871 results about "Catalytic hydrogenation" patented technology

The invention discloses application of a Ni-based reverse-phase catalyst in catalytic hydrogenation reaction of a nitro compound, nitro in the nitro compound is hydrogenated to reduce amino, the Ni-based reverse-phase catalyst is of an M / Ni reverse-phase structure, metal Ni for dissociating hydrogen serves as a carrier, nano metal M oxide is loaded on the carrier to serve as a loading phase, and reverse-phase interface active sites are constructed; wherein the metal M is one or two of Ce, Zr, Al, Y and Mg, and the mole fraction of the load phase metal M is 5-50% based on the mole fraction of all the metals in the catalyst being 100%. The preparation method of the catalyst is simple and easy to implement, the catalyst has a non-traditional supported reversed-phase structure, the activity of the catalyst is more excellent than that of a traditional supported catalyst when the catalyst is applied to the nitro-compound hydrogenation process, a traditional Raney nickel catalyst can be effectively replaced, a reaction system is clean and safe, repeatability is good, effective recycling can be achieved, and the catalyst is suitable for industrial production. The method is suitable for industrial production and has a good application prospect.

The invention belongs to the technical field of petroleum processing, and particularly relates to a catalyst and a preparation method and application thereof. The raw materials of the catalyst comprise a metal active component, a carrier and an auxiliary agent, the metal active component is sulfides of Mo and Ni elements, the carrier is spherical gamma-Al2O3 of 0.5-1 mm, and the auxiliary agent is P; the carrier is modified by using the metal active component and the auxiliary agent to serve as the catalyst. The high-activity catalyst is synthesized by adopting the strategy of changing the roasting temperature, adding the additive for doping modification and changing the molar ratio of metal active components, the additive is combined with surface aluminum atoms, the framework strength is enhanced, pore channel collapse caused by acid / water erosion is reduced, the water resistance and acid resistance of the catalyst are improved, and the catalytic reaction activity is further improved. The catalyst disclosed by the invention is accurate and controllable in structure, can be synthesized in batches, and can be applied to the co-catalytic hydrogenation process of biomass pyrolytic oil and / or a model compound thereof and petroleum distillate oil and / or VR.

A method for continuously producing m-xylylenediamine belongs to the technical field of organic synthesis and comprises the following steps: (1) mixing isophthalonitrile, toluene and liquid ammonia according to a mass ratio of 1: (3-5): (13-17) in a nitrogen atmosphere to form a reaction mixture; (2) heating the interior of a reaction bed containing a catalyst to 90-95 DEG C, continuously introducing hydrogen into the reaction bed, introducing the reaction mixture after the pressure intensity of the reaction bed is stable, and carrying out a catalytic hydrogenation reaction to generate a reaction product; and (3) carrying out gas-liquid separation on the reaction product, removing liquid ammonia from the liquid-phase product through an ammonia distillation process, and separating toluene and m-xylylenediamine through a rectification process to obtain m-xylylenediamine. According to the method, isophthalonitrile and hydrogen are used as raw materials, liquid ammonia and methylbenzene are used as reaction solvents, the raw materials and the reaction solvents are heated to 90-95 DEG C under the catalytic action of a catalyst for an exothermic reaction, m-xylylenediamine is generated through the reaction, and the reaction yield is larger than 99%.

The invention discloses a resource regeneration method of waste lubricating oil, relates to the technical field of petrochemical engineering, and belongs to the patent classification number C10M175 / 06. The preparation method comprises the following steps: adding a composite flocculant into the waste lubricating oil, heating and stirring, and then carrying out magnetic separation to obtain pretreated waste lubricating oil; uniformly mixing the pretreated waste lubricating oil, glycerol and a Ni / Al2O3 catalyst, then heating and reacting under pressure, and cooling to room temperature to obtain a catalytic hydrogenation product; and carrying out reduced pressure distillation on the catalytic hydrogenation product, recovering the lubricant base oil fraction, adding methanol and concentrated sulfuric acid into the distillation residual liquid, heating for esterification reaction, and separating the liquid to obtain the biodiesel. In the pretreatment process, the composite flocculant is used for removing acid and particle impurities in the lubricating oil, a traditional alkali adding neutralization precipitation process is replaced, the method is environmentally friendly, and the recovery cost of enterprises is reduced.

The invention relates to the technical field of chemical engineering, and particularly discloses a palladium-carbon catalytic hydrogenation reaction material treatment system, which comprises a three-dimensional workshop structure, an air-operated hoist, an air supply system, an air supply system and an air supply system, wherein the top of the three-dimensional workshop structure is provided with an elevator and a hoisting ton bag; the palladium-carbon circulating unit comprises a palladium-carbon preparation kettle, a hydrogenation reaction kettle, a decarbonization filter, a filter pressing cylinder, a sample splitter and a glove box which are connected in sequence, and the sample splitter is connected back to the palladium-carbon preparation kettle through a closed pipeline; the solid feeding unit comprises a ton bag feeder, a pneumatic valve and a spiral conveying pipe, and the tail end of the solid feeding unit is connected with a top feeding hole of the hydrogenation reaction kettle; the gas supply system comprises a hydrogen cylinder group and is connected to a gas distributor at the bottom of the hydrogenation reaction kettle through a pressure reducing valve and a flow regulating valve; through the multi-stage separation design and the safety interlocking mechanism of the palladium-carbon circulating unit, the recovery rate of the catalyst is increased, meanwhile, the pressure, temperature and stirring state are monitored in real time to trigger nitrogen purging or pressure relief, and the risks of hydrogen leakage and reaction out-of-control are reduced in combination with inert gas protection of the glove box.

The invention relates to a method for preparing a nerofloxacin chiral piperidylamine intermediate, which comprises the following steps of: carrying out condensation reaction on 5-hydroxy nicotinic acid which is simple and easy to obtain and is used as a raw material and different alcohols, screening through a series of asymmetric catalytic hydrogenation conditions to obtain optimal reaction conditions, and under the conditions, carrying out reaction on various 3, 3 '-dihydroxy nicotinic acid and 3, 3'-dihydroxy nicotinic acid to obtain the nerofloxacin chiral piperidylamine intermediate. The 2, 5-disubstituted pyridine quaternary ammonium salt is reduced into a tetrahydropyridine product, and the C5 site enantioselectivity of the product is excellent. The preparation method comprises the following steps: selecting methyl (R)-1-benzyl-5-hydroxy-1, 4, 5, 6-tetrahydropyridine-3-carboxylic acid methyl ester as a substrate, completely hydrogenating by using platinum dioxide hydrogen, and then carrying out methyl ester reduction, dehydroxylation, Mitsunobu reaction and protecting group removal to obtain a key chiral intermediate for industrial synthesis of a quinolone antibacterial drug nemonofloxacin with high enantioselectivity and high yield.

The utility model discloses a catalytic hydrogenation reactor for treating a biomass raw material with a high acid value and a high iodine value, and belongs to the technical field of oil product hydrogenation. The catalytic hydrogenation reactor comprises a reactor pressure-bearing container, an inner cylinder, an ash discharge port, a feeding assembly, a reaction assembly and a discharging assembly, the inner cylinder is arranged in the reactor pressure-bearing container, the feeding assembly and the reaction assembly are arranged in the inner cylinder, the reaction assembly comprises a ceramic tube bundle internal part, the discharging assembly is arranged above the inner cylinder, and the discharging assembly is arranged above the inner cylinder. The ash discharge port is formed in the center of the bottom of the reactor pressure-bearing container. By arranging the ceramic tube bundle internal part in the catalytic hydrogenation reactor, on one hand, the ceramic tube bundle internal part serves as a reaction assembly and has certain acid corrosion resistance, and on the other hand, the ceramic tube bundle internal part serves as a solid catalyst carrier, selective hydrogenation of high-acid-value and high-iodine-value biomass raw materials is achieved, the iodine value is effectively reduced, and coking of the high-iodine-value biomass raw materials in the reaction process is avoided; in addition, the acid value is maintained as far as possible while the iodine value is reduced, and the solid catalyst and the catalytic hydrogenation reactor are not corroded, so that the stability of the solid catalyst and the yield of the product are improved.

The invention discloses a magnetically separable reversed-phase catalyst, a preparation method thereof and application of the magnetically separable reversed-phase catalyst in hydrogenation upgrading recovery of aromatic polyester, and belongs to the technical field of reversed-phase catalysts and plastic recovery. The catalyst is formed by loading a metal oxide (MOx) on a metal carrier nickel, and is applied to hydrogenation recovery of aromatic polyester and conversion of aromatic polyester into high value-added aliphatic polyester. After dispersion, carrying out catalytic hydrogenation reaction on the aromatic polyester at a set temperature, a set rotating speed and a set hydrogen pressure, and completing conversion of the aromatic polyester after the reaction reaches a set time; according to the method, the aromatic polyester is completely converted into the fat polyester with high additional value by using the cheap and easily-separated reverse catalyst, so that the upgraded recycling of the polyester waste plastic is realized.

The invention discloses a preparation method and application of an oil-soluble heteropolyacid ionic liquid catalyst. The catalyst is composed of organic cations and inorganic anions, the cations are one of quaternary ammonium, imidazole and pyridine cations containing long-chain alkyl, the anions are heteropolyacid anions, the long-chain alkyl enables the catalyst to have good oil solubility, the catalyst can be efficiently dispersed in the waste grease, heteropolyacid provides active sites, and the catalyst can be used for treating the waste grease. Nano-scale active particles are formed after in-situ vulcanization, and the catalytic hydrogenation effect is achieved. The invention also provides a preparation method of the oil-soluble heteropolyacid ionic liquid catalyst, the catalyst can be prepared from tertiary amine and halogenated hydrocarbon through three-step reaction of alkylation, anion exchange and acid-base neutralization, the preparation process is simple, a highly toxic reagent is avoided, and the cost is low. The catalyst provided by the invention can be used for catalytic hydroisomerization of various waste oils and fats, has the characteristics of high conversion rate, low coking rate and high product calorific value, and has relatively high industrial application potential.

The invention relates to a preparation method of a carbon-based gold-containing bimetallic catalyst. The specific method comprises the following steps: carrying out secondary doping on eigenstate polyaniline, carrying out high-temperature pyrolysis in an inert atmosphere to obtain a heteroatom-doped carbon-based carrier, and changing the variety, the content and the distribution of heteroatoms on the carbon surface of the carrier by adjusting the variety and the content of acid. And preparing gold-containing bimetallic nanoparticles by using a colloid method, and depositing bimetallic particles by virtue of adsorption of the carbon carrier and bimetallic to obtain the carbon-based gold-containing bimetallic catalyst. Wherein the doping element can anchor and disperse the noble metal, and the introduced second metal can improve the hydrogenation activity of the catalyst. The catalyst is simple in preparation process, good in activity, excellent in selectivity and excellent in cycling stability, is particularly suitable for a reaction for preparing 4-chloroaniline through catalytic hydrogenation of 4-chloronitrobenzene, and has good application potential.

The invention relates to a catalyst for preparing 1, 4-cyclohexanedimethanol (CHDM) by catalyzing dimethyl terephthalate (DMT) hydrogenation and a preparation method thereof, non-noble metals nickel (Ni) and copper (Cu) are used as active components, silicon dioxide is used as a carrier, ammonia water in a solution is evaporated out after ammonia water precipitation, and a catalyst sample is obtained. The active components mainly adopt metal Ni and Cu elements with relatively low price, compared with noble metals such as ruthenium, rhodium, platinum and the like, the use cost of the catalyst is greatly reduced, the bimetallic catalyst Ni-Cu-SiO2 is prepared by an ammonia distillation method, 1, 4-cyclohexanedimethanol can be prepared by catalyzing dimethyl terephthalate hydrogenation by a one-pot method, and the catalyst has a wide application prospect. The preparation cost of the catalyst is relatively low, the dispersity and stability of the catalyst are improved by adopting an ammonia distillation method, the CHDM is prepared by adopting a one-pot method, the energy consumption is further reduced, the reaction procedure is simplified, and the preparation method is simple and is easy to amplify to industrial production.

The invention provides a method for preparing hydrogenated bisphenol A by continuous catalytic hydrogenation of a fixed bed. The method comprises the following steps: step A, mixing and preheating a bisphenol A solution, a low-carbon amine additive and hydrogen in a gas-liquid mixing preheater to prepare a reaction material; step B, enabling the preheated reaction material to flow through a fixed bed reactor preloaded with a Ru-based catalyst, and carrying out catalytic hydrogenation reaction in the fixed bed reactor to generate a product material; step C, separating the product material through a gas-liquid separator to obtain a hydrogenated bisphenol A solution and hydrogen, and recycling the hydrogen; and rectifying the hydrogenated bisphenol A solution to obtain hydrogenated bisphenol A. The method provided by the invention effectively overcomes the defect that the single-batch reaction time of the existing catalytic hydrogenation process reaches 4-12 hours, and greatly shortens the continuous catalytic hydrogenation reaction time; by adding the low-carbon amine auxiliary agent, the reaction activity is promoted, and the generation of dehydroxylation byproducts is reduced; the selectivity of the product can be effectively guaranteed, the product is easy to separate, the safety is good, the cost is obviously reduced, and industrial application is easy.

The invention provides a method for synthesizing 1, 3-butadiene by continuous catalytic conversion of acetylene, which comprises the following steps: S1, continuously introducing acetylene as a raw material into a reactor I for acetylene dimerization catalytic reaction to obtain primary reaction gas containing vinyl acetylene; and S2, continuously introducing the initial reaction gas and hydrogen into a reactor II, and carrying out selective catalytic hydrogenation reaction to obtain 1, 3-butadiene. The technical scheme of the invention provides a continuous catalytic process method, and 1, 3-butadiene is directly synthesized by using acetylene as a raw material through coupling acetylene catalytic dimerization reaction and vinyl acetylene selective catalytic hydrogenation reaction. The obtained product is easy to separate from a catalytic system, and the whole process flow is simple to operate, economical and environment-friendly, and has a good application prospect.

The invention belongs to the technical field of catalysts, and particularly relates to application of a non-noble metal supported catalyst in catalytic hydrogenation reaction and a method for catalyzing 5-methyl-3-hexene-2-ketone hydrogenation by using the non-noble metal supported catalyst to obtain methyl isopentanone. The invention provides application of a non-noble metal supported catalyst in catalytic hydrogenation reaction. The non-noble metal supported catalyst comprises a composite carrier and an active component supported in the composite carrier, the composite carrier is aluminum oxide and lanthanum oxide, and the active component comprises iron, cobalt, copper or nickel. The non-noble metal supported catalyst provided by the invention can provide catalytic active site density and electron transfer efficiency which are equivalent to or even better than those of a noble metal catalyst under interaction of an active center structure, electronic characteristics and a carrier; meanwhile, the unique d electron orbital characteristic is beneficial to stabilization of a reaction intermediate and reduction of transition state activation energy, so that the catalyst cost is remarkably reduced while the selectivity of catalytic hydrogenation is remarkably improved.

The invention discloses a short-Fe-C-bond Fe-based catalyst for catalyzing CO2 hydrogenation, a preparation method of the short-Fe-C-bond Fe-based catalyst and application of the short-Fe-C-bond Fe-based catalyst in preparation of C2 < + > high-added-value products, and belongs to the technical field of CO2 capture, utilization and storage. The catalyst is a carbon quantum dot doped Fe-based catalyst, and is prepared by the following steps: dissolving carbon quantum dots CQDs in an ethanol aqueous solution to obtain a CQDs dispersion liquid; and then adding cubic Fe2O3 nanoparticles, stirring for reaction, and drying to obtain the Fe-based catalyst with the short Fe-C bond. The short Fe-C bond Fe-based catalyst is simple to prepare and low in cost, can realize high-selectivity synthesis of C2 + products through one-step catalytic hydrogenation of CO2, and effectively reduces the selectivity of main C1 by-products CO and CH4. The invention develops a new regulation and control strategy for the electronic structure of the Fe-based catalyst for the CO2 hydrogenation catalytic reaction, provides a new thought for reasonably designing the catalyst with a directional synthesis function, and has a good application prospect in the field of CO2 capture, utilization and storage.

The present invention relates to the field of catalytic hydrogenation, and specifically relates to a preparation method and an application method of a ruthenium-based hydrogenation catalyst. The technical key points are as follows: Ni(NO3)2·6H2O and (NH4)H2W 12 O 40 ·xH2O are used to modify the Al2O3 support by the precipitation deposition method and then calcined to obtain a metal-modified support; then, ruthenium is loaded on the metal-modified support by the impregnation method and then calcined, and the hydrogenation catalyst is obtained after hydrogen reduction; wherein, the mass fraction of ruthenium is 0.5%, the mass fraction of Ni is 0.5 - 2.5%, the mass fraction of W is 0.5 - 2.5%, and the remaining components are the alumina support. In the present invention, ruthenium and alumina are respectively used for the selection of the active component and the support, and together with the auxiliaries nickel and tungsten, the synergistic effect among several metal elements improves the dispersion degree of the active component.

The invention discloses a Cu / ZrO2 catalyst with high Ov content, a preparation method of the Cu / ZrO2 catalyst and application of the Cu / ZrO2 catalyst in catalysis of CO2 hydrogenation for methanol preparation, and belongs to the technical field of CO2 capture, utilization and storage. The preparation method of the Cu / ZrO2 catalyst comprises the following steps: dissolving a Cu-containing precursor in water, carrying out ultrasonic dispersion, loading the Cu-containing precursor on a UIO-66 carrier by an equivalent-volume impregnation method, and drying to obtain a Cu / UIO-66 precursor; then, the Cu / UIO-66 precursor is subjected to carbonization treatment; and after cooling, carrying out oxidation treatment to prepare the Cu / ZrO2 catalyst with high Ov content. According to the invention, the Cu / ZrO2 catalyst is rapidly prepared by using a carbonization-oxidation-calcination technology for the first time, and excellent catalytic activity and stability are realized by limiting the size of Cu particles and adjusting the valence state of Cu by using the high Ov content of the Cu / ZrO2 catalyst. The prepared Cu / ZrO2 catalyst is stable in performance, so that the Cu / ZrO2 catalyst has good application prospect and value in the technical field of CO2 capture, utilization and storage.

The invention relates to a nickel-ruthenium-based solid superacid hydrogenation catalyst and a preparation method and application thereof, the method comprises the following steps: (NH4) 2S2O8 is dissolved in methanol, ZrO2 is added, stirring and ultrasonic treatment are continued, stirring and filtering are carried out, precipitate is dried overnight, solids are ground into powder after being cooled, and the powder is roasted at 550 DEG C for 3 h to obtain S2O8 < 2-> / ZrO2; the preparation method comprises the following steps: dissolving nickel salt and ruthenium salt in deionized water, performing ultrasonic treatment, adding S2O82- / ZrO2, continuing ultrasonic treatment, adding a NaBH4 solution for reduction, and changing the solution from light green to dark black; and filtering the mixture, drying in vacuum, and grinding to obtain the hydrogenation catalyst. According to the invention, a second metal Ru is introduced to modify a monometal Ni-based solid superacid catalyst 10% Ni-S2O8 < 2-> / ZrO2, and the bimetallic Ni-Ru catalyst is prepared. The catalyst has higher catalytic activity when applied to catalytic hydrogenation of coal model compounds.

The invention relates to the field of catalytic materials and discloses a copper-zinc-aluminum-alkylated graphite carbon combined catalyst as well as a preparation method and application thereof. The copper-zinc-aluminum-alkylated graphite carbon combined catalyst comprises a copper-zinc-aluminum catalyst and alkylated graphite carbon which are physically mixed, the alkylated graphite carbon is graphite carbon subjected to silane surface hydrophobic modification. The combined catalyst comprises a copper-zinc-aluminum catalyst and alkylated graphite carbon, and based on the hydrophobic property of the alkylated graphite carbon, in the reaction process of catalyzing CO2 hydrogenation to prepare methanol, the thermodynamic equilibrium limitation in the reaction of preparing methanol through carbon dioxide hydrogenation can be broken through by adjusting the equilibrium movement of element reaction, and the catalytic activity of the alkylated graphite carbon is improved. And meanwhile, agglomeration of metal particles can be effectively inhibited. Therefore, the combined catalyst of the present invention can exhibit efficient carbon dioxide conversion rate, excellent methanol selectivity and long-term stability.

The invention relates to the field of green energy, and discloses a hydrogen production and methanol co-production system and method.The hydrogen production and methanol co-production system comprises a water electrolysis hydrogen production unit, a carbon source supply unit, a hydrogen buffer storage unit, a methanol synthesis reaction unit, a gas separation and circulation unit and an intelligent regulation and control unit; the carbon source supply unit is used for providing CO2 or carbon-containing gas, the hydrogen buffer storage unit is connected with the output end of the water electrolysis hydrogen production unit and used for storing and adjusting hydrogen supply, and the input end of the methanol synthesis reaction unit is connected with the hydrogen buffer storage unit and the carbon source supply unit and used for catalytic hydrogenation reaction to generate methanol. Through cooperation of the water electrolysis hydrogen production unit and the hydrogen buffer storage unit, the problem of hydrogen production instability caused by renewable energy electric power fluctuation is effectively solved, continuous and stable hydrogen supply is achieved, and the raw material requirement of downstream methanol synthesis reaction is guaranteed.

A process for the production of isopropanol by catalytic hydrogenation of acetone, the process comprising: (a) feeding from top to bottom to an adiabatic reactor, the feed stream consisting of a gas stream comprising hydrogen and a liquid stream comprising fresh acetone; (b) passing the feed stream of step (a) through a fixed catalytic bed contained within the reactor, said catalytic bed operating in a trickle manner and containing at least one metallic copper-based catalyst, in order to obtain a reactor outlet effluent consisting of a liquid phase and a gas phase; (c) separating the effluent exiting the reactor by separating the liquid phase from the gas phase; (d) recycling a portion of the liquid phase obtained in step (c), referred to as a recycle stream, reintroducing the portion into the liquid stream of step (a) such that the ratio of the mass flow of the recycle stream to the mass flow of fresh acetone satisfies equation (I), referred to as the recycle ratio.

The invention belongs to the technical field of carbon dioxide conversion application and catalyst fine synthesis, and particularly relates to a thermal catalyst for preparing CO through CO2 hydrogenation, a preparation method of the thermal catalyst and application of the thermal catalyst in methanol preparation through a CO2 two-step method. The thermal catalyst comprises an S, N-doped reduced graphene oxide carrier, and MoS2 and FexN which are loaded on the S, N-doped reduced graphene oxide carrier; the molar ratio of Mo in the MoS2 to Fe in the FexN is (0.5-3.0): 1; the Fe < x > N comprises Fe < N > and / or Fe < 3 > N < 2 >. The key point of the invention is to design and synthesize a MoS2 / FexN / S, N-rGO thermal catalyst, regulate and control the ratio of Mo to Fe so as to well exert the synergistic effect of Mo and Fe, and combine the effects of S and N-rGO carriers to reduce the activation energy of CO2, improve the conversion rate of CO2 and promote the generation of CO, so that CO2 hydrogenation can be efficiently catalyzed to obtain high-concentration CO, the CO selectivity is high, and a process for preparing methanol from CO is combined, so that the production cost is reduced. Therefore, the methanol yield of the CO2 two-step methanol preparation process is remarkably improved.

The present invention relates to a production process for synthesizing hexamethylenediamine by catalytic hydrogenation of adiponitrile. The process comprises the following steps: 1) preparing a catalyst precursor; 2) calcining the catalyst precursor to obtain a catalyst; 3) catalytic hydrogenation of adiponitrile under the condition of the catalyst to synthesize crude hexamethylenediamine; 4) separating hexamethylenediamine from the discharge of a fluidized bed reactor containing crude hexamethylenediamine. The present invention uses Ni(NO3)2 and / or Mg(NO3)2 as main raw materials, doped with transition metal oxides, and then performs ultrasonic adsorption using Al2O3 as a catalyst carrier to load Ni(NO3)2 and / or Mg(NO3)2 and transition metal oxides on Al2O3, and obtains a catalyst through high-temperature calcination. The doping of transition metal oxides can improve the basicity of the catalyst, eliminating the need to add a strong basic co-catalyst in the catalytic reaction stage, reducing by-product formation. Moreover, it increases the specific surface area of the catalyst, thereby reducing the adsorption of the reaction product hexamethylenediamine on the catalyst, extending the service life of the catalyst, and saving the energy consumption for catalyst regeneration.

The invention relates to an ultrathin Ru / Co3O4 catalyst, Co3O4 serving as a carrier is of an ultrathin two-dimensional nanosheet structure, and Ru nanoparticles are uniformly loaded on the surface of the Co3O4. The preparation method comprises the following steps: dispersing Co3O4 in a mixture of deionized water and methanol to obtain a suspension; and adding ruthenium trichloride into the suspension, and irradiating the mixture with a xenon lamp to finally obtain the ultrathin Ru / Co3O4 catalyst. The invention relates to an ultrathin Ru / Co3O4 catalyst applied to photo-thermal CO2 hydrogenation. The method has the advantages that Co3O4 is of an ultrathin two-dimensional nanosheet structure, Ru is evenly loaded on the surface of Co3O4, Ru / Co3O4 has the high specific surface area, rich active sites are provided, the photo-thermal catalysis CO2 hydrogenation activity is remarkably improved, the problem that an existing catalyst is low in activity is solved, parameters such as the heating rate, the roasting temperature and time are accurately controlled, and Ru doping is combined, so that the catalytic activity of CO2 is greatly improved. Active component loss and structure collapse are effectively avoided, and the stability is enhanced.

The invention relates to a continuous preparation method of a supported catalyst and application of the supported catalyst in catalysis of furfural hydrocracking. The method comprises the following steps: adding Cu (NO3) 2.3 H2O, Ce (NO3) 3.6 H2O, Mg (NO3) 2.6 H2O and Al (NO3) 3.9 H2O into deionized water to form a solution A; naOH and Na2CO3 are taken and dissolved in deionized water, and a solution B is formed; then respectively introducing the solution A and the solution B into a feeding pump, then introducing into a membrane dispersion microreactor, and mixing to form a precipitate; and washing, drying, calcining and reducing to obtain the catalyst Cu-Ce / MgO-Al2O3. The catalyst prepared by the invention is used in a reaction for catalyzing furfural hydrocracking to prepare 1, 2-pentanediol, and shows excellent catalytic activity and stability, the conversion rate of furfural is as high as 99%, and the yield of 1, 2-pentanediol reaches 44%.

The utility model belongs to the technical field of chemical solvent preparation, and particularly relates to a tetrahydrofuran purification device. The utility model provides a tetrahydrofuran purification device. The tetrahydrofuran purification device comprises a feed port, a catalytic hydrogenation reaction part, a gas phase discharge port, a liquid phase discharge port, a heavy component removal tower and an absorption tower. In the application, through the catalytic hydrogenation part, the impurity dihydrofuran in the tetrahydrofuran is hydrogenated to generate the tetrahydrofuran, the impurities n-butyraldehyde and isobutyraldehyde are hydrogenated to generate alcohols which are easily separated from the tetrahydrofuran, through determination, the content of the impurity dihydrofuran in the purified tetrahydrofuran is reduced to 3 ppm or below, the alcohols are separated in the heavy component removal tower, and the content of the tetrahydrofuran in the tetrahydrofuran is reduced to 3 ppm or below. The purity and the quality of tetrahydrofuran are effectively improved, and the purification device structure and the purification process are simple.

The application discloses a kind of ruthenium grafting manganese aluminum hydrotalcite and catalytic method for C02 hydrogenation preparation formic acid, belong to catalyst technical field, in the application, under the optimized reaction condition, with methanol:water mixture as solvent (5:1), total pressure is 60bar, 60 DEG C, reaction 24 hours, with temperature controller to be heated to the temperature required for reactor.When the temperature inside the reactor reaches the specified temperature, start stirring at a fixed stirring speed (200-800 revolutions / min), after the required reaction time, stop stirring and heating, and allow the reactor to cool to room temperature. The hydrogenation products were analyzed by high performance liquid chromatography, the conversion number (TON) of formic acid reached more than 8000; RuMnAl-LDH was prepared by coprecipitation method, and RuMnAl hydrotalcite catalyst was obtained by heating and activation in a muffle furnace. The preparation process is simple, and the raw materials are easy to obtain. The RuMnAl-LDH catalyst prepared by the application has good catalytic activity and stability in the catalytic hydrogenation of formic acid to formic acid reaction, and has wide application prospect.

The present invention relates to a Ru-Ni bimetallic catalyst for the selective hydrogenation of a quinoline organic hydrogen storage carrier, and a preparation method therefor and the use thereof. In the catalyst, carbon nitride is used as a carrier, and metal nanoparticles Ru and Ni serve as active components and are jointly loaded on the carbon nitride carrier; and the carbon nitride is prepared by mixing carbon tetrachloride, ethidene diamine and nano-silica, reacting same to obtain a carbon nitride polymer, then calcining same at 750-850ºC, performing a desilicification treatment, and then filtering and drying same. The catalyst provided in the present application has good catalytic hydrogenation performance in the selective hydrogenation of the quinoline organic hydrogen storage carrier and can achieve the omission of a solvent in a reaction system; the reaction is simple, green and environmentally friendly, and the gravimetric hydrogen storage density of the system can be maximally ensured when a quinoline compound is used as an organic hydrogen carrier; moreover, the catalyst also has a good cycling stability.

The invention discloses a synthesis method of 9-dichloromethylene-5-amino-benzonorbornene and an intermediate product, the synthesis method comprises the following steps: firstly, synthesizing a cyclization compound 1 as shown in a formula 1 from a cold solution of 6, 6-dichlorofulvene and 1, 4-benzoquinone under the action of a solution of a catalyst I, carrying out oximation reaction on the cyclization compound 1 prepared in the step a and hydroxylamine salt under an alkaline condition, and carrying out post-treatment to obtain the 9-dichloromethylene-5-amino-benzonorbornene. Under the action of a catalyst II, adding the oximate 2 prepared in the step b into a closed container, carrying out hydrogenation reduction to obtain 9-dichloromethylene-5-amino-benzo norbornene, and directly treating the reduction product with acid to obtain 9-dichloromethylene-5-amino-benzo norbornene, namely the 9-dichloromethylene-5-amino-benzo norbornene, namely the 9-dichloromethylene-5-amino-benzo norbornene. According to the method, the cyclization compound is oximated firstly, then the residual carbonyl and two double bonds on the ring are subjected to one-step reduction through catalytic hydrogenation, the working procedure is optimized, meanwhile, reduction by using expensive sodium borohydride is avoided, the method is short in synthesis route and suitable for industrialization, and the production cost is reduced.

The invention discloses a method for preparing isostearic acid by hydrogenation of a bio-based carrier catalyst, and relates to the technical field of oleochemical engineering and catalyst preparation, and the method comprises the following steps: S1, preparing a bio-based supported catalyst; s2, taking isomerized oleic acid as a raw material, and carrying out catalytic hydrogenation reaction under the action of a catalyst; s3, separating a product obtained after the hydrogenation reaction to obtain isostearic acid; according to the method for preparing isostearic acid by hydrogenation of the bio-based carrier catalyst, oyster shells are selected as a catalyst carrier, and specific pretreatment and high-temperature firing are performed, so that waste biomass resources are converted into a high-specific-surface-area calcium oxide carrier with a natural nanoscale sheet-shaped superposed three-dimensional space structure; high-value utilization of waste resources is achieved, so that the effects that the cost of raw materials of the catalyst is remarkably reduced and the carrier is environmentally friendly are achieved, and the high-activity non-noble metal hydrogenation catalyst is obtained by adopting copper nitrate solution impregnation and combining with a loading mode of subsequent hydrogen reduction.