Embodiments are directed to a foam comprising the crosslinked reaction product of a maleic anhydride grafted polyolefin elastomer (MAH-g-POE), secondary alcohol, and a high melting point component. The foam comprises greater than or equal to 49 wt. %of the MAH-g-POE and the secondary alcohol. Further embodiments are directed to a process of physically foaming the foam.
C08L 51/06 - Compositions of graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bondsCompositions of derivatives of such polymers grafted on to homopolymers or copolymers of aliphatic hydrocarbons containing only one carbon-to-carbon double bond
C08L 25/02 - Homopolymers or copolymers of hydrocarbons
C08L 31/04 - Homopolymers or copolymers of vinyl acetate
C08J 9/12 - Working-up of macromolecular substances to porous or cellular articles or materialsAfter-treatment thereof using blowing gases generated by a previously added blowing agent by a physical blowing agent
2.
FOAM COMPRISING MALEIC ANHYDRIDE GRAFTED POLYOLEFIN ELASTOMER AND SECONDARY ALCOHOL
Embodiments are directed to a foam comprising the crosslinked reaction product of a maleic anhydride grafted polyolefin elastomer (MAH-g-POE) and greater than 0.4 wt. %of a secondary alcohol. Further embodiments are directed to a process of physically foaming the foam.
C08L 51/06 - Compositions of graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bondsCompositions of derivatives of such polymers grafted on to homopolymers or copolymers of aliphatic hydrocarbons containing only one carbon-to-carbon double bond
C08J 9/12 - Working-up of macromolecular substances to porous or cellular articles or materialsAfter-treatment thereof using blowing gases generated by a previously added blowing agent by a physical blowing agent
Embodiments are directed to a thermally cross-linked ethylene-based polymer comprising an ethylene-based polymer formed by high pressure (greater than or equal to 100 MPa and less than or equal to 400 MPa), free-radical polymerization of ethylene and one or more hydrocarbon-based molecules. Each of the one or more hydrocarbon-based molecules comprises three or more terminal alkene groups. The thermally cross-linked ethylene-based polymer, thermally cross-linked in the presence of oxygen, has a greater melt elongation relative to an ethylene-based polymer not subjected thermal crosslinking in the presence of oxygen. Further embodiments are directed to a process for making the thermally cross-linked ethylene-based polymer.
C08F 8/00 - Chemical modification by after-treatment
C08F 279/02 - Macromolecular compounds obtained by polymerising monomers on to polymers of monomers having two or more carbon-to-carbon double bonds as defined in group on to polymers of conjugated dienes
An effective stripping solution for positive photoresists contains: · more than 70 weight percent water; · From 5 to 19 weight percent alkanolamine; · From 10 to 24 weight percent glycol ether; and · Optionally, essentially no other solvents.
Embodiments are directed to a thermally cross-linked ethylene-based polymer comprising an ethylene-based polymer formed by high pressure (greater than or equal to 100 MPa and less than or equal to 400 MPa), free-radical polymerization of ethylene and one or more cyclicvinylsiloxane molecules. Each of the one or more cyclicvinylsiloxane molecules comprises two or more vinyl groups. The thermally cross-linked ethylene-based polymer, thermally cross-linked in the presence of oxygen, has a greater melt elongation relative to an ethylene-based polymer not subjected thermal crosslinking in the presence of oxygen. Further embodiments are directed to a process for making the thermally cross-linked ethylene-based polymer.
Embodiments are directed to a thermally cross-linked, ethylene-based, rigid article comprising an ethylene-based polymer formed by high pressure (greater than or equal to 100 MPa and less than or equal to 400 MPa), free-radical polymerization of ethylene and one or more hydrocarbon-based molecules. Each of the one or more hydrocarbon-based molecules comprises three or more terminal alkene groups. The thermally cross-linked ethylene-based, rigid article, thermally cross-linked in the presence of oxygen, has a greater melt elongation relative to an ethylene-based, rigid article not subjected thermal crosslinking in the presence of oxygen.
C08F 8/00 - Chemical modification by after-treatment
C08F 279/02 - Macromolecular compounds obtained by polymerising monomers on to polymers of monomers having two or more carbon-to-carbon double bonds as defined in group on to polymers of conjugated dienes
A polyurethane elastomer comprising the reaction product of an aliphatic polyisocyanate comprising a cyclohexane and having 70% trans structure, a polyol, and a chain extender which comprises at least 50 mole percent of a dianiline is useful in making articles such as non-pneumatic rollers. A kit for making such polyurethane elastomer can comprise a first part comprising a pre-polymer which is a reaction product of the polyisocyanate and the polyol and a second part comprising the chain extender.
Polyurethane adhesives may include an isocyanate prepolymer and a polyol component. The isocyanate prepolymer is the reaction product of 35 to 95 wt. % of a polyisocyanate, and 65 to 5 wt. % of a non-dimeric acid based polyester polyol. The non-dimeric acid based polyester polyol may include a reaction product of a primary polyol having a hydroxyl functionality of at least 3 and a weight average molecular weight 800 g/mol or less, a C4 to C20 non-dimeric acid dicarboxylic acid and a C10 to C20 aliphatic mono-carboxylic acid. The polyol component includes 20 to 80 wt. % of a hydrophobic polyol, 3 to 15 wt. % of a phosphate modified polyol, and 10 to 30 wt. % of a vegetable oil polyurethane polyol.
The present invention relates in part to a method for slowing the polyphosphine ligand usage rate in a hydroformylation process. It has been discovered that when a target concentration of total polyphosphorous compounds comprising polyphosphine ligand and polydentate ligand degradation products is maintained in a reaction zone, the usage rate of the polyphosphine ligand may be reduced.
C07C 45/50 - Preparation of compounds having C=O groups bound only to carbon or hydrogen atomsPreparation of chelates of such compounds by reaction with carbon monoxide by oxo-reactions
Embodiments are directed to an ultraviolet (UV) cross-linked, ethylene-based, rigid article comprising an ethylene-based polymer formed by high pressure (greater than or equal to 100 MPa and less than or equal to 400 MPa), free-radical polymerization of ethylene and one or more hydrocarbon-based molecules. Each of the one or more hydrocarbon-based molecules comprises three or more terminal alkene groups. The UV cross-linked, ethylene-based, rigid article has a greater melt elongation relative to an ethylene-based, rigid article not subjected UV crosslinking. Further embodiments are directed to a process for making the UV cross-linked, ethylene-based, rigid article.
C08F 8/00 - Chemical modification by after-treatment
C08F 279/02 - Macromolecular compounds obtained by polymerising monomers on to polymers of monomers having two or more carbon-to-carbon double bonds as defined in group on to polymers of conjugated dienes
Embodiments are directed to a thermally cross-linked, ethylene-based, rigid article comprising an ethylene-based polymer formed by high pressure (greater than or equal to 100 MPa and less than or equal to 400 MPa), free-radical polymerization of ethylene and one or more cyclicvinylsiloxane molecules. Each of the one or more cyclicvinylsiloxane molecules comprises two or more vinyl groups. The thermally cross-linked ethylene-based, rigid article, thermally cross-linked in the presence of oxygen, has a greater melt elongation relative to an ethylene-based, rigid article not subjected thermal crosslinking in the presence of oxygen.
Embodiments are directed to an ultraviolet (UV) cross-linked, ethylene-based, rigid article comprising an ethylene-based polymer formed by high pressure (greater than or equal to 100 MPa and less than or equal to 400 MPa), free-radical polymerization of ethylene and one or more cyclicvinylsiloxane molecules. Each of the one or more cyclicvinylsiloxane molecules comprises two or more vinyl groups. The UV cross-linked, ethylene-based, rigid article has a greater melt elongation relative to an ethylene-based, rigid article not subjected UV crosslinking. Further embodiments are directed to a process for making the UV cross-linked, ethylene-based, rigid article.
Embodiments are directed to an ultraviolet (UV) cross-linked ethylene-based polymer comprising an ethylene-based polymer formed by high pressure (greater than or equal to 100 MPa and less than or equal to 400 MPa), free-radical polymerization of ethylene and one or more hydrocarbon-based molecules. Each of the one or more hydrocarbon-based molecules comprises three or more terminal alkene groups. The UV cross-linked ethylene-based polymer has a greater melt elongation relative to an ethylene-based polymer not subjected UV crosslinking. Further embodiments are directed to a process for making the UV cross-linked ethylene-based polymer.
C08F 297/02 - Macromolecular compounds obtained by successively polymerising different monomer systems using a catalyst of the ionic or coordination type without deactivating the intermediate polymer using a catalyst of the anionic type
Embodiments are directed to an ultraviolet (UV) cross-linked ethylene-based polymer comprising an ethylene-based polymer formed by high pressure (greater than or equal to 100 MPa and less than or equal to 400 MPa), free-radical polymerization of ethylene and one or more cyclicvinylsiloxane molecules. Each of the one or more cyclicvinylsiloxane molecules comprises two or more vinyl groups. The UV cross-linked ethylene-based polymer has a greater melt elongation relative to an ethylene-based polymer not subjected UV crosslinking. Further embodiments are directed to a process for making the UV cross-linked ethylene-based polymer.
A grafted polymer formed from at least the following components a and b: a) at least one polyacrylic acid (PAA), and where some of its acid groups may be neutralized with at least one metal cation; and b) at least one compound of Structure I as described herein.
A composition comprising the following components a) and b) : a) at least one polyacrylic acid polymer (PAA), and b) at least one compound of Structure B below: wherein each of R1, R2, R3, R4, R5, R6, R7 and R8 is independently H, or an alkyl; and nl and n2 are each independently an integer ≥ 1.
The present disclosure provides a composition. In an embodiment, a polyethylene composition is provided and includes (A) at least 25 wt % of a high density polyethylene having (i) a density from 0.950 g/cm3 to 0.970 g/cm3, (ii) a melt index (I2) from 0.2 g/10 minutes to 2 g/10 minutes, and (iii) a molecular weight distribution (Mw(abs)/Mn(abs)) from greater than 4.0 to 30.0. The polyethylene composition also includes (B) a polyethylene enhancer that is an ethylene/C4-C8 α-olefin copolymer having (i) a density from 0.880 g/cm3 to 0.910 g/cm3, (ii) a melt index from 0.2 to 2.0 g/10 minutes, and (iii) LCBf/1000C value less than 0.015. The polyethylene composition has (1) a density from 0.915 g/cm3 to 0.925 g/cm3, (2) a melt index (I2) from 0.3 g/10 minutes to 1.0 g/10 minutes, (3) a Mw(abs)/Mn(abs) value from 5.0 to 11.0, (4) a low M-SCBDI value from 9.0 to 25.0, (5) a high M-SCBDI value from −8.0 to −12.0, (6) a first polyethylene fraction having (a) at least one peak in a temperature range from 40° C. to 79° C., and (b) an average Mw from 100,000 g/mol to 200,000 g/mol on an elution profile via improved comonomer composition distribution (iCCD) analysis method, (7) a second polyethylene fraction having (a) at least one peak in a temperature range from 800 C and 120° C., and (b) an average Mw from 90,000 g/mol to 250,000 g/mol on the elution profile via improved iCCD analysis method, and (8) a ratio of the average Mw of the first polyethylene fraction to the average Mw of the second polyethylene fraction is from 0.6 to 1.2. The present disclosure also provides a film made from the polyethylene composition.
The present disclosure provides for a supported bis(phenoxy-phenyl) (Sup-BPP) catalysts for production of polyethylene in a gas-phase polymerization process. The Sup-BPP catalysts of the present disclosure include an inert support in the presence of an aluminoxane compound, where the aluminoxane compound functions as a binding agent. The Sup-BPP can be mixed with the support and the binder in an inert hydrocarbon. The slurry is then dried, either under reduced pressure or spray dried, to produce the supported Sup-BPP catalyst. The supported Sup-BPP catalyst can be used for ethylene/alpha-olefin co-polymerizations in a gas phase reactor.
The present disclosure provides for a supported bis(phenoxy-phenyl) (Sup-BPP) catalysts for production of polyethylene in a slurry-phase polymerization process. The Sup-BPP catalysts of the present disclosure include an inert support in the presence of an aluminoxane compound, where the aluminoxane compound functions as a binding agent. The Sup-BPP can be mixed with the support and the binder in an inert hydrocarbon. The Sup-BPP catalyst can be used for ethylene/alpha-olefin co-polymerizations in a slurry-phase reactor.
A multilayer film may comprise a core layer, a first outer layer, and a second outer layer. The core layer may comprise a recycled polyethylene having a density from 0.912 g/cm3to 0.930 g/cm322) of from 1.0 g/10 min to 4.0 g/10 min as determined according to ASTM D1238 (2.16 kg at 190 °C). The recycled polyethylene may comprise less than or equal to 15 wt.% low density polyethylene. The core layer may be positioned between the first outer layer and the second outer layer. The first outer layer and the second outer layer each may comprise at least 60 wt.% of a polyethylene resin that is characterized by a specific MWCDI value, iCCD profile, or both.
B32B 27/08 - Layered products essentially comprising synthetic resin as the main or only constituent of a layer next to another layer of a specific substance of synthetic resin of a different kind
A method for processing hydrocarbons includes introducing a hydrocarbon feedstock into a treatment unit, the hydrocarbon feedstock includes used lubrication oil, wherein the used lubrication oil is derived from any one of Group I-V base oils as defined by the American Petroleum Institute. Then, treating the hydrocarbon feedstock to produce a treated hydrocarbon feedstock and separating the treated hydrocarbon feedstock in a first separation unit to obtain a hydrocarbon byproduct stream and a base oil. Then, upgrading the hydrocarbon byproduct stream to produce an upgraded hydrocarbon byproduct stream and blending the upgraded hydrocarbon stream with a fossil-based hydrocarbon feedstock to form a hydrocarbon blend. Additionally, introducing the hydrocarbon blend into a steam-cracking unit and cracking the hydrocarbon blend in the steam-cracking unit to obtain a cracked product including ethylene. Treating the hydrocarbon feedstock includes one or more of dewatering, defueling, de-asphalting, fractionation, and finishing.
C10G 55/04 - Treatment of hydrocarbon oils, in the absence of hydrogen, by at least one refining process and at least one cracking process plural serial stages only including at least one thermal cracking step
C10G 69/06 - Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only including at least one step of thermal cracking in the absence of hydrogen
C10G 69/12 - Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only including at least one polymerisation or alkylation step
C10G 21/00 - Refining of hydrocarbon oils, in the absence of hydrogen, by extraction with selective solvents
A process for upgrading a hydrocarbon fluid including introducing a first portion of the hydrocarbon fluid to a first electrically conductive tube, and introducing a second portion of the hydrocarbon fluid to a second electrically conductive tube. A DC current is applied to the first electrically conductive tube to heat the first portion of the hydrocarbon fluid within the first tube to a first reaction temperature to form a first product stream, and a DC current is applied to the second electrically conductive tube to heat the second portion of the hydrocarbon fluid within the second tube to a second reaction temperature to form a second product stream. The first product stream is introduced into a product channel through an outlet of the first electrically conductive tube, and the second product stream is introduced into the product channel through an outlet of the second electrically conductive tube.
C08L 51/06 - Compositions of graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bondsCompositions of derivatives of such polymers grafted on to homopolymers or copolymers of aliphatic hydrocarbons containing only one carbon-to-carbon double bond
24.
SYSTEMS AND METHODS FOR MEASURING CARBURIZATION OF AN ELECTRIFIED CRACKING COIL
A system for measuring carburization may comprise an electrified cracking electrified by a electric current; and first and second thermocouples separated by a length along the electrified cracking coil. Each thermocouple may comprise a first wire, a second wire, wherein the first wire and the second wire are joined at a junction proximate the electrified cracking coil, an electrically conductive sheath surrounding the first and second wires, wherein the electrically conductive sheath is in contact with the electrified cracking coil, a thermocouple sensor coupled to the first wire and the second wire opposite the junction, the thermocouple sensor configured to determine a temperature from a voltage difference between the first wire and the second wire, and a voltmeter electrically coupled to the electrically conductive sheath and configured to determine a voltage of the electrified cracking coil at a contact point between the electrically conductive sheath and the electrified cracking coil.
C10G 9/24 - Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils by heating with electrical means
G01K 7/02 - Measuring temperature based on the use of electric or magnetic elements directly sensitive to heat using thermoelectric elements, e.g. thermocouples
G01N 27/00 - Investigating or analysing materials by the use of electric, electrochemical, or magnetic means
G01N 27/04 - Investigating or analysing materials by the use of electric, electrochemical, or magnetic means by investigating impedance by investigating resistance
The present disclosure relates to an artificial turf yarn from post-consumer recycled material, a method for producing the artificial turf yarns and an artificial turf comprising the artificial turf yarns. The method comprises reducing moisture content of the post-consumer recycled material to less than 0.01 wt%. In the present disclosure, the method for producing artificial turf yarns exhibits good processability, i.e., a little fiber/monofilament breakage during processing, especially when PCR materials as used have a content of ≥50%and the monofilaments or yarns have a low a linear density ≤800 dtex.
D01F 6/04 - Monocomponent man-made filaments or the like of synthetic polymersManufacture thereof from homopolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds from polyolefins
D01F 6/46 - Monocomponent man-made filaments or the like of synthetic polymersManufacture thereof from mixtures of polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds as major constituent with other polymers or low-molecular-weight compounds of polyolefins
D06N 7/00 - Flexible sheet materials not otherwise provided for, e.g. textile threads, filaments, yarns or tow, glued on macromolecular material
A polymeric composition including 10 wt% to 85 wt% of a polar ethylene-based polymer based on the total weight of the polymeric composition. The polymeric composition is free of a non-polar ethylene-based polymer. Then polymeric composition also includes 15 wt% to 90 wt% of an intumescent flame-retardant mixture based on the total weight of the polymeric composition. The intumescent flame-retardant mixture includes piperazine pyrophosphate and a phosphoric acid compound. A weight ratio of piperazine pyrophosphate to phosphoric acid compound is from 0.79-1.19.
C08K 5/52 - Phosphorus bound to oxygen bound to oxygen only
H01B 3/44 - Insulators or insulating bodies characterised by the insulating materialsSelection of materials for their insulating or dielectric properties mainly consisting of organic substances plasticsInsulators or insulating bodies characterised by the insulating materialsSelection of materials for their insulating or dielectric properties mainly consisting of organic substances resinsInsulators or insulating bodies characterised by the insulating materialsSelection of materials for their insulating or dielectric properties mainly consisting of organic substances waxes vinyl resinsInsulators or insulating bodies characterised by the insulating materialsSelection of materials for their insulating or dielectric properties mainly consisting of organic substances plasticsInsulators or insulating bodies characterised by the insulating materialsSelection of materials for their insulating or dielectric properties mainly consisting of organic substances resinsInsulators or insulating bodies characterised by the insulating materialsSelection of materials for their insulating or dielectric properties mainly consisting of organic substances waxes acrylic resins
27.
THERMAL AND ELECTRICAL INSULATION OF ELECTRICALLY HEATED REACTION TUBES
An electrified reactor includes a reactor coil that is electrically connected to an electric power source, a first insulating layer that is electrically connected to the reactor coil, and a second insulating layer that is thermally connected to the first insulating layer. The first insulating layer is an electric insulating layer, and the second insulating layer is a thermal insulating layer.
B01J 8/06 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes with stationary particles, e.g. in fixed beds in tube reactorsChemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes with stationary particles, e.g. in fixed beds the solid particles being arranged in tubes
B01J 8/08 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes with moving particles
B01J 19/24 - Stationary reactors without moving elements inside
28.
SYSTEMS FOR DIRECTLY HEATING ELECTRIC TUBES FOR HYDROCARBON UPGRADING
A heating apparatus includes a pair of electrically conductive tubes, a feed channel having a fluid entrance and a grounded connection, a product channel having a fluid exit and a grounded connection, and a DC current voltage source. The feed channel is fluidly connected to inlets of the pair of electrically conductive tubes and the product channel is fluidly connected to outlets of the pair of electrically conductive tubes. The pair of electrically conductive tubes include a first electrically conductive tube and a second electrically conductive tube connected in series and the DC current voltage source is electrically connected to the first electrically conductive tube and the second electrically conductive tube.
BOARD OF REGENTS, THE UNIVERSITY OF TEXAS SYSTEM (USA)
Inventor
Katiyar, Amit
Taha, Motaz
Nguyen, Quoc
Abstract
An enhanced oil recovery (EOR) process uses light hydrocarbon injection gas and a hydrocarbon-soluble nonionic surfactant to create foam. The nonionic surfactant comprises hydrophilic polyethylene glycol-polypropylene glycol copolymer terminated by a lipophilic chain. An anionic surfactant that comprises linear alkyl-diaryloxide disulfonate is added to increase the cloud point of the nonionic surfactant and/or the hydrocarbon solubility of the nonionic surfactant.
C09K 8/584 - Compositions for enhanced recovery methods for obtaining hydrocarbons, i.e. for improving the mobility of the oil, e.g. displacing fluids characterised by the use of specific surfactants
C09K 8/594 - Compositions used in combination with injected gas
A hydroformylation process is disclosed having a reaction fluid comprising (a) at least one acidic compound selected from a phosphorus acidic compound or carboxylic acid compound, (b) a rhodium-organophosphorus ligand complex catalyst that comprises a rhodium complexed with an organophosphorous ligand, and, optionally, (c) free organophosphorus ligand. This reaction fluid is contacted with an aqueous extraction fluid to facilitate the separation of at least some of acidic compounds from the reaction fluid via an extraction zone aqueous effluent stream (extractor tails). The extractor tails are then sent to a decanter to facilitate further separation of the organic phase comprising rhodium from the water effluent, which can be sent for additional processing comprising wastewater treatment.
C07C 45/50 - Preparation of compounds having C=O groups bound only to carbon or hydrogen atomsPreparation of chelates of such compounds by reaction with carbon monoxide by oxo-reactions
C07C 45/80 - SeparationPurificationStabilisationUse of additives by liquid-liquid treatment
C07C 47/02 - Saturated compounds having —CHO groups bound to acyclic carbon atoms or to hydrogen
A phase separation learning model can receive fluid sample images and be operated to determine a presence or absence of phase separation in the fluid sample images. To do so, a computer vision learning model can be trained to identify objects in images via transfer learning utilizing a first plurality of fluid sample images to result in the phase separation learning model. A second plurality of fluid sample images can be input into the phase separation learning model, and the phase separation learning model can make a recommendation regarding the presence or the absence of phase separation within the second plurality of fluid sample images as a result of operation of the phase separation learning model.
A process for producing amines by reductive amination, the process includes introducing a feed stream, the feed stream comprising an amino alcohol and a reducing agent, and hydrogen in a reaction zone of a reactor, and contacting the feed stream with a catalyst in the reaction zone. A hydrogen flow rate into the reaction zone is adjusted, and a product stream comprising ethyleneamines is extracted. The catalyst includes a carrier component selected from alumina, silica, and combinations thereof; and an active component having a first metal, a second metal, and a third metal. The first metal is selected from cobalt, nickel, and copper, the second metal is selected from rhenium, ruthenium, chromium, zinc, sodium, calcium, magnesium, strontium, lithium, potassium, barium, cesium, lanthanum, tungsten, iron, silver, titanium, manganese, aluminum, rhodium, platinum, palladium, iridium, and combinations thereof, and the third metal is niobium.
C07C 209/16 - Preparation of compounds containing amino groups bound to a carbon skeleton by substitution of functional groups by amino groups by substitution of hydroxy groups or of etherified or esterified hydroxy groups with formation of amino groups bound to acyclic carbon atoms or to carbon atoms of rings other than six-membered aromatic rings
A process for producing amines by reductive amination, the process includes introducing a feed stream, the feed stream comprising an amino alcohol and a reducing agent, and hydrogen in a reaction zone of a reactor, and contacting the feed stream with a catalyst in the reaction zone. A product stream comprising ethyleneamines is extracted. The catalyst includes a carrier component selected from alumina, silica, and combinations thereof; and an active component having a first metal, a second metal, and a third metal. The first metal is selected from cobalt, nickel, and copper, the second metal is selected from rhenium, ruthenium, chromium, zinc, sodium, calcium, magnesium, strontium, lithium, potassium, barium, cesium, lanthanum, tungsten, iron, silver, titanium, manganese, aluminum, rhodium, platinum, palladium, iridium, and combinations thereof, and the third metal is niobium.
C07C 209/16 - Preparation of compounds containing amino groups bound to a carbon skeleton by substitution of functional groups by amino groups by substitution of hydroxy groups or of etherified or esterified hydroxy groups with formation of amino groups bound to acyclic carbon atoms or to carbon atoms of rings other than six-membered aromatic rings
A catalyst comprising a carrier component selected from alumina, silica, and combinations thereof; and an active component having a first metal, a second metal, and a third metal. The first metal is selected from a group consisting of cobalt, nickel, and copper. The second metal is selected from a group consisting of rhenium, ruthenium, chromium, zinc, sodium, calcium, magnesium, strontium, lithium, potassium, barium, cesium, lanthanum, tungsten, iron, silver, titanium, manganese, aluminum, rhodium, platinum, palladium, iridium, and combinations thereof. The third metal is niobium.
A process for producing amines by reductive amination, the process includes introducing a feed stream to a reaction zone, the feed stream comprising an amino alcohol and a reducing agent, introducing a recycle stream to a reaction zone, wherein the recycle stream comprises light alkylamines, and contacting the feed stream and the recycle stream with a catalyst in the reaction zone in the presence of hydrogen, and a product stream comprising ethyleneamines is produced. The catalyst includes a carrier component selected from alumina, silica, and combinations thereof; and an active component having a first metal, a second metal, and a third metal. The first metal is selected from cobalt, nickel, and copper, the second metal is selected from rhenium, ruthenium, chromium, zinc, sodium, calcium, magnesium, strontium, lithium, potassium, barium, cesium, lanthanum, tungsten, iron, silver, titanium, manganese, aluminum, rhodium, platinum, palladium, iridium, and combinations thereof, and the third metal is niobium.
C07C 209/16 - Preparation of compounds containing amino groups bound to a carbon skeleton by substitution of functional groups by amino groups by substitution of hydroxy groups or of etherified or esterified hydroxy groups with formation of amino groups bound to acyclic carbon atoms or to carbon atoms of rings other than six-membered aromatic rings
H2O2propeneH2O2PropenePropeneH2O2PropeneH2O2PropeneH2O2H2O2(nr) is in the range of from 0.02 to 1.03, maintaining the distillation in f). A second aspect of the invention is directed to a process for preparing propylene oxide, the process for preparing propylene oxide comprising at least a normal run stage with propene epoxidation and at least a stand-by stage without propene epoxidation, the process further preferably comprising intermediate shut-down stage(s) after a normal run stage and before a stand-by stage and/or start-up stage(s) after a stand-by stage and before a normal run stage. A third aspect of the invention is directed to propylene oxide obtained or obtainable from the process of the second aspect.
C07D 301/12 - Synthesis of the oxirane ring by oxidation of unsaturated compounds, or of mixtures of unsaturated and saturated compounds with hydrogen peroxide or inorganic peroxides or peracids
The present invention relates in a first aspect to a process for preparing propylene oxide. A second aspect of the invention is directed to a mixture, preferably for preparation of propylene oxide. A third aspect of the invention relates to the use of the mixture according to the second aspect of the invention for preparation of propylene oxide, a fourth aspect of the invention is directed to a method for preparing propylene oxide, wherein the mixture of the second aspect of the invention is brought into contact with a heterogeneous catalyst under epoxidation conditions, and a fifth aspect of the invention is related to propylene oxide, obtained or obtainable from a process according to the first aspect of the invention or from the method of fourth aspect of the invention.
C07D 301/12 - Synthesis of the oxirane ring by oxidation of unsaturated compounds, or of mixtures of unsaturated and saturated compounds with hydrogen peroxide or inorganic peroxides or peracids
C07D 303/04 - Compounds containing oxirane rings containing only hydrogen and carbon atoms in addition to the ring oxygen atoms
38.
ELECTRIC ISOLATION JOINTS AND SYSTEMS AND METHODS FOR UTILIZING THE SAME
An electric isolation joint may comprise a first electrically conductive pipe; a second electrically conductive pipe; and a cylindrical non-conductive material interposed between the first pipe and the second pipe, such that the first pipe and the second pipe do not contact each other, wherein: the first pipe, the second pipe, and the first cylindrical non-conductive material collectively define a sealed interior pipe surface of the electric isolation joint.
F16L 23/16 - Flanged joints characterised by the sealing means
C10G 9/24 - Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils by heating with electrical means
C10G 75/00 - Inhibiting corrosion or fouling in apparatus for treatment or conversion of hydrocarbon oils, in general
F16L 25/02 - Construction or details of pipe joints not provided for in, or of interest apart from, groups specially adapted for electrically insulating the two pipe ends of the joint from each other
A method for preparing silylated cellulose is disclosed. The method includes preparing a reaction product in the form of a paste and removing unreacted starting materials and/or by-products from the paste to form a powdered silylated cellulose.
A durable and inexpensive coating that has high solar reflectance and low dirt pickup can be made using a mixture containing: (a) From 20 to 40 weight percent of white cement; (b) From 5 to 30 weight percent of a vinyl ester copolymer which has a glass-transition temperature of −20° C. to 35° C.; (c) at least 0.1 weight percent of a cellulosic thickener, and (d) at least 30 weight percent white fillers in which 95 to 100 weight percent of particles have a particle size of no more than 75 microns, wherein the dry mix composition contains no more than 0.1 weight percent silica and no more than 5 weight percent pozzolans and wherein all weight percentages are based on the weight of the dry components (a)-(d). The dry components can be blended together to form a dry mix, and the dry mix can be mixed with water to form an aqueous coating composition that can be applied by brushing or rolling. The coating is especially useful as a roof coating.
A method of producing polyethylene glycol includes the steps of combining a tetra(ethylene glycol) initiator and one or more catalysts selected from the group consisting of MOH and MH to form a reaction mixture, wherein M is selected from the group consisting of an alkali metal and an alkaline earth metal, further wherein the reaction mixture comprises 1200 ppm or less of water as measured according to Karl Fischer Titration; adding ethylene oxide to the reaction mixture; and reacting the reaction mixture to form polyethylene glycol having a weight average molecular weight from 200 g/mol to 1000 g/mol as measured according to Gas Chromatography with Mass Spectrometry Detection.
C08G 65/26 - Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring from cyclic ethers and other compounds
42.
MULTILAYER FILMS AND ARTICLES COMPRISING MULTILAYER FILMS
Embodiments of the present invention relate to multilayer films, laminates, and articles. In one aspect, a multilayer film includes at least three layers: (a) a first layer, (b) a second layer, and (c) a third layer. Among other features, the second layer includes from 0.05 weight percent to 5.0 weight percent of at least one polydimethylsiloxane, based on the total weight of the second layer, wherein at least one of the polydimethylsiloxane has a weight average molecular weight, Mw, of from 20,000 g/mol to 700,000 g/mol.
B32B 27/08 - Layered products essentially comprising synthetic resin as the main or only constituent of a layer next to another layer of a specific substance of synthetic resin of a different kind
Embodiments of the present invention relate to multilayer films, bags, and other articles. In one aspect, a multilayer film comprises at least three layers: (a) a first skin layer, (b) a core layer, and (c) a second skin layer opposite the first skin layer. Among other features, the first skin layer and the core layer, while having different overall compositions, each comprise from 0.05 weight percent to 5.0 weight percent of at least one polydimethylsiloxane, based on the total weight of the respective layer, wherein at least one of the polydimethylsiloxane has a weight average molecular weight, Mw, of from 20,000 g/mol to 700,000 g/mol.
A method of making a powder polyvinyl chloride-based composition comprises blending an emulsion of a polyvinyl chloride resin and a flexible acrylic resin to form a polyvinyl chloride resin/flexible acrylic resin blend. The polyvinyl chloride/flexible acrylic resin blend is isolated to form the powder polyvinyl chloride-based composition. A powder polyvinyl chloride-based composition, a polyvinyl chloride formulation, an article formed from the powder polyvinyl chloride-based composition, and a method for forming the article are also disclosed.
B29K 105/00 - Condition, form or state of moulded material
B32B 5/18 - Layered products characterised by the non-homogeneity or physical structure of a layer characterised by features of a layer containing foamed or specifically porous material
B32B 27/06 - Layered products essentially comprising synthetic resin as the main or only constituent of a layer next to another layer of a specific substance
The present disclosure provides a laminate. In an embodiment, the laminate comprises a first machine direction oriented (1MDO) multilayer film. The 1MDO multilayer film comprises (a) a skin layer comprising (i) a skin layer (SL) first ethylene/α-olefin copolymer having a density from 0.870 g/cc to 0.920 g/cc, and (ii) an optional skin layer (SL) second ethylene/α-olefin copolymer having a density from 0.900 g/cc to 0.980 g/cc. The 1MDO multilayer film comprises (b) a first intermediate layer in direct contact with the skin layer. The first intermediate layer comprises (i) a first intermediate layer (FIL) first ethylene/α-olefin copolymer having a density from 0.940 g/cc to 0.980 g/cc, and (ii) a first intermediate layer (FIL) second ethylene/a-olefin copolymer having density from 0.916 g/cc to 0.980 g/cc. The 1MDO multilayer film comprises (c) a core layer in direct contact with the first intermediate layer (b). The core layer (c) comprises (i) a core layer (CL) first ethylene/a-olefin copolymer having a density from 0.915 g/cc to 0.980 g/cc. The 1MDO multilayer film comprises (d) a second intermediate layer in direct contact with the core layer. The second intermediate layer comprises an ethylene-based polymer. The 1MD0 multilayer film comprises (e) an interior layer in direct contact with the second intermediate layer. The interior layer comprises an ethylene-based polymer. The laminate comprises a second machine direction oriented (2MDO) film and an adhesive layer between the 1MDO multilayer film and the 2MDO film.
B32B 7/02 - Physical, chemical or physicochemical properties
B32B 7/12 - Interconnection of layers using interposed adhesives or interposed materials with bonding properties
B32B 27/08 - Layered products essentially comprising synthetic resin as the main or only constituent of a layer next to another layer of a specific substance of synthetic resin of a different kind
The present disclosure provides a process. The process includes (i) crosslinking pellets composed of a silane-grafted ethylene/α-olefin multi-block copolymer (Si-g-OBC) to a gel content from 10% to 80% to form crosslinked Si-g-OBC pellets; and (ii) foaming the crosslinked Si-g-OBC pellets to form crosslinked Si-g-OBC foam beads having a gel content from 10% to 80%.
An aqueous antimicrobial coating composition contains (A) an emulsion polymer comprising, by weight based on the weight of the emulsion polymer, (al) from 0 to 10%of structural units of an acetoacetyl functional monomer; (a2) from 0 to 8%of structural units of a monomer containing at least one heterocyclic group selected from the group consisting of imidazole, benzotriazole, and benzimidazole; and (a3) structural units of an additional monoethylenically unsaturated nonionic monomer; provided that the total concentration of (al) structural units of the acetoacetyl functional monomer and (a2) structural units of the monomer containing at least one heterocyclic group is at least 0.1%; (B) a silver salt present in an amount to provide 15 to 1000 ppm of silver, by weight based on the weight of the coating composition; and (C) from 0.3%to 5%of a protease, by weight based on the coating composition weight.
An adhesive composition contains: (i) an aqueous dispersion comprising a multistage polymer having a specific weight average molecular weight and comprises a first-stage polymer and a second-stage polymer at a specific weight ratio of the first-stage polymer to the second-stage polymer greater than 70: 30 to 95: 5; where the first-stage polymer (a) comprises a novel combination of (a1) structural units of an α, β-ethylenically unsaturated dicarboxylic acid, an anhydride thereof, or mixtures thereof; (a2) structural units of an acetoacetyl functional monomer; and (a3) structural units of an alkyl (meth) acrylate; and the second-stage polymer comprises a novel combination of (b1) structural units of an acetoacetyl functional monomer, and (b2) structural units of an alkyl (meth) acrylate; and (ii) a specific polyacid polymer, where the polyacid polymer is present in an amount of from 0.1%to less than 5%, by weight based on the total dry weight of the multistage polymer and the polyacid polymer.
C09J 151/00 - Adhesives based on graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bondsAdhesives based on derivatives of such polymers
C08F 265/06 - Polymerisation of acrylate or methacrylate esters on to polymers thereof
D06M 15/263 - Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds of unsaturated carboxylic acidsSalts or esters thereof
3-(Methylamino)propane-1,2-diol (MAPD) and its homologs are potentially useful alkanolamine components in aqueous absorbent that is used in carbon dioxide recovery from gas streams. MAPD can be generated in situ in the process by reaction of 3-(dimethylamino)propane-1,2-diol with a primary or secondary amine. A side reaction of MAPD and carbon dioxide can form an oxazolidinone side product, but the oxazolidinone side product can be decomposed to recover the MAPD by contact with alkali metal hydroxide.
B01D 53/14 - Separation of gases or vapoursRecovering vapours of volatile solvents from gasesChemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases or aerosols by absorption
A data manager for laboratory instruments can store a respective driver for different types of laboratory instruments. The driver for a given type of laboratory instrument can establish a connection with a laboratory instrument of one of the plurality of types, receive data from the laboratory instrument in a respective format, and convert the data from the respective format to a common laboratory information management system (LIMS) format. The data manager can upload the data in the common LIMS format to a LIMS.
G16H 10/40 - ICT specially adapted for the handling or processing of patient-related medical or healthcare data for data related to laboratory analysis, e.g. patient specimen analysis
G01N 35/00 - Automatic analysis not limited to methods or materials provided for in any single one of groups Handling materials therefor
An apparatus used in a fluidized reaction process may include a vessel including an inner surface, a cylindrical section housed within the vessel, a guide encircling the cylindrical section, a plurality of guide supports, and a plurality of springs. The cylindrical section may include a cylindrical outer surface. The guide may include a cylindrical body including a first surface facing the cylindrical section and a second surface opposite the first surface. The plurality of guide supports may each span from the inner surface of the vessel to the outer surface of the guide. The plurality of springs may be disposed between the first surface of the guide and the outer surface of the cylindrical section.
B01J 19/32 - Packing elements in the form of grids or built-up elements for forming a unit or module inside the apparatus for mass or heat transfer
C10G 11/00 - Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
B01J 8/00 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes
B01J 8/18 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes with fluidised particles
B01J 8/40 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed subjected to vibrations or pulsations
53.
METHOD FOR THE REDISTRIBUTION OF SILICON-BONDED GROUPS
The present disclosure provides a method of preparing a target compound. The method includes the step of combining (A) an organosilicon component and (B) a catalyst including a boron cluster to give a mixture. The method further includes preparing a reaction mixture including the target compound from the mixture. The organosilicon component (A) includes (A1) a first organosilicon compound having a silicon-bonded C1-C4 alkyl group. When the first organosilicon compound (A1) does not include a silicon-bonded halogen atom, the organosilicon component (A) includes a second organosilicon compound (A2) including at least one silicon-bonded halogen atom. The disclosure further provides a reaction product prepared according to the method.
B01J 31/14 - Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides containing organo-metallic compounds or metal hydrides of aluminium or boron
C07F 7/08 - Compounds having one or more C—Si linkages
2abcxx and an organosilicon compound conforming to the formula R3R4R533 groups, where each R is independently an alkyl group or a halogen atom; and -OR1groups. Each R1is an independently selected alkyl group. At least one X and/or at least one Y is a halogen atom. Subscript x is >0. R3 R4 and R5 are each independently selected from hydrocarbyl groups and halogen atoms, and Q is selected from H and halogen atoms.
B01J 31/14 - Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides containing organo-metallic compounds or metal hydrides of aluminium or boron
xyzx'x'R1y'z'z'. R is an alkyl group having from 1 to 4 carbon atoms. Each Q is an individually selected halogen atom. Each of subscripts x, y, and z are independently 1 or 2, subject to the proviso that x+y+z=4. Each R1 is an independently selected aryl group, and each of subscripts x', y', and z' are 1 or 2, subject to the provisos that x=x' and x'+y'+z'=4. A reaction product comprising the organosilicon compound prepared in accordance with the method is also provided.
B01J 31/14 - Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides containing organo-metallic compounds or metal hydrides of aluminium or boron
Embodiments of the present disclosure are directed towards thermally bonded articles including a polyethylene filament material and a multilayer backing material, where the polyethylene filament material is thermally bonded to the multilayer backing material.
B32B 27/12 - Layered products essentially comprising synthetic resin next to a fibrous or filamentary layer
B32B 27/08 - Layered products essentially comprising synthetic resin as the main or only constituent of a layer next to another layer of a specific substance of synthetic resin of a different kind
Disclosed herein are multimodal polyethylene compositions, and pipes including the same. The compositions include a first component and a second component, where the composition according to embodiments disclosed herein can have a density from 0.940 g/cm3to 0.955 g/cm32pp MW of greater than 150,000 g/mol at an elution temperature range of 90.0°C to 95.0°C. Pipes made from the compositions can have an improved balance of properties.
Disclosed herein are multimodal polyethylene compositions, processes for making the same, and pipes made from the same. The multimodal polyethylene composition includes a first component and a second component. The composition according to embodiments disclosed herein has a density from 0.940 g/cm3to 0.955 g/cm32pp MW of greater than 145,000 g/mol at an elution temperature range of 90.0°C to 95.0°C. Pipes made from the composition can have a desirable balance of properties, including slow growth crack and hydrostatic pressure properties.
Disclosed herein are a polyethylene composition including high density recycled polyethylene compositions, and a film including the same. The polyethylene composition according to embodiments disclosed herein includes a high density recycled polyethylene composition, a LDPE, and an ethylene-based elastomer. The combination of polymers, when used in a film can allow for the inclusion of recycled polyethylene in films without loss of desirable properties and with improved, maintained, or desirable film properties such as toughness and low gel content.
Embodiments of the present disclosure are directed towards thermally bonded articles including a polyethylene filament material and a multilayer backing material, where the polyethylene filament material is thermally bonded to the multilayer backing material.
B32B 27/08 - Layered products essentially comprising synthetic resin as the main or only constituent of a layer next to another layer of a specific substance of synthetic resin of a different kind
B32B 27/12 - Layered products essentially comprising synthetic resin next to a fibrous or filamentary layer
Hydrocarbons may be processed by a method including contacting a hydrocarbon feed stream with a particulate solid in a first particulate solids bed to form a product stream. The method may further including passing a portion or all of the particulate solid from the first particulate solids bed to a second particulate solids bed, from the second particulate solids bed to a third particulate solids bed, from the third particulate solids bed to a fourth particulate solids bed, and from the fourth particulate solids bed to the first particulate solids bed. The fourth particulate solids bed may fluctuate between a low-level state and a high-level state. A first particulate solids outlet may be positioned at or near the bottom of the fourth particulate solids bed. A second particulate solids outlet may be positioned in the top half of the fourth particulate solids bed during the low-level state. One or more bubble breakers may be positioned within the fourth particulate solids bed and above the second particulate solids outlet, wherein the fourth particulate solids bed may have a height of from 0-3 feet above the uppermost of the one or more bubble breakers in the low-level state, and wherein the fourth particulate solids bed may have a height of from 3-7 feet above the uppermost of the one or more bubble breakers in the high-level state.
B01J 8/18 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes with fluidised particles
B01J 8/28 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes with fluidised particles according to "fluidised-bed" technique with two or more fluidised beds, e.g. reactor and regeneration installations the one above the other
B01J 8/34 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes with fluidised particles according to "fluidised-bed" technique with stationary packing material in the fluidised bed, e.g. bricks, wire rings, baffles
C10G 11/18 - Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised bed" technique
62.
CATALYSTS THAT INCLUDE CHROMIUM AND METHODS FOR MAKING OLEFINIC MATERIALS THAT UTILIZE THE SAME
A method for making olefinic materials includes passing a hydrocarbon-containing feed and a catalyst into a reactor of an olefinic material production system, wherein the hydrocarbon-containing feed is reacted to form the olefinic material and the catalyst includes from 0.25 wt.% to 10 wt.% chromium and at least 85 wt.% of a support. The catalyst is passed to a combustor and heated by combusting a supplemental fuel or coke present on the catalyst. The catalyst is passed to an upstream reactor section, such that the catalyst is continuously cycled between the reactor and the combustor. A sulfur-containing compound is passed into the system and into contact with the catalyst. The catalyst may include from 0 wt.% to 0.1 wt.% of platinum, palladium, rhodium, iridium, ruthenium, osmium, or combinations thereof, from 0 wt.% to 10 wt.% of gallium, indium, thallium, or combinations thereof, and the support may include silica-containing zirconia.
21222a122 are independently a hydrocarbon chain comprising from 1 to 20 carbon atoms, X is a hydrogen atom or a vinyl group, and a is 2 or 3. Further embodiments are directed to methods for making the organometallic compound and methods for making polyolefin compounds utilizing the organometallic compound.
C07F 7/08 - Compounds having one or more C—Si linkages
C08F 4/64 - Titanium, zirconium, hafnium, or compounds thereof
C08F 4/6592 - Component covered by group containing a transition metal-carbon bond containing at least one cyclopentadienyl ring, condensed or not, e.g. an indenyl or a fluorenyl ring
Alkoxylations are performed by combining an alkylene oxide with a starter and a polyhedral borate catalyst. The polyhedral borate catalyst has the form [Cat+n12uvv]n-and/or [Cat+m10wzz]m-. The polyhedral borate catalysts are extremely active and therefore produce very high alkoxylation rates. When used to polymerize propylene oxide, the catalysts produce alkoxylated products that have high proportions of primary hydroxyl groups.
C08G 65/26 - Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring from cyclic ethers and other compounds
333, where R is an aryl group, and each Q is independently selected and defined above. The present disclosure further provides a reaction product prepared via the method.
B01J 31/14 - Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides containing organo-metallic compounds or metal hydrides of aluminium or boron
C07F 7/14 - Preparation thereof from halogenated silanes and hydrocarbons
A catalytically active salt including at least one boron cluster dianion and at least one cation. The cation includes a silylium cation having at least one silicon-bonded halogen atom. A composition including the catalytically active salt and at least one halosilane compound is also disclosed. A use of the catalytically active salt to couple an arene compound to a silicon atom of a hydridosilane compound is further disclosed. A use of the catalytically active salt to facilitate the exchange of one silicon-bonded alkyl group of a first silane molecule with a silicon-bonded halogen atom of a second silane molecule is also disclosed.
B01J 31/14 - Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides containing organo-metallic compounds or metal hydrides of aluminium or boron
A coated viscoelastic polyurethane foam includes a viscoelastic polyurethane foam having the coating thereon, the viscoelastic polyurethane foam having a resiliency of less than or equal to 20% as measured according to ASTM D3574, and a coating material on and embedded within the viscoelastic polyurethane foam, the coating material including an aqueous polymer emulsion and an encapsulated phase change material.
A process of upgrading a hydrocarbon feed may comprise combusting a hydrogen-containing fuel gas in a radiant section of a hydrocarbon upgrading furnace, thereby generating a flue gas; circulating the flue gas through a convection section of the hydrocarbon upgrading furnace, thereby heating one or more preheaters; recycling a percentage of the flue gas back into the radiant section; introducing a cracker feed mixture to a radiant section preheater, thereby preheating the cracker feed mixture; circulating the cracker feed mixture through the radiant section via the one or more coils; measuring a fluid temperature of the cracker feed mixture or a tube metal temperature of a portion of the one or more coils; and upon determining that the fluid or tube metal temperature falls outside a predetermined temperature range, altering a percentage of the flue gas recycled to the radiant section.
C10G 9/36 - Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils by direct contact with inert preheated fluids, e.g. with molten metals or salts with heated gases or vapours
The present disclosure is directed towards foam formulations having an isocyanate-reactive composition including: a first polyether polyol having an ethylene oxide content from 40 to 85 wt%, based on a total weight of alkylene oxides used to make the first polyether polyol and a hydroxyl number from 20 to 60 mg KOH/g; a second polyether polyol having an ethylene oxide content from 40 to 85 wt%, based on a total weight of alkylene oxides used to make the first polyether polyol and a hydroxyl number from 80 to 300 mg KOH/g; a third polyether polyol having a propylene oxide content equal to or greater than 80 wt%, based on a total weight of alkylene oxides used to make the third polyether polyol; a polyether siloxane surfactant; and an isocyanate composition including a MDI-based isocyanate.
A method for preparing a skin care formulation is provided comprising mixing: (a) a dermatologically acceptable carrier; (b) a skin care additive selected from the group consisting of (b.1) a color ingredient; (b.2) a UV radiation absorbing agent; and (b.3) a mixture of (b.1) and (b.2); and (c) a film forming emulsion prepared using a silicone - (meth)acrylate macromonomer of formula (A); wherein R1=monovalent hydrocarbon group of 1-12 carbons; R2=H or methyl; D2=divalent hydrocarbon group of 2-12 carbons; and a poly(alkylene glycol) (meth)acrylate macromonomer of formula (I) wherein R3=H or methyl; D3=ethylene or propylene; R4=H or an alkyl group of 1-4 carbons; and m is sufficient to provide a number average molecular weight of >200-5,000 g/mol.
A61K 8/895 - Polysiloxanes containing silicon bound to unsaturated aliphatic groups, e.g. vinyl dimethicone
A61K 8/81 - Cosmetics or similar toiletry preparations characterised by the composition containing organic macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds
A61Q 17/04 - Topical preparations for affording protection against sunlight or other radiationTopical sun tanning preparations
A method for preparing a skin care composition is provided comprising mixing: (a) a dermatologically acceptable carrier; (b) a skin care additive selected from the group consisting of (b.1) a color ingredient; (b.2) a UV radiation absorbing agent; and (b.3) a mixture of (b.1) and (b.2); and (c) a film forming emulsion prepared using a silicone - (meth)acrylate macromonomer of formula (A) wherein each R1is an independently selected monovalent hydrocarbon group of 1 to 12 carbon atoms; wherein D2is a divalent hydrocarbon group of 2 to 12 carbon atoms; wherein R2 is selected from the group consisting of H and methyl.
Embodiments are directed to a foamable composition comprising virgin ethylenevinyl acetate, greater than or equal to 15 phr ethylene-vinyl acetate recycled foam, elastomer, polarity modifier, a crosslinking agent, and a blowing agent. The elastomer comprises ethylene/alpha-olefin multi-block interpolymer, ethylene/alpha-olefin copolymer, or combinations thereof. The polarity modifier comprises ethylene-alkyl (meth)acrylate copolymer. Further embodiments are directed to foam articles comprising the foamable composition and processes for manufacturing the foam articles.
C08J 9/10 - Working-up of macromolecular substances to porous or cellular articles or materialsAfter-treatment thereof using blowing gases generated by a previously added blowing agent by a chemical blowing agent developing nitrogen
C08K 3/011 - Crosslinking or vulcanising agents, e.g. accelerators
C08K 3/013 - Fillers, pigments or reinforcing additives
The present invention is platinum(II) oxalate compound of the following formula: where R1, R2, and R3 are as defined herein. The platinum(II) oxalate compound of the present invention is useful as a catalyst in hydrosilylation reactions, especially the hydrosilylation of curable siloxanes.
The present invention is platinum(II) oxalate compound of the following formula: where R1, R2, and R3 are as defined herein. The platinum(II) oxalate compound of the present invention is useful as a catalyst in hydrosilylation reactions, especially the hydrosilylation of curable siloxanes.
A method of processing hydrocarbons includes contacting a hydrocarbon-containing feed with particulate solids in a reactor to form a hydrocarbon product, wherein debris having a size of greater than 1 cm is formed, and wherein the particulate solids have a size of less than 1 cm. A portion or all of the particulate solids and the debris are passed from the reactor to a stripper, wherein the stripper has a vertical passage through which the particulate solids and the debris move in a substantially downward direction through the stripper and the stripper has a debris filter that allows passage of the particulate solids but not of the debris through the debris filter. The debris filter is positioned in the vertical passage such that the debris is collected along a sidewall of the vertical passage.
B01J 8/00 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes
B01J 8/18 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes with fluidised particles
B01J 8/38 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation
C10G 11/18 - Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised bed" technique
76.
ALKOXYLATION PROCESSES USING PHOSPHONIUM CATALYSTS
Alkoxylations are performed by reacting a cyclic oxide with a starter in the presence of certain phosphonium catalysts. The phosphonium catalysts are highly active and effective in such small quantities that it is often unnecessary to remove catalyst residues from the product. The phosphonium catalysts are very effective in alkoxylating even low molecular weight starters such as glycerol and sorbitol.
C08G 65/26 - Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring from cyclic ethers and other compounds
77.
ALKOXYLATION PROCESSES USING PHOSPHONIUM DICATECHOLATE CATALYSTS
Polyethers are prepared by polymerizing a cyclic oxide in the presence of a starter and certain phosphonium catalysts. The phosphonium catalysts are highly active and effective in such small quantities that it is often unnecessary to remove catalyst residues from the product. The phosphonium catalysts are very effective in alkoxylating even low molecular weight starters such as glycerol and sorbitol.
The present disclosure provides a catalyst system. In an embodiment, the catalyst composition includes (A) a phenoxy imine precatalyst having a structure of Formula 1: (I) wherein M1 is a metal selected from Ti, Zr, or Hf; each X1 is independently a halogen atom; R1 and R5 each is independently selected from substituted/unsubstituted (C1-C20)hydrocarbyl, substituted/unsubstituted (C1-C20)heterohydrocarbyl; R3 and R7 each is independently selected from substituted/unsubstituted (C1-C20)hydrocarbyl, substituted/unsubstituted (C1-C20)heterohydrocarbyl, and a substituted (C1-C20)heterohydrocarbyl; and R2, R4, R6, and R8 each is hydrogen. The catalyst composition also includes (B) a metallocene precatalyst having a structure of Formula 2: (II) wherein M2 is a metal selected from Ti, Zr, or Hf;
The present disclosure provides a catalyst system. In an embodiment, the catalyst composition includes (A) a phenoxy imine precatalyst having a structure of Formula 1: (I) wherein M1 is a metal selected from Ti, Zr, or Hf; each X1 is independently a halogen atom; R1 and R5 each is independently selected from substituted/unsubstituted (C1-C20)hydrocarbyl, substituted/unsubstituted (C1-C20)heterohydrocarbyl; R3 and R7 each is independently selected from substituted/unsubstituted (C1-C20)hydrocarbyl, substituted/unsubstituted (C1-C20)heterohydrocarbyl, and a substituted (C1-C20)heterohydrocarbyl; and R2, R4, R6, and R8 each is hydrogen. The catalyst composition also includes (B) a metallocene precatalyst having a structure of Formula 2: (II) wherein M2 is a metal selected from Ti, Zr, or Hf;
C09D 183/08 - Polysiloxanes containing silicon bound to organic groups containing atoms other than carbon, hydrogen, and oxygen
C08G 77/20 - Polysiloxanes containing silicon bound to unsaturated aliphatic groups
C08G 77/28 - Polysiloxanes containing silicon bound to organic groups containing atoms other than carbon, hydrogen, and oxygen sulfur-containing groups
Thermally conductive compositions may include an isocyanate component, an isocyanate-reactive component and one or more thermally conductive fillers present in one or more of the isocyanate component and the isocyanate-reactive component. The isocyanate component includes a blocked isocyanate prepolymer formed from a reaction of a first prepolymer, prepared from the reaction of one or more polyols comprising an amine-initiated polyol and a polyisocyanate, and an alkyl phenol. The isocyanate-reactive component includes one or more polyetheramine.
C08G 18/10 - Prepolymer processes involving reaction of isocyanates or isothiocyanates with compounds having active hydrogen in a first reaction step
C08G 18/12 - Prepolymer processes involving reaction of isocyanates or isothiocyanates with compounds having active hydrogen in a first reaction step using two or more compounds having active hydrogen in the first polymerisation step
C08G 18/24 - Catalysts containing metal compounds of tin
H01M 10/653 - Means for temperature control structurally associated with the cells characterised by electrically insulating or thermally conductive materials
H01M 10/655 - Solid structures for heat exchange or heat conduction
A method of removing fouling may comprise contacting a fouling material attached to a surface with an aqueous cleaning solution comprising a sulfonic acid based surfactant such that at least a portion of the fouling material is removed from the surface.
Multilayer films are disclosed. The multilayer film may include a core layer and a heat seal layer where the heat seal lay comprises a polypropylene copolymer and a polyethylene copolymer. The polypropylene copolymer of the heat seal layer has specific properties such as ethylene content and iCCD elution profile to contribute to the desirable properties of the film. The multilayer film can form effective heat seals, even when in contact with heated contents. The multilayer film can be formed into a bag where the bag is suitable for carrying hot or heated contents.
B65D 33/22 - End- or aperture-closing arrangements or devices using adhesive applied to integral parts, e.g. to flaps using heat-activatable adhesive
B32B 1/00 - Layered products having a non-planar shape
B32B 27/08 - Layered products essentially comprising synthetic resin as the main or only constituent of a layer next to another layer of a specific substance of synthetic resin of a different kind
An additive manufacturing guide for variable size additive manufacturing is provided. The additive manufacturing guide includes an actuator movable between a maximum flow position and a minimum flow position. The additive manufacturing guide also includes an adjustable port defining a variable area outlet aperture. The actuator is configured to deform the adjustable port to selectively resize the variable area outlet aperture. The maximum flow position corresponds to a maximum area of the variable area outlet aperture and the minimum flow position corresponds to a minimum area of the variable area outlet aperture. An additive manufacturing system including the additive manufacturing guide is also provided. A method of additive manufacturing with variable bead sizes using the additive manufacturing guide is further provided.
B29C 64/118 - Processes of additive manufacturing using only liquids or viscous materials, e.g. depositing a continuous bead of viscous material using filamentary material being melted, e.g. fused deposition modelling [FDM]
B29C 64/393 - Data acquisition or data processing for additive manufacturing for controlling or regulating additive manufacturing processes
B29K 83/00 - Use of polymers having silicon, with or without sulfur, nitrogen, oxygen or carbon only, in the main chain, as moulding material
A molecular vocabulary can be added to a tokenizer of a language model. The molecular vocabulary can include character strings as words representing atomic environments, explicit atomic positions, and forward-connecting positions based on a molecular database that includes data describing molecules and their properties. A molecular syntax can be defined for the tokenizer that represents each of the molecules as a respective molecular sentence made up of tuples corresponding to a quantity of atoms in a respective molecule and including words from the molecular vocabulary. The molecules can be tokenized according to the molecular vocabulary and the molecular syntax. The language model can be trained to perform property prediction for molecules or to identify molecules having targeted properties using the tokenized molecules and their properties. The trained language model can perform property prediction for a molecule not in the molecular database or identify molecules having the targeted properties.
Methods include coating a substrate by applying a coating composition containing one or more branched alcohol alkoxylates having the general formula: where R1 includes C9 to C15 primary branched alcohols having a branching degree of 1.5 or more; R2 is methyl or ethyl group; m is in the range of 4 to 20; and n is in the range of 4 to 20. Coating formulations include those containing one or more surfactants containing one or more branched alcohol alkoxylates, and one or more binders.
H01B 3/44 - Insulators or insulating bodies characterised by the insulating materialsSelection of materials for their insulating or dielectric properties mainly consisting of organic substances plasticsInsulators or insulating bodies characterised by the insulating materialsSelection of materials for their insulating or dielectric properties mainly consisting of organic substances resinsInsulators or insulating bodies characterised by the insulating materialsSelection of materials for their insulating or dielectric properties mainly consisting of organic substances waxes vinyl resinsInsulators or insulating bodies characterised by the insulating materialsSelection of materials for their insulating or dielectric properties mainly consisting of organic substances plasticsInsulators or insulating bodies characterised by the insulating materialsSelection of materials for their insulating or dielectric properties mainly consisting of organic substances resinsInsulators or insulating bodies characterised by the insulating materialsSelection of materials for their insulating or dielectric properties mainly consisting of organic substances waxes acrylic resins
C08L 23/0892 - Copolymers of ethene with unsaturated hydrocarbons containing atoms other than carbon or hydrogen with monomers containing atoms other than carbon, hydrogen or oxygen
C08L 51/06 - Compositions of graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bondsCompositions of derivatives of such polymers grafted on to homopolymers or copolymers of aliphatic hydrocarbons containing only one carbon-to-carbon double bond
According to one or more embodiments, a method of removing fouling may comprise contacting a workpiece with a cleaning solution comprising a hydrocarbon or alcohol solvent and an alkyl sulfonic acid-based surfactant. The workpiece may comprise a metal surface with a fouling material attached thereto. The contacting the workpiece with the cleaning solution may cause at least a portion of the fouling material to be removed from the metal surface.
Embodiments of methods of producing high pressure ethylene-based polymer comprise polymerizing via free-radical polymerization at a pressure of at least 1000 atmospheres (atm) an ethylene monomer feed and optionally additional comonomer feed in the presence of radical scavenger to produce the high pressure ethylene-based polymer, wherein the radical scavenger comprises Structure 1: wherein: n can be 0 to 100; R1, R2 and R3 are each independently H, (C1-C40)hydrocarbyl, (C1-C40)heterohydrocarbyl, or an aromatic containing moiety; and R4-R8 are each independently H, OH, (C1-C40)hydrocarbyl, (C1-C40)heterohydrocarbyl, or an aromatic containing moiety with the proviso that at least one of R4-R8 needs to be OH.
Embodiments of methods of producing high pressure ethylene-based polymer comprise polymerizing via free-radical polymerization at a pressure of at least 1000 atmospheres (atm) an ethylene monomer feed and optionally additional comonomer feed in the presence of radical scavenger to produce the high pressure ethylene-based polymer, wherein the radical scavenger comprises Structure 1: wherein: n can be 0 to 100; R1, R2 and R3 are each independently H, (C1-C40)hydrocarbyl, (C1-C40)heterohydrocarbyl, or an aromatic containing moiety; and R4-R8 are each independently H, OH, (C1-C40)hydrocarbyl, (C1-C40)heterohydrocarbyl, or an aromatic containing moiety with the proviso that at least one of R4-R8 needs to be OH.
Alkoxylation reactions are performed in the presence of a phosphonium catalyst having the structure P+(XR1R2R3)A1 wherein R1 is a group having an unsubstituted or inertly substituted aromatic five-member ring having a direct bond between an atom of the aromatic five-member ring and the phosphorus atom, and each R2 is independently a group having an unsubstituted or inertly substituted, optionally heteroatomic, aromatic five- or six-member ring having a direct bond between a carbon atom of the optionally heteroatomic aromatic five- or six-member ring and the phosphorus atom. X is selected from fluorine, chlorine, bromine, iodine, C1-12 perfluoroalkyl, C1-12 alkyl, aryloxy and C1-12 alkoxy, and A is a weakly coordinating anion.
C07F 9/655 - Heterocyclic compounds, e.g. containing phosphorus as a ring hetero atom having oxygen atoms, with or without sulfur, selenium, or tellurium atoms, as the only ring hetero atoms
C07F 9/6553 - Heterocyclic compounds, e.g. containing phosphorus as a ring hetero atom having sulfur atoms, with or without selenium or tellurium atoms, as the only ring hetero atoms
C08G 65/10 - Saturated oxiranes characterised by the catalysts used
91.
AQUEOUS COATING COMPOSITION AND PROCESS FOR PREPARING THE SAME
An aqueous coating composition comprising (a) from 12.5% to 87% by weight based on the weight of the aqueous coating composition, of a film-forming polymer; (b) from 9.5% to 85% by weight based on the weight of the film-forming polymer, of a specific oligomer; and (c) from 2.5% to 50% by weight based on the weight of the film-forming polymer, of beads with a mean particle size of from 5.0 to 10.5 μm; and a process for preparing the aqueous coating composition.
C09D 4/06 - Coating compositions, e.g. paints, varnishes or lacquers, based on organic non-macromolecular compounds having at least one polymerisable carbon-to-carbon unsaturated bond in combination with a macromolecular compound other than an unsaturated polymer of groups
C09D 133/06 - Homopolymers or copolymers of esters of esters containing only carbon, hydrogen and oxygen, the oxygen atom being present only as part of the carboxyl radical
A process for continuously stripping a polymer dispersion with volatile organic compounds comprises the steps of: supplying steam to a first stripper; supplying steam to a second stripper; with specified steam distribution ratios between the first and second strippers; feeding the polymer dispersion into the first stripper; removing a portion of the volatile organic compounds from the polymer dispersion and transferring them to the steam in the first stripper; feeding the polymer dispersion and steam mixture from the first stripper into the second stripper; separating the steam from the polymer dispersion immediately after entering the second stripper; accumulating the polymer dispersion at the bottom of the second stripper; removing another portion of the volatile organic compounds from the polymer dispersion and transferring them to the steam in the second stripper; and extracting the polymer dispersion from the second stripper while maintaining a portion of the polymer dispersion in the second stripper during the process.
Reacting a waste polymeric product comprising a thermoset having urethane bonds, urea bonds, and/or isocyanurate bonds; a polycarboxylic acid or anhydride; a first polyether polyol having number average molecular weight of from 800 to 5000 grams/mole, and an average of at least 2 hydroxyl groups per molecule wherein at least 50%, hydroxyl groups are primary alcohol; a second a second polyether polyol having a number average molecular weight less than 350 grams/mole, and, optionally, a third polyether polyol having an average of from 1.8 to 7 hydroxyl groups per molecule and having a number average molecular weight of greater than 350 up to 1000 grams/mole can form a reaction product composition directly useful in forming new polyurethane materials.
C08J 11/26 - Recovery or working-up of waste materials of polymers by chemically breaking down the molecular chains of polymers or breaking of crosslinks, e.g. devulcanisation by treatment with organic material by treatment with organic oxygen-containing compounds containing carboxylic acid groups, their anhydrides or esters
94.
MULTI-LAYER STRUCTURES HAVING RECYCLE COMPATIBILIZERS
Embodiments of a multi-layer structure comprise a core layer comprising EVOH or nylon. The multi-layer structure also comprises an outer layer including polyethylene, a recycle compatibilization layer disposed between the core layer and the outer layer, and a tie layer disposed between the core layer and the recycle compatibilization layer. The recycle compatibilization layer comprises at least 60% by weight of a first polyethylene based on the weight of the recycle compatibilization layer, and a compatibilizer having a density from 0.855 to 0.915 g/cc and a melt index (I2) from 1.0 to 50.0 dg/mins. Moreover, the multi-layer structure includes greater than 5 wt.% of the EVOH or nylon and a ratio by weight of the compatibilizer to weight of EVOH or nylon ranging from 0.8:1 to 1:25. The multi-layer structures are recyclable while also demonstrating improved mechanical properties such as dart.
B32B 7/12 - Interconnection of layers using interposed adhesives or interposed materials with bonding properties
B32B 27/08 - Layered products essentially comprising synthetic resin as the main or only constituent of a layer next to another layer of a specific substance of synthetic resin of a different kind
Reacting a waste polymeric product comprising a thermoset having urethane bonds, urea bonds, and/or isocyanurate bonds, a polycarboxylic acid or an anhydride thereof, a first polyether polyol having an average of from 1.8 to 7 hydroxyl groups per molecule and having a number average molecular weight of greater than 350 grams/mole, a second polyether polyol having a number average molecular weight of no greater than 350 grams/mole wherein at least 50 percent of the hydroxyl groups in the second polyether polyol are secondary alcohol can form a reaction product composition directly useful in forming new polyurethane materials.
C08J 11/26 - Recovery or working-up of waste materials of polymers by chemically breaking down the molecular chains of polymers or breaking of crosslinks, e.g. devulcanisation by treatment with organic material by treatment with organic oxygen-containing compounds containing carboxylic acid groups, their anhydrides or esters
The present invention related to a retroreflective composition comprising a composite core and glass beads partially embedded therein, wherein the composite core comprises a poly(ethylene-vinyltrimethoxysilane) copolymer and titanium dioxide. The composition of the present invention is useful in the manufacture of a retroreflective road marking.
xx is 0 to 25; wherein each R1is independently selected from an alkylene radical containing 1 to 10 carbon atoms; wherein each R2 is independently selected from the group consisting of an alkyl group of 1 to 18 carbon atoms, an aryl group of 6 to 18 carbon atoms, an acyloxy group of 2 to 18 carbon atoms, and a hydrocarbonoxy-functional group of 1 to 18 carbon atoms.
A61K 8/58 - Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds containing atoms other than carbon, hydrogen, halogen, oxygen, nitrogen, sulfur or phosphorus
A method of making a morphology-improved polyethylene powder, the method comprising: contacting ethylene with a reactive olefin prepolymer in a gas phase reactor to make a morphology-improved polyethylene powder via gas phase polymerization; wherein the reactive olefin prepolymer comprises a component that is a polyolefin and a component that is an active metallocene derivative of a spray-dried silica-supported metallocene catalyst; wherein the reactive olefin prepolymer has a prepolymer/catalyst weight/weight ratio from 10:1.0 to 50:1.0, wherein the prepolymer weight is the total weight of the reactive olefin prepolymer and the catalyst weight is the weight of the spray-dried silica-supported metallocene catalyst.
C08F 210/18 - Copolymers of ethene with alpha-alkenes, e.g. EP rubbers with non-conjugated dienes, e.g. EPT rubbers
B01J 31/12 - Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides containing organo-metallic compounds or metal hydrides
B01J 37/00 - Processes, in general, for preparing catalystsProcesses, in general, for activation of catalysts
C08F 4/76 - MetalsMetal hydridesMetallo-organic compoundsUse thereof as catalyst precursors selected from metals not provided for in group selected from refractory metals selected from titanium, zirconium, hafnium, vanadium, niobium, or tantalum
Embodiments relate to a twin-screw extruder including two parallel screws, where each parallel screw includes a shaft, a plurality of threaded regions disposed along the length of the shaft. At least two of the threaded regions have different screw pitch, and each threaded region is defined by a ratio of screw pitch to screw diameter of 2.0 or less. There is also at least one non-threaded region disposed along the length of the shaft and adjacent at least one of the threaded regions, where the at least one non-threaded region comprise an uncovered shaft, a sleeve disposed over the shaft, or combination thereof. Further embodiments relate to processes of producing cellulose ether gel from a feed comprising water and cellulose derivatives by using the twin-screw extruder at a temperature below the thermal flocculation point to dissolve and swell the cellulose derivatives in the water to produce the cellulose ether gel.
B29B 7/48 - MixingKneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with more than one shaft with intermeshing devices, e.g. screws
Embodiments of the present disclosure are directed towards imide-containing polyols, methods for making imide-containing polyols, and methods for using imide-containing polyols.
C08J 9/00 - Working-up of macromolecular substances to porous or cellular articles or materialsAfter-treatment thereof
C08J 9/14 - Working-up of macromolecular substances to porous or cellular articles or materialsAfter-treatment thereof using blowing gases generated by a previously added blowing agent by a physical blowing agent organic
C08K 5/521 - Esters of phosphoric acids, e.g. of H3PO4
patents
