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40results about How to "Improve hydrogenation reactivity" patented technology

Heteropolyacid-containing aromatics hydrogenation catalyst and preparation method thereof

The invention discloses a heteropolyacid-containing aromatics hydrogenation catalyst and a preparation method thereof, relating to a catalyst. The invention provides the heteropolyacid-containing aromatics hydrogenation with high sulphur resistance and high activity and the preparation method thereof. The catalyst comprises caesium heteropolyacid salts, hydrogenated components and a carrier, wherein the heteropolyacid caesium salts are caesium phosphotungstate or caesium silicotungstate, and the like; the hydrogenated components comprise Ni transition metal element, and the like; the carrier is a porous heat-resisting inorganic material; and the contents of all the components of the catalyst in percentage by mass are that: 5-40 percent of heteropolyacid, 0.2-0.5 percent of caesium, 5-20 percent of hydrogenated component and the balance of carrier. The preparation method comprises the following steps of: adding an water-soluble nickel salt solution and water-soluble heteropolyacid caesium salts into the carrier and impregnating; drying solid matters obtained through liquid-solid separation, and then roasting; preparing an aqueous caesium heteropolyacid salt solution, adding the aqueous caesium heteropolyacid salt solution to the obtained solid matters; impregnating and drying; and tabletting and forming to obtain the heteropolyacid-containing aromatics hydrogenation catalyst.
Owner:XIAMEN UNIV

Ru-Co nanocatalyst and application of Ru-Co nanocatalyst in selective hydrogenation reaction of benzaldehyde compound

The invention relates to an active carbon loaded Ru-Co nanocatalyst and its application in a selective hydrogenation reaction of a benzaldehyde compound. The Ru-Co nanocatalyst is characterized in that a metallic ruthenium compound and a metallic cobalt compound undergo coprecipitation on an active carbon carrier and then reduction is carried out under a hydrogen atmosphere so as to obtain the Ru-Co nanocatalyst, wherein mass ratio of ruthenium to cobalt to active carbon in the prepared active carbon loaded Ru-Co nanocatalyst is 1: (10-100): (50-500). According to the selective benzaldehyde compound hydrogenation reaction catalyzed by the Ru-Co nanocatalyst, the benzaldehyde compound is converted to obtain corresponding benzyl alcohol. A preparation method of the catalyst is simple; raw materials are cheap and easily available; and the Ru-Co nanocatalyst is suitable for industrial production. In addition, the catalyst shows good activity and selectivity for the hydrogenation reaction of the benzaldehyde compound, and the catalyst is easy to recycle and reuse.
Owner:NANJING UNIV OF TECH

Method for preparing polymers

The invention relates to the field of copolymers, and discloses a method for preparing polymers. The method includes steps of (1), mixing glue solution of unsaturated polymers and hydrogenation catalysts with one another; (2), sequentially carrying out first hydrogenation reaction and second hydrogenation reaction on mixtures obtained at the step (1) in the presence of hydrogen; (3), removing solvents in reaction products obtained at the step (2). The hydrogenation catalysts contain organic compounds of organic aluminum and metal of VIIIB groups. The reaction temperatures of the first hydrogenation reaction range from -10 DEG C to 15 DEG C, and the reaction temperatures of the second hydrogenation reaction range from 40 DEG C to 120 DEG C. The method for preparing the polymers has the advantages that the hydrogenation reaction activity of the hydrogenation catalysts and the hydrogenation degrees of hydrogenation products can be improved, and the method is easy to operate and implement, short in reaction time and low in preparation cost.
Owner:CHINA PETROLEUM & CHEM CORP +1

Loaded nickel-based catalyst and preparation method and application thereof

The invention discloses a loaded nickel-based catalyst. The loaded nickel-based catalyst comprises an active component and a composite carrier, wherein the active component comprises nickel, zinc, iron and cobalt; the active component is loaded on the composite carrier to form the loaded nickel-based catalyst of which the structure is shown as Ni-Zn-Fe-Co / SiO2-TiO2; the loaded nickel-based catalyst comprises 30-80% by mass of nickel, 0.1-15% by mass of zinc, 0.1-5% by mass of iron, 0.1-15% by mass of cobalt, 10-50% by mass of silica, and 1-30% by mass of titanium dioxide. The prepared Ni-Zn-Fe-Co / SiO2-TiO2 loaded nickel-based catalyst is obvious in petroleum resin hydrogenation decoloring effect; the preparation processes and equipment are simple; the industrial production can be easilycarried out; and the loaded nickel-based catalyst has a good application prospect and has huge economic benefit.
Owner:SHANGHAI XUNKAI NEW MATERIAL TECH

Preparation method of catalyst for alkyne selective hydrogenation

The invention relates to a supported copper-base catalyst for alkyne selective hydrogenation. The catalyst comprises a carrier and following components loaded on the carrier: (a) 5 to 15 wt% of copper, (b) 0.5 to 3 wt% of iridium, (c) 0.5 to 3 wt% of phosphor, and optional zirconium and / nickel. The carrier is preferably chosen from aluminum oxide, titanium oxide, silicon oxide, titanium oxide-aluminum oxide, titanium oxide-silicon oxide, or aluminum oxide-silicon oxide, and most preferably, the carrier is titanium oxide-aluminum oxide. The catalyst can be used to eliminate alkyne in C4 fraction through hydrogenation, has the advantages of high catalytic activity, high selectivity, good stability, and long service life, and is capable of preventing sulfur and arsenic poisoning.
Owner:CHINA PETROLEUM & CHEM CORP +1

Preparation method of alumina carrier

The invention discloses a preparation method of an alumina carrier. The method comprises the following steps: using an acidic aluminum salt solution and an alkaline aluminate solution to carry out a glue-forming process through a parallel flow method, adding a gemini surfactant before the glue-forming process or during the glue-forming process, and after the glue-forming process, subjecting the glue to the processes of aging, filtering, washing, drying, forming, drying, and burning so as to obtain the alumina carrier. The gemini surfactant has the same advantages as those of negative ion surfactants and positive ion surfactants, thus the gemini surfactant is used to replace the negative ion surfactants and positive ion surfactants so as not to bring in new impurity ions; furthermore, the gemini surfactant has a large molecular weight and thus has a good pore-enlarging effect; and finally alumina particles, which have the advantages of large pore diameter, large pore volume, and high strength, are obtained. The alumina carrier can be used as a carrier of a hydro-treatment catalyst, and is especially suitable for being taken as a carrier of a residual oil hydro-treatment catalyst.
Owner:CHINA PETROLEUM & CHEM CORP +1

Preparation method of hydro-treatment catalyst

The invention discloses a preparation method of a hydro-treatment catalyst. The preparation method comprises the following steps: using an gemini surfactant acidic aluminum salt solution and an alkaline aluminate solution to carry out a glue-forming process through a parallel flow method, adding a gemini surfactant before the glue-forming process or during the glue-forming process, making the obtained alumina dry glue into an alumina carrier, and loading an active metal component on the alumina carrier through an impregnation method so as to obtain the hydro-treatment catalyst. The gemini surfactant has the same advantages as those of negative ion surfactants and positive ion surfactants, thus the gemini surfactant is used to replace the negative ion surfactants and positive ion surfactants so as not to bring in new impurity ions; furthermore, the gemini surfactant has a large molecular weight and thus has a good pore-enlarging effect; and finally a hydro-treatment catalyst, which has the advantages of large pore diameter, large pore volume, and high strength, is obtained. The hydro-treatment catalyst is especially suitable for residual oil hydro-treatment.
Owner:CHINA PETROLEUM & CHEM CORP +1

Preparation method for granular hydrogenation catalyst

The invention discloses a preparation method for a granular hydrogenation catalyst. The method comprises the following steps of: preparing aluminum hydroxide colloid at a relatively low temperature by adopting pH value oscillation colloid formation, adding an ammonia solution containing Mo and Ni after the low-temperature colloid formation, stabilizing the solution for certain time at a high temperature, filtering, washing, drying, crushing the dried colloid powder into granules, and thus obtaining the granular hydrogenation catalyst by roasting. By the method, the granular hydrogenation catalyst with large aperture, large specific surface area, low abrasion and uniform active metal distribution can be prepared. The hydrogenation catalyst is particularly suitable to be used as a boiling bed residuum hydro-treating catalyst, and can reduce the diffusion limitation of macromolecular compounds such as colloid and bituminous matter and the like in the residuum in the catalyst; the hydrogenation reaction activity of the catalyst can be improved; the catalyst has strong abrasion resistance; the consumption of the catalyst is reduced; and meanwhile, the influence of the catalyst on the downstream reaction or equipment is also reduced.
Owner:CHINA PETROLEUM & CHEM CORP +1

A benzene hydrogenation catalyst and a preparing method thereof

A benzene hydrogenation catalyst and a preparing method thereof are disclosed. The catalyst includes, based on mass of oxides, 90.3-97 wt% of an alumina carrier having a macroporous structure and adopting chitosan as a pore-enlarging agent, 0.2-4.9 wt% of an active component that is platinum oxide and 0.2-4.8 wt% of an active component that is palladium oxide. The macroporous alumina carrier comprises auxiliary components which are tin, lanthanum and potassium. The catalyst has high benzene hydrogenation activity, the rate of loss of precious metal active components is low, and an operation cycle is long.
Owner:QINZHOU UNIV

Purification method for glycol

The invention provides a purification method for glycol. The purification method comprises the following steps: (1) physical adsorption: allowing a crude glycol product to pass through an active carbon bed for physical adsorption so as to obtain a first material flow; and (2) hydrofinishing: subjecting the first material flow, hydrogen and a compound hydrogenation catalyst to a contact reaction, wherein the composite hydrogenation catalyst comprises continuous-phase carbon and dispersion-phase Raney alloy particles, the dispersion-phase Raney alloy particles are uniformly or nonuniformly dispersed in the continuous-phase carbon, and the continuous-phase carbon is prepared by carbonizing carbonizable organic matters or mixtures thereof. The method provided by the invention can realize high-efficiency purification and substantially improves the UV transmittance of glycol.
Owner:CHINA PETROLEUM & CHEM CORP +1

Hydrogenation method of butyronitrile latex

ActiveCN107200794AReduce the cost of hydrogenationImprove hydrogenation reactivityNitrile rubberHydrogenation reaction
The invention relates to the hydrogenation field of butyronitrile latex, and discloses a hydrogenation method of butyronitrile latex. The method includes steps of (1), mixing butyronitrile latex, hydrogenation catalyst and ligand; (2), orderly performing first hydrogenation reaction and second hydrogenation reaction on the mixture obtained in step (1) in the presence of hydrogen, wherein the reaction temperature of the first hydrogenation reaction is 0-30 DEG C, and the reaction temperature of the second first hydrogenation reaction is 50-180 DEG C; (3), removing solvent in the reaction product obtained in step (2). The method is applied to perform hydrogenation on the butyronitrile latex, improve the hydrogenation activity of the hydrogenation catalyst and hydrogenation degree of the hydrogenation product; the hydrogenation product is free from obvious gel growth by comparing with the nitrile rubber before the butyronitrile latex before hydrogenation; moreover, the hydrogenation method is simple in operation, short in reaction time, easy to practice, and low in hydrogenation cost.
Owner:CHINA PETROLEUM & CHEM CORP +1

Unsaturated copolymer hydrogenation method

The present invention discloses an unsaturated copolymer hydrogenation method, which comprises: (1) dissolving a unsaturated copolymer in an organic solvent, and carrying out inflation discharge deaeration; (2) adding a hydrogenation catalyst and a ligand, wherein the hydrogenation catalyst has the following general formula: M1aM2bXmLn; (3) introducing hydrogen, stirring, and carrying out a reaction, wherein the reaction conditions comprise that the reaction temperature is 0-30 DEG C, the hydrogen pressure is 0.05-15 Mpa, and the reaction time is 1-120 min; (4) heating to a temperature of 50-180 DEG C, maintaining the hydrogen pressure at 0.1-15 Mpa, and carrying out a reaction for 1-20 h; and (5) removing the organic solvent in the reaction product obtained in the step (4). With the method of the present invention, the catalyst application cost can be reduced, the reaction is easy to perform, the hydrogenation reaction activity is high, the hydrogenation degree of the hydrogenated product can be significantly improved, and the product does not have the significantly-increased gel content.
Owner:CHINA PETROLEUM & CHEM CORP +1

Hydrogenation catalysts carrier with nickel and cobalt, hydro-catalyst and its preparing method

The invention provides a carrier of pre-impregnating metal components, and hydrotreating catalyst containing the carrier, wherein carrier materials are Al 2 O3, SiO 2, TiO2, and a composite oxide of two of the Al2 O3, the SiO2, and the TiO2 which are prepared by a sol-gel method, a certain amount of molecular sieve is added into the carrier, saline solution containing nickel and cobalt is inducted in the process of the carrier materials prepared by a sol method, in order that the content of NiO and CoO in the carrier is 0.1 to 5 wt percent, the specific surface area of the obtained carrier containing the nickel or the cobalt is in 250 to 400 m <2> * g <-1>, and the pore volume is in 0.5 to 1.0 ml * g <-1>. The invention also provides a preparation method for the catalyst, group 6B metals and group 8 metals are taken as active components, the adoption of an equivalent-volumetric impregnation method produces the petroleum fraction hydrotreating catalyst, and the catalyst of the invention has excellent activity of hydrogen desulfurization and hydrodenitrification.
Owner:BC P INC CHINA NAT PETROLEUM CORP +1

Preparation method of palladium-based supported hydrogenation catalyst and catalyst thereof

The invention relates to a preparation method and application of a palladium-based supported hydrogenation catalyst. The problems that in a traditional preparation method, dispersion of an active component palladium cannot be accurately controlled, agglomeration is likely to happen at high temperature, and consequently the hydrogenation performance of a catalyst is poor are mainly solved. The preparation method comprises the steps: respectively dispersing palladium salt, zinc salt, an imidazole compound and a carrier in a solvent, proportionally mixing, and sequentially carrying out thermal reaction, reduction and roasting treatment on the mixture to obtain the palladium-based supported catalyst. The method is simple in technological process, easy to control and amplify in process, novel and unique in catalyst structure and high in p-carboxybenzaldehyde conversion efficiency, and has potential industrial application prospect in crude terephthalic acid hydrofining reaction.
Owner:CHINA PETROLEUM & CHEM CORP +1

Preparation method of copolymer

The invention discloses a preparation method of a copolymer. The method comprises the following steps: (1) dissolving an unsaturated copolymer in an organic solvent, and filling and draining and degassing; (2) adding a hydrogenation catalyst and a ligand, wherein the hydrogenation catalyst has the following general formula: (RmA)zRhXn; (3) filling hydrogen, stirring, and reacting at the reaction temperature of 0-30 DEG C and at hydrogen pressure of 0.05-15 Mpa for 1-120 min; (4) heating to 50-180 DEG C, keeping hydrogen pressure to 0.1-15 Mpa, and reacting for 1-20 h; and (5) removing an organic solvent in the reaction product obtained in the Step (4). By the method, application cost of the catalyst can be reduced, the reaction is easier to implement, hydrogenation reaction activity is high, hydrogenation degree of a hydrogenation product can be obviously raised, and the product has no obvious increase of gel content.
Owner:CHINA PETROLEUM & CHEM CORP +1

Supported nickel-based catalyst, preparation method and applications thereof

The present invention discloses a supported nickel-based catalyst, and provides a supported nickel-based catalyst, which comprises active components and a composite carrier, wherein the active components comprise nickel, zinc and magnesium, the composite carrier comprises silica and titanium dioxide, the active components are supported on the composite carrier to form the supported nickel-based catalyst with the structure of Ni-Zn-Mg / SiO2-TiO2, the mass content of nickel is 30-80%, the mass content of zinc is 0.1-15%, the mass content of magnesium is 0.1-15%, the mass content of silica is 10-50%, and the mass content of the titanium dioxide is 1-30%. According to the present invention, the prepared Ni-Zn-Mg / SiO2-TiO2 supported nickel-based catalyst has obvious hydrorefining effect on whiteoil, the preparation process and the equipment are simple, the method is suitable for industrialization, and the product has good application prospect and great economic benefit.
Owner:SHANGHAI XUNKAI NEW MATERIAL TECH

Preparation method of alumina carrier

The invention discloses a preparation method of an alumina carrier. The method comprises the following steps: using an acidic aluminum salt solution and an alkaline aluminate solution to carry out a glue-forming process through a parallel flow method, adding a gemini surfactant before the glue-forming process or during the glue-forming process, and after the glue-forming process, subjecting the glue to the processes of aging, filtering, washing, drying, forming, drying, and burning so as to obtain the alumina carrier. The gemini surfactant has the same advantages as those of negative ion surfactants and positive ion surfactants, thus the gemini surfactant is used to replace the negative ion surfactants and positive ion surfactants so as not to bring in new impurity ions; furthermore, the gemini surfactant has a large molecular weight and thus has a good pore-enlarging effect; and finally alumina particles, which have the advantages of large pore diameter, large pore volume, and high strength, are obtained. The alumina carrier can be used as a carrier of a hydro-treatment catalyst, and is especially suitable for being taken as a carrier of a residual oil hydro-treatment catalyst.
Owner:CHINA PETROLEUM & CHEM CORP +1

A kind of hydrogenation method of ternary nitrile latex

ActiveCN107200796BReduce the cost of hydrogenationImprove hydrogenation reactivityHydrogenation reactionReaction temperature
The invention relates to the field of ternary butyronitrile latex hydrogenation and discloses a hydrogenation method of ternary butyronitrile latex. The method includes the steps of firstly, mixing the ternary butyronitrile latex, a hydrogenation catalyst and a ligand; secondly, sequentially performing first hydrogenation reaction and second hydrogenation reaction on the mixture obtained in the first step in the presence of hydrogen, wherein the reaction temperature of the first hydrogenation reaction is 0-30 DEG C, and the reaction temperature of the second hydrogenation reaction is 50-180 DEG C; thirdly, removing solvent in the reaction product obtained in the second step. By using the hydrogenation method to hydrogenate the ternary butyronitrile latex, the hydrogenation reaction activity of the hydrogenation catalyst and the hydrogenation degree of the hydrogenated product can be increased, and the hydrogenated product has no evident gel increasing as compared with nitrile-butadiene rubber in the ternary butyronitrile latex before the hydrogenation. In addition, the hydrogenation method is simple to operate, short in reaction time, easy to implement and low in hydrogenation cost.
Owner:CHINA PETROLEUM & CHEM CORP +1

High-fluorine-containing C9 resin hydrogenation catalyst and preparation method and application thereof

The invention relates to a high-fluorine-containing C9 resin hydrogenation catalyst, which is composed of an active component M1, an auxiliary agent component M2 and a carrier component M3. Based on 100% of the total weight of the catalyst, the content of the M1 component is 37%-54%, the content of the M2 component is 4%-6%, and the balance is the M3 component. The component M1 contains Ni, Mo, Cu and Al, the component M2 contains Sm and Na, and the component M3 is amorphous silicon-aluminum MgAl2O4 composite oxide. The invention also discloses a preparation method and application of the catalyst. The catalyst provided by the invention is used for hydrogenation removal of fluorine and sulfur in C9 resin, and can effectively delay fluorine and sulfur poisoning of a rear-stage hydrogenation catalyst.
Owner:WUHAN KELIN FINE CHEM

A kind of preparation method of alkyne selective hydrogenation catalyst

The invention relates to a supported copper-base catalyst for alkyne selective hydrogenation. The catalyst comprises a carrier and following components loaded on the carrier: (a) 5 to 15 wt% of copper, (b) 0.5 to 3 wt% of iridium, (c) 0.5 to 3 wt% of phosphor, and optional zirconium and / nickel. The carrier is preferably chosen from aluminum oxide, titanium oxide, silicon oxide, titanium oxide-aluminum oxide, titanium oxide-silicon oxide, or aluminum oxide-silicon oxide, and most preferably, the carrier is titanium oxide-aluminum oxide. The catalyst can be used to eliminate alkyne in C4 fraction through hydrogenation, has the advantages of high catalytic activity, high selectivity, good stability, and long service life, and is capable of preventing sulfur and arsenic poisoning.
Owner:CHINA PETROLEUM & CHEM CORP +1

A kind of nickel-based glucose hydrogenation catalyst and preparation method thereof

The invention relates to a nickel-based glucose hydrogenation catalyst and a preparation method thereof. The catalyst is composed of main active components nickel and nickel oxide, additives, silicon oxide and zirconium oxide; the content of the main active component nickel is 3-40wt%, and the content of nickel oxide is 35-72%; the content of the auxiliary agent is 0.1-10wt% %; the silicon oxide content is 10-39wt%, and the rest is zirconia; wherein the auxiliary agent is one or both of cobalt and iron. The invention adopts a microwave-assisted co-precipitation method to synthesize the catalyst precursor slurry, and further crystallizes the slurry, then performs drying, roasting and reduction passivation to obtain a glucose hydrogenation catalyst. The particle size distribution of the catalyst prepared by the invention is uniform, and the average particle size is 7-15 μm. The catalyst is used for the hydrogenation reaction of glucose, has high activity, and is safe to use; the preparation method is simple in operation, good in batch preparation repeatability, and low in cost.
Owner:CNOOC TIANJIN CHEM RES & DESIGN INST +1
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