A multi-path cleaning system is provided for a fuel tank. The multi-path cleaning system includes a controller, a fuel polisher, and a plurality of controllable valves. The plurality of controllable valves are operatively connected to the controller, and each valve fluidly coupled to at least one of the inlet and outlet of the fuel polisher on a first side and the interior of the fuel tank on a second other side. The pump, when operated, causes fuel to be drawn through the inlet and discharged at the outlet of the fuel polisher, and to pass through at least one filter/water separator. Selective operation of the plurality of valves by the controller selectively fluidly couples portions of the interior of the fuel tank to the inlet and the outlet of the fuel polisher, thereby creating a plurality of fluid flow paths through the interior of the fuel tank.

The invention relates to a method for the treatment of water contaminated by thermal oil and collection of said oil (for example, a eutectic mixture of biphenyl and diphenyl oxide), formed by a cooling phase (2) for cooling (to a temperature between the freezing point of the thermal oil and that of water) the mixture (1) of water and thermal oil, followed by the collection (3) of the part (4) of frozen thermal oil (precipitated or in suspension) by means of mechanical filtering. The remainder of contaminated water is treated in absorption filters and in activated carbon adsorption filters. The equipment required to implement this method comprises a cooling unit, a unit for the separation of phases by means of mechanical filtering for the collection (3) of the frozen thermal oil part (4), a unit (6) of absorption filters and a unit (7) of adsorption filters (activated carbon unit).

Wastesolution treatment systems and methods are provided which may remove particulates and hydrocarbons from wastesolution. Embodiments may be used to treat scrubber wastesolution from exhaust gas cleaning (EGC) systems. Some embodiments may be used with terrestrial EGC systems and others may be used for maritime ship EGC systems. Certain embodiments remove free phase oil and particulates from the wastesolution. Some embodiments may utilize a biogenerator cultured with hydrocarbon degrading microorganisms to reduce the concentration of oils in the water. Certain embodiments may utilize a clarifier and filtration unit to remove contaminants in the water. The wastesolution may be recirculated through the system until the measured contaminant concentration drops below a threshold value. The treated wastesolution may be stored, reused, or may be safely discharged from the system.

A system adapted to condition an initial water feed stream including a water treatment subsystem, wherein the water treatment subsystem includes a first oxygen removal unit including a membrane filter, wherein the initial water feed stream flows through the membrane filter and the first oxygen removal unit is adapted to treat the initial water feed stream to remove a first portion of the dissolved oxygen to form a first deoxygenated water stream, a hydrazine stream dissolved into the first deoxygenated water stream, a second oxygen removal unit including a vessel filled with a palladium-doped resin, wherein the second oxygen removal unit is adapted to treat the first deoxygenated water stream including the hydrazine stream dissolved therein to catalytically remove a second portion of the dissolved oxygen to form a second deoxygenated water stream, and an oxygen scavenger feeder adapted to blend a chemical scavenger and the second deoxygenated water stream.

A filter assembly for fluid filtration having a push-activated lock and release mechanism. A push filter design activates a filter key lock upon insertion and extraction, where the filter key may be used simultaneously as a lock and as an identifier for particular filter attributes. The filter housing assembly may be attached to, and removed from, a filter base by a push-actuated release. Upon insertion, the filter key shifts the filter lock longitudinally to receive interlocking segments. Upon extraction, the same axial push shifts the filter lock further to align the interlocking fingers within gaps that allow for easy extraction. The specific key lock design allows a user to identify and match certain filter configurations received by the mechanical support, and reject other filter configurations.

A device for thickening a cryogenic slurry is disclosed. The device comprises a cryogenic slurry flow path, a cryogenic liquid discharge path, and a filter medium between the cryogenic slurry flow path and the cryogenic liquid discharge path. The cryogenic slurry comprises a solid and a cryogenic liquid. The cryogenic slurry is fed into the cryogenic slurry flow path, generally tangential to the filter medium. This causes a portion of the cryogenic liquid to cross the filter medium into the cryogenic liquid discharge path as a cryogenic liquid discharge and the cryogenic slurry to thicken to produce a thickened slurry. The filter medium comprises a cryogenically-stable material such that adsorption of gases is inhibited, deposition of solids is prevented, and temperature-change induced expansion and contraction of the filter medium is optimized.

A method for thickening a cryogenic slurry is disclosed. The method comprises providing a cryogenic slurry flow path, a cryogenic liquid discharge path, and a filter medium between the cryogenic slurry flow path and the cryogenic liquid discharge path. The cryogenic slurry comprises a solid and a cryogenic liquid. The cryogenic slurry is fed into the cryogenic slurry flow path, generally tangential to the filter medium. This causes a portion of the cryogenic liquid to cross the filter medium into the cryogenic liquid discharge path as a cryogenic liquid discharge and the cryogenic slurry to thicken to produce a thickened slurry. The filter medium comprises a cryogenically-stable material such that adsorption of gases is inhibited, deposition of solids is prevented, and temperature-change induced expansion and contraction of the filter medium is optimized.

Certain aspects of the invention relate to a composite for oil-water separation, synthesis methods and applications of the same. The composite includes a nanostructured powder or porous material having surfaces with nanoscale features, formed from a pristine powder or porous material by a surface nanostructuring process, and single or multilayers of a low surface energy oligomer or polymer coated on the surfaces of the nanostructured powder or porous material. The composite is hydrophobic (or superhydrophobic) and oleophilic (or superoleophilic) operably repelling water and absorbing oil, or oleophobic (or superoleophobic) and hydrophilic (or superhydrophilic) operably repelling oil and absorbing water.

A process is provided for separating an ionic liquid from a liquid hydrocarbon, using an integrated coalescing system. The integrated coalescing system for separating ionic liquid from a liquid hydrocarbon may comprise: a. a bulk settler, that separates an emulsion comprising the dispersed ionic liquid with a wide range of droplet sizes into a clean ionic liquid phase and a separated liquid hydrocarbon phase comprising retained droplets; b. a pre-coalescer that receives the separated liquid hydrocarbon phase, separates out solid particles from the separated liquid hydrocarbon phase, and begins to form coalesced droplets of the retained droplets; and c. a coalescer that receives an effluent from the pre-coalescer, wherein the at least one coalescer comprises multiple layers of media having a fine pore size, and produces a clean hydrocarbon stream that is essentially free of the dispersed ionic liquid and additional amounts of the clean ionic liquid phase.

The invention relates to a separation system for simultaneous removal of a solid phase particles and a dispersed phase droplets from a medium being a continuous phase to be purified by filtration, wherein said separation system comprises: a filtration-coalescing element (1) in a form of a fibrous structure, a separating element (2), which is a barrier layer for droplets of said dispersed phase and a drainage gap (3), disposed there between and separating said elements (1) and (2) from each other. Said filtration-coalescing element (1) is a non-woven fibrous structure in the form of a depth non-woven structure composed of fibers packed in a form of a cartridge and it comprises: a filtration layer (1a) being an initial depth filtration layer comprising polymer fibres of nanometric sizes, wherein said fibres composing the layer (1a) have extensively phobic surface properties and having across its thickness a porosity gradient, a coalescing layer (1b) and adjacently following it a dripping layer (1c), both composed of polymer fibres and jointly forming a coalescing structure (1b, c) packaged in the form of a depth gradient structure of fibres, and wherein a porosity gradient across the entire coalescing structure (1b, c) changes in the opposed direction with respect to said porosity gradient in said filtration layer (1a).