Patent classifications
B01D69/108
FILTRATION BASE FOR VACUUM DIAPHRAGM FILTRATION
A filtration base for vacuum membrane filtration applications comprises a membrane bearing area on the upper side of the filtration base, which has a bearing structure and a supporting contour surrounding the bearing structure for a membrane filter placed in the membrane bearing area. The supporting contour has at least one notch which is in flow connection with the bottom side of the membrane bearing area and which is arranged such that it is adapted to be selectively covered by a membrane filter placed in the membrane bearing area.
Film forming method for metal film and film forming apparatus for metal film
A solid electrolyte membrane is disposed between an anode and a substrate, and voltage is applied between the anode and the substrate while the solid electrolyte membrane is pressed onto the substrate so as to form a metal film on the substrate. In this film forming method, there is used the solid electrolyte membrane that includes: a first portion made of an ion permeable material; and a second portion made of a material having an electric insulating property and having a low permeability of metallic ions, the second portion being embedded in the first portion so as to be exposed from a surface of the solid electrolyte membrane, the surface of the solid electrolyte membrane facing the substrate.
SUPPORT, ZEOLITE MEMBRANE COMPLEX, METHOD OF PRODUCING ZEOLITE MEMBRANE COMPLEX, AND SEPARATION METHOD
A porous cylindrical support for use in supporting a zeolite membrane has a generally cylindrical inside surface having a central axis extending in the longitudinal direction and a generally cylindrical outside surface that surrounds the inside surface. A zeolite membrane is formed on the outside surface. A maximum value A and a minimum value B of a support thickness in a circumferential direction satisfy (A−B)/(A+B)≤0.3 in at least part of the support in the longitudinal direction, the support thickness being a radial distance between the inside surface and the outside surface. By reducing a variation in support thickness, it is possible to improve uniformity in the thickness of the zeolite membrane formed on the support.
NANOPOROUS GRAPHENE MEMBRANES
An article having a nanoporous membrane and a nanoporous graphene sheet layered on the nanoporous membrane. A method of: depositing a layer of a diblock copolymer onto a graphene sheet, and etching a minor phase of the diblock copolymer and a portion of the graphene in contact with the minor phase to form a nanoporous article having a nanoporous graphene sheet and a nanoporous layer of a polymer. A method of: depositing a hexaiodo-substituted macrocycle onto a substrate having a Ag(111) surface; coupling the macrocycle to form a nanoporous graphene sheet; layering the graphene sheet and substrate onto a nanoporous membrane with the graphene sheet in contact with the nanoporous membrane; and etching away the substrate.
UIO-66-NH2 DOPED ORGANOSILICON HIGH SALINITY WASTEWATER TREATMENT MEMBRANE AND A PREPARATION METHOD THEREOF
The invention belongs to the technical field of composite membrane, and in particular discloses a UIO-66-NH.sub.2 doped organosilicon high salinity wastewater treatment membrane and a preparation method thereof. The membrane is formed into UIO-66-NH.sub.2/organosilicon hybrid membrane on the prefabricated ceramic support surface through the dip-coating method by doping the UIO-66-NH.sub.2 metal-organic framework material into the organosilicon polymeric sol. The UIO-66-NH.sub.2/organosilicon hybrid membrane prepared by the present invention exhibits high water permeability (up to 1.6×10.sup.−10 m.sup.3/(m.sup.2 s Pa) and high salt retention (NaCl retention rate is more than 99.9.%) in the application of pervaporation desalination, and maintains stable membrane structure in the treatment process of TDS>5 wt % high salinity wastewater.
Nanoporous graphene membranes
An article having a nanoporous membrane and a nanoporous graphene sheet layered on the nanoporous membrane with the nanoporous membrane and the nanoporous graphene sheet in direct contact. A method of: depositing a layer of a diblock copolymer onto a graphene sheet, etching a minor phase of the diblock copolymer and a portion of the graphene in contact with the minor phase to form a nanoporous article having a nanoporous graphene sheet and a nanoporous layer of a polymer, and removing the nanoporous layer of a polymer.
BONDED BODY, SEPARATION MEMBRANE MODULE EQUIPPED WITH SAME, AND METHOD FOR PRODUCING ALCOHOL
The present invention addresses the problem of providing a bonded body which has a high airtightness and exhibits excellent durability under high-temperature and high-pressure conditions. This problem is solved by a bonded body in which a complex of a zeolite and an inorganic porous support, and a dense member are bonded together by an inorganic glass or an inorganic adhesive. The inorganic glass or the inorganic adhesive has a thermal expansion coefficient of 30×10.sup.−7/K to 90×10.sup.−7/K, and the inorganic glass has a softening point of 550° C. or lower. The present invention also addresses the problem of providing a method of efficiently producing an alcohol by installing a separation membrane in an alcohol synthesis reactor based on a bonding method that gives good sealing performance and durability under high-temperature and high-pressure conditions and in the presence of methanol vapor. This problem can be solved by an alcohol production method of obtaining an alcohol by allowing a raw material gas, which contains at least hydrogen and carbon monoxide and/or carbon dioxide, to react in the presence of a catalyst in a reactor. In the reactor for carrying out the reaction, an alcohol-selective permeable membrane bonded with a dense member is installed, and an alcohol generated by the reaction permeates and is recovered through the selective permeable membrane.
Method for producing a permeation membrane
Disclosed is a method for producing a palladium-based permeation membrane which is suitable for the separation of hydrogen from gas-gas or liquid-gas mixtures. The permeation membrane is produced by applying a palladium complex, dissolved in a solvent, to a nanoporous support system having pores in a size range of from 0.5 nm to 50 nm, removing the solvent by drying, removing of organic constituents of the palladium complex by a heat treatment, and carrying out a final heat treatment under reducing conditions at a temperature ranging from about 300° C. to about 900° C.
Gas in/outlet adapter system for a filtration device
The invention relates to a gas in/outlet-adapter system for a container/rack assembly for a diagnostic robot comprising: —a receptacle (15) comprising a gas-inlet wherein the receptacle (15) is attached to a container (12), —a nozzle (16) comprising a gas-outlet wherein the nozzle (16) is attached to a rack to supply the container (12) via the receptacle (15) with a gas at a defined pressure level, wherein the receptacle (12) —provides one opening (24) —which provides for a fluidic contact to the interior of the container (12) —and a second opening (25) —which provides for a gas leak-proof connection to the nozzle (16) on the rack when the receptacle (15) is placed over the nozzle (16), and wherein the nozzle (16) —provides one opening (26) —which provides for a fluidic contact to a tubing system of the rack—and a second opening (27) —which provides for a fluidic contact to the nozzle (16) when the receptacle (15) is placed to cover the nozzle (15).
AMMONIA SEPARATION METHOD AND ZEOLITE
Provided is a method for separating ammonia gas using zeolite membrane having excellent separation stability at a high temperature capable of separating ammonia gas from a mixed gas composed of multiple components including ammonia gas, hydrogen gas, and nitrogen gas to the permeation side with high selectivity and high permeability. Also provided is a method for separating ammonia by selectively permeating ammonia gas from a mixed gas containing at least ammonia gas, hydrogen gas, and nitrogen gas using a zeolite membrane, wherein the ammonia gas concentration in the mixed gas is 1.0% by volume or more.