An anaerobic electrochemical membrane bioreactor (AnEMBR) can include a vessel into which wastewater can be introduced, an anode electrode in the vessel suitable for supporting electrochemically active microorganisms (EAB, also can be referred to as anode reducing bacteria, exoelectrogens, or electricigens) that oxidize organic compounds in the wastewater, and a cathode membrane electrode in the vessel, which is configured to pass a treated liquid through the membrane while retaining the electrochemically active microorganisms and the hydrogenotrophic methanogens (for example, the key functional microbial communities, including EAB, methanogens and possible synergistic fermenters) in the vessel. The cathode membrane electrode can be suitable for catalyzing the hydrogen evolution reaction to generate hydrogen.

According to one embodiment of the present invention, a forward osmosis-type fresh water composite system includes: a fuel cell device that has a cathode electrode in which carbon dioxide supplied from a plant is converted into carbonate ion (CO.sub.3.sup.2?) and an anode electrode that produces electric energy by reacting the carbonate ion (CO.sub.3.sup.2?) with hydrogen and discharges the carbon dioxide; and a carbon dioxide collection unit that reacts the carbon dioxide supplied from the fuel cell device and water supplied from the outside with ammonia separated from a draw solution separation unit so as to produce a high-concentration draw solution and then supplies the high-concentration draw solution to a forward osmosis separation device.

The invention relates to a bioreactor for treating water fluid(s), and/or for producing a desired end product by biomass and/or for producing biomass. The invention relates also to methods for manufacturing and using such a bioreactor. The bioreactor (BR) includes at least a first processing unit (Z.sub.F), a second processing unit (Z.sub.2), a last processing unit (Z.sub.L), and, optionally, additional processing unit(s) (Z.sub.3, Z.sub.4) between the second processing unit (Z.sub.2) and the last processing unit (Z.sub.L) in a plug flow configuration; at least one forward circulation system (FCS, FCS1, FCS2) for circulating biomass (BM) from the first processing unit (Z.sub.F), to the last processing unit (Z.sub.L) and/or to additional processing unit(s) (Z.sub.3, Z.sub.4); and at least one reverse circulation system (RCS, RCS1, RCS2) for circulating biomass (BM) from the last processing unit (Z.sub.L) and/or from the additional processing unit(s) (Z.sub.3, Z.sub.4) to the first processing unit (Z.sub.F).

System (100) and method for processing biomass. The system comprises a combined heat and power plant (102), an interface (114) for feeding biogas to a traffic fuel production unit, interfaces (114) to a district heating system (106a) and an electrical grid (106b), and a hydrolysis device (108), a digestion device (110), a dryer (116) and a heat recovery unit (112), which are operatively coupled for transferring heat, intermediate products and final products of the process, wherein raw biomass is received into the hydrolysis device (108), biomass processed by the hydrolysis device (108) is fed to the digestion device (110), biogas obtained in the digestion device (110) is fed to the traffic fuel production unit (104), heat is recovered from the hydrolysis device (108), biomass processed by the digestion device (110) is dried by the heat recovered from the hydrolysis device (108), heat is recovered from the dryer (116), heat recovered from the dryer (116) is fed to the hydrolysis device (108) to be used in pre-heating of the received raw biomass, heat recovered from the dryer (116) is fed to the district heating (106a), and production of electricity is fueled by the dried biomass from the dryer (116).

Systems and methods for producing and extracting a gas from a wastewater fluid including multiple sheets or layers that form a composite membrane. The composite membrane includes a sandwich structure in which a dry matrix layer is surrounded by a first layer including a first immobilized bacteria and a second layer including a second immobilized bacteria. The first immobilized bacteria and the second immobilized bacteria can be configured to produce a gas from one or more compounds in a wastewater fluid. The dry matrix layer can be configured to receive the gas from the first and second layers, and the gas can be extracted from the membrane. The hydrophobic coatings can be disposed between the dry matrix layer and one or both of the first and second layers. An adhesive interface can be disposed between the dry matrix layer and one or both of the first and second layers.

Disclosed herein is a method and apparatus that uses a brine from a well that is used to both generate electricity and recover valuable minerals present in the brine. The method and apparatus uses a hydrophobic membrane to separate water vapor from the brine to concentrate the brine that is then used to recover the minerals.

A reverse osmosis system and method of operating the same includes a membrane housing comprising a reverse osmosis membrane therein. The membrane housing has a feed fluid input, a brine outlet and a permeate outlet; The system further includes a charge pump, a plurality of valves and a tank having a volume comprising a movable partition dividing the volume into a first volume and a second volume. The plurality of valves selectively couples the charge pump to the first volume or the second volume and the brine outlet to the second volume or the first volume respectively.

An integrated utility system (10) comprising; i) a power supply (12); and ii) a wastewater treatment system (20), wherein waste energy from the power supply (12) is utilized in the wastewater treatment system (20).

The present process relates to thermally hydrolyzing sludge in a thermal hydrolysis system. A flash tank or waste heat boiler is located downstream of the thermal hydrolysis system. Hydrolyzed sludge is continuously directed into the flash tank or waste heat boiler for recovering supplemental steam. The supplemental steam is used independently or in combination with live steam produced by a main boiler to heat sludge being directed into the thermal hydrolysis system.

Described is a system for integrated water treatment and cooling in the steel industry. The system includes a waste heat recovery unit, a wastewater treatment system, a water-cooling system, a solar thermal system, and an electric energy production system. The waste heat recovery unit receives waste heat generated by a steelmaking plant. The wastewater treatment system treats wastewater produced by the steelmaking plant and produces treated water. The water-cooling system cools the treated water and returns the cooled treated water to the steelmaking plant for reuse. The solar thermal system collects solar energy, and the electric energy production system generates electricity from the solar energy and the waste heat and uses the generated electricity to power the wastewater treatment system and the water-cooling system.