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1597 results about "Conversion reaction" patented technology

Method for preparing salvianolic acid A by catalytically converting salvianolic acid B

The invention discloses a method for preparing salvianolic acid A by catalytically converting salvianolic acid B. The method is characterized in that the converted raw material is a salvia miltiorrhiza aqueous extract (salvianolic acid B=>50%) primarily purified through combined chromatography; the concentration of the raw material salvianolic acid B is 0.5-2%; urea is taken as the catalyst; the mole ratio of urea to the salvianolic acid B is 0.3-0.7; the conversion reaction temperature is 100-125 DEG C; and the reaction time is 3-6 hours. The method has the following beneficial effects: urea is taken as the catalyst, thus greatly shortening the time for which the salvianolic acid B is in easily destroyed state and remarkably increasing the yield of the salvianolic acid A; the primarily purified salvia miltiorrhiza extract is taken as the converted raw material, thus not only removing the metal ions which are not beneficial to conversion but also removing most colloid-like impurities and frontal impurities which are not beneficial to following separation of the salvianolic acid; and the directional conversion rate of the salvianolic acid B to the salvianolic acid A prepared by the method is not less than 10% and even reaches 60%.
Owner:SUZHOU LEINA PHARMA RES DEV +1

Shunting-type isothermal sulfur-tolerant conversion process and equipment thereof

ActiveCN101704513ASatisfy conversion rate requirementsMeet the requirements of adiabatic conversion control temperature riseHydrogenChemical industryShunt typesSulfur
The invention discloses a shunting-type isothermal sulfur-tolerant conversion process. The process comprises the following steps: shunting raw coal gas from exterior into at least two parts; leading overheat stream in the first part of the raw coal gas to increase the temperature to 200-300 DEG C; and then entering a first-stage conversion reaction step to carry out a conversion reaction and generate first conversion gas; and conveying the other part of the raw coal gas to next-stage conversion reaction step to carry out a conversion reaction. The catalyst bed of a shift converter has the advantages of stable temperature, simple control, convenient operation and low output CO content. The invention has the advantages of short conversion flows, few equipment, reduced resistance, great byproduct stream amount, high overheat temperature, stream pressure and heat recovery rate, and the like, thereby achieving the aims of reducing conversion stages, equipment number and resistance fall, decreasing investment, having great byproduct stream amount and high overheat temperature, stream pressure and heat recovery rate, reducing conversion stream consumption and outward wastewater discharge, protecting the environment and easily maximizing the device equipment. The invention also discloses shunting-type isothermal sulfur-tolerant conversion equipment used by the process.
Owner:SHANGHAI INT ENG CONSULTING

Process for producing olefins

A process is described for producing an olefins stream from a first vapor effluent stream from an oxygenate to olefin conversion reaction, said first vapor effluent stream comprising C2 and C3 olefins, C4 hydrocarbons, and C2 to C6 carbonyl compounds. In the process, the temperature and pressure of the first vapor effluent stream are adjusted to produce a second vapor effluent stream having a pressure ranging from about 100 psig to about 350 psig (790 to 2514 kPa) and a temperature ranging from about 70° F. to about 120° F. (21 to 49° C.), said second vapor effluent stream containing about 50 wt. % or more C4 hydrocarbons based upon the total weight of C4 hydrocarbons in the first vapor effluent stream. The second vapor effluent stream is then washed with a liquid alcohol-containing stream to produce a third vapor effluent stream, whereafter the third vapor effluent stream is washed with liquid water to provide a fourth vapor effluent stream comprising the C2 and C3 olefins and about 1.0 wt. % or less C2 to C6 carbonyl compounds.
Owner:EXXONMOBIL CHEM PAT INC

Synthetic method of ZSM-5 zeolites

The invention belongs to the synthesis field of aluminosilicate ZMS (Zeolite Molecular Sieve), and relates to a synthetic method of ZSM-5 zeolite molecular sieves. ZSM-5 zeolites are high-silicon micro-porous zeolites with unique three-dimensional ten-membered ring crossing aperture passages, the diameters of the aperture passages are close to the sizes of benzene rings, and the ZSM-5 zeolites can be widely applied to petroleum refining, petrochemical industry and fine chemicals synthesis. Particularly, nano-sized ZSM-5 zeolites achieve larger external surface area and higher intracrystalline diffusion rate, and have higher activity and selectivity as well as strong coking deactivation-resisting capability in hydrocarbons catalysis conversion reactions. The synthetic method regulates the polymerization degrees of silicon sources and aluminum sources respectively by adding acid and alkali so as to obtain highly reactive reactants, and can rapidly achieve nucleus formation in large quantities in a system so as to obtain nano-sized zeolites. The synthetic method is not limited by the types of the silicon sources and the aluminum sources, has strong applicability to raw materials, changes the activity of the raw materials through simple regulation, and can rapidly synthesize products of the nano-sized ZSM-5 zeolites with well crystallinity under the dosage conditions of no template and low-cost templates.
Owner:DALIAN UNIV OF TECH

Technology device and method for preparing propylene by dehydrogenating propane or propane-enriched low carbon hydrocarbon

The invention provides a technology device and method for preparing propylene by dehydrogenating propane or propane-enriching low carbon hydrocarbon. The device comprises a reacting/regenerating part and a product fractionating part. A reacting/regenerating system is divided into a parallel type arrangement scheme and a coaxial type arrangement scheme by a fluidized bed reacting/regenerating technology, wherein a raising pipe of the parallel type reacting/regenerating system is an internal or external raising pipe, and a raising pipe of the coaxial type reacting/regenerating system is an external raising pipe. The method comprises the steps: leading raw materials and reaction products to enter into a raising pipe reactor after heat exchange; performing a dehydrogenating conversion reaction under the conditions that the reaction temperature is 500-700 DEG C, the pressure is 0.1-0.4MPa, and the ratio of a microspherical catalyst to oil is 5-60, wherein the microspherical catalyst consists of chromium, rare earth oxides, alkali metal oxides and a gamma-Al2O3 carrier, preferably, the temperature is 550-670 DEG C, the pressure is 0.1-0.15MPa, and the ratio of the microspherical catalyst to oil is 6-14; leading the reaction products and the raw materials to enter into a gas-oil separator to separate a gas phase, a liquid phase from a water phase after heat exchange and cooling; leading the separated gas to enter into a gas compressor to be compressed and be transported to an absorbing/stabilizing part; pumping the liquid to an absorbing tower; transporting the liquefied gas from a return tank at the top of a stabilizing tower to a propylene/propane separating tower by a charging pump of a propylene tower; discharging the fine propylene separated from the top of the tower out of the device as a product; discharging the separated byproduct hydrogen out of the device; and returning products at bottom of the tower to the reacting/regenerating part to be recycled.
Owner:卓润生 +1

Chitosan modified alginate hydrogel three-dimensional porous bracket and preparation method thereof

InactiveCN101773683ARich sourcesControllable physical and chemical propertiesProsthesisPhosphateFreeze-drying
The invention relates to a chitosan modified alginate hydrogel three-dimensional porous bracket with specific in-vitro degradability and a preparation method thereof. The method comprises the following steps: dissolving sodium alga acid serving as a raw material in phosphate buffer solution; performing amidation reaction of a carboxyl group in the sodium alga acid and an amino group in a cross-linking agent cystamine or dimethyl cystinate under the activation of water-soluble carbodiimide to form a chemically crosslinked hydrogel; performing freeze drying on the hydrogel to obtain a porous bracket material of the hydrogel; and performing surface modification on the porous bracket by using chitosan. In solution of a reducing agent such as cysteine with an appropriate concentration, a disulfide bond in a hydrogel cross-bridge is degraded through a disulfide bond-sulfydryl conversion reaction, so the porous bracket is decomposed and dissolved and disappears. Therefore, the porous bracket can be used as an in-vitro cell culture template material. The hydrogel porous bracket researched by the invention has the characteristics of simple preparation, rich raw material source, low cost and availability. Various physiochemical performances, mechanical strength, degradation rate and surface properties of the bracket material are controllable within a large range.
Owner:TIANJIN UNIV

Core-shell type aromatic conversion catalyst, preparation method and application thereof

InactiveCN101722033AGuaranteed to be completely wrappedDecrease the external area char rateMolecular sieve catalystsHydrocarbon by metathesis reactionAlcoholCore shell
The invention relates to a core-shell type aromatic conversion catalyst, a preparation method and application thereof, mainly solving the problems of strong acidity of an outside surface, rapid inactivation speed and low selectivity of aromatic shape selective catalysis in previous molecular sieve based catalysts. The invention adopts the following technical scheme: the preparation method that ZSM-5 crystal grain is taken as a core and a high silicon MF1 molecular sieve shell layer is formed on the outside surface of the core crystal by secondary growth is used for synthesizing the core-shell type zeolite molecular sieve with tightly-bonded core and shell and communicated pore canals, then the catalyst is prepared by shaping and baking 10-100% of core-shell type zeolite molecular sieves and the balance binder in terms of weight percent to better solve the above problems. The invention can be used in industrial production of aromatic conversion reactions of toluene disproportionation, toluene methylation, xylene isomerisation, trimethylbenzene cracking, cumin cracking and styralyl alcohol alkylating.
Owner:CHINA PETROLEUM & CHEM CORP +1

Method for producing base oil of lubricating oil by using Fischer-Tropsch synthesis wax

The invention relates to a method for producing base oil of lubricating oil by using Fischer-Tropsch synthesis wax. The method comprises the following steps of: (a) enabling the Fischer-Tropsch synthesis wax to be in contact with a hydrofining catalyst in a hydrofining reaction region I to obtain the Fischer-Tropsch synthesis wax subjected to hydrogenating alkene saturation and deoxidization; (b) enabling the Fischer-Tropsch synthesis wax obtained in the step (a) to be in contact with a hydrogenating isomerization catalyst in a wax hydrogenating conversion reaction region A to obtain wax converting generation oil with depression of pour point; (c) enabling the wax converting generation oil obtained in the step (b) to be in contact with the hydrogenating isomerization catalyst in a wax hydrogenating conversion reaction region B to obtain a wax converting generation oil with further depression of pour point; (d) enabling the wax converting generation oil with further depression of pour point, obtained in the step (c), to be in contact with the hydrofining catalyst in a hydrofining reaction region II to obtain wax converting generation oil subjected to hydrofining; and (e) separating the generation oil obtained in the step (d) in a distillation region to obtain the base oil of the lubricating oil.
Owner:CHINA PETROLEUM & CHEM CORP +1

Comprehensive utilization process for low-carbon-emission Fischer-Tropsch synthesis tail gas

The invention discloses a comprehensive utilization process for a low-carbon-emission Fischer-Tropsch synthesis tail gas. The process is used for converting the non-circular tail gas generated after the Fischer-Tropsch synthesis reaction into synthesis gas containing hydrogen through water vapor reforming, and then separating and extracting high-purity hydrogen from the synthesis gas containing hydrogen for use. The comprehensive utilization process comprises the following steps: 1) obtaining converted gas through a water vapor conversion reaction, 2) obtaining a hydrocarbon fuel through a Fischer-Tropsch synthesis reaction, 3) converting a hydrocarbon compound containing two or more than two carbon atoms into methane after a pre-reforming reaction, 4), converting methane and water vapor into hydrogen and carbon monoxide through a reforming reaction, 5) separating gases respectively containing hydrogen and carbon monoxide, 6) and providing heat for a reforming reactor. The process disclosed by the invention can be used for effectively utilizing the Fischer-Tropsch synthesis tail gas, especially the tail gas containing a large amount of inert components, and converting the tail gas into the hydrogen for use. Meanwhile, the comprehensive utilization process disclosed by the invention can be used for effectively utilizing residual combustible components after the hydrogen in the reforming gas is separated, thereby enhancing the utilization efficiency of the energy.
Owner:WUHAN KAIDI ENG TECH RES INST CO LTD

Process for multistage residue hydroconversion integrated with staight-run and conversion gasoils hydroconversion steps

This invention relates to a novel integrated hydroconversion process for converting heavy atmospheric or vacuum residue feeds and also converting and reducing impurities in the vacuum gas oil liquid product. This is accomplished by utilizing two residue hydroconversion reaction stages, two vapor-liquid separators, and at least two additional distillate ebullated-bed hydrocracking / hydrotreating reaction stages to provide a high conversion rate of the residue feedstocks.
Owner:INST FR DU PETROLE

Process for the preparation of multimetallic catalysts that can be used in reactions for transformation of hydrocarbons

The invention relates to a process for the preparation of a catalyst comprising:a) The preparation of a colloidal oxide suspension of a first metal M1 that consists in the neutralization of a basic solution by an acidic mineral solution that contains the precursor of the metal M1,b) Bringing into contact the precursor of the promoter M2, either directly in its crystallized form or after dissolution in aqueous phase, with the colloidal suspension that is obtained in stage a),c) Bringing into contact the colloidal suspension that is obtained in stage b) with the substrate,d) Drying at a temperature of between 30° C. and 200° C., under a flow of air.The invention also relates to a process for the treatment of an olefinic fraction that uses the catalyst prepared [by] said preparation process.
Owner:INST FR DU PETROLE
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