320 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.

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.

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 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.

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.

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 present invention relates to a process for the preparation of polycyclic aliphatic dialdehydes by hydroformylation of polycyclic aliphatic diolefins in the presence of synthesis gas over an organophosphorus ligand modified metal catalyst system having a transition metal of the 8th-10th subgroup, wherein the hydroformylation is carried out by means of a water-soluble diphosphine or triarylphosphine complex catalyst at a pressure of greater than or equal to 0.5 MPa and less than or equal to 10 MPa and at a temperature of greater than or equal to 70° C. and less than or equal to 150°° C. in a homogeneous liquid reaction phase, the homogeneous liquid phase comprising at least one non-aqueous solvent, diolefin and / or mono- and / or dialdehydes thereof as reaction products and an aqueous catalyst solution, the proportions of these components in the solution being controlled so as to obtain a single-phase solution under the reaction conditions.

A process for producing an aldehyde is disclosed. The process comprises: hydroformylating an olefin to form the aldehyde using a hydroformylation catalyst; recovering an effluent stream comprising the aldehyde, hydrogen and the hydroformylation catalyst; passing the effluent stream to a stripper; contacting the effluent stream with a strip gas in the stripper to produce a stripped effluent stream having a lower hydrogen concentration than the effluent stream; and recovering the stripped effluent stream.

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 present application provides a catalyst for preparing oxygen-containing compounds by olefin hydroformylation reaction, and a preparation method and use thereof, the catalyst is Fe x Co y M, the catalyst contains 0.1-15wt% M, 85-99.9wt% Fe and Co, the atomic ratio of x to y is 0.1-10, and M is a metal element. When the catalyst is used for preparing oxygen-containing compounds by olefin hydroformylation reaction, the conversion rate of olefin can reach 93-99.9%, and the selectivity of oxygen-containing compounds can reach 89-98.8%; and the catalyst is in a solid state during the reaction, which is easy to realize solid-liquid separation with the product, and also avoids the loss of the catalyst during the separation process.

The utility model belongs to the field of chemical reaction, and particularly relates to an automatic reaction system which comprises a microfluidic device, the microfluidic device is provided with a gas supply module for supplying gas, and the interior of the microfluidic device is used for hydrogenation reaction and hydroformylation reaction; the first mechanical arm module is used for moving a reagent; the first mechanical arm module and the micro-fluidic module are in signal connection with the control module. The utility model provides an automatic reaction system and aims to solve the problem of safety risk of manual operation in the prior art.

This invention provides a method for determining the deactivation temperature and deactivation characteristics of a hydroformylation catalyst, comprising: S1. preparing a hydroformylation reaction solution; S2. measuring the reaction solution and placing it in an adiabatic testing instrument to simulate a hydroformylation reaction, stopping the heating when the temperature reaches T0 and incubating the reaction under adiabatic conditions; recording the temperature change and obtaining the highest temperature T. m S3. After cooling the test ball, remove half of the reactant material, add the hydroformylation reaction raw material, and heat up to simulate the hydroformylation reaction. When the temperature reaches T1, stop heating and perform an adiabatic reaction. Record the highest temperature T. mf S4. Compare T1 and T m and T mf If T mf =T1, catalyst deactivation temperature is T m Irreversible inactivation; if T mf =T m The catalyst deactivation temperature is T m Reversible inactivation; if T mf >T m Remove the material from the test sphere and repeat steps S2 to S4. The judgment method of this invention has a short testing cycle, high safety, and eliminates the need for sample separation and component analysis. It provides guidance for research on catalyst operating limits and the selection of homogeneous catalyst recovery temperatures.

The present invention concerns a process for utilizing waste streams from an oxo synthesis plant by gasification and an oxo process plant comprising the necessary units for oxo synthesis and at least one gasifier G. The process comprises a conversion of a waste stream W1 purged from the alcohol upgrading unit ALUU and optionally also of a waste stream W2 purged from a hydroformylation reaction unit HRU. The conversion by a gasification process in at least one gasifier G results in synthesis gas which can then be utilized e.g., for as a feedstock for an oxo process or production of other chemicals in another chemical production plant.

The application provides a method and device for continuously preparing aldehyde compounds through a hydroformylation reaction. The method for continuously preparing aldehyde compounds through the hydroformylation reaction comprises the following steps: using a catalyst to catalyze an olefin raw material and synthetic gas to perform a hydroformylation reaction, so as to obtain a reaction product containing aldehyde compounds; and separating the reaction product, so as to obtain the aldehyde compounds and recover the catalyst. The hydroformylation reaction comprises a homogeneous reaction or a heterogeneous reaction. The method can solve the problem of a large amount of catalyst loss in the hydroformylation reaction in the prior art and is suitable for the field of Fischer-Tropsch synthesis.

A method for producing a higher alcohol from a waste plastic feedstock is disclosed, comprising: (a) providing a hydrocarbon feed stream comprising a pyrolysis oil feed obtained from pyrolysis of plastic waste, wherein the pyrolysis oil comprises at least 20 wt % higher olefins with a carbon number in the range C5-C20, based on its total hydrocarbon content; (b) contacting the hydrocarbon feed stream with synthesis gas under hydroformylation conditions in the presence of a hydroformylation catalyst and recovering a hydroformylation product; (c) subjecting the hydroformylation product to hydrogenation and / or a distillation to recover a higher alcohol product.

The invention belongs to the technical field of organic-inorganic compounding, and aims to solve the problem of treatment of temporomandibular joint osteoarthritis (TMJOA). Magnesium-gallic acid metal organic framework (Mg-GA MOF) particles are synthesized through a hydrothermal method, hyaluronic acid is subjected to hydroformylation and double-bond modification to obtain OHAMA, and the magnesium-gallic acid metal organic framework (Mg-GA MOF) particles and the OHAMA particles are compounded to prepare the MOF-Gel composite hydrogel. The hydrogel is injectable and high in tissue retention rate, has dual effects of inhibiting pyroptosis and promoting regeneration on condylar cartilage cells, can effectively promote cartilage repair, shows a good effect in TMJOA treatment, and has a wide application prospect.

The invention relates to a method for catalyzing olefin hydroformylation by using a molecular sieve confinement monatomic catalyst, which comprises the following steps: performing hydroformylation on olefin with an R1R2C = CH2 structure and synthesis gas CO / H2 at the temperature of 80-120 DEG C to obtain a product R1R2CH-CH2CHO or R1R2CH (CHO)-CH3. According to the method, Rh1-coated zeolite is used as a catalyst, and an active site monatomic rhodium metal of the catalyst is confined in a molecular sieve frame structure. The catalyst for catalyzing hydroformylation of styrene has the advantages of high conversion rate, high selectivity and high catalytic efficiency. And the catalyst has selective hydroformylation catalysis performance, and realizes accurate selective catalysis of reactant olefin molecules smaller than molecular sieve pore size # imgabs0 #.

The application discloses a rhodium-catalyzed desymmetrization hydroformylation method for constructing polychiral center carbon ring nucleosides. The method for constructing polychiral center carbon ring nucleosides comprises the following steps: under the condition of an inert atmosphere, an acetylacetone dicarbonyl rhodium metal precursor and a chiral ligand are added into an organic solvent to prepare a catalyst solution, the catalyst solution is mixed with a substrate, and a reaction is carried out under the condition of a hydrogen atmosphere and a carbon monoxide atmosphere; after the reaction is completed, filtration and purification are carried out, and polychiral center cycloalkyl aldehyde is obtained; and the aldehyde group is converted to obtain the polychiral center carbon ring nucleosides. The method for constructing polychiral center carbon ring nucleosides has the advantages of high selectivity, wide substrate compatibility, high reaction efficiency, easy conversion of products, and the like. The whole reaction process can obtain polychiral center cycloalkyl aldehyde in one step with extremely high enantioselectivity and diastereoselectivity, the aldehyde group is converted, polychiral center carbon rings can be obtained with high yield, high dr value and high ee value, and the method is simple and easy to operate.

A Method for the synthesis of ω-amino acids or derivatives thereof, includes the following steps synthesis of an ω-oxoester / linear acid by hydroformylation by CO / H2 mixture of at least one monounsaturated acid / ester, the monounsaturated acid / ester preferably resulting from a reaction of metathesis of oils / fats from renewable sources; synthesis of a linear ω-amino acid / ester and / or ω-aminoamide, subjecting the aforementioned ω-oxoester / linear acid to reductive amination; and possible synthesis of a linear ω-amino acid, subjecting the aforementioned linear ω-aminoester and / or ω-aminoamide to hydrolysis.

The invention belongs to the technical field of preparation methods of fine compounds, and particularly relates to a preparation method of 3-(3-isopropyl phenyl) butyraldehyde. The method comprises the following steps: by taking a mixed material of m-isopropenyl cumene and phenylcyclopentene as a raw material, carrying out carbonylation reaction under the action of a catalyst; the catalyst is a noble metal carbonyl catalyst; after the reaction is finished, a reaction product is rectified, and isopropenyl isopropyl benzene is obtained; and carrying out formylation reaction on the product, and separating to obtain the 3-(3-isopropyl phenyl) butyraldehyde. The method has the advantages that raw material sources are simplified, physical and chemical properties of products obtained after different components react are changed through different reaction conditions of the different components in the reaction process, the purposes of separation, removal and purification are easily achieved, then the target product is obtained through the hydroformylation reaction, high purity is kept, and the method is suitable for industrial production. And moreover, the conversion rate is more thorough, and the cost can be greatly reduced compared with the existing production technology economically.

The present application relates to a kind of high selectivity synthesis method of secondary aldehyde.The synthesis method includes the following steps: adding catalyst, ligand, solvent into reaction device, and importing olefin and synthesis gas, so that the reaction system is under heating to carry out first stage reaction;After first stage reaction is carried out for 10-300 minutes, continue to import synthesis gas into reaction device, so that the pressure of reaction system is increased, and second stage reaction is carried out, to obtain secondary aldehyde;The pressure of reaction system during first stage reaction is 0.1-0.5 MPa;Olefin is terminal olefin or mixture containing terminal olefin.The present application first carries out low-pressure isomerization, then high-pressure hydroformylation, cooperates with specific kind of big steric hindrance monodentate phosphite ligand, controls the molar ratio of ligand and catalyst, and the three produce synergies, so that terminal olefin or terminal olefin in mixture material is first isomerized in situ, then together with original internal olefin is converted into target secondary aldehyde product with high selectivity.