flocculated solids are removed from the top of the sand bed.

Abstract: Apparatus for and a method of reducing solids and controlling surges in the flow of effluent from the clarifier chamber of an aerobic wastewater treatment plant. The apparatus is mounted inside the clarifier chamber of the wastewater treatment plant and connected to an outlet pipe of the plant. The apparatus includes a cylindrical tubular weir positioned in a cylindrical housing connected to the outlet pipe of the clarifier. The surge control weir assembly restricts the flow of the effluent from the clarifier resulting in an accumulation of effluent in the surge control weir assembly from which it flows at a rate proportioned to the volume retained in the assembly and resulting in a settling of minute suspended solids in the clarifier chamber. The surge control weir provides a final screening of the effluent through aerobic bacteria which grow in the slots of the assembly to digest the last solid particles from the water as the water slowly passes through the assembly.

Abstract: The present invention provides a floating media bioclarifier having an economical structure which allows energy efficient and water conserving backwashing of the floating media. The bioclarifier includes a filter chamber fluidly connected to a charge chamber which is adapted for accumulating air. A trigger device positioned between the charge chamber and filter chamber selectively allows the flow of air from said charge chamber to said filter chamber. An air source is connected to the charge chamber and slowly supplies air thereto. The backwash cycle is initiated by the trigger device allowing air to escape from the charge chamber into the filter chamber and adgitate the floating media. Simaltaneously, water from the filter chamber flows into the charge chamber. After the trigger device closes, air agains accumulate in charge chamber in preparation for another backwash cycle.

Abstract: A stationary hydraulic jump is utilized in a multi-phase mixing system to mix components present in a plurality of separate phases. The flow rate and film height of a liquid phase in a first pipe section is metered and combined with a flow rate metered gas phase to form a stationary hydraulic jump in a second pipe section. The jump position is monitored and maintained stationary. A mixed fluid flows from the jump. A variety of solid, liquid, and gaseous components may be mixed in the hydraulic jump through appropriate selection of the liquid and gas phase components.

Abstract: This invention provides a biological injector suitable for biologically treating a fluid flowing through or contained in a collection or treatment system. The biological injector comprises at least one porous section for containing bacterial cultures, at least one non-porous solid section and at least one removable piece which, combinedly, form an enclosed container. Each porous section is attached to at least one non-porous solid section. At least one non-porous solid section is used as a base to which some components of the biological injector can be attached. Each removable piece is attached to one non-porous solid section. The biological injector may include means for fastening the biological injector to a selected location within the collection or treatment system. The biological injector may include means for feeding liquid bacterial cultures and additives to the fluid.

Abstract: A process for the treatment of a liquid reactive medium with a gas comprising dispersing the gas in a liquid in which the gas is sparingly soluble to form a dispersion thereof, said liquid being maintained at a pressure (P1) greater than the pressure (P2) of the liquid reactive medium and the amount of said gas dispersed therein being in excess of its saturation point in the liquid; and introducing the dispersion into the liquid reactive medium having a demand for the gas which is in excess of the amount of gas capable of being dissolved therein at the prevailing conditions in the treatment zone.

Abstract: A process is provided for treating aqueous streams contaminated with electron affinic contaminants. Accordingly, these contaminants are removed by producing a reactive intermediate that is generated in-situ and then reacting the reactive intermediate thus produced with the electron affinic contaminant. The reactive intermediate is produced in the aqueous stream by maintaining low levels of oxygen in the stream and by providing a reducing radical precursor, such as an alcohol, to the aqueous stream.

Abstract: The treatment medium comprises 5 cm cubes of soft, open-cell foam. The container basket is made from plastic mesh, arranged as a cylinder, 80 cm diameter, 100 cm high. The blocks are packed semi-tightly into the basket. The dirty water to be treated is sprinkled onto the foam from above. The container supports the saturated foam blocks in the air, and air circulates freely through the mesh. The container and blocks may be compressed for transport. A separate sub-container holds the top-most blocks, for easy replacement. Cleaned water drains out underneath the baskets. The baskets stand up on their own, and there is free service-access to the baskets during operation, for service.

Abstract: An improved process for removing phosphate from waste water comprising simultaneously injecting a coagulating agent upstream and downstream of a stage of biological oxidation in aerobic medium.

Abstract: A portable wastewater treatment system for recycling an aqueous surfactant solution utilized in a parts washer assembly for cleaning parts. The system including a contaminated solution storage tank, a treated solution storage tank, and a portable wastewater treatment apparatus wherein contaminated aqueous surfactant solution is collected in the contaminated solution storage tank, withdrawn from the contaminated solution storage tank, injected with air and passed into a mixing zone where the mixture is sprayed with water. The treated solution in the mixing zone is passed into a quiescent zone where light sludge is passed to the top of the quiescent zone and heavy sludge is passed to the bottom of the quiescent zone, the treated wastewater being disposed between the light sludge and the heavy sludge and the treated wastewater being passed from the quiescent zone into a discharge zone where the treated wastewater is discharged therefrom. The heavy sludge is selectively discharged from the quiescent zone.

Abstract: An apparatus and method for supplying a vapor-phase nutrient to contaminated soil for in situ bioremediation. The apparatus includes a housing adapted for containing a quantity of the liquid nutrient, a conduit in communication with the interior of the housing, means for causing a gas to flow through the conduit, and means for contacting the gas with the liquid so that a portion thereof evaporates and mixes with the gas. The mixture of gas and nutrient vapor is delivered to the contaminated site via a system of injection and extraction wells configured to the site and provides for the use of a passive delivery system. The mixture has a partial pressure of vaporized nutrient that is no greater than the vapor pressure of the liquid. If desired, the nutrient and/or the gas may be heated to increase the vapor pressure and the nutrient concentration of the mixture.

Abstract: A liquid current type biochemical reactor and methods of use thereof are provided. The reactor is useful in purifying groundwater and wastewater by the process of biodegradation. Also provided is a liquid transport-stirring apparatus for use in biochemical reactors which transports and stirs large amounts of fluids with a small driving force.

Abstract: Preheated diluent and steam are introduced into a container containing waste material typically comprised of a sludge mixture of liquid and solid material including hydrocarbons. The material is thereby heated and its viscosity reduced to form a pumpable slurry. The slurry is pumped out of the container and its viscosity is adjusted to the optimum for separating the solids and liquids. The solids are then separated from the liquid, any valuable material in either the solids and the liquid are recovered and the rest disposed of.