This specification describes a process and apparatus for treating water comprising selenium. A process is described having the steps of treating the wastewater influent using a biological reduction process to produce an intermediary stream and reducing the concentration of unconsumed constituents in the intermediary stream by means of filtration optionally with upstream coagulation or flocculation. When compared to the wastewater influent, the intermediary stream preferably has reduced concentration of the selenium species when compared to the wastewater influent. When compared to the intermediary stream, the effluent preferably has reduced concentration of one or more of the inorganic non-metallic constituents (such as nitrogen, phosphorous and sulphur), metallic constituents or organic constituents. An apparatus is described herein having a fixed film reactor configured to receive a wastewater influent, and a membrane filter configured to receive effluent from the fixed film reactor.

A method for achieving rapid startup of a denitrification biofilter tank, which belongs to the technical field of biofilm sewage treatment. The specific steps are: 1. selecting heterotrophic denitrification or mixotrophic denitrification to treat influent sewage; 2. when the heterotrophic denitrification is used, pretreating the filter material with sodium carboxymethyl cellulose solution and then adding rhamnolipid after the introduction of sewage until the biofilter tank system starts successfully; 3. when the mixotrophic denitrification method is used, the filter tank is inoculated after the introduction of sewage, and the rhamnolipid is added thereto and is changed to sulfur source after operation for a while until startup is complete. The invention solves the problem that the denitrification biofilter tank in the sewage treatment is particularly slow in the mixotrophic state, and has a good application prospect.

A tank is disclosed as having a tub therein that divides the volume of the tank into an anoxic chamber inside the tub and an equalization chamber outside of the tub. The anoxic chamber anoxically treats wastewater while the equalization chamber equalizes fluctuations in wastewater influent as well as provides a holding space for wastewater if power to the tank is cut off. The tank can be part of a system for treating wastewater, such as one with an anaerobic tank having an anaerobic chamber for anaerobically treating wastewater, an aerobic/filtration tank having a filtration sub-tank therein that divides the volume of the tank into a filtration chamber inside the sub-tank and an aerobic chamber outside of the sub-tank. The aerobic chamber can aerobically treat wastewater while the filtration chamber has a membrane unit for filtering wastewater.

A system and method of treating wastewater. In one embodiment, the system comprises a biological reactor fluidly connected to a source of wastewater and having a treated wastewater outlet, a fixed film biological reactor connected to the source of wastewater and having a fixed film effluent outlet, and a ballasted system fluidly connected to the fixed film effluent outlet. The ballasted system may comprise a ballast reactor tank configured to provide a ballasted effluent, and a source of ballast material fluidly connected to an inlet of the ballast reactor tank. The system may further comprise a bypass line having an inlet fluidly connected to the source of wastewater, a first outlet fluidly connected to the ballasted system, and a second outlet fluidly connected to the fixed film biological reactor, the bypass line configured to bypass the fixed film biological reactor.

The invention relates to processes and equipment for treatment of a feedstock by anaerobic organisms to produce a methane containing biogas that can be used as a source of energy. The invention is particularly concerned with producing methane from a waste plant material such as produced by fermentation processes used in the alcoholic beverages industry, such as from brewing/distilling processes which employ grain material for fermentation.

Installation for the biological treatment of water comprising a sequencing batch reactor (SBR) characterized in that said sequencing batch reactor (1) receives purifying plants (2) provided with at least partially submerged roots (3) and moving hollow carriers (4) made of hard plastic on which a biomass grows.

A system and apparatus configured to facilitate on-site treatment of wastewater from a residence is described. The system is configured to immediately treat wastewater as it is generated, on an as-needed basis, and works to remove undissolved down solids and reduce dissolved materials concentrations to a uniform level prior to transmission of the wastewater to municipal waste water treatment facilities and/or any non-drinking application. The system employs a two-stage treatment apparatus where the first stage is configured to pre-grind and decompose undissolved solids of the wastewater and the second to reduce dissolved materials concentrations. The first stage uses turbidity meters, and the second stage uses pH, BOD and conductivity to ensure a uniform output from each stage. A fast decomposer has rotating filters which operational modes ensure that the filters do not become clogged with solids in a cake form simultaneously.

The present invention provides an ecological method for denitrification and phosphorus removal in wastewater treatment process, which relates to the field of sewage treatment technology, The present invention provides a nitrogen and phosphorus removal system, comprising a nitrogen and phosphorus removal unit and a sulfate adsorption unit. The nitrogen and phosphorus removal unit is packed with coarse sand layer, deoxidizing layer and sulfur/iron mixture layer, while the sulfate adsorption unit is filled with modified hydrotalcite. Both of the units are filled with solid material, which effectively avoid the contamination that causes by liquid carbon source feeding. The application of the present invention can realize a completely denitrification, which achieve a maximum removal rate of 100%, a phosphorus removal efficiency of about 80%. The TP concentration is below 0.5 mg/L in the treated effluent, while the average sulfate removal rate is about 50%.

Multiple embodiments are described for water and wastewater treatment using bio-ZVI to remove nitrate, nitrite, perchlorate, chlorinated organic compounds, nitroaromatic compounds, arsenic, selenium, phosphorus, etc. from water. ZVI may also provide an iron nutrient to enhance biological activity, and the oxidized ferric can serve as flocculent to improve sludge dewater characteristics.

A method for biologically treating nitrogen while minimizing energy and carbon source usage uses an aerobic tank, a first anoxic tank, and a second anoxic tank. The method includes introducing feed water by dividedly introducing the feed water to the aerobic tank and the first anoxic tank; converting ammonia nitrogen into nitrate nitrogen in the aerobic tank; converting the nitrate nitrogen into nitrite nitrogen through partial denitrification in the first anoxic tank using organic material contained in the feed water; and converting the nitrite nitrogen and ammonia into nitrogen gas in the second anoxic tank using an anammox microorganism. The ammonia nitrogen is converted by determining aeration intensity, aeration time, and/or aeration amount depending on an ammonia concentration in the aerobic tank. The nitrate nitrogen is converted by determining a reaction time of the first anoxic tank based on nitrate and nitrite concentrations in the first anoxic tank.