A method and apparatus for collection and disposal or utilization as a carbon neutral fuel of fats, oil and grease that includes a first porous container, a second porous container, and a grease trap having an inlet and an outlet. The first porous container is positioned proximate the grease trap inlet and the second porous container is positioned proximate the grease trap outlet. The first and second porous containers are formed of a porous fabric and contain an absorbent, organic hydrocarbon material capable of absorbing a quantity of fats, oil and grease. The second porous container may be positioned on either side of the grease trap outlet (within the grease trap or intermediate the outlet and an exit pipe) and may be held in a stationary manner via a tether and/or a hinged door having a flange for capturing and holding the porous container in a stationary manner.

An automated process and accompanying apparatus simultaneously separates and measures the flow rate of any multiphase mixture of immiscible fluids. Such separation and measurement can occur in a single vessel, or multiple vessels. Liquid levels, together with a material balance analysis, are utilized to determine constituent liquid flow rates. The vessel(s) can be remotely operated and monitored in real time, while also allowing for automated or manual calibration.

An automated process and accompanying apparatus simultaneously separates and measures the flow rate of any multiphase mixture of immiscible fluids. Such separation and measurement can occur in a single vessel, or multiple vessels. Liquid levels, together with a material balance analysis, are utilized to determine constituent liquid flow rates. The vessel(s) can be remotely operated and monitored in real time, while also allowing for automated or manual calibration.

A cyclonic inlet diverter for initiating the separation of a multi-phase inlet fluid flow comprises an enclosed tubular body mounted crosswise within a larger separator vessel. The inlet diverter includes a splitter plate positioned within a center portion of the tubular body and configured to split the inlet flow into a first stream and a second stream, and a swirl plate positioned on each side of the splitter plate with angled surfaces configured to increase the cyclonic motion of the first and second streams within the tubular body. The inlet diverter further includes elongate apertures formed through bottom sidewall portions of the tubular body on each side of the splitter plate, an axial aperture formed through opposing end caps of the tubular body, and at least one radial aperture formed through lateral sidewall portions of the tubular body proximate each opposing end cap.

A cyclonic inlet diverter for initiating the separation of a multi-phase inlet fluid flow comprises an enclosed tubular body mounted crosswise within a larger separator vessel. The inlet diverter includes a splitter plate positioned within a center portion of the tubular body and configured to split the inlet flow into a first stream and a second stream, and a swirl plate positioned on each side of the splitter plate with angled surfaces configured to increase the cyclonic motion of the first and second streams within the tubular body. The inlet diverter further includes elongate apertures formed through bottom sidewall portions of the tubular body on each side of the splitter plate, an axial aperture formed through opposing end caps of the tubular body, and at least one radial aperture formed through lateral sidewall portions of the tubular body proximate each opposing end cap.

There is an inlet baffle assembly for use in an in-line interceptor for separating FOG from wastewater and a method of cleaning the inlet baffle assembly without the need for removal from the interceptor. The inlet baffle assembly has an inlet baffle for the grease collecting chamber of an in-line interceptor which defines a flow channel through which influent enters the collecting chambers and has a moveable section moveable between open and closed positions. The inlet baffle assembly also has a flow control element to control the rate of flow of influent entering the flow channel when the moveable section is in the closed position. The flow control element is accessible for cleaning when the moveable section is in the open position. After cleaning, the moveable section is moved into the closed position to facilitate fluid flowing through the inlet baffle assembly into the grease collecting chamber.

There is an inlet baffle assembly for use in an in-line interceptor for separating FOG from wastewater and a method of cleaning the inlet baffle assembly without the need for removal from the interceptor. The inlet baffle assembly has an inlet baffle for the grease collecting chamber of an in-line interceptor which defines a flow channel through which influent enters the collecting chambers and has a moveable section moveable between open and closed positions. The inlet baffle assembly also has a flow control element to control the rate of flow of influent entering the flow channel when the moveable section is in the closed position. The flow control element is accessible for cleaning when the moveable section is in the open position. After cleaning, the moveable section is moved into the closed position to facilitate fluid flowing through the inlet baffle assembly into the grease collecting chamber.

Water permeable coated substrates and filtration membranes are provided comprising: (a) a porous substrate; (b) an optional primer layer applied to a substrate surface (a), wherein the primer layer comprises silica and/or an organometallic compound; (c) a superhydrophilic coating layer applied to the porous substrate (a), or the primer layer (b), wherein the superhydrophilic layer comprises a superhydrophilic polymer or silicate; and (d)

an optional tie layer applied to the superhydrophilic coating layer (c), wherein the tie layer comprises silica and/or an organometallic compound. The water permeable coated substrates and filtration membranes may further include (e) an oleophobic coating layer applied to the superhydrophilic coating layer (c), or the tie layer (d), wherein the oleophobic coating layer comprises a fluoropolymer having reactive functional groups. Each layer of the coated substrate is covalently bonded to adjacent layers. Methods of separating an oil-in-water emulsion are also disclosed.

Water permeable coated substrates and filtration membranes are provided comprising: (a) a porous substrate; (b) an optional primer layer applied to a substrate surface (a), wherein the primer layer comprises silica and/or an organometallic compound; (c) a superhydrophilic coating layer applied to the porous substrate (a), or the primer layer (b), wherein the superhydrophilic layer comprises a superhydrophilic polymer or silicate; and (d)

an optional tie layer applied to the superhydrophilic coating layer (c), wherein the tie layer comprises silica and/or an organometallic compound. The water permeable coated substrates and filtration membranes may further include (e) an oleophobic coating layer applied to the superhydrophilic coating layer (c), or the tie layer (d), wherein the oleophobic coating layer comprises a fluoropolymer having reactive functional groups. Each layer of the coated substrate is covalently bonded to adjacent layers. Methods of separating an oil-in-water emulsion are also disclosed.

A disclosed subsea sediment separation and filtration system includes first and second separation devices, a spreader apparatus, and a storage device. The first separation device receives a water/sediment/oil mixture and from a subsea surface and separates the mixture into a first component containing cleaned sediment and a second component containing a water/oil mixture. The spreader apparatus disperses the cleaned sediment of the first component into a subsea environment of the spreader apparatus. The second separation device receives the second component from the first separation device and separates the second component into a cleaned water component and an oil component. The second separation device disperses the cleaned water component into a subsea environment of the second separation device and provides the oil component to the storage device. The first separation device may include a plurality of hydrocyclone devices, and the second separation device may include a high pressure hydrocyclone device.