Abstract: Wastewater is treated though primary treatment of the water by way of a micro-sieve to produce a primary effluent and primary sludge. There is secondary treatment of the primary effluent by way of a membrane bioreactor (MBR) or an integrated fixed film activated sludge (IFAS) reactor to produce a secondary effluent and a waste activated sludge. The micro-sieve may have openings of 250 microns or less, for example about 150 microns. In a process, a gas transfer membrane is immersed in water. Pressurized air flows into the gas transfer membrane. An exhaust gas is withdrawn from the gas transfer membrane and used to produce bubbles from an aerator immersed in the water.

Abstract: This raw-material liquid concentration system is for use in a pharmaceutical product manufacturing process, and employs a membrane-distillation method involving: bringing a raw-material liquid containing a solvent and a solute into contact with cooling water through a membrane-distillation membrane; passing the solvent in the raw-material liquid through the membrane-distillation membrane in the form of vapor; and causing the solvent to move toward the side of the cooling water, wherein the membrane-distillation membrane is a porous membrane that has a water contact angle of at least 90° at the surface thereof, has an average pore diameter of 0.02-0.5 ?m, and has a porosity of 60-90%.

Abstract: A distillation apparatus having a hot liquid block, a thermoelectric module (TEM), a condensation surface, a feed liquid chamber having a feed chamber inlet, a feed chamber outlet, and a membrane disposed on at least one side of the feed liquid chamber. One side of the membrane faces to the condensation surface. An air gap of 1 mm to 20 cm separates the condensation surface and the membrane. A permeate outlet in fluid communication with the air gap. A heating unit in fluid communication with the feed liquid chamber and the hot liquid block. A cooling unit in fluid communication with the permeate outlet. A multi-stage distillation apparatus with a plurality of distillation apparatuses. A process of distilling water, by feeding a liquid into the distillation apparatus through the hot block inlet and collecting distilled water from the permeate outlet.

Abstract: The disclosure relates to assembled membranes used in water treatment systems, including membranes used in reverse osmosis procedures and methods for making and using the membranes.

Abstract: A reverse osmosis apparatus including a reverse osmosis unit having a housing; a cylindrical drum rotatably disposed inside the housing wherein a lateral gap therebetween defines a intervening chamber, and including an outer cylindrical wall and an inner cylindrical wall to define an inner cylindrical feed chamber and an outer annular separation chamber therewithin; and at least one channeling structure defining a permeate channel extending radially from the inner cylindrical wall to the outer cylindrical wall, wherein a first channel end is closed and a second channel end opens into the intervening chamber. The at least one channeling structure including a membrane element extending lengthwise forming a semi-permeable interface between the permeate channel and a feed-flow-region in fluid communication with the inner cylindrical feed chamber. The apparatus including a pump to pressurize the inner cylindrical feed chamber, and a motor to rotate the cylindrical drum for generating centrifugal force.

Abstract: An apparatus for roll-to-roll nanomaterial dispersion papermaking includes a suction pressure for consolidating nanomaterials on a fluid permeable filter in one region of the filter and an opposite pressure region or regions for separating a mat of the consolidated nanomaterials and transferring the mat to a transfer roller. A transfer roller may have a suction pressure within the transfer roller to help transfer the mat from the filter to the transfer roller, for example. An inlet port distributes nanomaterials using row and zone inlets, for example.

Abstract: A thin-film-composite hollow-fiber membrane includes a phase-inversion layer, which is in the form of a hollow fiber, and an active layer coated on the phase-inversion layer. The active layer selectively allows passage of water molecules but rejects at least some dissolved ions. The thin-film-composite hollow-fiber membrane can have an internal burst pressure of at least 4 MPa. In a method for forming the membrane, the polymer concentration in the spinning dope from which the hollow-fiber substrate is formed can have a polymer concentration no greater than 5% below the critical concentration.

Abstract: A membrane separation system is provided comprising at least two membranes in series. A first membrane in the series is oleophobic and comprises: (a) a porous substrate; and (b) an oleophobic coating layer applied to at least one surface of the substrate. A second membrane in the series is hydrophilic. The second membrane may comprise a hydrophilic porous substrate, and/or the second membrane further comprises a hydrophilic coating layer applied to at least one surface of the second membrane substrate. Also provided are methods of separating aqueous emulsions, comprising: (i) contacting an aqueous emulsion with the membrane separation system described above; and (ii) allowing water in the emulsion to permeate through the membrane separation system to yield an aqueous product stream.

Abstract: An electrolytic eluent generator includes an electrolyte reservoir, an eluent generation chamber, and an ion exchange membrane stack. The electrolyte reservoir includes a chamber containing an aqueous electrolyte solution including an electrolyte; and a first electrode. The eluent generation chamber including a second electrode. The ion exchange connector includes an ion exchange membrane stack, and a compression block.

Abstract: A gas separation membrane includes a porous layer, a first resin layer provided at a surface on one side of the porous layer, the first resin layer including an organopolysiloxane, and a second resin layer provided at a surface of the first resin layer on a side opposite to that of the porous layer, the second resin layer including an organopolysiloxane. The first resin layer has a porosity greater than that of the second resin layer. The second resin layer is chemically bonded to the first resin layer.

Abstract: The present disclosure belongs to the technical field of porous membrane material preparation, and specifically relates to a reverse osmosis composite membrane with an ultrathin desalting layer and a preparation method thereof; the intermediate layer is introduced after modifying the polysulfone base membrane, the modified polysulfone base membrane support layer may strengthen the bonding to the desalting layer through a covalent bond, and the thickness of the desalting layer is reduced to be ?10 nm, so that the desalination rate of the membrane is not greatly affected while increasing the membrane flux. Compared with the membrane having a conventional thickness of the desalting layer, the water flux of the reverse osmosis composite membrane with an ultrathin desalting layer may be increased by about 0.5 times, while the desalination rate has a small change.

Abstract: An apparatus for accelerated dissolution of carbonates with buffered pH. The apparatus includes a mixer, a dissolution reactor and a pH correction reactor. The mixer includes: a chamber; a water supply; a carbonic gas supply; and a carbonate supply. Water, carbonic gas and carbonate are provided to the chamber in predetermined continuous flow rates to obtain a design flow rate of lean mixture at the outlet. The dissolution reactor includes a duct connected to the chamber receiving the lean mixture and allowing at least partial dissolution of the carbonate which transforms the lean mixture into an ionic mixture according to the reaction CaCO3+CO2+H2O? Ca(HCO3)2. The pH correction reactor comprises a duct and a hydroxide supply. The mixture is then released into the sea. Embodiments also relate to a method for the accelerated dissolution of carbonates with buffered pH for the permanent sequestration of CO2 in the sea in the form of bicarbonates.

Abstract: A submersible aeration apparatus includes an air passage formed on a pump chamber to draw air into the pump chamber. A suction port formed on a lower side of the pump chamber draws liquid into the pump chamber. An impeller draws air through the air passage and liquid through the suction port. An ejection passage ejects the air and liquid. The impeller includes a main plate portion to cover a connection port connecting the air passage to the pump chamber. A vane portion protrudes downward from a lower surface of the main plate portion on the suction port side. The main plate portion has a cut-out part connecting the air passage and the pump chamber, and a groove part recessed from an upper surface of the main plate portion toward the lower surface and extending from an inner peripheral side toward an outer peripheral side of the main plate portion.

Abstract: An apparatus to move and aerate liquid is disclosed. The apparatus includes a frustoconical base forming a gas chamber. The gas chamber includes one or more inner apertures to allow gas flow into a mixing chamber to aerate and, subsequently, move liquid into a liquid riser for subsequent movement back into the liquid supply. The gas chamber further includes one or more outer apertures to allow gas flow directly into liquid of the liquid supply surrounding the liquid riser. Preferably, the liquid exiting the liquid riser aids in dispersing the liquid aerated by the one or more outer apertures.

Abstract: According to the present invention, there is provided a foaming apparatus that discharges a foamable material obtained by mixing gas into a viscous material of a resin and dispersing bubbles in a liquid of the viscous material. The foaming apparatus includes: a pipe; a material supply unit; a gas supply unit; a first gear pump; a second gear pump; a third gear pump; a mixer; a discharge unit; and a control unit.

Abstract: The present invention relates to a device (1) for the generation of micro and nano bubbles of gas in a liquid comprising: an outer tubular body (10) with an extension along a longitudinal axis a-a; an inlet (20) for a flow of liquid; an outlet (30) of the flow of liquid in fluid communication with said inlet (20); a central body (40) contained in a central area of said outer tubular body (10). The central body (40) comprises—a pre-chamber (41) containing a gas; —an air intake (42) in connection with said pre-chamber (41) and with an external source of gas; —a converging element (52), configured to concentrate the flow of liquid at the inlet; —a Venturi chamber (44) in fluid contact with said pre-chamber (41), configured to suck the gas from the pre-chamber (41) and generate micro and nano bubbles of gas in the liquid that passes through it.

Abstract: A stirring device includes the following. A rotating holder is capable of performing a rotating operation in a state where the rotating holder holds a cartridge that accommodates a liquid agent in which a solute is precipitated in a solvent by the liquid agent being left still. A drive motor causes the rotating holder to perform the rotating operation. A posture controller corrects a stop position of the rotating holder to position the cartridge in a first posture in a case where an operation of the drive motor is stopped in a state where the cartridge is in a second posture that is different from the first posture. The first posture is a state in which the cartridge is in a normal stop posture.

Abstract: the present invention relates to a magnetic mixer to which a disposable resin liquid pouch is applied instead of a metal tank, for accommodating and mixing liquids therein, to minimize cross-contamination of liquids to be mixed due to an unwashed residue, increase a magnetic coupling force between rotors for driving an impeller inside the liquid pouch and an impeller outside the liquid pouch by a magnetic coupling method, and prevent separation of the impeller in liquids to be mixed, and a magnetic mixing system.

Abstract: A mixing attachment for use with a reciprocating mechanism of a reciprocating hand tool, to quickly and efficiently mix contents of paint cans or other containers, may include a support member and one or more retention ring assemblies. The support member may be disconnectably connected to the reciprocating mechanism. The one or more retention ring assemblies may be attached to the support member. The retention ring assemblies may be mounted in a longitudinal slot on the support member and include an adjustable band and a securing mechanism for tightening the adjustable band about an outer surface of a paint can.

Abstract: Systems for hydrocarbon pyrolysis are provided, which may comprise a reactor configured to contain a liquid metal; a heater operably coupled to the reactor to form a heating zone; a cooler operably coupled to the reactor to form a cooling zone; a gas delivery assembly comprising an inlet and configured to deliver a feed gas comprising a hydrocarbon as a plurality of bubbles through the liquid metal; an outlet configured to deliver a product gas to a separation assembly, the product gas formed from pyrolysis of the hydrocarbon in the liquid metal, the product gas comprising H2 and carbon; and the separation assembly configured to separate the carbon from other components of the product gas. The reactor is configured to entrain the carbon from pyrolysis of the hydrocarbon in the liquid metal into the product gas without accumulating the carbon in the interior chamber during pyrolysis.

Abstract: A catalytic synthesis reactor is described, said reactor comprising a catalytic bed with an annular cylindrical shape delimited by a gas inlet header and a gas outlet header, wherein at least one of said headers has a multiple-wall structure comprising an outer perforated plate having a load-bearing function, an expanded metal plate acting as a spacing element, and a thin micro-perforated plate facing the catalyst and having a catalyst's retaining function.

Abstract: A fluidizing device for treating particulate material and to a method using the fluidizing device. The fluidizing device includes an inflow base that can be moved relative to the fluidizing unit. The inflow base in an emptying position is positioned at least partly below the top edge of a material outlet by moving the inflow base relative to the fluidizing unit, so that a fluid connection is formed between the material outlet arranged in the distributor chamber and the fluidizing chamber past the inflow base in order to discharge treated material from the fluidizing unit.

Abstract: The present invention relates to the stabilization of an effective ingredient by using a mineral material. In the present invention, the effective ingredient can be stably supported using the mineral material, and a microcapsule obtained by the manufacturing method according to the present invention, when discharged to nature, causes no environmental problems due to encapsulation ingredients thereof being the same as soil ingredients, and thus can avoid micro-plastic issues.

Abstract: The present invention relates to the field of chemical synthesis. Specifically, the present invention relates to methods, materials, compositions, and devices for multiplexing chemical synthesis. In particular, the present invention provides novel methods, materials, compositions, and devices to synthesize plurality of chemical compounds, including but not limited to nucleic acids, peptides, saccharides, and phospholipids. Specifically, the present invention provides methods, materials, compositions, and devices to first form plurality of isolated wells on a solid substrate and then to carry out plurality of chemical reactions in the isolated wells, in parallel, and on the same substrate.

Abstract: The disclosure relates to a photoreactor for performing photocatalytic reactions with a particulate photocatalyst loaded in the reactor. The photoreactor includes an internal wall having an outer surface and defining an interior volume, and a transparent external wall having an outer surface and an opposing inner surface. The internal and external walls are spaced apart so that they together define a reaction volume between the walls. The photoreactor further includes an external light transmission apparatus, such as a light source and/or a light guide, positioned around the external wall and being adapted to transmit light through the external and into the reaction volume. When a particulate photocatalyst loaded in the reaction volume is irradiated by external light transmission apparatus while a reactant is flowing through the reaction volume, a photocatalytic reaction can be performed to form a desired reaction product.

Abstract: This disclosure provides systems and methods for the on-demand synthesis, separation, purification and formulation of chemicals, and particularly for the on-demand production of pharmaceutical products. More particularly, the disclosure provides continuous-flow on-demand systems, comprising one or more reagent holding/dispensing containers, continuous-flow chemical synthesis modules and/or one or more separation, crystallization, filtration, wash and/or formulation modules, additionally comprising automated detection systems and methods for monitoring reagents, products and processing parameters and automated control systems and methods for controlling processing conditions and parameters.

Abstract: In a reactor apparatus including a reactor having a straight body, an agitation shaft, and an agitating blade, dimensions of the straight body, dimensions of the agitating blade, and a set value of a number of rotations of the agitation shaft satisfy a relationship represented by N(b/d)(L/D)/n?6.0. N represents a number of agitating blades, b represents a maximum value [m] of blade widths of the agitating blades, d represents a maximum value [m] of blade diameters of the agitating blades, L represents a length [m] of the straight body in an extending direction, D represents a maximum value [m] of diameters of inscribed circles substantially inscribed in the straight body, and n represents the set value of the number of rotations [rps] of the agitation shaft.

Abstract: A reactor apparatus includes a reactor having a tubular shape, and a plurality of first cooling pipes arranged inside the reactor, for circulating a coolant. Each of the plurality of first cooling pipes has a serpentine portion that extends while repeatedly bending. The serpentine portion includes a plurality of extending portions that extend linearly or extend while curving, and a plurality of bending portions which couple ends of two adjacent extending portions, among the plurality of extending portions. At least two of the plurality of first cooling pipes have different distances from an inner wall surface of the reactor.

Abstract: A sequestration system includes: an electrolysis part having an electrolysis cell having an anode, a cathode, an anode flow path facing on the anode, and a cathode flow path facing on the cathode; and a reaction part configured to switch a first operation and a second operation, the first operation including producing solid carbon using a catalyst from a first raw material containing a first fluid to be introduced from the cathode flow path, and the second operation including performing a reaction of a second raw material containing a second fluid to be introduced from the anode flow path and solid carbon to be deposited on the catalyst to remove at least a part of the deposited solid carbon from the catalyst.

Abstract: Provided is an apparatus for an aldol condensation reaction having high productivity at low cost. Specifically, the apparatus for an aldol condensation reaction according to the present invention has an effect of having high productivity by preventing a drop in a conversion rate due to an increase in a residence time when increasing a facility scale, allows conditions of raising a concentration of a catalyst and a temperature, and has an effect of minimizing a content of the catalyst used at the same yield as compared with a conventional apparatus. In addition, costs required for increasing a facility scale may be minimized without adding a device such as a pump separately, and an amount of harmful wastewater produced may be minimized.

Abstract: A synergistic composition can be used to treat water containing nitrogen compounds and phosphorus compounds. The synergistic composition includes iron filings, clay particles, aluminum particles, and sand particles. The iron filings, clay particles, and aluminum particles act synergistically to remove nitrogen compounds and phosphorus compounds from water. Specifically, the clay particles attract the nitrogen compounds and the phosphorus compounds to be absorbed onto a surface of the iron filings and the clay particles. The aluminum particles react with the nitrogen compounds via an oxidation reaction to form ammonia compounds, and react with the phosphorus compounds to produce aluminum phosphate. As such, the synergistic relationship between the iron filings, clay particles, and aluminum particles remove nitrogen and phosphorus compounds from water and recover the compounds in usable forms, namely, ammonia and aluminum phosphate.

Abstract: Provided are a mercapto group-loaded layered double hydroxide (LDH)-based magnetic composite particle, and a preparation method and use thereof. The method includes: dissolving a water-soluble divalent magnesium salt and a water-soluble trivalent aluminum salt in water to obtain a mixed salt solution; pumping ammonia water into the mixed salt solution, and performing reaction I under stirring, subjecting an obtained product to centrifugation, and washing product obtained with deionized water; mixing the product with water, ethanol, and a coupling agent KH-580 to obtain a mixture, subjecting the mixture to reaction II while stirring to obtain mercapto group-loaded LDH; mixing the mercapto group-loaded LDH with ferroferric oxide and sodium alginate, adding deionized water thereto, and stirring to obtain a homogeneous mixed solution; adding the homogeneous mixed solution into a calcium chloride solution dropwise to form a magnetic bead; and leaving the magnetic bead to harden, and then washing and drying.

Abstract: A method of forming a product for separating gases includes forming a three-dimensional ceramic support, heating the three-dimensional ceramic support at a temperature for an effective duration of time to result in the conductive ceramic material having a plurality of intra-material pores, and incorporating a sorbent additive into the intra-material pores of the conductive ceramic material. Moreover, the three-dimensional ceramic support includes an electrically conductive ceramic material configured for joule heating.

Abstract: The present disclosure relates to compositions, devices and methods for removing/filtering out microorganisms from a given fluid. The composition of the present invention comprises a non-water imbibing, biocompatible filament and at least one affinity ligand that is capable of capturing the microorganism(s). The invention also discloses methods for detection, diagnosis, and/or treatment.

Abstract: Disclosed herein are embodiments of matrixes made of a porous size exclusion support and a cationic moiety for separating one or more small molecules from one or more large molecules in a sample using differences in one or more properties such as the size of the molecules, charge of the molecules, the isoelectric point (pI) of the molecules, and/or any combination of these properties including methods, systems, and kit embodiments. Also disclosed herein are embodiments of a method of making the matrixes and using the matrixes for separating small molecules from one or more large molecules in a sample.

Abstract: The instant disclosure sets forth a process for re-activating a mineral residue. The process includes providing a mineral residue, which includes a core and a shell around the core. In certain examples, the core comprises calcium (Ca), magnesium (Mg), or a combination thereof. The Ca and Mg is not present as elemental Ca or Mg but rather as a compound of Ca or of Mg, such as but not limited to Ca(OH)2 or Mg(OH)2. In certain examples, the shell comprises an oxide, a hydroxide, a carbonate, a silicate, a sulfite, a sulfate, a chloride, a nitrate, or nitrite, of calcium (Ca) or of magnesium (Mg), or a combination thereof. The process includes (a) fractionating the mineral residue; (b) contacting the mineral residue with an acid and fractionating the mineral residue; or (c) contacting the mineral residue with a base and fractionating the mineral residue. As a result, the mineral residue's core is exposed.

Abstract: Methods for synthesizing a water-soluble titanium-silicon complex are disclosed herein. The titanium-silicon complex can be utilized to produce titanated solid oxide supports and titanated chromium supported catalysts. The titanated chromium supported catalysts subsequently can be used to polymerize olefins to produce, for example, ethylene based homopolymer and copolymers.

Abstract: A composite oxidation catalyst for use in an exhaust system for treating an exhaust gas produced by a vehicular compression ignition internal combustion engine is disclosed. The composite oxidation catalyst comprises a honeycomb flow-through substrate monolith and two catalyst washcoat zones arranged axially in series on and along the substrate surface.

Abstract: A method for preparing a supported Ru and/or Ni catalyst includes mixing a magnesium precursor, a zinc precursor, or a nickel precursor with an aluminum precursor in solid phase to form a first mixture; adding an auxiliary agent to the first mixture to form a second mixture, wherein the auxiliary agent is to increase a specific surface area; calcining the second mixture at a first temperature to obtain a spinel carrier; placing the spinel carrier in a solution of a Ru and/or Ni metal salt to impregnate the spinel carrier with the Ru and/or Ni metal salt to obtain an impregnated carrier; and after drying, calcining the impregnated carrier at a second temperature to obtain the supported Ru and/or Ni catalyst.

Abstract: Disclosed are a Ni-based catalyst for an unsteady-state trace CO, methanation reaction, and a preparation method thereof. The Ni-based catalyst according to the disclosure is composed of an active metal Ni and an oxide support, wherein the oxide support is composed of a rare earth oxide (REO) and an inert oxide; and the rare earth oxide and the inert oxide exhibit an excellent synergistic effect to ensure both high reactivity and weak adsorption and desorption interference. The Ni-based catalyst has a mass percentage of the active metal Ni of 40 wt. % to 90 wt. %, and a mass percentage of the REO of 0.5 wt. % to 20 wt. %, a balance being the inert oxide. The preparation method of the disclosure is a co-precipitation method, including a direct mixing for co-precipitation, a constant-speed dropwise addition for co-precipitation, and a microchannel mixing for co-precipitation.

Abstract: The present technology provides a fluid catalytic cracking (FCC) catalyst composition that includes a Y-zeolite that includes a rare earth element or oxide thereof and an alumina matrix, wherein the alumina matrix includes y-AhCb or pseudo-boehmite and a dopant; and the dopant is selected from a Group IIIB metal, Group IVB metal, Group IV A element, Group VA element, an oxide thereof, or a combination of two or more thereof.

Abstract: A process for preparing a catalytic cracking catalyst includes steps of mixing raw materials including a rare earth-containing NaY molecular sieve obtained by contacting a NaY molecular sieve with a rare-earth salt solution or a mixed solution of rare-earth salt solution and ammonium salt solution, filtering, and water-washing, an inorganic oxide binder and a natural mineral, slurrying and shaping into shaped bodies; hydrothermally calcining shaped bodies in an atmosphere condition where a pressure is externally applied and an aqueous solution containing an acidic substance or an alkaline substance is externally added; and then ammonium-exchanging to remove the alkali metal. The present invention optimizes and shortens the preparation process of the catalyst, which can reduce the preparation cost, and the prepared catalyst has excellent heavy oil conversion ability, higher gasoline and diesel yield, lower coke selectivity, and relatively reduces the used amount of the molecular sieve in the catalyst.

Abstract: A novel synthetic crystalline molecular sieve material, designated boron SSZ-41 is provided. The boron SSZ-41 is a boronzincosilicate molecular sieve having the framework structure of SSZ-41. It can be synthesized using 1,1?-(1,4-butanediyl)bis[4-aza-1-azoniabicyclo[2.2.2]octane] dications as a structure directing agent. The boronzincosilicate SSZ-41 may be used in organic compound conversion reactions and/or sorptive processes.

Abstract: Zeolite catalysts and systems and methods for preparing and using zeolite catalysts having the CHA crystal structure are disclosed. The catalysts can be used to remove nitrogen oxides from a gaseous medium across a broad temperature range and exhibit hydrothermal stability at high-reaction temperatures. The zeolite catalysts include a zeolite carrier having a silica-to-alumina ratio from about 15:1 to about 256:1 and a copper to alumina ratio from about 0.25:1 to about 1:1.

Abstract: Disclosed herein are methods for preparing isotopically modified polyunsaturated lipids containing 1,4-diene systems involving selective isotopic modification of one or more bis-allylic positions of the polyunsaturated lipids in the presence of a transition metal catalyst.

Abstract: A method for making a magnetic-nanoparticle-supported catalyst includes reacting a ferrocenyl phosphine compound with an amino alcohol compound to form a ligand having a phosphine group, an amine group and at least one hydroxyl group; anchoring the ligand to a surface of magnetic nanoparticles via an oxygen atom of the hydroxyl group to form a ligand complex; combining the ligand complex with a metal precursor comprising Rh to bind the metal precursor with the ligand complex and form the magnetic-particle-supported catalyst. The magnetic-particle-supported catalyst is a Rh complex of magnetic-Fe3O4-nanoparticle-supported ferrocenyl phosphine catalyst.

Abstract: A catalytic system comprising a REDOX catalyst and a porous polymeric matrix wherein the porous polymeric matrix has pores with a size from 1 to 1000 nm and it is covalently functionalized with functional groups R1 or, alternatively, with functional groups R?1 and R2. The REDOX catalyst comprises an isoalloxazine moiety which has one or more functional groups R3; R1 and R2 are capable of forming non-covalent reversible interactions with R3; R1 and R2 are in a molar concentration excess with respect to the molar concentration of the REDOX catalyst; and R1 and R?1 are electron donor or electron acceptor groups having a REDOX potential between +2.70 to ?2.5 V as determined by cyclic voltammetry using an Ag/AgCl electrode as reference.

Abstract: In a photocatalyst which is obtained by adding a co-catalyst to semiconductor particles containing strontium titanate and which causes a water decomposition reaction in which water molecules are decomposed into oxygen molecules and hydrogen molecules according to light emission, the semiconductor particles are doped with barium or additionally with scandium. A method of synthesizing a semiconductor for the photocatalyst includes a process of synthesizing semiconductor particles containing strontium titanate doped with barium by mixing barium titanate or additionally with scandium oxide into strontium chloride or mixing strontium titanate or additionally scandium oxide into strontium chloride and barium chloride and performing firing.

Abstract: A process for producing an eggshell catalyst, comprising the coating of the outer surface of a geometric shaped support body with a catalytically active multielement oxide or a powder P, wherein the powder P, after being coated, is converted by thermal treatment to a catalytically active multielement oxide, and one or more liquid binders, wherein the coating is conducted in a horizontal mixer and the Froude number during the coating in the horizontal mixer is from 0.0160 to 0.1200.

Abstract: A method for activating a catalyst is described comprising the steps of: (i) installing a reduced and passivated catalyst containing crystallites of a catalytic metal comprising nickel, cobalt or iron in elemental form encapsulated by a layer comprising an oxide of the catalytic metal in a reactor, such as a steam methane reforming reactor, in which it is to be used, and (ii) heating the reduced and passivated catalyst in the reactor under a vacuum or an inert gas to a temperature in the range (TT?X) to (TT+Y), where TT is the Tammann temperature of the catalytic metal in elemental form in degrees Centigrade, X is 400 and Y is 200, to form a catalytically active surface on the catalyst without requiring the application of a reducing gas.