A fluid-forwarding sludge-discharge device for a settlement basin, the device including: a pressurized water spraying unit of which one end is disposed adjacent to the floor of the settlement basin; a sludge suction cover which is disposed on an upper part of the floor such that the lower part thereof covers the upper part of the sludge-receiving unit in a state having an open box shape and collection guide plates which are provided joined to the floor of the settlement basin and guide the sludge being moved by means of the pressurized water spraying unit such that the sludge flows towards the sludge inflow recess.

One or two continuous recirculation loops are utilized for the well-site equipment that separates produced fluids into sand, liquid, and gas during drill out and flow back that occurs after fracturing a subterranean formation. When one recirculation loop is utilized, the recirculation loop continuously recirculates fluid between the recirculation chamber of the disclosed sand removal apparatus and a shaker device. When two recirculation loops are utilized, the first recirculation loop continuously recirculates fluid between a recirculation chamber of the disclosed sand removal apparatus and a shaker device, and the second recirculation loop continuously recirculates fluid between the recirculation chamber and a gas separator.

A de-sanding tank with a vertical exterior wall and an interior conical bottom with a solids outlet located at a lower tip of the conical bottom. Downwardly and tangentially oriented water jet nozzles within the tank cause a swirling action to remove solids. An enclosing space located between the vertical wall and the conical bottom has a honey-combed structure of closed pore foam as reinforcement for the conical bottom. Compartments within the honey-combed structure fill with water as the vessel is placed in service to add support for the conical bottom. Water enters the compartments via downwardly facing bottom openings that fill a common void located at the bottom of the enclosing space and then into the compartments. Weep holes provided between the top of each compartment and the interior of the tank allow the air from the compartments to enter the tank as the compartments fill.

A stormwater vault and a process for servicing the stormwater vault speeds the process of cleaning a stormwater vault. The stormwater vault has a built in liquefaction system for liquefying settled debris in the vault which works together with a sloped or angled floor in the vault. The settled debris is flushed toward the inlet to a vacuum removal line inserted into the vault through an access opening for removing the settled debris from the vault.

Example embodiments relate to a separator system comprising a compartment body defining an interior cavity, the interior cavity formed by interior walls of the compartment body. The separator system may further comprise an input section operable to receive an input mixture for housing in the interior cavity. The separator system may further comprise an output section. The separator system may further comprise a particulate-directing subsystem. The particulate-directing subsystem may comprise a disturbance assembly arranged along at least a bottom portion of the interior cavity. The disturbance assembly may comprise at least one rotary member operable to rotate in a first rotary direction and a second rotary direction. The particulate-directing subsystem may further comprise a discharge assembly arranged proximate to the output section. The discharge assembly may be configured so as to encourage particulates of the input mixture present in the interior cavity to pass through the output section.

An aim of the invention is to provide a bioreactor and a waste water treatment method that employs this tank, whereby anaerobic and aerobic microorganism treatment can be continuously carried out, even when the volume of the bioreactor is large, and whereby installation costs can be minimized. The invention comprises an outer tank (2), a cylindrical inner tank (3) disposed inside this outer tank and having openings above and below, a circulation rate control device (4) for controlling the circulation rate of water to be treated in the bioreactor, the circulation rate control device (4) being provided at an upper part of this cylindrical inner tank, a cylindrical control plate (5) for bringing about sedimentation of sludge, the cylindrical control plate (5) being provided at the outer circumference of an upper part of the cylindrical inner tank, a treated-water quality measurement device (6) that is provided outside and inside of the cylindrical inner tank, a waste water supply opening (10) that is provided in the circulation pathway of the water to be treated circulating through the outer tank and inner tank, a treated water discharge opening (11) that is provided in an upper part of the outer tank.

A high-rate sedimentation tank includes a hopper configured to be supplied with raw water including floc, at least one circular orifice pipe disposed at a lower portion of the hopper and configured to have the floc deposited therein as a sludge while passing the floc included in the raw water therethrough, and a sludge outlet configured to discharge the sludge deposited by passing through the circular orifice pipe to an outside of the hopper.

A slurry removal system includes a tank, an eddy pump, and a pipe system. The tank is configured to receive a mixture of solid material and liquid. The eddy pump has a pump inlet connected to the tank and a pump outlet. The pipe system is connected to the pump outlet and including a discharge line and a recirculation line. The eddy pump is configured to pump the mixture of solid material and liquid from the tank through the pump inlet to the recirculation line to form an essentially homogeneous mixture, and configured to pump the essentially homogeneous mixture from the tank through the pump inlet to the discharge line to remove the homogeneous mixture from the tank.

A method and apparatus for treating wastewater using a sequencing batch reactor wherein the biological solids are densified through hydraulic and organic selection pressures. Wastewater is introduced to the reactor near the end of the treatment cycle under anaerobic conditions following the effluent withdrawal step and prior to the start of next treatment cycle. A floating sludge withdrawal apparatus is used in conjunction with a floating surface mixer to selectively remove lighter flocculant solids and retain denser solids by temporarily reducing the mixing energy during the wasting process.

The invention relates to a system and a method for preventing sediment formation in at least one tank during heat extraction of thermal energy from wastewater from properties, which the system comprises; at least one pump pit, a wastewater inlet, a pump, a pump pit outlet and a drain opening, at least one buffer tank, and at least one collector tank 1, a heat exchanger, in the collector tank, a heat pump, and an accumulator for accumulating heat. To avoid sediment formation, at least one of the pump pit, the buffer tank or the collector tank comprises at least one ejector for compressed air arranged therein, which ejector is connected to a compressed air device for controlling the supply of compressed air to at least one of the at least one pump pit, the buffer tank or the collector tank through the at least one ejector.