828results about "Preparation by hydrogenation" patented technology

A shaped, activated, fixed-bed Raney metal catalyst prepared by a method comprising preparing a mixture of powders comprising at least one catalyst alloy of (1) at least one catalytically active Raney process metal, a leachable alloy component and optionally a promoter, (2) at least one binder containing at least one pure Raney metal and (3) a moistening agent. Shaping, calcining and activating said catalyst and doping said catalyst with rhenium.

PCT No. PCT/EP96/00163 Sec. 371 Date Oct. 15, 1997 Sec. 102(e) Date Oct. 15, 1997 PCT Filed Jan. 17, 1996 PCT Pub. No. WO96/22265 PCT Pub. Date Jul. 25, 1996A dilute ethylene stream, e.g., one produced by steam cracking, is oxonated to yield propanal, without the need to separate other lower hydrocarbons.

The invention relates to a catalyst used in a ring-opening hydrogenation reaction of a furan derivative. The catalyst is applied to direct preparation of one-step ring-opening hydrogenation of 1,5-pentanediol and 1,2-pentanediol by taking furfural or furfuryl alcohol serving as a raw material under a mild condition. The catalyst can provide two active ingredients, namely the ring-opening active center of a transition metal oxide and the hydrogenation active center of Pt, Pd, Rh, Ru, Co or Ni, wherein the active center of the transition metal oxide is mainly used for adsorbing furfural or furfuryl alcohol and directly hydrogenating a furan ring for opening the furan ring; and the hydrogenation active center of a noble metal or Co, Ni and the like is mainly used for quickly hydrogenating an intermediate material and hydrogenating subsequent enol so as to obtain 1,5-pentanediol and 1,2-pentanediol. An environmentally-friendly, reproducible, low-cost, mild and effective method is provided for producing 1,5-pentanediol and 1,2-pentanediol. The high-performance ring-opening hydrogenation catalyst is also suitable for the ring-opening hydrogenation reaction of other furan derivatives.

The invention discloses a method for producing mixed butanol and coarse octanol by using waste liquid discharged from an octanol device as a raw material, which belongs to a method for preparing acyclic monohydric alcohols, and is characterized by using a raw material fractionation unit, a hydrogenation synthesis unit and a product distillation unit, wherein the raw material fractionation unit comprises three fractionation devices: a butyraldehyde fractionation tower, a butanol fractionation tower and a C8 fractionation tower; the hydrogenation synthesis unit and the product distillation unit are suitable for hydrogenating and distilling a butyraldehyde fraction and a C8 fraction from the raw material fractionation unit alternately; and the product distillation unit comprises a light component removing tower device and a heavy component removing tower device. The method for producing the mixed butanol and coarse octanol by using the waste liquid discharged from the octanol device as the raw material, which is energy-saving and environmentally-friendly, can realize the recycling of the waste liquid discharged from the octanol device, reduce the waste water treatment cost of the octanol device and improves the technical indexes of treated water.

The invention discloses a supported ruthenium catalyst and a preparation method thereof. The preparation method is characterized in that the preparation method comprises the following steps: 1, preprocessing a carrier with a soluble alkaline earth metal salt, wherein the mass of the soluble alkaline earth metal salt accounts for 0.1-20% of the mass of the carrier; and 2, dipping the alkaline earth metal salt processed carrier with a material which comprises a primary active component metallic ruthenium and an assisted catalytic component comprising one or several of Ni, Co, Pd and Pt, wherein the mass of the primary component metallic ruthenium accounts for 0.1-5% of the carrier, and the mass of the secondary component comprising one or several of Ni, Co, Pd and Pt accounts for 0.01-5% of the mass of the carrier. The catalyst of the invention is mainly applied to the selective hydrogenation process of an aromatic ring of an aromatic compound, wherein the aromatic ring of the aromatic compound has at least one alkyl group, one ester group, one hydroxyl group or an amino group and also has at least one C1-8 alkyl group. Compared with catalysts prepared with the prior art, the catalyst of the invention has the advantages of low cost, simple preparation method, high activity, good selectivity, high safety in the operation of the aromatic ring hydrogenation, realization of the operation of the aromatic ring hydrogenation under a low pressure, and good economy.

The invention discloses a method for preparing cyclohexanol by catalyzing phenol hydrogenation by taking a porous carbon material loaded base metal as a catalyst. The synthetic route of the traditional two-step method comprises phenol hydrogenation and cyclohexanol dehydrogenation, and the catalysis of phenol hydrogenation in preparing cyclohexanol is mainly completed through metals, namely nanometer noble metal Pd, Ni radical and the like which have higher activated cracked hydrogen molecules. The method is characterized in that cyclohexanol is prepared in the presence of a solvent by using the porous carbon material loaded base metal as the catalyst, taking phenol or a phenol derivative as a raw material and catalyzing hydrogenation; a general formula of the catalyst is aM@CXy, wherein a indicates the weight percentage content of the metals contained in the catalyst, M indicates the base metal, C indicates carbon, X indicates a doped mixed element, and y indicates the weight percentage content of the mixed element. The method disclosed by the invention can be used for reducing the usage cost of the catalyst by recovering the catalyst by adopting a simple filtering method, and can obtain cyclohexanol by directly concentrating filter liquor obtained through filtration.

The invention relates to a catalyst for preparation of hydrogenated bisphenol A. The catalyst comprises: by mass, 100 parts of modified compound alumina carriers and 1 to 3 parts of precious metals as active ingredients. The modified compound alumina carriers comprise: by mass, 30 to 80 parts of pseudo-boehmite, 10 to 40 parts of aluminum hydroxide, 1 to 5 parts of an alkali metal and 1 to 5 parts of phosphorus. The active ingredients comprise two of Pd, Ru and Rh. The modified compound alumina carriers are adopted and are loaded with multiple precious metals to form the catalyst which is a hydrogenation catalyst having high activity, high selectivity and high loading capacity. The catalyst can realize preparation of a high trans-form/trans-form ratio isomer product under the condition of a trace amount of a stabilizer.

The invention aims at providing a new loop opening hydrogenation reaction method for furan derivant, which changes a reaction way by changing the traditional mechanism of catalytic reaction, realizes transformation from the traditional way of hydrogenation first and ring opening secondly to the way of ring opening first and hydrogenation secondly, and reduces the activation energy of reaction, thus greatly reducing reaction pressure and cost, alleviating operation difficulty, and have good industrial application prospect.

The invention discloses a biomass carbon-based material high-load nano-metal catalyst, as well as a preparation method and application thereof. The catalyst is prepared by soaking shaddock peel powderin a nitrate solution having a certain concentration, drying and calcining, metal simple component serves as the active component, and organic carbon serves as the carrier; the nitrate is ferric nitrate, cobalt nitrate, nickel nitrate or copper nitrate; and the metal simple component is iron, cobalt, nickel or copper. The catalyst has the characteristics of environment-friendly raw materials, simple preparation process and high hydrogenation selectivity, has a good effect when being applied to a hydrogenation reaction of biomass derivatives, for instance, the furfuryl alcohol yield at a relatively low temperature of 170 DEG C can be 98,9 percent when the furfuryl alcohol is prepared by a furfuryl alcohol selective hydrogenation reaction.

A hydrogenation catalyst and a method of hydrogenating a hydrocarbon compound as a substrate using the same are provided. The hydrogenation catalyst includes inorganic nanoparticles and a nitrogen-doped reduced graphene oxide support for supporting the inorganic nanoparticles, and the hydrocarbon compound is derived from a biomass and contains a functional group. Therefore, the hydrogenation catalyst which exhibits a high conversion rate and high selectivity, is stable, and can be easily separated after a hydrogenation reaction, and whose catalytic activities are not significantly altered even when recovered and repeatedly recycled can be provided. The method of hydrogenating a hydrocarbon compound in which hydrogen can be directly produced in a reactor using formic acid as a hydrogen source without supplying additional hydrogen gas and simultaneously be used under normal pressure can also be provided.

The invention discloses an octanol hydrorefining catalyst, which belongs to the field of hydrorefining catalytic materials. The prepared catalyst is used for modifying a carrier by using a rare earth element, reducing the amount of an active component of a nickel ion entering a carrier framework and improving the content of surface nickel species; the active component is loaded by adopting a hydrothermal deposition method, the dispersion of nickel salts on the surface of a carrier pore canal by using hydrothermal high-temperature and high-pressure conditions and forming nickel precipitation with proper size at the loading initial period of the active component by using a deposition reaction, so the invention can effectively control the amount of the nickel ions entering the carrier, improve the content of the surface nickel species and simultaneously can avoid the growth of nickel oxide particles; and the catalyst greatly increases the surface nickel active site, effectively improves the utilization rate of the active component of nickel and has higher catalytic reaction activity during hydrorefining the octanol at higher airspeed. The result shows that the hydrogenation rate of an unsaturated substance in crude octanol reaches over 90 percent when the temperature is 120DEG c, the pressure is 2.5MPa, the ratio of hydrogen to liquid for feeding is 8:1 and the airspeed is 30<-1>hour.

The invention relates to a continuous preparation method of hydrogenated bisphenol A. The method comprises the following steps: carrying out a hydrogenation reaction on a prepared bisphenol A raw material in a fixed bed hydrogenation reactor under the action of a precious metal supported hydrogenation catalyst, returning the obtained hydrogenation products to the reactor according to a certain proportion in order to carry out cycle hydrogenation in order to control the ratio of the cis-trans structure in the hydrogenation product, and carrying out gas-liquid separation, normal pressure solvent removal, reduced pressure byproduct removal and sheeting treatment on the extracted partial hydrogenation products to obtain the final hydrogenated bisphenol A product, and recycling separated hydrogen and solvent. The method has the advantages of simple process flow, high controllability of the reaction process, realization of continuous preparation of the hydrogenation products, stable performances of the target product, and increase of the cis-trans isomer ratio in the hydrogenation products through the partial cycling process of the hydrogenation products, and allows the converstion rate of the hydrogenation reaction to reach 100%, the selectivity to be more than 95%, the purity of the product to be more than 97% and the cis-trans isomer ratio to reach 60%.

The invention discloses a preparation method of a supported nickel catalyst, which comprises the following steps of: reacting soluble nickel salt solution and a precipitator to obtain a green precipitate, wherein the precipitator is mixed solution of sodium silicate and sodium carbonate, the Na<+> concentration is 0.1-1 mol/L, the amount of the sodium silicate is calculated according to the content of SiO2 in a carrier, and the amount of the sodium carbonate is 10-30 percent more than that of nickel nitrate based on a stoichiometric ratio; washing the precipitate by distilled water and carrying out supercritical drying or azeotropic distillation drying to obtain a supported nickel catalyst precursor; roasting the supported nickel catalyst precursor for 2-5 hours under N2 atmosphere at 200-600 DEG C, changing the N2 atmosphere into H2 atmosphere, and reducing the supported nickel catalyst precursor for 2-4 hours under H2 atmosphere at 300-550 DEG C to obtain the supported nickel catalyst with the surface area of high active metal nickel. The surface area of the obtained catalyst is 250-450m<2>/g, the average aperture is 4-16nm, and the pore volume is 1.0 -1.9cm<3>/g. The surface area of the active metal nickel of the obtained catalyst is 40-70m<2>/g. The catalyst prepared by using the method can be used for catalyzing hydrogenation of a benzene ring.

The present invention relates to synthesis process of cyclohexanone and cycloexanol, especially through hydrogenating phenol. Phenol material, C1-C2 fatty alcohol and water in the weight proportion of 1 to 2.5-40 to 10-160 are reacted in one step at 100-300 deg.c temperature and 1-10 MPa pressure and in the action of Renny Ni catalyst or active carbon supported palladium catalyst to synthesize cyclohexanone and cycloexanol. The present invention features no need of outer hydrogen supply for hydrogenating phenol and the use of relatively cheap Renny Ni catalyst, and has the advantages of high safety, simplified technological process, low production cost, high phenol converting rate, high total cyclohexanone and cycloexanol selectivity near 100 %, no side product and easy product separation.

The invention relates to a method for preparing butanediol by carrying out two-stage bed catalytic hydrogenation on butynediol. Aiming at the requirements on the suitability for a reaction system which contains water or fluctuating water content in a process for preparing the butanediol by carrying out two-step hydrogenation on the butynediol, and the inhibition on the generation of carbon deposit, the inventor proposes that: a hydrogenation catalyst A and a hydrogenation catalyst B in a two-stage bed respectively contains a carrier, a metal active component and silane groups, further, the silane groups are grafted through a silylanizing treatment, wherein the content of the silane groups in the total weight of the hydrogenation catalysts is 0.1-12 wt%. Compared with the prior art, under the premise of ensuring that the hydrogenation catalysts have better activity and better selectivity, the method provided by the invention has obvious raw material suitability, and the presence of water hardly influences on the catalytic performance of the hydrogenation catalysts; and meanwhile, the generation of the carbon deposit on the surfaces of the catalysts can be obviously inhibited, and the service life of the catalysts is prolonged, so that the hydrogenation reaction system can have a longer stable running cycle.

An object of the present invention is to provide a method for manufacturing an optically active menthol having fewer steps, which generates less environmentally polluting waste because a catalytic reaction is involved in all of the steps, and is capable of saving a production cost. The present invention relates to a method for manufacturing an optically active menthol, including the following steps: A-1) asymmetrically hydrogenating at least one of geranial and neral to thereby obtain an optically active citronellal, B-1) conducting a ring-closure reaction of the optically active citronellal in the presence of an acid catalyst to thereby obtain an optically active isopulegol, and C-1) hydrogenating the optically active isopulegol to thereby obtain an optically active menthol.

Shaped Raney metal fixed-bed catalysts are doped with rhenium. Saturated or unsaturated esters are hydrogenated to their corresponding mono- or polyhydroxyalcohols.

The alpha form of nickel (II) hydroxide is formed by dissolving a compound of nickel (II), such as nickel acetate, in a water miscible dihydric alcohol (diol), such as ethylene glycol, propylene glycol and suitable oligomers, and adding a suitable base such as sodium carbonate. The α-Ni(OH)₂ precipitate is separated from the diol-based mother liquor and dried. This stable α-Ni(OH)₂ can be calcined at temperatures in the range of about 573K to about 1073K to form nanometer-size particles of NiO having, for example, fibrous shapes. And the small particles of NiO can be reduced with hydrogen to form small, fibrous nickel particles. Both the NiO particles and Ni particles have utility as catalysts and offer utility in applications requiring electronic and/or magnetic properties.

The invention relates to the technology of a catalyst for preparing cyclohexane from phenol, aiming at providing a high-dispersion dual-functional catalyst for hydrogenating and deoxidizing phenol and the preparation method of the catalyst. The catalyst is prepared by the following steps: loading active metal Pt on Al-modified ordered mesoporous molecular sieve Al-SBA-15 (x) by a complexing agent trimethoxysilylpropanethiol through an in-situ synthesis method, and is shown in a formula 1% Pt-(SH)/ Al-SBA-15(x), wherein 1% represents the mass fraction of Pt in the catalyst, and x represents the molar ratio of silicon and aluminum in Al-SAB-15 and is 7-300. The catalyst prepared by the preparation method is used for improving the quality of phenolic compounds in a biological oil system and is beneficial to conversion of the phenolic compounds which are unstable, corrosive and hard to burn in the biological oil into hydrocarbon which is stable and easy to burn, thus the conversion rate of phenol and the selectivity of alkane can be improved. The conversion rate of the phenol hydrogenating and deoxidizing reaction can reach 100.0% under the optimum condition, and the selectivity of cyclohexane can reach 99.0%. The preparation method of the catalyst is simple to operate, integrates with a plurality of steps of operation, and does not need extra reduction activation treatment.

The invention belongs to the technical field of organic synthesis, in particular to a method for synthesizing L-menthol. The method for synthesizing L-menthol takes myrcene as an initial raw material and comprises the following steps: amination reaction: diethylamine and myrcene carry out amination reaction to obtain geranylamine; isomerization reaction: the geranylamine carries out isomerization reaction under the catalytic action of chiral catalyst to obtain intermediate enamine; hydrolysis reaction: the enamine carries out hydrolysis reaction in an acidic medium to produce intermediate D-citronellal; cyclization reaction: the D-citronellal generates L-isopulegol by lewis acid catalyst and organic solvent; and hydrogenation reaction: the L-isopulegol is hydrogenated to obtain L-menthol. The method for synthesizing L-menthol has the yield of more than 90 percent, the GC purity of higher than 99.0 percent and the specific rotation of -49 degrees to -50 degrees, the raw material myrcene has wide sources and lower cost, and the whole method has simple technology, good repeatability and high yield and is quite suitable for large-scale industrialized production.