Class / Patent application number | Description | Number of patent applications / Date published |
096007000 | Plural separate barriers | 65 |
20100307341 | Water trap - A water trap ( | 12-09-2010 |
20120174790 | WATER-VAPOR-PERMEABLE MEMBRANE, HOLLOW-FIBER MEMBRANE, AND HOLLOW-FIBER MEMBRANE MODULE - A water vapor permeable membrane is provided comprising a dense layer and a support layer that are adjacent to each other, wherein the dense layer contains voids with a void length of 0.1 μm or less and the dense layer has a thickness of 0.1 μm or more and 2 μm or less while in the support layer, void (a), i.e. the void with the largest length in the 2 μm thick region measured from the boundary between the dense layer and the support layer into the support layer, has a length of 0.3 μm or more and void (b), i.e. the void with the largest length in the region ranging between 2 μm and 4 μm measured from the boundary into the support layer, has a length of 0.5 μm or more, the length of the void (b) being larger than that of the void (a). A water vapor permeable membrane having both a high water vapor permeability and a low air leakage is provided. | 07-12-2012 |
20130239812 | HYDROGEN PURIFIER - Techniques are generally described herein for the design and manufacture of hydrogen generation apparatuses and systems. Other embodiments may also be disclosed and claimed. Some methods described herein pressing together a first end plate, one or more intermediate plates, and a second end plate using a press to form a hydrogen purifier module, and placing a plurality of clips around the hydrogen purifier module to hold the first end plate, the one or more intermediate plates, and the second end plate together. | 09-19-2013 |
20130319242 | VENTILATION SCREEN - A ventilation screen for protecting against rain water and other elements includes a plurality of air passages. The air passages enable air flow from one side of the screen to the other but preferably without linear communication between both sides through the air passages. The air passages present an upwardly traveling trajectory from the exposed space to the protected space, preferably with lateral changes of direction as well. Therefore rain water that comes directly from precipitation or splashing from an adjacent surface cannot reach a protected space. The geometry of the air passages provides protection against other environmental or man made elements. | 12-05-2013 |
20140013951 | Thermal Conditioning for Air Separation Modules - Thermal conditioning for an area surrounding one or more air separation canisters includes directing the exhaust gas of the thermal conditioning unit to the area surrounding the canisters. The area may be defined by a housing in which the canisters are positioned. | 01-16-2014 |
20140150656 | METHODS AND SYSTEMS FOR TURBULENT, CORROSION RESISTANT HEAT EXCHANGERS - Disclosed are various turbulent, corrosion-resistant heat exchangers used in desiccant air conditioning systems. | 06-05-2014 |
20140150657 | METHODS AND SYSTEMS FOR TURBULENT, CORROSION RESISTANT HEAT EXCHANGERS - Disclosed are various turbulent, corrosion-resistant heat exchangers used in desiccant air conditioning systems. | 06-05-2014 |
20140165836 | AIR SEPARATION MODULE MANIFOLD FLOW STRUCTURE AND SYSTEM - An air separation module has an inlet for receiving a source of air. The inlet communicates with an inlet manifold and the inlet manifold communicates with a plurality of canisters. The canisters are provided with hollow fibers constructed such that oxygen can permeate the fiber and nitrogen passes through the fiber. A jacket manifold surrounds the canisters and the jacket manifold receives oxygen that has permeated the fibers. The canisters extend to a downstream end, and to an outlet. The jacket manifold communicates with a jacket outlet manifold and an outlet for separated oxygen. The outlet for the jacket manifold is at a downstream end of the canisters. | 06-19-2014 |
20140283690 | MEMBRANE CONTACTOR FOR DEHUMIDIFICATION SYSTEMS - A contactor configured for use in a dehumidification system is provided including a plurality of contact modules. Each contact module has a porous membrane that defines an internal space through which a hygroscopic material flows. A membrane property of the porous membrane of at least one contact module is substantially different than the other membranes of the plurality of contact modules. | 09-25-2014 |
20140298993 | HYDROGEN SEPARATION MEMBRANE MODULE WHICH HAVE MIXING PART - Provided is a hydrogen separation membrane module, and more particularly, a hydrogen separation membrane module having a mixing part capable of increasing hydrogen purification efficiency by maximizing a mixing effect and a dispersion effect of a mixture gas supplied to the hydrogen separation membrane using the mixing part provided with a microchannel to supply the mixture gas to the hydrogen separation membrane. | 10-09-2014 |
20150059577 | Membrane Separation Assembly for Fuel Gas Conditioning - A membrane separation assembly that includes an integrated filter element and at least one membrane module housed within a first vessel and a second vessel containing at least one membrane module, which is stacked or aligned adjacent to the first vessel. The first vessel is configured to allow liquids to be trapped and removed from the assembly, and gases to flow to and through the membrane modules of the first vessel and the membrane modules of the second vessel, which are ultimately withdrawn from the assembly. The assembly is useful in the conditioning of fuel gas to separate methane from C | 03-05-2015 |
20150096443 | NONWOVEN FELT WITH HOLLOW COMMODITY POLYMER FIBERS FOR AIR FILTRATION - An air filter assembly includes a felt of hollow commodity polymer fibers having nonporous walls. | 04-09-2015 |
20150096444 | NONWOVEN FELT WITH HOLLOW SPECIALTY POLYMER FIBERS FOR AIR FILTRATION - An air filter assembly includes a felt of hollow specialty polymer fibers having nonporous walls. | 04-09-2015 |
20150306529 | VENTILATION MEMBER - A ventilation member of the present invention includes: a support having a through hole serving as an air passage between an interior space and an exterior space of a housing when the support is attached to the opening of the housing; a filter member disposed on the support to cover an aperture of the through hole that opens into the interior space; and an air-permeable membrane disposed on the support to cover an aperture of the through hole that opens into the exterior space. The through hole includes: a first air passage extending in a predetermined direction from one end of the first air passage to the other end of the first air passage, the one end forming the aperture that opens into the interior space; a second air passage having one end connected to a side of the first air passage and the other end forming the aperture that opens into the exterior space; and a dead end passage extending in the predetermined direction from the other end of the first air passage. | 10-29-2015 |
20160166980 | CONTAINER-TYPE BIOGAS PURIFICATION FILM METHOD PURIFICATION SYSTEM | 06-16-2016 |
096008000 | Parallel hollow fibers or cylinders (e.g., bundled, etc.) | 29 |
20090193974 | Cross-pleated membrane cartridges, and method and apparatus for making cross-pleated membrane cartridges - A membrane cartridge is manufactured by repeatedly folding and joining two strips of membrane to form a cross-pleated cartridge with a stack of openings or fluid passageways configured in an alternating cross-flow arrangement. The cartridge can be modified for other flow configurations including co-flow and counter-flow arrangements. Methods for manufacturing such cross-pleated membrane cartridges, as well as apparatus used in the manufacturing process are described. Cross-pleated membrane cartridges comprising water-permeable membranes can be used in a variety of applications, including in heat and water vapor exchangers. In particular they can be incorporated into energy recovery ventilators (ERVs) for exchanging heat and water vapor between air streams being directed into and out of buildings. | 08-06-2009 |
20100024649 | AIR SEPARATION MODULE WITH LOAD CARRYING CENTER TUBE - An air separation module comprising a bundle of hollow elongated membranes, and a pressure vessel enclosing the bundle. The pressure vessel includes an outer tube, end caps at opposite ends of the tube, and an inner tube located within the fiber bundle. The inner tube is fixedly mechanically connected at opposite ends to the end caps to form a structural spine of the pressure vessel, whereby loads acting on the air separation module are transferred between the end caps primarily by the center tube. | 02-04-2010 |
20100050875 | Gas exchange membrane in particular for use in an artificial lung and method for the production of a gas exchange membrane of this type - A gas exchange membrane is for use in an artificial lung. The membrane consists of a foamed, closed-cell material, in particular of silicone rubber. The membrane is produced by extruding a basic material which contains a foaming agent. The extrudate is then foamed. The result is a gas exchange membrane which has an increased gas exchange performance compared to known material due to the high permeability of the surface. | 03-04-2010 |
20100107880 | HOLLOW FIBER MEMBRANE DEHUMIDIFIER - A hollow fiber membrane dehumidifier includes: a dehumidification container composed of a lower trunk provided with an exhaust gas inlet section, an upper trunk provided with an exhaust gas outlet, and a body trunk; a lower tube plate for constructing an exhaust gas inlet chamber in the body trunk; an upper tube plate for constructing an exhaust gas outlet chamber in the body trunk; a partition plate for partitioning the interior of the body trunk to an exhaust gas processing chamber and a purge gas chamber; a plurality of hollow fiber membrane modules inserted into each through hole of an upper tube plate, the partition plate and the lower tube plate; and a sealing material held in sealing groove formed in the hollow fiber membrane module for sealing among an upper head, a lower head, the upper tube plate, the partition plate and the lower tube plate. | 05-06-2010 |
20100212501 | Membrane Filter Element with Multiple Fiber Types - A natural gas stream is passed through a single membrane element that is fabricated with two or more distinct types of membrane fibers. The membrane fibers have different characteristics in order to reduce the number of membrane elements required for gas separation and to improve gas separation performance due to changing gas composition because of permeation as the gas travels through the membrane element. | 08-26-2010 |
20100212502 | AIR DRYER FOR ELECTRICAL ENCLOSURES - An air dryer having an internal orifice designed into an outlet end cap that eliminates the need for external valves or regulators to control the flow of air through the dryer. The internal orifice, which can be press-fit or threaded into the end cap, provides a consistent and stable outlet flow and dew point and eliminates the need for instruments to measure outlet flow and dew point. The orifice size can be easily changed for changing outlet flow and dew point. A protective tubular shroud is provided for shielding a membrane module of the dryer, and for routing sweep gas to a bottom vent. | 08-26-2010 |
20100263537 | HEATED BLANKET FOR AIR SEPARATION MODULE - An air separation module and blanket has an air separation module having an air inlet, an oxygen outlet and a nitrogen outlet. At least one tank has air separation elements for separating oxygen from air, and delivers the separated oxygen to the oxygen outlet, and delivers nitrogen to the nitrogen outlet. A resistance heating element is positioned between the blanket and the air separation module. Further, an inventive blanket for use with the air separation module is also disclosed and claimed. | 10-21-2010 |
20100326278 | SHELL FEED TYPE GAS SEPARATION MEMBRANE MODULE - A gas separation membrane module has a vessel housing a hollow fiber element including a hollow fiber bundle consisting of a number of hollow fiber membranes ( | 12-30-2010 |
20110146491 | SEPARATION MEMBRANE MODULE AND FUEL VAPOR PROCESSING APPARATUS EQUIPPED WITH THE SAME - A separation membrane module for separating a specific component from a mixture containing a plurality of components includes a plurality of separation stages each including a plurality of hollow fiber membranes arranged in parallel to each other. The separation stages are connected in series via connection portions allowing passage of the mixture. At lease one parameter relating to separation by the hollow fiber membrane or membranes in each separation stage is determined to provide effective separation throughout the separation stages. | 06-23-2011 |
20110303091 | SWEEP AIR SYSTEM FOR MEMBRANE AIR DRYER - A membrane dryer includes a shell having an inner tube and an outer tube and a bundle of hollow fibers supported in the shell. A dryer air inlet into the hollow fibers and a sweep air outlet from the inner tube are at a first end of the shell. A dryer air outlet into the hollow fibers and a sweep air inlet from the inner tube are at a second end of the shell. The inner tube has a first set of circumferential openings into the sweep air space adjacent the first end of the shell and a second set of circumferential openings into the sweep air space adjacent the first end of the shell; and a second plug is in the inner tube between the first and second set of openings. | 12-15-2011 |
20120255443 | OXYGEN SEPARATION MODULE AND APPARATUS - A module and an apparatus incorporating such module utilizing a plurality of tubular membrane elements, each configured to separate oxygen from an oxygen containing feed stream when an electric potential difference is applied to induce oxygen ion transport in an electrolyte thereof. The tubular membrane elements can be arranged in a bundle that is held in place by end insulating members. The insulating members can be positioned within opposed openings of end walls of a heated enclosure and can incorporate bores to allow an oxygen containing feed stream to flow past exposed ends of the tubular membrane elements for cooling the end seals of such elements. Further, first and second manifolds can be provided in a module in accordance with the present invention to collect separated oxygen from two separate portions of the tubular membrane elements. | 10-11-2012 |
20120272826 | ZEOLITE MEMBRANE AND PROCESS FOR PRODUCING ZEOLITE MEMBRANE - There are provided a process for producing a zeolite membrane which, even when large, has few defects and which has higher separation performance than conventional zeolite membranes, and a zeolite membrane obtained by the process. In the process, the structure-directing agent is removed in the atmosphere having an O | 11-01-2012 |
20120304862 | FLAT PANEL CONTACTORS AND METHODS - Porous membrane contactors and/or their methods of manufacture and/or use are provided. In at least selected embodiments, the present invention is directed to flat panel hollow fiber or flat sheet membrane contactors and/or their methods of manufacture and/or use. In at least certain particular embodiments, the present invention is directed to hollow fiber array flat panel contactors, contactor systems, and/or their methods of manufacture and/or use. In at least particular possibly preferred embodiments, the contactor is adapted for placement in an air duct (such as an HVAC ductwork) and has a rectangular frame or housing enclosing at least one wound hollow fiber array or membrane bundle. | 12-06-2012 |
20130042762 | GAS FILTER WITH CHAMBER COMPRISING CARBON NANOTUBES FOR FILTERING CO2 - A gas filter comprises a housing ( | 02-21-2013 |
20130220127 | OXYGEN SEPARATION MODULE AND APPARATUS - A module and an apparatus incorporating such module utilizing a plurality of tubular membrane elements, each configured to separate oxygen from an oxygen containing feed stream when an electric potential difference is applied to induce oxygen ion transport in an electrolyte thereof. The tubular membrane elements can be arranged in a bundle that is held in place by end insulating members. The insulating members can be positioned within opposed openings of end walls of a heated enclosure and can incorporate bores to allow an oxygen containing feed stream to flow past exposed ends of the tubular membrane elements for cooling the end seals of such elements. Further, first and second manifolds can be provided in a module in accordance with the present invention to collect separated oxygen from two separate portions of the tubular membrane elements. | 08-29-2013 |
20140047982 | GAS SEPARATION MEMBRANE MODULE AND METHOD OF REPLACING A HOLLOW FIBER ELEMENT - A gas separation membrane module, comprising: a hollow fiber element having a hollow fiber bundle consisting of a number of hollow fiber membranes and a tube sheet provided at an end of the hollow fiber bundle for binding the hollow fiber membranes; a vessel having an opening through which the hollow fiber element is inserted or removed; a lid member having a gas outlet formed therein and attached to cover the opening of the vessel; and a perforated plate having a plurality of through holes for forming gas channels formed therein, the perforated plate being mounted between the tube sheet and the lid member, the gas separation membrane module performing gas separation by supplying mixed gas to the hollow fiber membranes. | 02-20-2014 |
20140208947 | AIR SEPARATION MODULE WITH CLAM SHELL AXIAL SUPPORT - An air separation module includes a housing, a bundle of hollow fiber membranes, and a clam shell axial support assembly. The axial support assembly includes two supportive elements, each supportive element including a flow-through component. The flow-through component includes a plurality of openings through which a supply of fluid (e.g. oxygen enriched air) may pass. The axial support assembly is secured around the bundle of hollow fiber membranes at a position radially inward from the housing and radially outward from the fiber bundle. | 07-31-2014 |
20140208948 | Gas Separation Modules and Methods for Forming - A gas separation module includes at least one inlet port, a plurality of outlet ports, and a plurality of hollow fiber membranes. Individual fibers have a feed end and a product end with a retentate interior side and a permeate exterior side. The module includes a feed tubesheet within the shell segregating the at least one inlet port and the permeate side of the fibers. The feed tubesheet includes a matrix and at least one segment joint. The segment joint separates segments of the feed tubesheet from one another. A formation method includes positioning a hollow fiber membrane material in association with at least one tubesheet segment joint and applying a matrix. The method includes forming a feed tubesheet from cured matrix and the segment joint and forming a plurality of hollow fiber membranes from the fiber material. The segment joint separates segments of the feed tubesheet from one another. | 07-31-2014 |
20140311344 | System and Method for Welding a Plurality of Small Diameter Palladium Alloy Tubes to a Common Base Plate in a Space Efficient Manner - The tube assemblies are joined together into a matrix by a plate. The plate has a first surface, an opposite second surface and a plurality of holes. Each hole has a countersunk region that descends into the plate from the first surface. Tube assemblies are provided. Each tube assembly has a first end, an opposite second end, and a flare structure. The flare structure is sized to be fully received within the countersunk region. The tube assemblies extend through the holes in the plate. The flare structure of each tube assembly is welded to the plate within the countersunk region of each hole through which each tube assembly passes. | 10-23-2014 |
20140318372 | Membrane Separation Modules - A system using membranes for separating a desired component from a liquid or gas mixture to obtain a high-concentration organic solvent, such as in a plant for fermenting a biomass feedstock (e.g., corn or sugarcane) to produce ethanol. A module for removing water from the ethanol/water mixture comprises multiple vessels or elements connected together in series and supported by a frame. Each element includes a number of flow tubes concentrically enclosing a tubular membrane leaving an annular space between the membrane's outer wall and the flow tube's inner wall. The preferred membrane is a hollow ceramic (e.g., zeolite) tube. An ethanol/water vapor is passed through the space between the tube walls, and a vacuum is pulled on the membrane's hollow core. Water molecules selectively move through the membrane. Multiple passes through a series of elements having the concentric tubes and membranes gradually reduces the water content of the ethanol. | 10-30-2014 |
20150007729 | GAS SEPARATION MEMBRANE MODULE AND METHOD FOR GAS SEPARATION - A process for producing nitrogen-rich air by feeding high temperature air at 150° C. or more to an air separation membrane module is described. After being placed at 175° C. for two hours, the air separation module exhibits a shape-retention ratio of 95% or more in one embodiment. The nitrogen-rich air can be fed to a fuel tank for an aircraft, for example. | 01-08-2015 |
20150053085 | Single End, Shell-Side Feed, Hollow Fiber Membrane Separation Module - A shell-side feed, hollow fiber, fluid separation module arranged for counter-flow includes a hollow fiber membrane bundle with each individual hollow fiber membrane in the bundle having an open fiber end and a sealed fiber end. The open fiber ends are encapsulated in a tubesheet located toward the permeate fluid outlet end of the module. The sealed fiber ends are tubesheet-free, uniformly spaced, and located toward the non-permeate fluid outlet end of the module. | 02-26-2015 |
20150107453 | WATER RECOVERY DEVICE - A water recovery device that allows a first gas to flow inside hollow fiber membranes and a second gas to flow outside the hollow fiber membranes, and that exchanges moisture between the first gas and the second gas, includes a hollow fiber membrane bundle in which plural pieces of the hollow fiber membranes are bundled, a storage case housing the hollow fiber membrane bundle in its inside, and a housing having an introduction hole and a discharge hole of the first gas and an introduction hole and a discharge hole of the second gas, and housing the storage case in its inside. The hollow fiber membrane bundle includes a first gas bypass passage that penetrates through an internal part of the hollow fiber membrane bundle in an axial direction and that has a channel cross-sectional area larger than a channel cross-sectional area inside the hollow fiber membrane. | 04-23-2015 |
20150107454 | HOLLOW FIBER MEMBRANE MODULE - A hollow fiber membrane module comprising a bundling tube including a body part and head parts placed at both terminals of the body part and O-rings with which the bundling tube is fitted into a housing being attached to outer circumferential surfaces of the head parts, wherein at least one of the head parts are divided into two in a place closer to a terminal of the bundling tube than places where the O-rings are attached while maintaining a cylindrical shape of the head part, and the divided parts have a slidable structure while maintaining a coupled condition therebetween that forms the cylindrical shape. The hollow fiber membrane module is capable of preventing damage effectively on a hollow fiber membrane or the bundling tube due to expansion or contraction of the hollow fiber membrane to be caused by change of an external environment such as temperature. | 04-23-2015 |
20150107455 | Hollow Fiber Module of a Device for Separating Fluids and Method for Producing Same - A hollow fiber module of a device for separating fluids has hollow fibers with walls that have partially permeable structures. The hollow fibers are positioned parallel to each other. At least one areal fluid-permeable spacer medium with a structure that is self-supporting an areal state of the at least one spacer medium is provided and arranged between the hollow fibers such that the at least one spacer medium surrounds at least partially circumferentially a first one of two neighboring hollow fibers at least on a side of the first hollow fiber that is facing the second one of the two neighboring hollow fibers. | 04-23-2015 |
20150375171 | DEHUMIDIFYING DEVICE AND DEHUMIDIFYING MODULE - The present application discloses a dehumidifying device including a base configured to define an inlet channel for first air flow, and an outlet channel for second air flow less humid than the first; and a first dehumidifier including a first inlet and outlet in communication with the inlet and outlet channel, and configured to dehumidify the first air between the first inlet and the first outlet to generate the second air. The base includes a first base portion configured to define first inlet and outlet regions for the first and second air flows; and a second base portion configured to define second inlet and outlet regions in communication with the first inlet and outlet regions. The first and second inlet regions form at least a part of the inlet channel. The first and second outlet regions form at least a part of the outlet channel. | 12-31-2015 |
20160023164 | GAS SEPARATION MEMBRANE MODULE WITH IMPROVED GAS SEAL - Parallel membrane elements are arranged in parallel within a pressure vessel. A sealing body is disposed within the pressure vessel and is compressed against an inner surface of the pressure vessel to provide a leak-right seal in between a feed gas side of the sealing body and a non-permeate side of the sealing body. The sealing body may be slid within the pressure vessel without damaging the sealing body and in all cases without requiring mechanical assistance. | 01-28-2016 |
20160089635 | GAS SEPARATION MODULES AND METHODS FOR FORMING - A gas separation module includes at least one inlet port, a plurality of outlet ports, and a plurality of hollow fiber membranes. Individual fibers have a feed end and a product end with a retentate interior side and a permeate exterior side. The module includes a feed tubesheet within the shell segregating the at least one inlet port and the permeate side of the fibers. The feed tubesheet includes a matrix and at least one segment joint. The segment joint separates segments of the feed tubesheet from one another. A formation method includes positioning a hollow fiber membrane material in association with at least one tubesheet segment joint and applying a matrix. The method includes forming a feed tubesheet from cured matrix and the segment joint and forming a plurality of hollow fiber membranes from the fiber material. The segment joint separates segments of the feed tubesheet from one another. | 03-31-2016 |
20160151744 | MEMBRANE CARTRIDGE SYSTEM | 06-02-2016 |
096009000 | Barriers connected in series | 21 |
20080236394 | HONEYCOMB STRUCTURE AND METHOD FOR MANUFACTURING HONEYCOMB STRUCTURE - A honeycomb structure includes a ceramic block formed by a plurality of pillar-shaped honeycomb fired bodies each having a large number of cells longitudinally disposed in parallel with one another with a cell wall between the cells. The plurality of honeycomb fired bodies are combined with one another by interposing an adhesive layer with a sealing material layer formed on a peripheral face of the ceramic block and include a plurality of different shapes of the honeycomb fired bodies. A thickness of a peripheral wall forming the peripheral face of the ceramic block is virtually even. A shape of a cell located at an outermost periphery of the ceramic block is virtually identical with a shape of a cell located at a place other than the outermost periphery of the ceramic block. On the peripheral wall of the honeycomb fired body, a step is provided. | 10-02-2008 |
20090126571 | PARTICULATE MATERIAL PROCESSING APPARATUS AND PARTICULATE MATERIAL PROCESSING SYSTEM - A particulate material processing apparatus has a vessel and a processing tank. The vessel has a charging port for charging a particulate material into the vessel. The processing tank receives the particulate material charged from the charging port. The processing tank is shaped so as to narrow towards the bottom. At least the lower part of the processing tank is made of a gas-permeable material that allows the process gas for processing the particulate material to pass through. The upper part of the processing tank has lower gas permeability than the lower part of the processing tank. | 05-21-2009 |
20090282981 | Gas Diluter - A gas diluter which comprises: dilution chambers in which a first gas is mixed with a second gas to reduce the concentration of the first gas; connecting passages with which the dilution chambers are connected serially; branched passages through which the first gas is distributed to the dilution chambers, an introduction passage through which the second gas is introduced into the dilution chamber, which is located at one end of the serially connected dilution chambers; and a discharge opening through which the gas obtained by mixing the first gas with the second gas is discharged from the dilution chamber, which is located at the other end of the serially connected dilution chambers. | 11-19-2009 |
20090301307 | Gas Separation Membrane - A gas separation membrane has: a polymeric microporous membrane which has a polyolefin as a main component, and which is manufactured by wet phase separation process, and has a porosity of 20 to 80%, an average pore diameter of 1 to 100 nm and a piercing strength at 100° C. of 2 to 50 N; and a gas-separating thin film, which is provided on at least one surface, and/or the interior of the polymeric microporous membrane, and which comprises a fluorine-containing gas-separating resin as a main component, and has an average thickness of 0.01 μm to less than 0.4 μm. The gas separation membrane having an oxygen-nitrogen separation factor not smaller than 1.4. | 12-10-2009 |
20100018397 | COMPOSITE MEMBRANE MATERIAL FOR HYDROGEN SEPARATION AND ELEMENT FOR HYDROGEN SEPARATION USING THE SAME - A composite membrane material characterized by comprising a hydrogen-permeable membrane which is selectively permeable to hydrogen and is formed by rolling to a thickness of 30 μm or less which is difficult for the membrane by itself to retain its shape, and a shape-retention mesh which is disposed on at least one side of the hydrogen-permeable membrane and is composed of a wire of a high-melting metal which does not cause thermal diffusion into the hydrogen-permeable membrane, wherein the hydrogen-permeable membrane and the shape-retention mesh are superposed and subjected to a pleat processing in a non-bonded state so that they are separable and the hydrogen-permeable membrane has a surface area increased at least 3 times per unit area. This material is used to constitute a hydrogen separation element. | 01-28-2010 |
20100043638 | AIR FILTER UNIT WITH AT LEAST ONE MAIN AIR FILTER AND AN AUXILIARY FILTER - In an air filter unit ( | 02-25-2010 |
20100050876 | Sodium Bicarbonate Vacuum Bag Inserts - A vacuum cleaner bag filter with one or more filter walls forming a generally air permeable enclosure having a bag opening through it, and a flange attached to the one or more filter walls to cover the bag opening. The filter walls have a working surface area through which air can pass during use, and the flange is a relatively rigid structure having an air inlet passing into the air permeable enclosure. One or more deodorizing sheets are attached to an inner surface of the one or more filter walls. The deodorizing sheets include a first sheet layer, and sodium bicarbonate particles operatively associated with the first sheet layer. The deodorizing sheets may cover less than about 30% of the working surface area, a single deodorizing sheet may be provided, and the deodorizing sheets may be attached to the filter walls by an air impermeable adhesive that covers at least about 5% of the surface area of the deodorizing sheets. Also provided is a vacuum cleaner filter having a filter and a deodorizing sheet attached thereto by an air-impermeable adhesive. | 03-04-2010 |
20100263538 | Hydrogen Purifier Module and Method for Forming the Same - A hydrogen purifier utilizing a hydrogen-permeable membrane to purify hydrogen from mixed gases containing hydrogen is disclosed, with improved sealing means where the seals are formed by first melting a metal with a low temperature melting point, and then allowing the metal to form a subsequent alloy which has a melting temperature above the operational temperature of the purifier. The improved seal allows for the fabrication of hydrogen purifiers at lower temperatures than conventional methods such as brazing. Various metallurgical combinations and methods for achieving the seal are disclosed. | 10-21-2010 |
20100282085 | Hydrogen Purifier Module with Membrane Support - A hydrogen purifier utilizing a hydrogen-permeable membrane to purify hydrogen from mixed gases containing hydrogen is disclosed. Improved mechanical support for the permeable membrane is described, enabling forward or reverse differential pressurization of the membrane, which further stabilizes the membrane from wrinkling upon hydrogen uptake. | 11-11-2010 |
20110041693 | OLEOPHOBIC LAMINATED ARTICLE - An article comprising a microporous membrane. A first porous fabric is laminated to a first side of the microporous membrane. A second porous fabric is laminated to a second opposite side of the microporous membrane to form a laminate with the membrane and the first porous fabric. The laminate has two fabric sides separated by the microporous membrane. A treatment material is applied to the laminate to form a treated laminate. The treated laminate has an oil resistance of at least a number 7 determined by AATCC 118 testing on both fabric sides and has an air permeability through the treated laminate of at least 0.01 CFM per square foot determined by ASTM D737 testing. | 02-24-2011 |
20110203458 | MEMBRANE GAS DRYERS INCORPORATING ROTATABLE FITTINGS - A membrane gas dryer includes an upstream fitting assembly, a downstream fitting assembly, a purge tube, and a sample element. The upstream fitting assembly and the downstream fitting assembly include fitting bodies and barrier sleeves. The fitting bodies and the barrier sleeves form purge plenums that are in fluid communication with the purge tube. Sealing interfaces on the fitting bodies maintain fluid-tight seals around the purge plenums as the barrier sleeves rotate about fitting bodies. The sample element includes a water-permeable membrane and passes inside the purge tube such that moisture in a sample gas flowing in a downstream direction through the sample element between the fitting body to the downstream fitting body passes moisture through the water-permeable membrane and into a purge gas flowing in the purge tube in one of an upstream direction or a downstream direction between the purge plenums. | 08-25-2011 |
20110232491 | HYDROGEN-PROCESSING ASSEMBLIES AND HYDROGEN-PRODUCING SYSTEMS AND FUEL CELL SYSTEMS INCLUDING THE SAME - Hydrogen-processing assemblies, components of hydrogen-processing assemblies, and fuel-processing and fuel cell systems that include hydrogen-processing assemblies. The hydrogen-processing assemblies include a hydrogen-separation assembly positioned within the internal volume of an enclosure in a spaced relation to at least a portion of the internal perimeter of the body of the enclosure. | 09-29-2011 |
20110239866 | INTEGRATED MEMBRANE MODULE FOR GAS DEHYDRATION AND GAS SEPARATION - An integrated fiber membrane module for air dehydration and air separation includes dehydration and separation units disposed concentrically in a generally cylindrical module. Air flows through the outer dehydration unit, becomes dried, and is then directed, in an opposite direction, through the separation unit. The permeate gas from the separation unit serves as a sweep gas for the dehydration unit. A portion of dried gas produced by the dehydration unit may be used as a sweep gas for the separation unit, and also for the dehydration unit. The module makes it feasible to dry and separate air using a device which occupies relatively little space, and which is therefore especially suited for use in aircraft and in other cramped environments. | 10-06-2011 |
20120000363 | Air filter device - An air filter device includes a permeation film arranged at a boundary portion between an outside air passage and an inside air passage, such that one side surface of the permeation film is exposed to outside air in the outside air passage and the other side surface of the permeation film is exposed to inside air in the inside air passage. The permeation film is configured such that specific gas passes through the permeation film between the outside air passage and the inside air passage. Furthermore, a turbulent flow generation portion is provided to generate a turbulent flow in at least one of the outside air flowing through near the one side surface of the permeation film and the inside air flowing through near the other side surface of the permeation film. | 01-05-2012 |
20120085238 | STAGED MEMBRANE SYSTEM FOR GAS, VAPOR, AND LIQUID SEPARATIONS - The present invention involves the use of a multi-stage membrane system for gas, vapor, and liquid separations. In this multi-stage membrane system, high selectivity and high permeance or at least high selectivity polybenzoxazole membranes or cross-linked polybenzoxazole membranes are applied for a pre-membrane or both the pre-membrane and the secondary membrane. A primary membrane can be from conventional glassy polymers. This multi-stage membrane system can reduce inter-stage compression cost, increase product recovery and product purity for gas, vapor, and liquid separations. It can also save the cost compared to the system using all the high cost polybenzoxazole membranes or cross-linked polybenzoxazole membranes. | 04-12-2012 |
20120118155 | SYSTEMS AND METHODS FOR MULTI-STAGE AIR DEHUMIDIFICATION AND COOLING - The present disclosure relates to systems and methods for dehumidifying air by establishing a humidity gradient across a water selective permeable membrane in a dehumidification unit. Water vapor from relatively humid atmospheric air entering the dehumidification unit is extracted by the dehumidification unit without substantial condensation into a low pressure water vapor chamber operating at a partial pressure of water vapor lower than the partial pressure of water vapor in the relatively humid atmospheric air. For example, water vapor is extracted through a water permeable membrane of the dehumidification unit into the low pressure water vapor chamber. As such, the air exiting the dehumidification unit is less humid than the air entering the dehumidification unit. The low pressure water vapor extracted from the air is subsequently condensed and removed from the system at ambient conditions. | 05-17-2012 |
20120186452 | Multiple Layer HEPA Filter and Method of Manufacture - A multiple layer HEPA filter media includes, in an exemplary embodiment, a first layer that includes a nonwoven synthetic fabric formed from a plurality of bicomponent synthetic fibers with a spunbond process, and having a bond area pattern of a plurality of substantially parallel discontinuous lines of bond area. The filter media also includes a second layer laminated onto the first layer. The second layer is formed from a micro-porous membrane. Further, the filter media includes a third layer laminated onto the second layer, with the third layer including a synthetic nonwoven fabric formed from a plurality of synthetic fibers. The synthetic fibers include at least two different synthetic fibers having different melting points. The third layer has a cover factor of less than about seven. In addition, the multiple layer filter media further includes a plurality of corrugations. | 07-26-2012 |
20130098246 | Exhaust Gas Treating System Using Polymer Membrane For Carbon Dioxide Capture Process - Disclosed is an exhaust gas treating system having an exhaust gas treating apparatus for carbon dioxide capture process which additionally removes harmful substances remaining in the gas discharged from the existing flue-gas desulfurization process by using separation membrane so as to efficiently carry out the carbon dioxide capture process. The exhaust gas treating system using polymer membrane, comprises a carbon dioxide capture equipment for capturing carbon dioxide from the exhaust gas of a boiler, a flue-gas denitrification equipment placed between the boiler and the carbon dioxide capture equipment, a dust-collecting equipment and a flue-gas desulfurization equipment. | 04-25-2013 |
20130247761 | Method and System for Membrane-Based Gas Recovery - A fast gas is recovered from a feed gas containing a fast gas and at least one slow gas using a gas separation membrane. A controller may control a control valve associated with a partial recycle of a permeate gas from the membrane for combining with the feed gas. A controller may control a control valve associated with the backpressure of a residue gas from the membrane. | 09-26-2013 |
20140013952 | FILTER GROUP FOR FLUIDS - A filter group ( | 01-16-2014 |
20150314241 | CONSTRUCTIONS FOR FLUID MEMBRANE SEPARATION DEVICES - Described herein is a construction comprising (a) a support sheet having a base, comprising (i) a plurality of rails extending from the base wherein each rail of the plurality of rails extends continuously down a length of the support sheet and each rail comprises a first side surface and an opposing second side surface and a top surface; and (ii) a plurality of first protrusions extending from the base, wherein the plurality of first protrusions are located between the plurality of rails; and (b) a selectively permeable membrane having a first major membrane surface contacting at least the top surface of at least two rails enclosing a flow channel having a height extending between the base of the support sheet and the first major membrane surface, wherein the plurality of protrusions change the height of the flow channel along its length along the longitudinal axis of the flow channel. | 11-05-2015 |