The present disclosure relates generally to systems, apparatuses, and processes for preparing a gas-infused additive that is useful within gas-floatation systems configured to separate solids and/or oils from a liquid within a suspension. The gas-infused additive can be injected into systems having a floatation consolidator to provide additional dissolved gas to the system. Advantageously, the processes and apparatuses disclosed herein are compatible with systems and processes having a single injection point for the addition of an additive or gas, without requiring substantial modification or reconfiguration of the system. The inventions described herein additionally teach that the gas-infused additive can be prepared and injected downstream of any pump present within the system, thereby protecting the pump from the damaging effects of cavitation corrosion and similar phenomena.

An automated produced water treatment system that injects ozone or an ozone-oxygen mixture upstream of produced water separators, with the dose rate changing dynamically as the produced water quality changes, as determined by continuous monitoring of the produced water quality by a plurality of sensors that detect water quality parameters in real time. The system may operate as a “slipstream” injection system, that draws a portion of produced water from the produced water pipeline and injects ozone or an ozone-oxygen mixture back into the pipeline with disrupting or slowing normal operations. Disinfectants or other additives may also be injected. The treatment system may be wholly or partially contained in mobile containers or trailers, for on-the-fly use in existing produced water treatment facilities.

An automated produced water treatment system that injects ozone or an ozone-oxygen mixture upstream of produced water separators, with the dose rate changing dynamically as the produced water quality changes, as determined by continuous monitoring of the produced water quality by a plurality of sensors that detect water quality parameters in real time. The system may operate as a “slipstream” injection system, that draws a portion of produced water from the produced water pipeline and injects ozone or an ozone-oxygen mixture back into the pipeline with disrupting or slowing normal operations. Disinfectants or other additives may also be injected. The treatment system may be wholly or partially contained in mobile containers or trailers, for on-the-fly use in existing produced water treatment facilities.

There is disclosed processes and systems for improving the efficiency of the separation of insoluble contaminants from a fluid in a floatation unit.

There is disclosed processes and systems for improving the efficiency of the separation of insoluble contaminants from a fluid in a floatation unit.

A separation unit for separating contaminants, such as oil, from water comprises at least one inlet section and a separation tank having an outlet for effluent, an outlet for liquid reject, and an outlet for gas. The inlet section comprises an inlet for influent, a gas injector for injecting gas into the influent, a turbulent mixing assembly for mixing the influent and the gas, and a diffuser for reducing a flow velocity of the mixed influent and gas. The separation unit is adapted to control a level of a gas-liquid interface in the tank by regulating leakage of gas using a liquid reject valve in the outlet for liquid reject and/or a gas reject valve in the outlet for gas. The separation unit maintains the level of the liquid interface below an entrance of the outlet for liquid reject during a normal mode of operation, and, during a fluid reject mode of operation, opens the liquid reject valve and raises the level of the liquid interface to be equal to or above the entrance of the outlet for liquid reject.

A separation unit for separating contaminants, such as oil, from water comprises at least one inlet section and a separation tank having an outlet for effluent, an outlet for liquid reject, and an outlet for gas. The inlet section comprises an inlet for influent, a gas injector for injecting gas into the influent, a turbulent mixing assembly for mixing the influent and the gas, and a diffuser for reducing a flow velocity of the mixed influent and gas. The separation unit is adapted to control a level of a gas-liquid interface in the tank by regulating leakage of gas using a liquid reject valve in the outlet for liquid reject and/or a gas reject valve in the outlet for gas. The separation unit maintains the level of the liquid interface below an entrance of the outlet for liquid reject during a normal mode of operation, and, during a fluid reject mode of operation, opens the liquid reject valve and raises the level of the liquid interface to be equal to or above the entrance of the outlet for liquid reject.

A wastewater treatment system comprises a fluid conveyance, one or more filtration vessels, one-way valves, and a backwash collection conduits. The filtration vessels each have a vessel inlet and a vessel outlet. Filtration media is positioned between the respective vessel inlet and the respective vessel outlet. Each respective vessel inlet communicates with the fluid conveyance. Each one-way valve is located at the inlet of the respective filtration vessel to regulate a flow of fluid from the fluid conveyance into the respective filtration vessel and to prevent the fluid from exiting the respective filtration vessels through the one-way valves. Each backwash collection conduit communicates with each filtration vessel by a drain conduit, the drain conduit having an outlet that is above a top of a fluid volume in the backwash collection conduit so as to provide an air gap.

Provided are nanonets comprising a) a surfactant aggregate having an average aggregate diameter; and b) a polymer having an average particle diameter which average particle diameter is the same or smaller than the average aggregate diameter, wherein the nanonet has a diameter larger than the average particle diameter. Also provided are kits therefor and methods for sequestering non-water moieties from aqueous solutions using nanonets.

Provided are nanonets comprising a) a surfactant aggregate having an average aggregate diameter; and b) a polymer having an average particle diameter which average particle diameter is the same or smaller than the average aggregate diameter, wherein the nanonet has a diameter larger than the average particle diameter. Also provided are kits therefor and methods for sequestering non-water moieties from aqueous solutions using nanonets.