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71 results about "Higher alkanes" patented technology

Higher alkanes are alkanes having nine or more carbon atoms. Nonane is the lightest alkane to have a flash point above 25 °C, and is not classified as dangerously flammable. The term higher alkanes is sometimes used literally as "alkanes with a higher number of carbon atoms". One definition distinguishes the higher alkanes as the n-alkanes that are solid under natural conditions.

Method for preparing alkane fuel with high cetane number by catalyzing plant oil or long-chain fatty acid by Ru catalyst and application thereof

The invention provides a method for preparing alkane fuel with a high cetane number by catalyzing plant oil or long-chain fatty acid by a Ru catalyst, which comprises the following steps: (1) mixing plant oil or long-chain fatty acid with a solvent in proportion; (2) adding a catalyst with the hydrogenation function into the mixed solution in step (1); (3) reacting in reducing atmosphere to obtain long-chain alkane with a main component of C15-C18. The method for catalyzing plant oil or long-chain fatty acid by a Ru catalyst provided by the invention has a high fatty acid conversion rate and a high alkane yield. In addition, the method of the invention is simple in process, convenient for operation, and mild in reaction condition; the whole reaction process is basically free of carbon deposition; the catalyst is cheap, easily available, and suitable for multi-time repeated use without activity reduction. The product of the invention can be used directly as diesel oil, and has important economic and social meaning for vehicle liquid fuel sustainable supply.
Owner:UNIV OF SCI & TECH OF CHINA

Catalyst used for alkane catalytic dehydrogenation and preparation method thereof

A catalyst for alkane dehydrogenation comprises a component A and a component B, wherein the component A is an oxide selected from one or more of La, Fe, Zn, Cu, Co or Ce, and the content of the component A in the catalyst accounts for 0.5 to 50 wt%, preferably 10-30 wt%; the component B is a mixed oxide or a composite oxide selected from one or more of SiO2, Al2O3, ZrO2, Ga2O3 and MgO, and the content of the component B in the catalyst accounts for 50 to 99.5 wt%, preferably 70-90 wt%. The catalyst provided by the invention has high alkane single-pass conversion and high selectivity of olefin, after repeated regeneration, the reactivity is very stable, and the catalyst is used in a circulating fluidized bed reaction device.
Owner:CHINA UNIV OF PETROLEUM (EAST CHINA)

Preparation method of magnesium aluminate spinel for catalyst carrier

The invention relates to a preparation method of magnesium aluminate spinel for a catalyst carrier; a sol-gel method is adopted for preparation, and the preparation method comprises the following steps: (1) under a condition of the temperature of 50-80 DEG C, mixing water and ethylene glycol together; (2) adding citric acid, a magnesium source and an aluminum source into the ethylene glycol aqueous solution with the molar ratio of citric acid (CA) to Mg to Al of 6 to (0.9-1) to (2-2.2); (3) heating the solution until the solution becomes a transparent red gel, and aging; and (4) at the temperature of 350-500 DEG C, roasting for 2-4 h, grinding, again roasting for 2-12 h at the temperature of 600-800 DEG C, and thus obtaining the magnesia alumina spinel carrier. The prepared magnesia alumina spinel product is mainly used for a carrier of a low-carbon alkane dehydrogenation reaction catalyst, is loaded with 0.01-0.5 wt.% of a platinum-family transition metal element, 0.01-1 wt.% of Sn, and has smaller size, higher specific surface, and suitable pore structure; and compared with a conventional dehydrogenation catalyst carrier, the carrier has the characteristics of high alkane conversion rate, good stability, and good monoolefine selectivity.
Owner:DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI

Preparation method of dehydrogenation catalyst

The invention discloses a preparation method of a dehydrogenation catalyst. The preparation method comprises the following steps: (1) the ZSM-5 molecular sieve, aluminum oxide, sesbania powder and a dilute nitric acid solution are mixed, pulping, mixing and kneading, band extrusion, drying, and calcination are carried out, and the aluminum oxide carrier doped with ZSM-5 molecular sieve is obtained; wherein relative crystallinity of the ZSM-5 molecular sieve is 40-80%; (2) the carrier obtained in the step (1) is impregnated with an Sn-containing precursor, drying and calcination are carried out, and an Sn-loaded aluminum oxide carrier is obtained; (2) chloroplatinic acid, potassium nitrate and water are uniformly mixed, an impregnating solution is obtained, and the carrier obtained in the step (2) is impregnated with the impregnating solution; (4) programmed heating and drying, calcination, washing, drying and dehydration, and modification with a metal additive are carried out for the carrier which is treated by the impregnation in the step (3), and the dehydrogenation catalyst is obtained. The catalyst has the advantages of high alkane transformation efficiency, good alkene selectivity and good stability in the dehydrogenation reaction of light alkanes.
Owner:CHINA PETROLEUM & CHEM CORP +1

Method for preparing low-carbon alkane dehydrogenation catalyst

The invention discloses a method for preparing a low-carbon alkane dehydrogenation catalyst. The method comprises the following steps: 1)mixing a ZSM-5 molecular sieve, alumina, sesbania powder and a dilute nitric acid solution, beating the materials, kneading the materials, extruding the materials, drying and performing calcination to obtain a ZSM-5 molecular sieve-doped alumina carrier; 2) impregnating the carrier by using a Sn-containing predecessor solution, drying the carrier and performing calcination on the carrier to obtain the Sn-containing carrier; 3) dropping ammoniacal liquor and adding the material into a ZnCl2 aqueous solution, preparing a Zn(NH3)4C12 solution, adding a platinum-containing compound to prepare an impregnation solution; and 4) performing impregnation on the Sn-containing carrier by using the impregnation solution in the step 4), drying the material, and performing calcination to obtain the low-carbon alkane dehydrogenation catalyst. The prepared low-carbon alkane dehydrogenation catalyst has high alkane conversion rate, alkene selectivity and good stability in a low carbon alkane dehydrogenation reaction.
Owner:CHINA PETROLEUM & CHEM CORP +1

Low carbon alkane dehydrogenation olefin production catalyst and preparation method thereof

The present invention provides a low carbon alkane dehydrogenation olefin production catalyst and a preparation method thereof. According to the catalyst, a carrier is loaded with 0.01-5% by mass of a platinum group transition metal element, 0.01-10% by mass of a gold element, 0.01-10% by mass of a Group VIA metal element, and 0.01-10% by mass of an alkali metal element; or 0.2-15% by mass of a halogen element and 0.01-3% by mass of a sulfur element are added to be adopted as a modification component; the Group VIA metal element, the platinum group transition metal element, the gold element, the alkali metal element, the halogen element and the sulfur element are sequentially and respectively impregnated onto a carrier such as silica, a molecular sieve, magnesium-aluminum spinel or alumina, and a steam treatment is performed after the Group VIA metal element, the platinum group transition metal element and the gold element are impregnated and loaded on the carrier, wherein the Group VIA metal element, the platinum group transition metal element, the gold element, the alkali metal element, the halogen element and the sulfur element are adopted as catalyst components; and the catalyst has characteristics of high alkane conversion rate, high monoene selectivity and good stability.
Owner:PETROCHINA CO LTD +1

Method for preparing fuel oil with high alkane content by co-cracking non-edible grease and waste plastic

Provided is a method for preparing fuel oil with high alkane content by co-cracking non-edible grease and waste plastic. The method comprises the steps that 1, the waste plastic is cut and broken into fragments of which the area is smaller than 100 cm<2>; 2, the waste plastic and the non-edible grease are mixed according to the mass ratio of 1:1-1:10; 3, the mixture is fed into a cracking reactor, air in the reactor is replace by nitrogen, heating is conducted, the heating rate is 5-300 DEG C/min, when the temperature of reactant is increased to 150 DEG C, a stirring device is started, heating is conducted continuously, the temperature of the cracking reaction is controlled to range from 350 DEG C to 600 DEG C, the reaction time is 2-90 min, and after gas-solid separation is conducted on a cracking reaction product, condensation is conducted on the gas, and the fuel oil with the high alkane content is obtained. By means of the method for preparing the fuel oil with the high alkane content by co-cracking the non-edible grease and the waste plastic, according to the problems that the plastic structure is compact and coking is serious in the cracking process, the swelling effect of the grease on the plastic and the characteristic that glycerin residues in the grease release free state hydrogen atoms under specific cracking conditions are fully utilized. The stable and high-quality liquid fuel oil of which the oil productivity is over 85% and the alkane content reaches up to 74% is obtained.
Owner:浙江加宝新能源科技有限公司

Liquid acid alkylation reactor and alkylation reaction method

The invention relates to a liquid acid alkylation reactor and an alkylation reaction method. The reactor comprises a liquid acid inlet (1), a hydrocarbon inlet (2), a hydrocarbon feeding distributor (3), a mixed reaction zone and an acid hydrocarbon outlet (5), wherein the hydrocarbon inlet and the liquid acid inlet are positioned above the mixed reaction zone, the acid hydrocarbon outlet (5) is positioned below the mixed reaction zone, the hydrocarbon feeding distributor comprises a radial distribution part and an axial distribution part, the radial distribution part and the axial distribution part are communicated with each other, the pipeline extending directions of the radial distribution part and the axial distribution part are perpendicular to each other, the radial distribution partis arranged above the mixing reaction zone, the raw material inlet of the radial distribution part is communicated with the hydrocarbon inlet, the axial distribution part comprises a feeding verticalpipe (3.3), the top end of the feeding vertical pipe is communicated with the radial distribution part, the bottom end of the feeding vertical pipe is a free end, the bottom end of the feeding vertical pipe extends into the mixing reaction zone in the axial direction of the reactor, and a plurality of distribution holes (3.4) are formed in the pipe wall of the feeding vertical pipe at intervals in the axial direction. According to the alkylation reactor, in-situ multi-section feeding can be achieved so as to ensure high alkane-olefin ratio.
Owner:SINOPEC ENG +1

Method for producing aromatic hydrocarbon through light hydrocarbon dehydrogenation aromatization

The invention provides a method for producing aromatic hydrocarbon by light hydrocarbon dehydrogenation aromatization. The method comprises the following steps: 1) under dehydrogenation reaction conditions, carrying out dehydrogenation reaction on a light hydrocarbon material flow to obtain a material flow containing olefin; and 2) under aromatization reaction conditions, contacting the olefin-containing material flow with an aromatization catalyst, and carrying out an oligomerization/aromatization reaction to obtain an aromatic hydrocarbon-containing material flow. The thinking set that a bifunctional catalyst is used in the prior art is broken through, dehydrogenation and oligomerization/aromatization are separated, different conditions are used for executing in steps, and the following effects are achieved: 1) light hydrocarbon conversion can be independently controlled by changing the conditions of a dehydrogenation zone so as to realize minimum inactivation; and 2) the product selectivity can be independently controlled in oligomerization/aromatization, and the lowest methane selectivity and reverse reaction are achieved. The method has the advantages of high alkane conversion rate, high liquid aromatic hydrocarbon yield, slow catalyst deactivation and easy regeneration of the catalyst.
Owner:CHNA ENERGY INVESTMENT CORP LTD +1
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