Abstract: A connectable element comprising a center piece and a connecting piece. The center piece includes a connecting portion and at least one encircling groove The connecting piece includes an end portion and an eye in a portion. The end portion of the connecting piece is attached to the connecting portion of the center piece. The eye complementarily fits the encircling groove of an adjacent center piece.

Abstract: A printed material with a sticker integrally includes a sticker and a mounting paper to be attached with the removed sticker. The printed material includes a sheet body that is applied with printing of at least the sticker and the mounting paper, a sticker region that is formed by folding at least a part of the sheet body, and a mounting paper region that is formed in a region other than the sticker region. In the printed material, at least one of the sticker formed in the sticker region is a standing sticker including a standing fold that extends in a transverse direction of the sheet body, and an adhesive part and a non-adhesive part that are formed on a back surface of the sticker to face each other across the standing fold.

Abstract: A multi-effects desalination system includes a plurality of vessels, including a first vessel, a second vessel, a third vessel, a fourth vessel, and a fifth vessel. Each vessel includes a plurality of heat tubes, a sprayer, and a housing including a preheater tube bundle. Each sprayer can be disposed above a respective plurality of heat tubes in each vessel for discharging saline water onto the plurality of heat tubes. A first tube connects a compressor unit with the first vessel. A second tube extends between a saline water source and a plurality of sprayers. Each vessel is configured to accommodate a different effect or stage of desalination occurring in the system. The housing can be configured for collecting fresh water. The fresh water collected in each housing can be transferred by the third tube to a fresh water tank.

Abstract: A downcomer apparatus for use in a multi-stage bubble column humidifier. The humidifier comprises at least a first, second and third stage, wherein each of said stages includes an inlet, an outlet and a chamber defined by said stage, in fluid communication with the inlet and the outlet. In the humidifier, a heated liquid fluid stream flowing downwardly exchanges mass and heat with a cooler carrier gas stream flowing upwardly through the bubble column. A bubble generator comprising a perforated plate, or sparger, passes the carrier gas, such as air, from a lower chamber to form bubbles in a fluid, such as water, forming a bath on an upper chamber. An off-set arrangement of downcomer apparatuses, wherein said apparatus comprises a funnel, a watergate, and a downcomer, is used to prevent a recirculation of humid bubbles from the upper chamber to the lower chamber, thus preventing the air stream from circumventing the bubble generator in the form of the humid bubbles.

Abstract: Disclosed is a process for simultaneous production of benzene lean gasoline and recovery of high purity aromatics from narrow boiling light cracked gasoline fractions. The present invention provides a vacuum based two stage extractive distillation process, with pure NMP, for production of benzene lean gasoline (benzene content less than 0.4 Weight %) by recovery of high purity aromatics (purity more than 99 Weight %) from cracked gasoline fractions (boiling in the range of 40-90° C.) comprising benzene in the range of 10-30 weight % and close-boiling non-aromatic hydrocarbons like paraffins, iso-paraffins, olefins, di-olefins (including conjugated di-olefins), and naphthenes in the range of 70-90 weight % along with impurities containing but not limited to oxygenates, metals, chlorides, sulphur compounds, nitrogen compounds and organic peroxides.

Abstract: A liquid separator and concentrator is disclosed. An example liquid separator and concentrator includes a separator column. A spray chamber has a sprayer nozzle to spray an influent within the spray chamber and create a falling film in the separator column. A heating jacket surrounds the separator column, wherein the heating jacket heats the falling film to evaporate at least one portion of the falling film and leaves a concentrate. A concentrate collection vessel receives the concentrate from the separator column.

Abstract: A moving section that moves in the horizontal plane direction at above a collection container section where collection containers are set is provided with a nozzle holding section for holding a nozzle, and a waste port holding section for holding a waste port. The moving section is capable of moving the nozzle holding section or the waste port holding section. Accordingly, one of a state where the waste port is at a position immediately below the tip of the nozzle and a state where the waste port is not at the position immediately below the tip of the nozzle may be achieved.

Abstract: Adjustable weir apparatus (101) with a wellhead separator system (6) fed by petrochemical source (1) with oil box (24) and water box (23) along with outlets for oil (25) and water (18). An adjustment assembly (12) may pass through a stuffing box (7), into a wellhead separator system (6), by way of a linkage assembly (13) connecting the adjustment assembly (12) to the adjustable weir assembly (5). The adjustable weir assembly (FIG. 5) may include an o-ring (34), a tube pin (15), an adjustable tube (22), and a nipple adapter (35) to allow adjustment while still maintaining an environment sufficiently proof against leakage.

Abstract: A deoxygenation apparatus reduces the concentration of dissolved oxygen in a target liquid. The deoxygenation apparatus includes a reservoir for holding the target liquid, a gas supply part for supplying an additive gas different from oxygen into the target liquid in the reservoir, a storage part for storing correlation information indicating the relationship between the concentration of dissolved oxygen in the target liquid and a total supply amount that is a total amount of the additive gas supplied from the gas supply part into the target liquid from when supply was started, and a calculation part for obtaining the concentration of dissolved oxygen in the target liquid on the basis of the total supply amount and the correlation information. The concentration of dissolved oxygen in the target liquid is easily acquired without measuring the concentration of dissolved oxygen in the target liquid with an oxygen analyzer.

Abstract: A cyclonic separator is provided, comprising at least one cyclonic chamber in the form of a cylindrical tube, having an upper inlet end and a lower liquid outlet end, at least one involute chamber located adjacent to and in fluid communication with the upper end of each of the at least one cyclonic chambers. The involute chamber comprises an involute inlet and a gas outlet proximal an upper end of the involute chamber. An inlet manifold is in fluid communication with said at least one involute chamber via the involute inlet. Said involute inlet of said involute chamber is laterally separated from said gas outlet. A method is further provided for separation of a mixed heavy phase/light phase process stream.

Abstract: The invention relates to a process additive formulation and a method for foam reduction and/or for increasing drainage in a process comprising an aqueous medium. The process additive formulation comprises an acrylate and/or methacrylate copolymer, optionally with acrylic acid or methacrylic acid, in an organic diluent, and mineral oil or vegetable oil.

Abstract: An apparatus and method for treatment of food process waste water, comprising a tank for receiving a food process waste water influent via an influent pump and discharging a treated food process waste water effluent via an effluent pump; a floating decanter disposed in the tank; a valved outlet formed in the bottom of the tank; an upper level float switch operationally connected to the floating decanter; a lower level float switch operationally connected to the floating decanter and to the effluent pump; and a timer operationally connected to the floating decanter and the effluent pump. Solids are settled from the waste water and drawn off through the tank bottom after a supernatant fluid is drawn off through the floating decanter. The supernatant fluid is passed through a filtration and membrane water purification apparatus to generate purified water.

Abstract: An apparatus and method for treatment of food process waste water, comprising a tank for receiving a food process waste water influent via an influent pump and discharging a treated food process waste water effluent via an effluent pump; a screen decanter disposed in the tank;, the screen having a porosity of about 50 micrometers; and a timer operationally connected to the floating decanter and the effluent pump. Solids are settled from the waste water and drawn off through the tank bottom after a supernatant fluid is drawn off through the floating decanter. The supernatant fluid is passed through a filtration and membrane water purification apparatus to generate purified water.

Abstract: An apparatus and method for treatment of food process waste water, comprising a tank for receiving a food process waste water influent via an influent pump and discharging a treated food process waste water effluent via an effluent pump; a screen decanter disposed in the tank; the screen having a porosity of about 50 micrometers; and a timer operationally connected to the floating decanter and the effluent pump. Solids are settled from the waste water and drawn off through the tank bottom after a supernatant fluid is drawn off through the floating decanter. The supernatant fluid is passed through a filtration and membrane water purification apparatus to generate purified water.

Abstract: A filter cartridge includes a cylindrical filter media including an axial channel; and first and second end caps releasably secured to first and second end portions of the filter media respectively, each of the first and second end caps including an annular wall, a hollow cylinder, a filter netting disposed on an inner end of the hollow cylinder, and a plurality of equally spaced projections on an outer surface of the hollow cylinder. The first end portion of the filter media is fastened between the annular wall and the hollow cylinder of the first end cap and the second end portion of thereof is fastened between the annular wall and the hollow cylinder of the second end cap. There are further provided concentric bottom ridges between the hollow cylinder and the annular wall.

Abstract: A filter element has a pleated composite and first and second end elements mounted to opposite first and second ends of the filter element. The pleated composite has a filter medium layer and a grooved mesh drainage layer pleated with the filter medium layer. The grooved mesh drainage layer has a plurality of strands and a plurality of grooves formed in the strands. The grooved mesh drainage layer directs fluid via the grooves to or from the filter medium layer and the filter medium layer removes one or more substances from fluid flowing through the filter medium layer.

Abstract: The invention relates to a filter device for polymer melts, having a filter screen (1), through which the polymer melt to be purified is guided, wherein the filter device comprises at least one scraping element (2), which glides across the upstream surface (4) of the filter screen (1) with its scraping edge (3), or rests on the surface (4) with its end area nearest the scraping edge (3), and lifts off and/or scrapes off the contaminations (6) adhering to the surface (4) and those present in front of the screen orifices (5) in the course of its movement across the surface (4). According to the invention it is provided that the scraping edge (3) has a curvature (7) at least in the end area of the same, leading in the direction of movement (16), the radius (R) of which is less than 90%, preferably less than 50%, in particular less than 20% of the maximum diameter, or of the maximum orifice width of the screen orifices (5).

Abstract: The present invention relates to a removal apparatus for green algae capable of persistently removing the green algae floating in water and which is easy to manufacture and manage because of its simple structure. The removal apparatus for green algae comprises a screen unit that pulls the green algae out of the water by rotation as a part thereof is submerged into the water; a first cleaning unit that sprays air in the direction from the inside of the screen unit to the outside; a second cleaning unit that sprays air from the outside of the screen unit to the inside; a first collecting unit positioned outside of the screen unit and in which the green algae removed by the first cleaning unit is stacked; and a second collecting unit positioned inside of the screen unit and in which the green algae removed by the second cleaning unit is stacked.

Abstract: A fluid pump includes a pump housing; an inlet which introduces fluid into the pump housing; an outlet which discharges the fluid from the pump housing; a pump section which pumps the fluid from the inlet to the outlet; and a strainer through which the fluid passes in order to enter the inlet. The fluid pump extends along an axis and the strainer includes a straining medium configured to allow the fluid to pass therethrough while preventing foreign matter of a predetermined size from passing therethrough. The straining medium defines a strained volume with the pump housing such that the strained volume is defined radially between the straining medium and the pump housing and such that the strained volume is in fluid communication with the inlet.

Abstract: A fuel filter comprises a filter housing having a fuel inlet and a fuel outlet, and a laminate positioned within said filter housing, the laminate comprising a first layer and a second layer having methyl hydroxyethyl cellulose between said first layer and said second layer, wherein the fuel filter is configured to direct fuel received at the fuel inlet to the fuel outlet through the laminate.

Abstract: An endcap bypass plug includes a body and a plurality of leg members. The body includes an upper surface, a lower surface, and an outer side surface joining the upper and lower surfaces. The plurality of leg members are connected to and extend away from the upper surface of the body. Adjacent leg members of the plurality of leg members are spaced apart by a distance to form a plurality of radial passages defining a plurality of radial fluid-flow paths. Each leg member includes a head portion having an upper surface. The head portion includes a nose portion extending radially outwardly from the head portion and including a ramp surface and a lower surface. The ramp surface of the nose portion is connected to the upper surface to define an upper edge. The ramp surface is connected to the lower surface of the nose portion to define a lower edge.

Abstract: A method, an apparatus and a system connects a high-capacity filtration screen to a regular-capacity filtration screen through an adapter. The adapter is positioned adjacent to the high-capacity filtration screen. Barbs protrude from the high-capacity filtration screen to interlock with the adapter. Barbs extend from the adapter and insert into corresponding orifices in the regular-capacity filtration screen. The filtration screens and adapter are installed in a separator. A tapered edge of the adapter is aligned with the filtration screens. A cross-member extends from a first side to a second side of the adapter. A support beam is positioned lengthwise along an underside of the adapter.

Abstract: A treatment solution supply method includes: a degassed treatment solution generating step of degassing a treatment solution by a degassing mechanism to generate a degassed treatment solution; a treatment solution storing step of storing the degassed treatment solution in a container; a filter solution-passing step of bringing a downstream side from a filter connected to a downstream side from the container via a treatment solution supply pipe to a negative pressure with respect to a pressure in the container to pass the treatment solution in the container through the filter; and a negative pressure maintaining step of maintaining a state in which the downstream side from the filter is brought to the negative pressure, for a predetermined period, after stopping supply of the treatment solution from the container to the filter.

Abstract: A filter medium (10) has a first layer of media (12), a second layer of media (18), and at least one third layer of media (20). The second layer of media (18) is arranged behind the first layer of media (12) in the intended flow direction (16) of the filter medium, and the third layer of media (20) is arranged behind the second layer of media (18) in the intended flow direction (16) of the filter medium. The first layer of media (12) has fibers, and the second layer of media (18) has nanofibers. Also disclosed is a filter element (50) which has such a filter medium (10) and the use of such a filter medium (50) as a fuel filter.

Abstract: To provide a fibrous laminate having excellent secondary processability in processing into a filter or the like by laminating a fibrous layer composed of ultrafine fibers with another fibrous layer and strongly adhering and uniting each interlayer while reduction of characteristics of the ultrafine fibers is suppressed at a minimum to compensate insufficiency of mechanical strength and rigidity of a layer of ultrafine fibers. The fibrous laminate includes fibrous layer I composed of ultrafine fibers having a mean fiber diameter of 10 to 1,000 nm and fibrous layer II composed of thermo-fusible conjugate fibers having a mean fiber diameter of 5 to 100 ?m, in which contact points between the ultrafine fibers and the thermo-fusible conjugate fibers are bonded by melting of the thermo-fusible conjugate fibers composing the fibrous layer II, and the fibrous layer I and the fibrous layer II are laminated and united by the formed bonding points.

Abstract: A gas purifier is disclosed for removing solid and liquid particles and to control humidity and volatile concentration in a gas stream. The device comprises of a plurality of vane-baffle elements. Each element comprising of a planar vane having a L-shaped cross section and a tubular baffle having a G-shaped cross section, wherein the baffle is attached to the vane forming a vane-baffle element. Each tubular baffle is annular allowing a secondary fluid to flow through it. A plurality of zig-zag shaped baffled partitioned are formed by attaching a plurality of vane-baffle elements to each other. A plurality of gas-stream passage ways are formed by vertically aligning said plurality of zig-zag partitions at a predefined partition spacing.

Abstract: In order to provide a filter system for separating off contaminants from a stream of untreated gas that contains contaminants that is of simple construction and is operable efficiently, it is proposed that the filter system should include the following: a base construction through which the stream of untreated gas is guidable and which includes at least one filter module receptacle for receiving at least one filter module, and at least one filter module which is selectively arrangeable on and/or in the at least one filter module receptacle and/or removable therefrom, wherein the at least one filter module includes a plurality of filter element receptacles for receiving a plurality of mutually independent filter elements.

Abstract: Embodiments of the present disclosure improve the accuracy of abnormality diagnosis of a particulate filter using the output value of a PM sensor provided downstream of the particulate filter in an exhaust passage. A configuration of the invention compares a change rate of an output value of the PM sensor prior to execution of a filter diagnosis process of diagnosing an abnormality of the filter based on the output value of the PM sensor, with a reference value and determines whether a filter abnormality process is to be performed. A higher value is set to the reference value, which is to be compared with the change rate of the output value of the PM sensor, in the case where the deposition amount of PM between electrodes of the PM sensor is expected to be large, compared with the case where the deposition amount of PM is expected to be small.

Abstract: Embodiments of the present disclosure may improve the accuracy of abnormality diagnosis of a particulate filter using the output value of a particulate matter (PM) sensor provided in an exhaust passage. A time when deposition of PM between electrodes of the PM sensor is restarted after completion of a sensor recovery process may be specified as a PM deposition restart time. A process of diagnosing an abnormality of a filter based on the output value of the PM sensor at a first determination time after the PM deposition restart time may be specified as a filter diagnosis process. To determine, whether the filter diagnosis process is to be performed, a change rate of the output value of the PM sensor in a time period from the PM deposition restart time to a predetermined second determination time before the first determination time, may be compared with a threshold value.

Abstract: An air cleaner assembly and components therefor are provided. Features are described providing for installation of a preferred filter cartridge in a housing. A filter cartridge arrangement is described and shown. Methods of assembly and use are also described.

Abstract: An air purification system for purifying polluted air includes a scrubber in which a pollutant in the polluted air is transferred to a scrubber liquid. A biological treatment unit includes at least one substantially flat substrate to support a microorganism population to remove the transferred pollutant from the scrubber liquid when the scrubber liquid with the transferred pollutant is distributed on the substrate. A plane of the substrate is substantially parallel to a direction of flow of the air from the scrubber.

Abstract: Porous aromatic framework polymers functionalized with Brønsted acid moieites are prepared by polymerization of a three-dimensional organic aryl or heteroaryl monomer and its copolymerization with a second aryl or heteroaryl monomer functionalized with one or more Brønsted acid moiety. The polymers are characterized by a stable three-dimensional structure, which, in exemplary embodiments, includes interpenetrating subunits within one or more domain of the bulk polymer structure. The polymers are of use in methods of adsorbing ammonia and amines and in devices and systems configured for this purpose.

Abstract: An End Cap for an Assembly Used in the Preparation of Compressed Gas An end cap for attaching to one or more filter elements and respective filter bowls is disclosed. The end cap has a tubular body formed by extrusion and this body has a series of apertures formed therein. The apertures include an end aperture for attachment to a filter bowl and another end aperture for attachment to another filter bowl or to a sealing disc. The body also has a pair of sidewall apertures to act as inlet and outlet the filter assembly. The end cap also has a plastic insert for insertion into the body, the insert having a conduit portion for directing a stream of gas from the inlet to a filter element through one of the end apertures.

Abstract: Methods, systems, and devices for an automotive vehicle air cleaning system are provided which may be configured to operate in at least an adsorption mode and an in-situ regeneration mode are disclosed. The system includes at least one type of sorbent material configured to remove CO2 from a cabin of an automotive vehicle according to a repeated adsorption-desorption swing cycle, a first inlet configured to supply a first airflow of air from the cabin to the system during an adsorption mode, and a first outlet configured to return the first airflow after passing over and/or through the sorbent material during the adsorption mode. The system includes a second inlet configured to supply a second airflow of outside air to the system during a regeneration mode, a second outlet to return the second airflow after passing over and/or through the sorbent material during the regeneration mode.

Abstract: A method for regenerating sulfur rich carbenium pseudo ionic liquid is described. The method includes contacting the sulfur rich carbenium pseudo ionic liquid containing at least one sulfur compound with at least one silane compound in a regeneration zone under regeneration conditions. The carbenium pseudo ionic liquid comprises an organohalide and a metal halide. The silane compound reacts to form a silyl compound, resulting in a carbenium pseudo ionic liquid phase and an organic phase containing the sulfur and the silyl compound.

Abstract: The present invention relates to scrubbers, particularly though not exclusively to scrubbers for treating hydrogen sulfide and mercaptan containing air streams and to scrubber media for use therein. There are provided scrubber media comprising a polycarboxylic acid composition. Also provided are methods of treating a scrubber media by addition of a polycarboxylic acid composition as well as scrubber apparatus containing a scrubber media comprising a polycarboxylic acid composition. Also provided are methods of treating a gas stream by introducing a gas stream into a scrubber media which comprises a polycarboxylic acid composition and a polycarboxylic acid composition for use to extend the operating life of a scrubber media.

Abstract: A method of treating oil and gas streams to remove total organic sulfur or total acid gas including the step of treating the gas stream with a solution of an amine, physical solvent, and water wherein the amine solution may optionally also contain an activator.

Abstract: A gas separation system includes: first, second, and third gas separation membrane units. A first retentate gas line connects a retentate gas discharge port of the first unit and gas inlet port of the second unit. A first permeate gas line connects a permeate gas discharge port of the first unit and gas inlet port of the third unit. A feed gas mixture supply line is connected to a gas inlet port of the first unit, and provided with first compression elements. The first permeate gas line is provided with second compression elements. The permeate gas discharge port of the second unit is connected by a second permeate gas line to the suction side of the first compression elements in the feed gas mixture supply line. A retentate gas discharge port of the third unit is connected by a third retentate gas line to the first retentate gas line.

Abstract: A multi-tower blower purge dryer system for use with a compressed air stream provided from a compressor is disclosed. In one form the system includes two dryers that can be alternated to dry the compressed air stream. The tower used to dry the compressed air stream can be referred to as the drying tower, and the tower being regenerated can be referred to as the regenerated tower. A number of valves and passages are used to connect the towers to one another and/or to an intake passage from the compressor. A blower purge heater is provided to regenerate the dryers. After a regeneration step in which a tower may be relatively warm, the valves can be actuated to place the warm regenerated tower in fluid communication with the intake passage from the compressor, which can then provide air to the drying tower. In this manner the regenerated tower is cooled.

Abstract: Provided are a reclaimer that introduces a part of an absorbent that has absorbed CO2 or H2S in a flue gas through an introduction line and stores the absorbent, a heating section that heats the absorbent stored in the reclaimer to obtain recovered vapor, and a mixing tank disposed on the introduction line through which the absorbent is introduced into the reclaimer, and which introduces an absorbent (lean solution) and an alkaline agent for mixing thereof.

Abstract: A system and method is disclosed for recovering reagents that are used in removing contaminants from a flue gas stream. The system and method includes contacting the flue gas stream with reagents such as ammonia and sulfuric acid to create an ammonium sulfate stream. The ammoniated sulfate stream is forwarded to an electrodialysis unit wherein the reagents are regenerated and recirculated back to the system.

Abstract: Disclosed herein are methods for C2 capture that use phase change ionic liquids (PCILs) to remove the C02 from flue gas or other gas streams containing C02. PCILs have high C02 uptake and form a liquid PCIL- C02 complex when they react with C( )2. When the liquid PCIL- C02 complex is heated to regenerate the solid PCIL material by removing the carbon dioxide, part of the heat needed to release the C02 can be supplied by the heat of fusion of the PCIL as it solidifies. Utilization of the heat of fusion of the PCIL to assist in its own regeneration can substantially reduce the parasitic energy loss associated with post-combustion C02 capture.

Abstract: The exhaust gas-purifying catalyst of the invention includes a noble metal, and crystallites that form CZ composite metal particles which serve as a carrier supporting the noble metal and contain at least zirconium (Zr) and cerium (Ce). The CZ composite oxide particles (crystallites) further contain crystal growth-suppressing fine particles which are fine metal particles comprising primarily a metallic element M that melts at 1,500° C. or above and which suppress crystal growth by the CZ composite oxide particles. The content of the metallic element M included in the CZ composite oxide particles, expressed in terms of the oxide thereof, is 0.5 mol % or less of the total oxide.

Abstract: A draw solute including an ionic oligomer having a repeating unit that includes at least two phosphonate moieties and counter ions thereof, and a forward osmosis device and method for water treatment using the draw solute and an aqueous solvent, are disclosed.

Abstract: A connecting system (1) has at least one connector (2) for a filter cassette (4) that can be inserted into a filter holder and has filter layers (5) between two end plates (6), and seals (7) between the filter layers (5) and/or between the end plates (6) and an adjacent filter layer (5). The connector has tensioning parts that engage in one another in a longitudinally displaceable manner and that can be fixed to the end plates (6) via their ends facing away from one another. The connector exerts a pretensioning force onto the end plates (6) when it is deflected to its maximum extent. The pretensioning force pulls the end plates (6) towards the filter layers (5), and when a contact-pressure force superimposed on the pretensioning force is applied to the end plates (6), the tensioning parts can be pushed towards one another correspondingly with the end plates (6).

Abstract: A membrane separation apparatus includes: a shell, wherein an inner surface of the shell is an arc surface, and at least one medium inlet and at least one medium outlet used for discharging a medium that is separated are arranged on the shell; a rotor arranged inside the shell, wherein at least two contact ends that are always in slidably contact with the inner surface of the shell are arranged on an outer surface of the rotor, the outer surface of the rotor and the inner surface of the shell form sealed separate cavities between the adjacent contact ends, and an empty part inside the rotor is used as a medium storage chamber; and separation chambers arranged inside the rotor.

Abstract: The present invention is directed to polymer compositions comprising a bulk material (P1) and an amphiphilic polyethersulfone block copolymer (P2) and to membranes prepared thereof. Furthermore, the present invention is directed to the use of amphiphilic polyethersulfone block copolymers as antifouling agents and/or pore size control agents in filtration membranes.

Abstract: The present invention provides nanofiltration membranes with reduced chemical reactivity that can be utilized in manufacturing processes where reactive feedstocks and/or products are utilized or produced. Methods of making and using the membranes are also provided.

Abstract: The present disclosure provides a multi-channel hollow fiber including a tubular matrix having a first end and a second end, and a plurality of channels formed through the tubular matrix and extending between the first end and the second end. The multi-channel hollow fiber of the present disclosure provides enhanced adsorption or separation efficiency for gas and liquid. Meanwhile, the content of an adsorption material in the multi-channel hollow fiber can be increased to 95 wt %, and the multi-channel hollow fiber has good mechanical strength.

Abstract: Disclosed are copolymers which are useful in hydrophilically modifying porous fluoropolymer supports. An example of the copolymers is: Also disclosed are a method of preparing such copolymers, a method of modifying porous fluoropolymer surfaces, and hydrophilic fluoropolymer porous membranes prepared therefrom. Also disclosed is a method of filtering fluids by the use of the hydrophilic fluoropolymer porous membranes.