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787results about How to "Improve catalytic selectivity" patented technology

Method for ion liquid abstraction-catalytic oxidation desulfurization

InactiveCN101220293AMild reaction conditionsGood catalytic activity and selectivityRefining with oxygen compoundsIonTungsten
The invention relates to a method which uses ionic liquids extraction coupling tungsten, molybdenum and other polyoxometallate to catalyst oxidation so as to reduce the content of sulfur in the oil. The invention dissolves the catalyst into the ionic liquid and the volume ratio of the ionic liquid and the oil is 1:3 to 1:5, and the quantity range of the catalyst and the sulfur compounds is 1:100 to 4:100. The concentration of the aqueous hydrogen peroxide is 5 percent to 40 percent, and the content range with the sulfur compounds in the oil is 1:2 to 1:10. When the temperature is between 30 and 70 DEG C and the reaction time is 0.5 to 3 hours, coupling catalyst oxidation is extracted to reduce the content of sulfur in the oil to be less than 10 ppm. Compared with the traditional method, the method has the advantages that the sulfur has high removal efficient, and the reaction system is very simple, and the reaction condition is very soft and no pressure equipment is needed; the separation is very convenient and the ionic liquid can be recycled.
Owner:CRPC INNOVATION ENERGY

Process for the start-up of an epoxidation process, a process for the production of ethylene oxide, a 1,2-diol, a 1,2-diol ether, a 1,2-carbonate, or an alkanolamine

A process is provided for the start-up of an ethylene epoxidation process comprising: (a) contacting a catalyst bed comprising a high selectivity epoxidation catalyst with a feed comprising ethylene, oxygen and an organic chloride for a period of time until an increase of at least 1×10−5 mole-% of vinyl chloride (calculated as the moles of vinyl chloride relative to the total gas mixture), preferably 2×10−5 mole-% of vinyl chloride is detected in a reactor outlet gas or a recycle gas loop; and (b) subsequently adjusting the quantity of organic chloride in the feed to a value sufficient to produce ethylene oxide at a substantially optimum selectivity.
Owner:SHELL OIL CO

Catalyst and method used for preparing 1,3-butadiene by oxidative dehydrogenation of n-butene

The invention discloses a catalyst and a method used for preparing 1,3-butadiene by oxidative dehydrogenation of n-butene. The catalyst is a cobalt and magnesium modified zinc ferrite catalyst which is obtained by proportioning a ferric salt, a zinc salt, a cobalt salt, a magnesium salt and a deionized water in a mole ratio, regulating pH value with ammonia water, concentrating, filtering, drying, roasting, cooling, grinding and screening. The method for preparing 1,3-butadiene by utilizing the catalyst comprises the following steps of: with C4 fraction produced by MTO (methanol to olefin) as a raw material, carrying out catalytic oxidative dehydrogenation reaction on a reaction mixture which is formed by the C4 fraction, air and vapour under the action of the cobalt and magnesium modified zinc ferrite catalyst so as to efficiently prepare1,3-butadiene, wherein the main ingredient of the C4 fraction is n-butene. The method disclosed by the invention has the advantage that the C4 fraction is not required to be refined to remove impurities such as oxygenated chemicals, thus the method disclosed by the invention is a simple and efficient method for preparing a high-additional-value product by utilizing C4 resource of the MTO.
Owner:SHAANXI COAL & CHEM TECH INST

Catalyst for Catalytic Cracking Fluidized Bed

The present invention relates to a catalyst for catalytic cracking fluidized-bed, and the technical problems to be primarily solved by the present invention are high reaction temperature, low cryogenic activity of catalysts and worse selectivity during the preparation of ethylene-propylene by catalytically cracking naphtha. The present invention uses the composition having the chemical formula (on the basis of the atom ratio): AaBbPcOx, so as to magnificently solve said problems. The present invention therefore can be industrially used to produce ethylene and propylene by catalytically cracking naphtha.
Owner:CHINA PETROCHEMICAL CORP +1

2, 5-dihydroxy methyl furan or 2, 5-dihydroxy methyl tetrahydrofuran synthesis method

InactiveCN103804329AWide variety of sourcesHigh catalytic activity and selectivityOrganic chemistryFructoseHexose
The invention relates to a method which uses a sugar catalyst to directly synthesize 2, 5-dihydroxy methyl furan or 2, 5-dihydroxy methyl tetrahydrofuran. The method comprises the steps that fructose and other hexose is used as a raw material, and is dehydrated in the presence of a solid acid catalyst to generate 5-hydroxymethyl furfural; the solid acid is separated; a hydrogenation catalyst is added; and reaction with hydrogen inlet is carried out under normal temperature and pressure to generate the 2, 5-dihydroxy methyl furan or 2, 5-dihydroxy methyl tetrahydrofuran. The method has the advantages of mild reaction condition, cheap and easily obtained raw material, easy reaction process operation, and high yield of 2, 5-dihydroxy methyl furan or 2, 5-dihydroxy methyl tetrahydrofuran.
Owner:DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI

Porous carbon-loaded composite material catalyst as well as preparation method and application thereof

The invention discloses a porous carbon-loaded composite material catalyst as well as a preparation method and application thereof. The catalyst consists of a carrier, an active component and a carbon quantum dot, wherein the active component and the carbon quantum dot are loaded on the carrier; the size of the carbon quantum dot is not more than 10 nm; the carrier is porous activated carbon; the active component is one of or a combination of several of platinum, palladium, iridium, ruthenium and rhodium; based on the mass of the carrier, the loading quantity of various metals in the active component is shown as follows: the platinum is 0-10.0 percent by weight, the palladium is 0-10.0 percent by weight, the iridium is 0-10.0 percent by weight, the ruthenium is 0-10.0 percent by weight, and the rhodium is 0-5.0 percent by weight; the loading quantity of the platinum, the rhodium and the palladium is not 0; the total loading quantity of the active component is more than 0.5 percent by weight and is not more than 20 percent by weight; based on the mass of the carrier, the loading quantity of the carbon quantum dot is not more than 15.0 percent by weight. The invention further provides application of the porous carbon-loaded composite material catalyst to the reaction of synthesis of chloroaniline by selective catalytic hydrogenation of chloro-nitrobenzene. The catalyst has the characteristics of being high in conversion rate, high in catalytic activity and high in stability.
Owner:ZHEJIANG UNIV OF TECH

Catalyst using phosphine-phosphoramidite ester as ligand, its preparation method and application

The invention relates to a catalyst which uses the phosphor-phosphamide as ligand, which is the phosphor-phosphamide ligand metallic complex of chiral ferrocenyl bone, wherein, the metal is rhodium, ruthenium, iridium, platinum or palladium; and the mol rate between the ligand and the metal precursor is 1.1:1-2.2:1. The ligand is compounded from chiral ferrocenyl to intermediate compound via several reaction steps, to be processed condensation with phosphite ester chloridate to attain the phosphor-phosphamide ligand with different chiral centers. Said ligand has new structure, stable property, simple compounding method, and wider application to the catalyst, which has higher catalysis activity (TON reaches 10000) and higher spatial selectivity (ee reaches more than 99%) in catalyzing asymmetry hydrogenization of itaconic acid, etc.
Owner:DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI

Nitrogen-doped activated carbon supported noble metal catalyst and application thereof

The invention discloses a nitrogen-doped activated carbon supported noble metal catalyst and an application thereof. The catalyst is composed of a carrier and an active component; the carrier is nitrogen-doped activated carbon; the active component is one of palladium, platinum, rhodium, ruthenium and iridium; and the load of the active component is not higher than 15wt% based on the mass of the carrier. The invention provides the application of the nitrogen-doped activated carbon supported noble metal catalyst to reaction for preparing an alkyl-containing halogenated aromatic aminocompound shown as a formula (II) by carrying out catalytic hydrogenation reduction on an alkyl-containing halogenated aromatic nitrocompound shown as a formula (I) to show that the nitrogen-doped activated carbon supported noble metal catalyst has the characteristics of high hydrogenation reaction rate, high catalytic activity, high selectivity and high stability.
Owner:ZHEJIANG UNIV OF TECH

Method for producing lactic acid by using glycerin and special catalyst for production of lactic acid by using glycerin

The invention provides a method for producing lactic acid by using glycerin and a special catalyst for the production of the lactic acid by using the glycerin. The catalyst provided by the invention is obtained by loading 0.1 to 30 mass parts of an active ingredient onto 100 mass part of carrier, wherein active ingredient is (1) Pt or (2) a composite of Pt and other noble metals. The catalyst can be used in the production of the lactic acid by using the glycerin. In the presence of the catalyst of the invention, the glycerin can be converted into the lactic acid effectively under a mild reaction condition. The catalyst of the invention has the advantages of high activity and selectively, easy preparation, low price, easy industrialization, long service life, loss prevention and good application prospective.
Owner:PEKING UNIV

Method of preparing adipinic acid using bionic catalytic oxggen to oxidize cyclohexane

InactiveCN1556088AHigh catalytic activity and selectivityOxidation depth is easy to controlOrganic compound preparationCarboxylic compound preparationSolventCyclohexane
A bionic process for preparing hexanedioic acid by catalytic oxidation of cyclohexane features that under existance of catalyst which may be metallic phthalocyanine, single-nucleus metallic porphyrin, or mu-oxy-dual-nucleus metallic porphyrin, the hexane and O2 take part in oxidizing reaction at 110-160 deg.C for 4-32 hr.
Owner:BEIJING UNIV OF TECH
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