Provided is a reciprocating submerged membrane filtration apparatus including: a membrane tank comprising a submerged membrane and configured to intake influent wastewater to be treated, the influent wastewater being filtered through the submerged membrane to produce treated water; and a reciprocation apparatus configured to move the membrane to create an inertia force which shakes foulants off from the submerged membrane under oxygen-deficient conditions, wherein the submerged membrane comprises a microfiltration (MF) membrane or an ultrafiltration (UF) membrane.

A stormwater runoff treatment substrate includes a lower pyrite substrate layer and an upper biochar substrate layer. The lower pyrite substrate layer includes pyrite, oyster shell powder, and sandy materials in a volume ratio of 10:5:85. The upper biochar substrate layer includes biochar or activated carbon, organic nutrient soil, and sandy materials in a volume ratio of 20:3:77.

In a method of anaerobic treatment of an organic waste stream (1), a stream originating from an anaerobic reactor (5) is fed to a first separating unit (33) to be separated into a sludge fraction (7) containing between 50% and 80% of the solids by weight and a second fraction (7). The second fraction (7) is fed from the first separating unit (33) into a Dissolved Gas Floatation (DGF) unit (16). The sludge fractions (7) and (9) from the separator units (33) and (16) are fed back to an inlet 41 of the reactor 5.

The present disclosure relates, according to some embodiments, to systems and methods for processing organic compounds, such as manure or other organic waste. Embodiments may comprise a first containment or mixing chamber, a first anaerobic chamber, and a second anaerobic chamber. A first anaerobic chamber may receive organic compounds from a first containment or mixing chamber, and may provide a fluid stream to a second anaerobic chamber. The second anaerobic chamber may comprise a substrate, such as lava rock, with bacteria growing thereon. Further, biogas generated in one or both of the first anaerobic chamber and the second anaerobic chamber may be purified in a first stage using a water scrubber to remove a majority of the carbon dioxide and other contaminants from the biogas, and in a second stage using a pressure swing adsorption unit to reduce carbon dioxide and other contaminants to pipeline acceptable levels. Further yet, carbon dioxide and hydrogen sulfide gases generated during the biogas purification process may be injected into a water-containing chamber in the presence of bacteria and oxygen to convert the hydrogen sulfide to elemental sulfur and/or sulfate

The present invention relates to an anaerobic reactor for the treatment of industrial and other wastewaters at psychrophilic temperatures, the reactor comprising a mixing chamber in which is located, during use, a granular sludge fluidised bed, the reactor further comprising a biofilm chamber fed from the mixing chamber and housing a biofilm colonised pumice-based carrier material, and a separation chamber in fluid communication with the biofilm chamber and in which treated effluent and biogas produced within the reactor are separated.

A system that recycles waste so that the effluent coming out of the system actually equals a potable water standard with essentially no contaminated sludge. The solids in wastewater are subjected to aeration and enzymes in a digester for a period of time. The cleanest portion of the water from the digester is then clarified. Sludge, as well as scum, from the clarifier is vacuumed back to the digester. Clear water from the clarifier is delivered to a Recycling stage for filtering to remove suspended solids. When the recycling process housing reaches saturation, a back-flushing process with clean water sends all of the captured suspended solids back into the Digester.

System and methods for treating multi-component waste streams. In general, systems and methods described herein employ a first chamber and a second chamber separated by a barrier and a filtration component that is fluidically connected to the first and second chambers. A waste stream to be treated will flow into the first chamber for treatment of the carbon-containing waste, then into the filtration component for the separation of the stream into a solid waste fraction and a liquid waste fraction.

In a system and process, sludge is treated by two stages of anaerobic digestion in series separated by intermediate thickening and hydrolysis. The hydrolysis product is transferred to the second digester essentially without dilution.

The present invention relates to a system capable of maximizing biogas production by mixing dry feed at a predetermined ratio with digestive fluid discharged from an anaerobic digestion tank, which is a front-end process of a wastewater treatment system, and then introducing it into a digestion tank. The present invention implements a new type of system which separates the digestive fluid discharged from an anaerobic digestion tank, which is a front-end process of the wastewater treatment system, into solid and liquid in a sedimentation tank, and then mixes treated water with dry feed at a predetermined ratio and reintroduces it into the digestion tank, and also introduces digested slime and sludge into dryer equipment, thereby providing a system for producing biogas using a mixed liquid of digestive fluid treated water and dry feed that can maximize the production of biogas (methane gas) to reduce energy costs, increase the production of dry substances to reduce waste disposal costs, and increase the resource recycling rate.

Systems and methods are disclosed for treating wastewater, such as food and beverage industry wastewater, pulp and paper wastewater, textile wastewater, tannery wastewater, pharmaceutical wastewater, etc., which contains high concentration of COD along with high concentrations of nitrogen and phosphorus to yield a low COD output along with a low phosphorous output and a low nitrogen output. One system comprises a buffer tank, an anoxic tank, an oxic tank, and a membrane bioreactor tank fluidically connected in series with pure oxygen blown into the oxic tank.