564 results about "Hydroformylation" patented technology

The invention belongs to the technical field of catalysts, and particularly relates to a supported Co-based catalyst with a nano molybdenum carbide auxiliary as well as a preparation method and application of the supported Co-based catalyst. The preparation method comprises the following steps: depositing molybdenum oxide on the surface of a carrier material by adopting an atomic layer deposition method, then carrying out carburizing treatment to obtain a molybdenum carbide catalyst, depositing cobalt oxide on the surface of the molybdenum carbide catalyst by adopting the atomic layer deposition method, and then carrying out reduction treatment to obtain the supported cobalt-based catalyst with the nano molybdenum carbide assistant. According to the preparation method provided by the invention, the size of molybdenum carbide and the dispersity and valence state of cobalt are controlled by regulating and controlling the deposition times of molybdenum oxide, and the prepared catalyst has excellent catalytic activity and stability in the hydroformylation reaction of long-chain olefin with the carbon atom number being greater than or equal to 5.

A method for the generation of a gas mixture including carbon monoxide, carbon dioxide and hydrogen for use in hydroformylation plants, including the steps of evaporating water to steam; feeding the steam to a solid oxide electrolysis cell (SOEC) or an SOEC stack at a sufficient temperature for the cell or cell stack to operate while effecting a partial conversion of steam to hydrogen; utilizing the effluent SOEC gas including H2 together with CO2 from an external source as feed for a RWGS reactor in which the RWGS reaction takes place, converting some of the CO2 and H2 to CO and H2O; removing some of or all the remaining steam from the raw product gas stream; using said gas mixture comprising CO, CO2 and H2 for liquid phase hydroformylation utilizing carbon monoxide and hydrogen as reactants, while recycling CO2 to the RWGS reactor.

The invention belongs to the field of petrochemical industry, and relates to a production method of isononyl alcohol and a production device of isononyl alcohol. The production method of the isononyl alcohol comprises the following steps: C8 olefin, synthesis gas and a catalyst enter a raw material reactor to react to obtain a hydroformylation reaction product, the hydroformylation reaction product enters a product separation unit to separate and remove by-products, and then the hydroformylation reaction product enters an aldehyde hydrogenation unit to react to obtain the isononyl alcohol. The invention has the following beneficial effects: the product separation unit removes most of non-condensable steam, light components and water through a low-vacuum flash evaporation-high-vacuum evaporation two-stage process, reduces the load of a high-vacuum system, and saves energy consumption; the circulation path of the catalyst is shortened through the efficient and rapid separation process of the catalyst, and decomposition of the catalyst is reduced; by applying the vacuum evaporator, low-pressure and low-temperature rapid separation of materials is achieved, the catalyst circulation process is short, the separation temperature is low, and meanwhile energy consumption is saved.

The invention discloses a cobalt-rhodium-doped nitrided activated carbon supported composite catalyst and a preparation method thereof, and application of the catalyst in preparation of aldehyde by catalyzing olefin, especially application of diisobutylene in preparation of isononanal. In the composite catalyst, the content of Rh is 0.2-1.5 wt% in terms of Rh atoms, the content of Co is 0.1-0.8 wt% in terms of Co atoms, the mass ratio of Co to Rh is 10: 1-1: 1, preferably 2: 1, and Co and Rh exist in the form of nanoclusters or monatomic atoms and are connected to a carbon nitride skeleton structure in the form of covalent bonds. According to the composite catalyst, the structure mainly comprises micropores and is provided with a small number of mesopores and macropores, the adsorption capacity of the material is enhanced, meanwhile, the material belongs to a heterogeneous catalytic material, the technical problem that the material is difficult to recycle is solved, cyclic utilization is facilitated, and the use cost is reduced. The catalyst can realize high-efficiency hydroformylation of diisobutylene to prepare isononanal, can be recycled and has an industrial application prospect in the aspect of olefin hydroformylation.

The invention relates to the technical field of heterogeneous catalysis and fine chemical engineering, and discloses a rhodium-tungsten para-site MOF-based catalyst as well as preparation and application thereof. The invention relates to a rhodium-tungsten para-site MOF-based catalyst, which is composed of a catalytic active component, a metal additive and a carrier. The rhodium-tungsten para-site MOF-based catalyst provided by the invention takes a metal organic framework material as a carrier, an active component Rh and a metal additive W are stably anchored on the surface of the carrier, and an Rh-WOx para-site is successfully constructed; the rhodium-tungsten para-site MOF-based catalyst provided by the invention shows excellent catalytic activity and excellent cycle stability in olefin hydroformylation reaction, and overcomes the technical bottlenecks that noble metals in a homogeneous catalysis system are easy to lose and energy consumption is high in a product separation process; an efficient and stable catalyst design thought is provided for olefin hydroformylation reaction, and the catalyst has a good industrial application prospect.

The invention provides a heat extraction distribution structure for an isononyl alcohol hydroformylation reactor, and relates to the technical field of isononyl alcohol hydroformylation reactors, the heat extraction distribution structure comprises an inner tube box and an outer tube box, the inner tube box is arranged in the outer tube box, a heat extraction medium inlet cavity is formed in the inner tube box, and a heat extraction medium outlet cavity is formed between the inner tube box and the outer tube box; the heat exchange pipes are U-shaped pipes, a heat removal medium inlet and a heat removal medium outlet are formed in the two ends of each heat exchange pipe correspondingly, and the heat removal medium inlets and the heat removal medium outlets communicate with the heat removal medium inlet cavity and the heat removal medium outlet cavity correspondingly; the distribution plate is provided with a plurality of positioning through holes and a distribution structure, and each heat exchange tube penetrates through two positioning through holes; the problems that in the prior art, a gas-liquid up-flow type bubbling bed reactor is not internally provided with internal components, gas distribution and heat extraction cannot be achieved, and the conversion rate of reaction is low are solved.

The invention discloses an amidoximation hydrotalcite material as well as a preparation method and application thereof, and the method comprises the following steps: grafting and modifying an amino group on hydrotalcite to obtain an amination modified hydrotalcite material; grafting and modifying an aldehyde group on the amination modified hydrotalcite material to obtain an aldehyde modified hydrotalcite material; carrying out condensation reaction on the hydroformylation modified hydrotalcite material and a reagent containing amino and cyano groups at the same time to obtain a cyanylation modified hydrotalcite material; and carrying out amidoximation reaction on the cyanation modified hydrotalcite material and an oximation reagent to obtain the cyanation modified hydrotalcite material. The amidoximation hydrotalcite powder material prepared by the preparation method disclosed by the invention can realize high-specificity recognition and efficient adsorption on uranyl ions.

The invention relates to an olefin hydroformylation homogeneous catalysis continuous reaction process and system. The process comprises the following steps: mixing raw materials olefin, synthesis gas and a metal catalyst, and then carrying out hydroformylation reaction; removing a light component containing the product aldehyde from the hydroformylation reaction liquid to obtain a heavy component containing the metal catalyst; uniformly mixing the heavy component with a first extraction agent, and performing phase splitting to obtain a first heavy component phase and a first extraction agent phase; a metal catalyst and a second extraction agent are separated from the first extraction agent phase, the metal catalyst is circularly used for the hydroformylation reaction, and the second extraction agent is used as the first extraction agent mixed with the heavy components. Based on the characteristics of solubility difference and specific gravity difference between the metal catalyst and other substances in the heavy components under specific conditions, the heavy components in a reaction system are reacted at a lower temperature on the premise of not additionally adding a reagent which can influence the activity of the catalyst, and the activity of the catalyst can be well maintained within a longer reaction time.

A process for producing branched aldehyde intermediates from alpha olefins, and further reacting said branched aldehyde intermediates via hydrogenation reactions, surfactant forming reactions and other chemical derivative forming reactions to produce branched alcohols, branched surfactants and other branched derivatives. A process for producing isomerized olefins, branched aldehydes, branched alcohols, branched surfactants and other branched derivatives through isomerization, hydroformylation, hydrogenation, surfactant forming reactions and other derivative forming reactions.

A process for the manufacture of styrene acrylic copolymers having a renewably-sourced carbon content comprises the steps of: a) subjecting a feedstock comprising a renewably-sourced ethanol to dehydration to produce a renewably-sourced ethylene stream; b) subjecting at least a portion of the renewably-sourced ethylene stream to an olefin-interconversion, to obtain a renewably-sourced propylene; the olefin- interconversion comprising (i) and (ii): (i) ethylene dimerization to obtain n-butenes; (ii) metathesis reaction between n-butenes obtained according to (i) and ethylene to obtain propylene; and c) subjecting a portion of the renewably-sourced propylene to an oxidation reaction to produce acrylic acid; d) subjecting a portion of the renewably- sourced propylene to a hydroformylation reaction with syngas to produce n-butyraldehyde; e) subjecting the n-butyraldehyde to hydrogenation to produce n-butanol; f) esterifying acrylic acid obtained in step c) and the n-butanol to produce n-butyl acrylate; g) subjecting ethylene to an alkylation reaction with benzene to produce ethylbenzene; h) subjecting the ethylbenzene to a dehydrogenation reaction to produce styrene; i) copolymerizing the styrene and the n-butyl acrylate to produce a styrene acrylic copolymer. The process has a high renewably-sourced carbon content, in particular an increased renewably-sourced carbon content with respect to the renewably-sourced carbon content available in a cracker-based process.

The invention discloses a method for preparing 1, 3-propylene glycol by hydrating and hydrogenating acrolein, which comprises the following steps: carrying out hydration reaction by taking an acrolein aqueous solution as a raw material and taking acylated and aminated modified polystyrene resin as a catalyst; carrying out flash evaporation or gas stripping on the product after the reaction to remove acrolein, condensing and recovering the removed acrolein, and carrying out hydrogenation reaction on the acrolein-removed mixed solution serving as a hydrogenation raw material on a metal catalyst; and after the reaction is finished, performing flash evaporation on the product to remove water and light components, and performing vacuum rectification to obtain a high-purity 1, 3-propylene glycol product. According to the method, the modified resin is used for catalyzing the acrolein hydration reaction, the overall yield of the 1, 3-propylene glycol can be increased, the catalyst modification process is simple, the cost is low, the additional value of the final product is high, and the method is suitable for industrial production.

The invention discloses a composition and a method for preparing high-carbon aldehyde through water / oil two-phase hydroformylation. The composition comprises a rhodium catalyst, a water-soluble phosphine ligand and a quaternary ammonium salt cationic surfactant, the structural formula of the quaternary ammonium salt cationic surfactant is shown in a formula (I), R1, R2, R3, R4 and R5 are independently selected from methyl, ethyl and C3-C18 straight-chain or branched-chain alkane, and X is F, Cl or Br; the molar ratio of the water-soluble phosphine ligand to the rhodium catalyst is (0.1-20): 1; the molar ratio of the quaternary ammonium salt cationic surfactant to the rhodium catalyst is (0.05-100): 1. # imgabs0 #

The invention discloses a system device and a method for producing aldehyde compounds through supergravity two-phase hydroformylation. The system device comprises a supergravity reactor, a buffer tank, a first circulating pump, a tower kettle heat exchanger, a circulating heat exchanger, a split-phase tank, a second circulating pump, a crude aldehyde transfer pump, a supergravity rectification unit, a tower kettle reboiler, a product extraction pump and a cold and hot all-in-one machine. According to the system device, under the condition that a polar solvent and a surfactant are not added, the two-phase hydroformylation reaction process can be greatly enhanced through the supergravity reactor, the technological process is shortened, and then a product is separated and purified through the supergravity rectification unit to obtain an aldehyde compound; the problems of low two-phase hydroformylation reaction efficiency, serious self-polymerization in a hydroformylation product purification process and the like in the prior art are solved; by utilizing the method, the olefin conversion rate is more than 90%, the aldehyde selectivity of the product is more than 99%, the purity of the purified product is more than 99%, and the loss amount of the catalyst is less than or equal to 0.5 mg / kg.

The invention relates to glucose and pH dual-response hydrogel capable of intelligently responding to release of platelet-rich plasma, preparation and application, and belongs to the field of cellulose materials.Chitosan is alkalized and then subjected to carboxymethylation treatment, and carboxymethyl chitosan is obtained; the preparation method comprises the following steps: oxidizing nano cellulose to obtain hydroformylation modified nano cellulose; carboxymethyl chitosan and hydroformylation modified nano cellulose are mixed, glucose oxidase, platelet-rich plasma and nano cerium oxide particles are added in the mixing process, and the glucose and pH dual-response hydrogel capable of intelligently responding to release of platelet-rich plasma is obtained. According to the invention, a cross-linking agent is not needed, the operation is simple, the cost is low, the hydrogel can be rapidly formed, and the hydrogel can be automatically and gradually dissolved to release micromolecular substances wrapped in the hydrogel after being stimulated by glucose and pH change, is environment-friendly, has good biocompatibility, and is beneficial to promoting the application of the hydrogel in the fields of diabetes wound dressings and the like.

The invention relates to the technical field of organic catalysis, in particular to a method for preparing glycolaldehyde by catalyzing formaldehyde hydroformylation. The method comprises the following steps: introducing CO and H2 into a mixed solution of paraformaldehyde, a rhodium compound, a ligand and a solvent, and reacting to prepare glycolaldehyde, the ligands comprise a ligand 1 and a ligand 2; the ligand 1 is selected from one or more of compounds as shown in the following L1-L8: # imgabs0 #; the structural formula of the ligand 1 is as shown in the specification, the structural formula of the ligand 2 is as shown in the specification, namely # imgabs1 # or # imgabs2 #, R1 is H, (CH2) ACH3, O-(CH2) ACH3, X or CX3, the value range of A is 0-3, and X is a halogen atom. According to the method disclosed by the invention, different ligands are subjected to dominant combination and cooperate with the rhodium-based catalyst, so that glycolaldehyde is obtained with high conversion rate and high selectivity under relatively mild conditions.

The invention discloses a tandem catalysis method for improving the catalytic efficiency of preparing higher alcohol by CO2 hydrogenation, which comprises the following steps: two sections of fixed bed reactors are connected in series, the first section of reactor is filled with a catalyst for preparing olefin by CO2 hydrogenation, and the second section of reactor is sequentially filled with an olefin hydroformylation catalyst and a catalyst for preparing alcohol by aldehyde hydrogenation. According to the invention, segmented catalysis is carried out on the complex process of preparing higher alcohols through CO2 hydrogenation, and a catalyst for preparing olefins through CO2 hydrogenation, a hydroformylation catalyst and an aldehyde hydrogenation catalyst are respectively arranged in an upstream-segment reactor and a downstream-segment reactor, so that the efficiency and selectivity of preparing higher alcohols through CO2 hydrogenation are improved; through tandem catalysis, the selectivity of by-product hydrocarbons can be effectively reduced, the utilization rate of carbon is improved, the selectivity and space-time yield of higher alcohols are remarkably improved, and the separation cost of products is reduced.

The invention provides a method for judging the inactivation temperature and the inactivation characteristic of a hydroformylation catalyst. The method comprises the following steps: S1, preparing a hydroformylation reaction solution; s2, measuring the reaction liquid, filling the reaction liquid into an adiabatic test instrument to simulate a hydroformylation reaction, and when the temperature is increased to T0, stopping heating and carrying out an adiabatic reaction; recording the temperature change, and obtaining the highest temperature Tm; s3, cooling the test ball, taking out half of a reaction material, adding a hydroformylation reaction raw material, heating to simulate a hydroformylation reaction, stopping heating when the temperature is increased to T1, carrying out an adiabatic reaction, and recording the highest temperature Tmf; s4, comparing T1, Tm and Tmf; if Tmf is equal to T1, the inactivation temperature of the catalyst is Tm, and irreversible inactivation is carried out; if Tmf is equal to Tm, the inactivation temperature of the catalyst is Tm, and reversible inactivation is carried out; if Tmfgt; and Tm, taking out the material in the test ball, and repeating the steps S2-S4. The judgment method disclosed by the invention is short in test period and high in safety, does not need separation and component analysis on a test sample, and has guiding significance on catalyst operation upper limit and homogeneous catalyst recovery temperature selection research.

The invention belongs to the technical field of grinding materials, and particularly discloses an elastic brush wheel for a precise packaging carrier plate and a preparation method, and the elastic brush wheel comprises a supporting pipe, a sponge coating the surface of the supporting pipe, rubber coating the surface of the sponge, and a grinding sheet coating the surface of the rubber. The grinding sheet is prepared from the following raw materials in parts by weight: 1-5 parts of polyvinyl alcohol, 12-21 parts of distilled water, 5-20 parts of phenolic resin, 7-10 parts of hydroformylation agent, 5-6 parts of catalyst and 40-70 parts of grinding material, so that the grinding sheet can be better attached to the surface of a packaging carrier plate, and the elastic brush wheel can improve the grinding efficiency on the basis of carrying out continuous line production on the packaging carrier plate. And the grinding precision and the grinding uniformity of the packaging carrier plate are greatly improved, so that the machined packaging carrier plate has the precision requirement for surface roughness.

A process reacts olefins having 4 to 20 carbon atoms and the feed stream used, containing at least linear olefins and branched olefins, is distilled between two reaction steps and only the high-boiler phase obtained in this distillation is subjected to the second reaction, a heterogeneously catalysed hydroformylation, a homogeneously catalysed hydroformylation or a homogeneously catalysed alkoxycarbonylation.

The invention relates to a method for preparing aldehyde through butene hydroformylation, which comprises the following steps: dissolving a rhodium catalyst, a phosphite ester ligand and a butene raw material in an amide solvent to obtain a premixed solution, and keeping the premixed solution at 0 DEG C or below; adding the premixed liquid into a mixed atmosphere of hydrogen and carbon monoxide; heating the premixed solution to a preset temperature, and reacting for a preset time to obtain a mixed solution; after the mixed liquid is layered, upper liquid is obtained through liquid separation, an aldehyde product is obtained, and the butene raw material comprises at least one of 1-butene and 2-butene. In the reaction process, a ligand does not need to be supplemented, and the problem of more impurities caused by hydrolysis does not exist.

Ru catalyzed cascade hydroformylation / hydrogenation / esterification using imidazole ligands.

The present invention provides an iridium-based catalyst, a preparation method thereof, and a method for catalytic hydroformylation of propylene. The structural formula of the iridium-based catalyst is where Ph is a phenyl group, x is any one of 0, 1, and 2, and X is any one of Cl, NO<subgt;3< / subgt;, BF<subgt;4< / subgt;, PF<subgt;6< / subgt;, and acac. The iridium-based catalyst disclosed in the present invention has good catalytic effect and high activity, and can still maintain high catalytic performance after being used multiple times.

The present invention discloses an eggshell type catalyst, and a preparation method and application thereof in propylene hydroformylation reaction. The eggshell type catalyst uses phosphine ligand resin pellets with developed pore structure as a carrier and one, two or more than two of metals Rh, Co, Ir, Ru and Pd as active components. The spatial distribution of the active metal components in the resin pellets is effectively regulated through a method of finely regulating the porous channel structure of the carrier resin pellets and adding competitive adsorption and coordination, so that the prepared eggshell type catalyst has the characteristics of high activity in the propylene hydroformylation reaction and good selectivity of n-butyraldehyde in the product aldehyde.

Bis-phosphites having 2-phenylphenol flanking structural units and their use in hydroformylation.

The invention provides a catalyst for adjusting the normal / isomeric ratio of a butyraldehyde product and an adjusting method of the catalyst. The catalyst comprises a ligand A, a ligand B and a rhodium substrate, wherein the ligand A is one or more of # imgabs 0 #, # imgabs 1 #, # imgabs 2 # or # imgabs 3 #; and the ligand B is # imgabs4 #. The invention provides a catalyst for adjusting the normal / isomer ratio of a formaldehyde product in the process of preparing butyraldehyde through a propylene hydroformylation reaction, and the catalyst has propylene hydroformylation catalytic activity after complexing a ligand A, a ligand B and a rhodium substrate based on an accurately designed ligand combination. A mixed ligand composed of a ligand A and a ligand B according to a certain proportion is added in a propylene hydroformylation reaction to be complexed with rhodium, so that the n-iso-ratio of butyraldehyde can be flexibly adjusted in a range of 1-17.3.

A method for the generation of a gas mixture including carbon monoxide, carbon dioxide and optionally hydrogen for use in hydroformylation plants or in carbonylation plants, including mixing an optional steam with carbon dioxide in the desired molar ratio, feeding the resulting gas to a solid oxide electrolysis cell (SOEC) or an SOEC stack at a sufficient temperature for the cell or cell stack to operate while effecting a partial conversion of carbon dioxide to carbon monoxide and optionally of steam to hydrogen, removing some or all the remaining steam from the raw product gas stream by cooling the raw product gas stream and separating the remaining product gas from a liquid, and using the gas mixture containing CO and CO2 for liquid phase synthesis reactions utilizing carbon monoxide as one of the reactants while recycling CO2 to the SOEC or SOEC stack.

This invention discloses a ruthenium catalyst supported on a phosphine-containing porous organic polymer and its preparation method. The phosphine-containing porous organic polymer serves as both a support and a solid ligand. The phosphine-containing porous organic polymer ligand is a random copolymer, and its structure can be represented by general formula I. The ruthenium catalyst supported on the phosphine-containing porous organic polymer according to this invention has a large specific surface area and contains a hierarchical porous structure, enabling efficient direct preparation of alcohols from olefins via reductive hydroformylation, and is easily recyclable. It exhibits excellent activity and regioselectivity in the direct preparation of alcohols from olefins via reductive hydroformylation, with an alcohol selectivity of nearly 90% and a high ratio of straight-chain alcohols to branched-chain alcohols.

This invention belongs to the field of homogeneous catalysis technology, and particularly relates to a method for the hydroformylation of propylene to prepare isobutyraldehyde. The method includes: in the presence of a bidentate P-N ligand and a rhodium metal compound, introducing propylene and syngas to carry out a hydroformylation reaction to prepare isobutyraldehyde. The structural formula of the bidentate P-N ligand is as follows: [Insert structural formula here]. Wherein, R1 is selected from one of C2-C4 alkyl groups, substituted or unsubstituted phenyl groups; R2 is selected from one of hydrogen, C1-C4 alkyl groups, alkoxy groups, substituted or unsubstituted phenyl groups. This method provides a highly active P-N ligand, which, while reducing the amount of rhodium catalyst, maintains high activity and can significantly improve the conversion rate of propylene, as well as the selectivity and yield of isobutyraldehyde.

A process for producing branched aldehyde intermediates from alpha olefins, and further reacting said branched aldehyde intermediates via hydrogenation reactions, surfactant forming reactions and other chemical derivative forming reactions to produce branched alcohols, branched surfactants and other branched derivatives. A process for producing isomerized olefins, branched aldehydes, branched alcohols, branched surfactants and other branched derivatives through isomerization, hydroformylation, hydrogenation, surfactant forming reactions and other derivative forming reactions.

The invention discloses a method for improving the selectivity of normal aldehyde in a high-carbon olefin hydroformylation reaction, the catalyst takes one, two or more than two of metals Rh, Co, Ir, Ru, Pt, Pd and Fe as an active component, and a carrier is an improved phosphine-containing porous organic polymer. The heterogeneous catalyst provided by the invention has good performance in the hydroformylation reaction of high-carbon olefins.