Patent classifications
B01F23/23421
Flow straightening vane for aerator
The present inventions are generally directed to surface aerators for aerating water or wastewater in a basin, lagoon or tank. In particular, the present inventions relate to flow straightening vanes incorporated into an aerator volute tube that straighten the intake and discharge flow thereby minimizing or eliminating torque on the unit and on the mooring components of the aeration assembly. The present inventions also improve mixing and aeration.
FLOW STRAIGHTENING VANE FOR AERATOR
The present inventions are generally directed to surface aerators for aerating water or wastewater in a basin, lagoon or tank. In particular, the present inventions relate to flow straightening vanes incorporated into an aerator volute tube that straighten the intake and discharge flow thereby minimizing or eliminating torque on the unit and on the mooring components of the aeration assembly. The present inventions also improve mixing and aeration.
ALCOHOLIZER FOR RECEIVING A FLUID
The disclosure provides an alcoholizer for receiving a fluid, the alcoholizer includes a fixing component configured with a bearing and a turbine blade movably connected to the fixing component through the bearing. When the turbine blade is configured to receive the fluid, the bearing is driven to rotate. The alcoholizer of the present disclosure facilitates quick decanting of brewing liquid (such as red wine) by mixing the liquid with air.
MIXING/AERATING APPARATUS WITH AN IMPELLER
An improved mixing apparatus for mixing a liquid within a liquid body is provided. Generally, the improved mixing apparatus may comprise: a supporting element (1) with a partly conical volute with an upper corrugated free edge; a top-mounted power drive (2); and an impeller (4) mounted on said shaft (3) for rotation therewith.
WATER CARBONATION INFUSION PUMPS
Devices for carbonating drinking water are disclosed. The devices include a container that is configured to hold a volume of carbonated drinking water; a CO.sub.2 gas supply line that is configured to deliver CO.sub.2 gas to the volume of carbonated drinking water within the container; and a variable speed electric motor located outside of and adjacent to an external surface of the container. In addition, the devices include a turbine type impeller that is magnetically coupled to and driven by the variable speed electric motor. The turbine type impeller is configured to rotate at variable speeds and spray carbonated drinking water transferred from a bottom portion of the container into an air space located above the volume of carbonated drinking water and the top internal surface of the container.
Method of controlling a circulation-type wastewater treatment plant via a stored parameter relationship in a control unit
A plant and method for controlling such a plant suitable for treatment of waste water. The plant includes a basin, a flow generating machine adapted to generate a liquid flow in the basin, equipment in the basin that effects the momentum of the liquid flow, and a control unit. The method includes the steps of: storing a predetermined relationship between the operational speed N of the flow generating machine and an operational parameter P from which the torque M of the flow generating machine may be derived, determining the operational speed N, determining a set value of the operational parameter P of the flow generating machine, determining a real value of the operational parameter P of the flow generating machine, and adjusting the operational speed N if the real value of the operational parameter P is different than the set value of the operational parameter P.
Combination submersible and floating aerator
An aeration system may have a submersible aerator that may be located on the bottom of a body of water and a floating aerator that may operate directly above the submersible aerator. The submersible aerator may create a laminar column of bubbles and may be powered by an air compressor. The floating aerator may use a motor driven propeller to agitate water on the water surface. A controller may determine when to operate the aerators, and may operate them separately or together in some instances. Some embodiments may have a controller that operates the aerators differently based on energy supply, which may vary in solar powered systems with a battery bank.
SYSTEMS AND METHODS FOR FORMATION OF BIOLOGICALLY ACTIVE GRANULES AND BIOLOGICALLY ACTIVE GRANULES
In one embodiment, hydrodynamic cavitation lyses influent bacteria, releasing intracellular enzymes, and creates CaCO.sub.3 seed crystals that are discharged at the base of the water column. Bottom-dwelling upflow anaerobic sludge blanket (UASB)-like granules grow in a dense, viscous N, P & Ca++ rich fluid (hydrolytic brine). The brine hydrolyzes ancient sludge and fresh solids into simple liquids. The granules convert hydrolyzed liquids into gas. New CaCO.sub.3 seeds grow at the produced gas/supernatant interface and propagate across the entire lagoon. Once the sludge inventory is digested, there is an excess of granules that modulate their gross productivity in response to substrate load, pH, and temperature. In one specific example, the treated lagoon has no odor, is free of gelled sludge and effluent
PLANT FOR TREATMENT OF LIQUID AS WELL AS METHOD FOR CONTROLLING SUCH A PLANT
A plant and method for controlling such a plant suitable for treatment of waste water. The plant includes a basin, a flow generating machine adapted to generate a liquid flow in the basin, equipment in the basin that effects the momentum of the liquid flow, and a control unit. The method includes the steps of: storing a predetermined relationship between the operational speed N of the flow generating machine and an operational parameter P from which the torque M of the flow generating machine may be derived, determining the operational speed N, determining a set value of the operational parameter P of the flow generating machine, determining a real value of the operational parameter P of the flow generating machine, and adjusting the operational speed N if the real value of the operational parameter P is different than the set value of the operational parameter P.