Abstract: An apparatus for an inertial separation of air in an electric aircraft, wherein the apparatus includes an intake duct configured to intake an airflow, an inertial air separator configured to separate the airflow into a clean airflow and a dirty airflow, a propulsor configured to intake the clean airflow, wherein the propulsor includes a stator and a rotor, and a heat exchanger configured to intake the dirty airflow.

Abstract: A filter holder comprises: a plurality of filter frames disposed such that at least some thereof are adjacent to each other; and a folding member which supports filter frames, from among the plurality of filter frames, adjacent to each other so as to be rotatable with respect to each other. The folding member comprises: a folding part which has a predetermined thickness and is flexible so as to be foldable by means of rotation of the adjacent filter frames adjacent with respect to each other; and a plurality of edge parts which are connected to the respective sides of the folding part with the folding portion therebetween and rotate together with the adjacent filter frames, and wherein when viewed from a cross-section of the folding member, the edge parts may have a greater thickness than the folding part.

Abstract: An intelligent filter construction for household appliances, in particular for drying/washing-drying machines, for separating solid particles from liquid or gaseous fluids, comprises a synthetic monofilament precision fabric material, of a weft and warp type, with which is integrally associated a capacitive sensor adapted to measure in real time values of a moisture in an air flow passing through the fabric material thereby optimizing the household appliance operating cycle.

Abstract: An air intake unit, a compressor drawing atmospheric air through the air intake unit into the compressor unit, a cooling unit which cools the compressed air, a filter unit which filters the cooled air, a gas separator which separates the filtered air, a separated gas outlet which receives the separated gas, and a heat exchange apparatus comprising a body having a first fluid inlet and outlet, a second fluid inlet and outlet, a first fluid conduit between the first fluid inlet and outlet, and a second fluid conduit between the second fluid inlet and outlet. The heat exchange apparatus allows heat exchange between conduits and is arranged to receive compressed atmospheric air at the first fluid inlet and supply it from the first fluid outlet to the cooling unit, and receive filtered air at the second fluid inlet and supply it from the second fluid outlet to the gas separator.

Abstract: An air filter for spray coating, comprising: a housing designed for showing a cuboid shape, with a face forming an air inlet and an opposed face forming an air outlet; one or more accordion panels with fold lines, to be accordion folded about the fold and to be located in the housing for forming a filtering barrier; the one or more accordion panels of the filtering barrier comprising at least one pair of flap portions configured to be folded to form a converging profile followed aeraulically by a trapping chamber formed by one of the accordion panels, and openings forming escape lateral passages of the trapping chamber(s).

Abstract: A particle agglomeration system for improving filtering capacity of an HVAC system is disclosed. The system may include a first plate. The first plate may include a first sound generator. The system may include a second plate. The second plate may include a second sound generator. The system may include a frame. The frame may be configured to position the first plate relative to the second plate. A standing sound wave may be formable between the first sound generator and the second sound generator.

Abstract: Tungsten precursors with high purity and methods for purifying tungsten precursors are provided. The method for purifying a precursor may comprise at least one of the following steps: obtaining a source vessel containing WCl4, WOCl4, and one of WCl5 or WCl6; separating the WCl5 or the WCl6 from at least a first portion of the WOCl4; separating the WCl5 or the WCl6 from at least a second portion of the WOCl4; recovering a precursor in a collection vessel; or any combination thereof.

Abstract: An air treatment system for at least partially removing at least one gaseous contaminant contained in indoor air of a room structured for human occupants. The system may comprise an air treatment assembly having an indoor air inlet configured to receive indoor airflow directly from a room, a regenerable adsorbent material configured to adsorb at least one gaseous contaminant contained in the indoor airflow, at least one airflow element for directing the indoor airflow to flow through the air treatment assembly, an indoor air outlet for expelling the indoor air, from the air treatment assembly back into the room, a purge air inlet configured to receive and direct purge air over and/or through the adsorbent material for removal of at least a portion of the at least one gaseous contaminant, and a purge air outlet for expelling the purge air out of the air treatment assembly.

Abstract: The present invention provides a system of capturing carbon dioxide (CO2) and other gases from combustion engines. The system includes a housing having a plurality of compartments fluidly connected to one another. The housing can be disposed within an exhaust system of a vehicle to capture CO2 prior to being expelled therefrom. The compartments form a cartridge that is removable from the housing and interchangeable with a second cartridge. Each of the end compartments are closed with a semipermeable filter that allows gases and small molecules to pass through, but not solids or liquids. A first compartment is filled with activated charcoal or silica gel to adsorb CO2, wherein a second compartment is filled with a nitrogen containing compound, such as ammonia. A chemical reaction occurs between the nitrogen and remaining gases forming an inert byproduct, such as, ammonium carbonate, ammonium bicarbonate, ammonium carbamate, and/or urea.

Abstract: The present invention relates to a system for treating gaseous hydrogen, comprising an inlet (10a) for supplying gaseous hydrogen, a drying unit (30) with an active drying material for removing moisture from the supplied hydrogen, an adsorption unit (50) with an active adsorption material for adsorbing impurities from the dried hydrogen, and an outlet (10b) for drawing off treated hydrogen. According to the invention, the mass ratio between the active drying material and the active adsorption material is in the range of 1.5:1 to 50:1. The invention further relates to a plant comprising such a system for providing compressed treated gaseous hydrogen and a method for treating gaseous hydrogen.

Abstract: Provided are apparatus and systems for performing a swing adsorption process. This swing adsorption process may involve performing dampening for fluctuations in the streams conducted away from the adsorbent bed unit. The process may be utilized for swing adsorption processes, such as rapid cycle TSA and/or rapid cycle PSA, which are utilized to remove one or more contaminants from a gaseous feed stream.

Abstract: Methods, systems, and apparatus for setting a rotational speed of a rotor of a compressed-gas dryer system, without communication from an associated compressor (e.g., without knowing compressor speed or load). Such communication is not always practical or possible (e.g., in the case where a dryer may be provided by a different manufacturer as compared to the compressor). In such a case, the speed or load at which the dryer should run can be determined by making an FAD calculation, so as to determine the volumetric flow rate through the inlet into the drying zone of the dryer. This measurement can be made at the inlet (a venturi or other nozzle), or elsewhere in the system (e.g., other inlets or outlets). Determination of flowrate of compressed-gas to be dried can be done independent of any communication with the compressor. This can be done by measuring inlet temperature, pressure, and pressure drop.

Abstract: The present invention aims to provide a carbon dioxide absorbent that can efficiently absorb, fix, and simply separate and recover carbon dioxide in the air. The present invention relates to an atmospheric carbon dioxide absorbent consisting of an amine selected from the group consisting of m-xylylene diamine, benzylamine, phenethylamine, p-methoxybenzylamine, and p-trifluoromethylbenzylamine, and water, and having the amine content of 1 to 50 wt % with respect to the total amount. The present invention also relates to a method for generating carbon dioxide which uses the aforementioned carbon dioxide absorbent and is simple and superior in energy efficiency.

Abstract: Method and system for electrochemically compressing hydrogen. In one embodiment, the system includes a membrane electrode assembly (MEA) that includes a polymer electrolyte membrane (PEM), an anode, and a cathode. First and second gas diffusion media are positioned adjacent the cathode and anode, respectively. A humidifying membrane is positioned next to the second gas diffusion medium on a side opposite the anode. A water supply is connected to the humidifying membrane, and a hydrogen gas supply is connected to the second gas diffusion medium. A hydrogen gas collector including a back pressure regulator is connected to the first gas diffusion medium. Separators, positioned on opposite sides of the MEA, are connected to a power source. In use, hydrogen is electrochemically pumped across the MEA and collected in the hydrogen gas collector. The PEM is kept properly humidified by the humidifying membrane, which releases water into the second gas diffusion medium.

Abstract: A biogas collection and purification system that includes a plurality of sources of biogas and a network of conduits configured to convey the biogas from the sources to a central processing facility for processing the biogas into methane. The central processing facility removes impurities to convert biogas to biomethane and may include an H2S removal stage; an activated carbon scrubber; a gas drier; and a carbon dioxide removal stage. The facility also has a biomethane gas compressor configured to deliver the biomethane for use in power plants, for CNG production. Ancillaries to the system include fuel cells for direct electricity generation from biogas/biomethane.

Abstract: Methods and systems integrate direct carbon capture and desalination processes to various degrees, benefiting from synergies in the combined processes. A method includes receiving an input liquid comprising a brine reject stream from a water treatment facility and pre-treating the input liquid. The pre-treatment includes one or more of filtration, a reverse osmosis, and ion exchange. The method also includes performing an electrochemical process on the input liquid to produce at least one hydroxide-rich stream and capturing CO2 from air using the hydroxide-rich stream and a passive air capture system, thereby producing a liquid carbonate solution containing air-captured CO2. In some cases byproducts and recovered water can be used by the water treatment facility and/or the carbon capture process.

Abstract: The invention present provides a method (and suitable apparatus) to convert biomass to ethanol, comprising gasifying the biomass to produce raw syngas; feeding the raw syngas to an acid-gas removal unit to remove at least some CO2 and produce a conditioned syngas stream; feeding the conditioned syngas stream to a fermentor to biologically convert the syngas to ethanol; capturing a tail gas from an exit of the fermentor, wherein the tail gas comprises at least CO2 and unconverted CO or H2; and recycling a first portion of the tail gas to the fermentor and/or a second portion of the tail gas to the acid-gas removal unit. This invention allows for increased syngas conversion to ethanol, improved process efficiency, and better overall biorefinery economics for conversion of biomass to ethanol.

Abstract: An indoor smoker includes an exhaust duct and an air handler fluidly coupled with the exhaust duct for urging a flow of smoke from a smoking chamber, through the exhaust duct, and out of a discharge vent. A catalytic converter is positioned within the exhaust duct, the catalytic converter comprising a catalytic element and a catalyst heater, and an air quality monitoring system is operably coupled to the exhaust duct. A controller is configured to measure an air quality of the flow of smoke passing through the exhaust duct using the air quality monitoring system, determine that an emissions control failure has occurred based at least in part on the air quality, and stop the flow of smoke in response to determining that the emissions control failure has occurred.

Abstract: Catalyst for the abatement of ammonia from the exhaust of gasoline internal combustion engines The present invention relates to a catalyst comprising a carrier body having a length L extending between a first end face and a second end face, and differently composed material zones A, B and C arranged on the carrier body, wherein material zone A comprises rhodium and/or nickel and/or cerium; material zone B comprises platinum; and material zone C comprises a zeolite which is able to store ammonia and to catalyze the selective catalytic reduction of NOx.

Abstract: A system for producing desalinated water from seawater or other saline water, wherein the system comprises the following equipment features or equipment items, in a typical direction of flow: a subsea seawater inlet, a subsea pretreatment stage, at least comprising one or more of a subsea filter and/or a subsea seawater pre-treatment unit and/or a subsea coarse screen unit, and/or a hydrocyclone, a subsea feed pump, fluidly coupled to, a subsea RO unit, a subsea product pump fluidly coupled to a RO unit product outlet, a product line fluidly coupled to the subsea product pump, and a RO unit reject outlet, preferably coupled to a reject line. The system is distinctive in that: the subsea seawater inlet is at a depth below or within the thermocline layer of the seawater, that is below the epipelagic zone, or as close as feasible if the local depth is insufficient to reach the thermocline layer, and wherein the system preferably is without any barrier fluid supply to the subsea pumps.

Abstract: A solid type nano-pore sequencer is arrayed easily. In a liquid column separation device including first and second base materials, a liquid feeding unit supplies fluids to a gap between the two base materials. Hydrophilic and hydrophobic regions are disposed on a surface of the second base material, and the hydrophilic region is disposed to oppose a predetermined position of the first base material where a substance to be measured is made to pass through. Also, a flow passage space includes at least one inlet and outlet through which fluids can flow in and out. A representative length of the hydrophilic region is made larger than a distance between the first and second base materials, and thereby a liquid column capable of connecting the first base material and the second base material is formed by making two or more immiscible fluids to flow by the liquid feed unit.

Abstract: The present concentration device includes a membrane module having a first and a second flow paths that are separated by a semipermeable membrane, the module including a U-shaped tube in which the semipermeable membrane is disposed, a first flow-path-inlet and a first flow-path-outlet connection parts, and a second flow-path-inlet and a second flow-path-outlet connection parts, the device including an introducing unit for introducing a subject solution with a predetermined pressure into the first flow path from the first flow-path-inlet connection part, separating the subject solution into a concentrate and a permeate through the semipermeable membrane, passing the permeate through the second flow path, draining the concentrate from the first flow-path-outlet connection part, introducing the subject solution with a pressure lower than the predetermined pressure into the second flow path from the second flow-path-inlet connection part, and draining a diluent diluted with the permeate, from the second flow-path

Abstract: A membrane filter for submerged operation for filtering a liquid, comprising membrane elements and geyser elements for flushing the membrane elements in pulses using a gas, each membrane element having: hollow fiber membranes secured in a base element, each hollow fiber membrane having a lumen into which a liquid permeate is filterable out of the liquid, a permeate collection cavity connected to the lumens of the hollow fiber membranes for collecting the permeate from the hollow fiber membranes, a permeate outlet for discharging the permeate out of the permeate collection chamber, and a tubular housing enveloping the hollow fiber membranes of the membrane elements and penetrated by the permeate outlet, wherein the geyser elements are installed below the membrane elements, and each of the geyser elements having: a gas collection cavity and an outlet device for discharging the gas in pulses upwards out of the gas collection cavity.

Abstract: The present invention provides a method for analyzing a halogenated structure in a composite semipermeable membrane. The method for analyzing a composite semipermeable membrane according to the present invention includes: a step A for immersing the composite semipermeable membrane in a solution containing alkali and at least one of nicotinamide and a derivative thereof; and a step B for performing fluorescence analysis on the solution obtained in step A.

Abstract: Porous liquid-filtering membranes are provided having a boundary region substantially surrounding the pore region and having greater tear resistance than the pore region.

Abstract: Various embodiments of a system and method for enriching a concentration of components of interest in an air flow are described. The system includes an apparatus for enriching a concentration of components of interest in an air flow. The apparatus includes a chamber and a tube having a tube wall made of a selectively permeable material positioned within the chamber. A first end of the tube is connected to the inlet port of the chamber and a second end of the tube is connected to the outlet port of the chamber. The selectively permeable material has a lower permeability to components of interest than to inert gases, and the selectively permeable material is non-reactive with components of interest. The apparatus is configured to receive a sample stream and the chamber is maintained at a chamber pressure that is different than a stream pressure of the sample stream.

Abstract: A preparation method of a high-moisture-permeability fluorine-containing super-oleophobic microporous membrane is provided having the following steps: (1) preparing a white opaque mixture of fluorine-containing polymers: adding the materials in sequence according to a weight ratio of A50%˜90%:B3%˜25%:C0%˜35%:D0 %˜3%, and stirring and mixing uniformly in a non-shear manner; A is a blend of a high molecular weight polytetrafluoroethylene dispersion resin and a fluorine-containing ion exchange resin; B is a fluorine-containing alkyl acrylate monomer, or a fluorine-containing alkyl methacrylate monomer, or a mixture thereof; C is a polyurethane acrylate prepolymer, or a fluorine-free alkyl acrylate monomer, or a mixture thereof; D is a high temperature free radical initiator; (2) pouring the white opaque mixture into the blank pressing column barrel, and pressing a blank; (3) calendering into strips; (4) stretching and thermally shaping to form a membrane.

Abstract: The present disclosure relates to a polyether block polyamide/polydimethylsiloxane (PDMS) composite membrane for gas separation, and a preparation method and use thereof, and belongs to the technical field of membrane separation. In the present disclosure, an amphoteric copolymer PDMS-polyethylene oxide (PEO) (PDMS-b-PEO) is introduced into an intermediate layer to adjust the interfacial binding performance, thereby promoting preparation of an ultra-thin polyether block polyamide composite membrane. Studies have shown that the surface enrichment of PEO segments not only inhibits a dense SiOx layer formed due to a plasma treatment of a PDMS intermediate layer, but also provides additional hydrophilic sites and interfacial compatibility for the subsequent selective layer. The use of PDMS-b-PEO in an intermediate layer allows the successful preparation of a selective layer with a thickness of about 50 nm.

Abstract: Current cartridge-style mixers due not have the ability to measure mixing performance nor determine the need for maintenance based on performance. Risks of non-homogeneous mixing and insufficient maintenance can exist with cartridge-style mixers. A mixing system comprises a mixing apparatus, a first switch, a magnetic switch, and a controller. The mixing apparatus is configured to receive a cartridge and to mix a material. The mixing apparatus comprises a linear actuator configured to translate the cartridge or plunger in a vertical direction and a spindle configured to rotate a plunger. The first switch is configured to measure a number of strokes per unit of time of operating the linear actuator. The magnetic switch is configured to measure a speed of the spindle. The controller is configured to receive one or more mixing parameters, actuate the spindle and the linear actuator, and actuate a light to indicate if there was sufficient mixing.

Abstract: The specification relates to the device for thermal-catalytic decomposition—pyrolysis of waste organic materials, comprising: the reservoir, linked by means of the supply line with the reactor, where in the line is arranged the valve, wherein the reactor contains the heating element and/or the radiation source situated approximately up to the maximum level corresponding to ? of the height from the bottom of the reactor; and the temperature sensor placed up to the maximum level corresponding to ? of the height from the bottom of the reactor, wherein the output line protrudes from the lid of the reactor with the linked cooler, wherein the end of the output line is connected to the orifice on the receiver to contain liquefied products via the branch to exhaust product gases.

Abstract: A reactor for the decomposition of hydrocarbons includes: a structural catalyst for the decomposition of hydrocarbons having a structure in which a reaction gas may flow from one end to the other end when installed properly in a reaction chamber; and the heat source that is installed inside or outside the reaction chamber and capable of heating the structural catalyst for the decomposition of hydrocarbons. The structural catalyst for the decomposition of hydrocarbons has a shape encompassing a boundary wall surface or a boundary side that separates the structural catalyst for the decomposition of hydrocarbons from the heat source when viewed from a cross-section vertical to a direction of flowing a reaction gas, as well as the reaction furnace in which the reactor is embedded together with a catalyst module.

Abstract: Vapor delivery apparatus configured for generating a gaseous precursor from solid source precursor particles in a fluidized bed are disclosed. In addition, vapor phase reactors including a vapor delivery apparatus including a fluidized bed of solid precursor are also disclosed. Methods for monitoring and a controlling a vapor delivery system including a fluidized bed also disclosed.

Abstract: Disclosed herein is a method for generating capsules with a hydrogel matrix. The method includes the steps: providing in a first chamber a dispersed aqueous phase, the dispersed aqueous phase including water and a hydrogel matrix-forming agent, in which the hydrogel matrix-forming agent is configured to form a hydrogel matrix upon exposure to a gelation inducer; providing in a second chamber a continuous oil phase, the continuous oil phase including oil and at least one first surfactant. The first and second chambers are fluidic connected by one or more channels, preferably by micro-channels. The method further includes: guiding the dispersed aqueous phase from the first chamber through the one or more channels into the second chamber to form an emulsion or dispersion of the dispersed aqueous phase in the continuous oil phase and exposing the hydrogel matrix-forming agent to a gelation inducer to form capsules with a hydrogel matrix.

Abstract: The invention relates to an apparatus for analyzing reaction systems with a liquid phase (13) and a gas phase (15), the apparatus (1) comprising at least two tank reactors (3), a common feed line (5), a common drain line (25) for the liquid phase and a common drain line (21) for the gas phase, each tank reactor (3) being connected to the common feed line (5) by a supply line (7), to the common drain line (25) for the liquid phase by a liquid withdrawal line (27) and to the common drain line (21) for the gas phase by a gas withdrawal line (23), wherein the pressure in each tank reactor (3) is controlled by one of: (a) a pressure control (31) in the common feed line (5); (b) a pressure line (29) which is connected to the gas space of each tank reactor (3); (c) a pressure control (31) in the common drain line (21) for the gas phase and a flow restrictor (33) in the common drain line (25) for the liquid phase or a pressure control (31) in the common drain line (25) for the liquid phase and a flow restrictor (3

Abstract: The present invention relates to a reaction unit (10) configured to receive a reaction solution or culture media and configured to be placed inside a thermocycler, said reaction unit (10) comprising an elongated hollow body (12) extending along a flowing axis X, the hollow body (12) thus displaying a first opening (14) at its first extremity (16) and a second opening (18) at its second extremity (20). The walls of the hollow body (12) are at least partially made of a thermally conductive material. The reaction unit (10) further comprises at least one filter element (22) extending inside the hollow body (12), the filter element (22) being sealingly secured to the walls of the hollow body (12) over its complete circumference, leading any fluid flowing from the first opening (14) to the second opening (18) to cross the at least one filter element (22).

Abstract: The present disclosure relates to a furnace comprising: a plurality of groupings, wherein each grouping in the furnace is adjacent to each other and separated by a gap, wherein each grouping comprises: (a) one row of tubes and optionally additional rows of tubes comprising a plurality of tubes containing a catalyst for converting a gaseous feed, wherein each row of tubes is parallel to each other; (b) at least two rows of burners comprising having a first and second row of outer burners and optionally additional rows of burners comprising a plurality of burners, and as described herein, (c) wherein the plurality of burners within each grouping is configured such that the ratio of B/G is greater than 1.3 and the ratio of B/W is less than 1.3, wherein W, B and G are as defined herein.

Abstract: A reactor for carrying out a chemical reaction using multiphase alternating current, includes a reactor chamber surrounded by thermally insulating reactor walls and multiple substantially straight reaction tubes. The reaction tubes run between at least one tube inlet opening and at least one tube outlet opening in opposite reactor walls and consist of a material that permits electrical resistance heating. Two electrically conductive bridges spaced apart along the reaction tubes are provided, each of which electrically conductively connects the reaction tubes to one another. Electrically conductive power input arrangements are provided extending through one or more input openings in one of the reactor walls. Each reaction tube is electrically conductively connected to one of the power input arrangements. Each power input arrangement is electrically conductively connected between the bridges to one of the reaction tubes and is connected or connectable to one of the phases of the alternating current.

Abstract: A synthetic fuel production system and related techniques are disclosed. In accordance with some embodiments, the disclosed system may be configured to produce a liquid fuel using carbon dioxide extracted from the air and hydrogen generated from aqueous solutions by electrochemical means (e.g., water electrolysis). In production of the fuel, the disclosed system may be configured, in accordance with some embodiments, to react the carbon dioxide and hydrogen, for example, to form methanol. The disclosed system also may be configured, in accordance with some embodiments, to utilize one or more subsequent reaction steps to produce a given targeted set of hydrocarbons and partially oxidized hydrocarbons. For example, the disclosed system may be used to produce any one (or combination) of: ethanol; dimethyl ether; formic acid; formaldehyde; alkanes of various chain length; olefines; aliphatic and aromatic carbon compounds; and mixtures thereof, such as gasoline fuels, diesel fuels, and jet fuels.

Abstract: A silicon-based solid amine sorbent for CO2 and the making method thereof including: providing a silicon source liquid which is a silicate solution or a liquid organosilicate, wherein the silicate solution comprises water and a first silicate dissolved in the water; mixing the silicon source liquid with a precipitant to perform a precipitation reaction to obtain a product liquid containing a precipitate, wherein the precipitate is a second silicate or silicic acid; filtering out the precipitate and washing the precipitate with water; mixing the precipitate filtrated out but not dried yet with an organic alcohol and then performing an azeotropic distillation to obtain a dehydrated precipitate; calcining the dehydrated precipitate to obtain a silicon-based support, wherein the silicon-based support is a powder of the second silicate powder or a silica powder; and impregnating the silicon-based support with an organic amine solution and then drying to obtain the silicon-based amine-containing solid sorbent for C

Abstract: This invention provides for removal of toxic heavy metal contamination from water using inositol hexakisphosphate. Inositol hexakisphosphate (InsP6 or IP6 aka phytic acid) is a ubiquitous polyphosphorylated carbohydrate with numerous biological and industrial functions including chelation of cations. IP6 hexa-citrate (IP6-citrate) was synthesized and characterized for use as metal chelator in the purification of water. The synthesized IP6-citrate was used to modify the surface of cellulose and the IP6-citrate-modified cellulose subsequently used to remove Pb, Cr and Cd from aqueous solutions. Atomic Absorption Spectrometry and differential pulse anodic stripping Voltammetry were used to test the levels of the heavy metals in water samples before and after the application of IP6-citrate-modified cellulose. The use of IP6-citrate modified cellulose decreased the amount of Cd, Cr and Pb in the water samples by 95-99%. IP6-citrate modified cellulose was superior to IP6-cellulose alone.

Abstract: A carbon dioxide absorbent containing a polyamine compound (A) having an alicyclic hydrocarbon structure, wherein a content of the polyamine compound (A) is 60% by mass or more.

Abstract: The present invention relates to a method for producing water-absorbent resin particles, the method including crosslinking a polymer by a surface crosslinking agent by reacting the polymer with the surface crosslinking agent in a mixture of a powder of polymer particles containing the polymer and a crosslinking agent solution containing the surface crosslinking agent and water, in which the surface crosslinking agent includes an alkylene carbonate, a use amount (mass) of the surface crosslinking agent is 0.00110 or less with respect to a mass of 1 of a total amount of solid contents of the polymer particles, and a content (mass) of the alkylene carbonate is 0.009 or more and 0.027 or less with respect to a mass of 1 of water in the crosslinking agent solution.

Abstract: A method for producing core-shell porous silica particles including: a step of forming a shell precursor by continuously adding a silica source-containing liquid into an aqueous suspension containing non-porous silica particles, a cationic surfactant, a basic catalyst, and an alcohol under conditions that a pH of the reaction system is from 7 to 13 and a pH value change of the reaction system is 1.5/10 min to form a shell precursor on a surface of non-porous silica particles; and a step of forming a porous shell by removing the cationic surfactant from the shell precursor, to form a porous shell; wherein in the step of forming the shell precursor, when a specific surface area of the non-porous silica particles is Xm2/g, a used amount of the non-porous silica particles is Yg, and a used amount of the silica source is Zcm3, Z/(XY) being from 0.01 to 10.

Abstract: Improved catalytic materials for and methods of oxidative dehydrogenation (ODH) of short chain alkanes or ethylbenzene to the corresponding olefins are disclosed. The disclosed methods use catalysts made by impregnating boron onto the surface of oxidized amorphous carbon, and result in higher selectivity and a lower induction period than methods using conventional ODH catalysts.

Abstract: An object of the present invention is to provide a CeO2—ZrO2-based complex oxide having a sufficiently reduced particle size and a method for producing the CeO2—ZrO2-based complex oxide, and there are provided a complex oxide containing a zirconium element, a cerium element, and optionally another rare earth metal element, wherein D50 and D90 of the complex oxide measured by a laser diffraction scattering particle size distribution measurement method are 0.5 ?m or less and 1 ?m or less, respectively, and a method for producing the complex oxide.

Abstract: A catalyst material includes molybdenum (Mo): vanadium (V). the molar ratio of Mo:V being between 1:0.12 and 1:0.49; tellurium (Te), the molar ratio of Mo:Te being between 1:0.01 and 1:0.30; niobium (Nb), the molar ratio of Mo:Nb being between 1:0.01 and 1:0.30; and beryllium (Be), the molar ratio of Mo:Be being from 1:1 to 1:50.

Abstract: The present invention relates to a novel supramolecular self-assembly, a carbon nitride and a photocatalyst using same, and a manufacturing method therefor. The present invention can provide, by using a supramolecular self-assembly, a carbon nitride having a high N—C?N bonding ratio, a photocatalyst having excellent photocatalytic activity under visible light, and a manufacturing method therefor, the supramolecular self-assembly comprising: a plurality of complex units formed by hydrogen bonding two or more nitrogen-containing compounds to each other; and linker units connecting the plurality of complex units by hydrogen bonds, wherein the nitrogen-containing compounds and the linker units are each independently a —NH group and capable of hydrogen bonding with the —NH group, and the supramolecular self-assembly contains one or more heteroatoms selected from the group consisting of N, S, and O.

Abstract: Disclosed are a hydrogenation catalyst, a preparation method for same, and applications thereof. Also disclosed is a hydrogenation reaction method employing the hydrogenation catalyst. The hydrogenation catalyst of the present invention comprises a binding agent and an active component. The active component comprises nickel and a group VIB metal element. The binding agent comprises zirconium oxide and aluminum oxide. The catalyst of the present invention has nickel serving as the main active ingredient and is inexpensive. Moreover, the catalyst of the present invention exhibits an increased catalytic activity in a hydrogenation reaction of phenolic compounds and specifically provides an increased low-temperature reaction activity. The catalyst of the present invention is applicable in a continuous production process, thus implementing the continuous production of a hydrogenated bisphenol A product and providing the product with high and stable quality.

Abstract: Provided is a process for hydrocracking normal paraffins into lighter normal paraffins with minimal formation of iso-paraffins. The process comprises hydrocracking a hydrocarbon feedstock comprising normal paraffins under hydrocracking conditions. The reaction is run in the presence of a selected catalyst, e.g., an LTA-type zeolite, with a requisite topology and acid site density. The zeolite has a framework type with voids greater than 0.50 nm in diameter, which are accessible through apertures characterized by a longest diameter of less than 0.50 nm and a shortest diameter of more than 0.30 nm. The reaction conducted in the presence of such a selected zeolite produces an n-paraffin rich product.

Abstract: A multifunctional catalyst, a method for producing the same, and a method for using the same are provided. The multifunctional catalyst is applicable for recycling a polyester fabric. The multifunctional catalyst includes a carrier, and a first functional ionic liquid and a second functional ionic liquid that are grafted on the carrier. The carrier is an inorganic composite powder material, and is composed of following chemical components: C: Na—Ni/Al2O3. In a process of recycling the polyester fabric, the multifunctional catalyst simultaneously decolorizes and depolymerizes the polyester fabric. The first functional ionic liquid is used to decolorize the polyester fabric, and the second functional ionic liquid is used to depolymerize the polyester fabric.