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49results about How to "Reasonable hole structure" patented technology

Preparation method of catalyst for continuous production of succinic anhydride from hydrogenation of maleic anhydride

The invention provides a catalyst for continuously producing butanedioic anhydride by maleic anhydride hydrogenation. The catalyst is a nickel loaded catalyst prepared by an equivalent-volume impregnation method, wherein in the catalyst, the content of nickel is 13 to 20 weight percent, the content of accelerating agent is 1 to 7 weight percent, and a carrier is a composite oxide of SiO2 and Al2O3 or SiO2-Al2O3. A preparation method for the catalyst comprises the following steps: impregnating impregnation solution blended by ammonia water and active metal salt solution on a carrier subjected to baking pretreatment at a temperature between 400 and 800 DEG C by the equivalent-volume impregnation method to form the catalyst through drying, baking and reducing treatment. The catalyst is applied to continuously preparing the butanedioic anhydride by maleic anhydride hydrogenation on a fixed bed reactor, the conversion rate of maleic anhydride is more than or equal to 99.98 percent, and theselectivity of the butanedioic anhydride is more than or equal to 98.85 percent. The catalyst achieves the technical-scale continuous production of the butanedioic anhydride, and has the advantages of high activity, good selectivity, high yield (more than or equal to 98.83 percent) and long service life.
Owner:SHANXI UNIV

High-abrasion resistance lithium-containing iron series Fischer-Tropsch synthetic catalyst, catalyst bonding agent containing blending silica sol and preparation method and application thereof

The invention provides a high-abrasion resistance lithium-containing iron series Fischer-Tropsch synthetic catalyst and a preparation method thereof. The catalyst comprises the following elements of: Fe, Cu, K, Li and SiO2 in a weight ratio of 100:(1.5-15):(1.5-15):(0.1-8):(10-60). The invention also provides a catalyst bonding agent for preparing the Fischer-Tropsch synthetic catalyst and a preparation method thereof and application of the catalyst bonding agent containing blending silica sol of lithium silicate and potassium silicate to the preparation of the high-abrasion resistance lithium-containing iron series Fischer-Tropsch synthetic catalyst. The catalyst bonding agent contains the blending silica sol of the lithium silicate and the potassium silicate, and lithium-ion and potassium-ion interactive arrangement chain sections are positioned on a polysilicate molecular chain. The lithium-containing iron series Fischer-Tropsch synthetic catalyst has high mechanical strength and hydrothermal stability and high Fischer-Tropsch synthetic activity, and is suitable to be used in a slurry reactor; and a preparation process is simple and is suitable for large-scale production.
Owner:CHNA ENERGY INVESTMENT CORP LTD +2

Preparation method of biomass-based nano-silica aerogel

The invention relates to a preparation method of biomass-based nano-silica aerogel. The method comprises the following steps: acidifying straws used as a raw material by hydrochloric acid to remove impurities, pyrolyzing the acidified straws at a high temperature, and combing a high-speed vibration ball mill with an ultrasonic dispersion process to extract biomass-based nano-silica from the raw material straws; carrying out a heating reaction on the biomass-based nano-silica and a NaOH solution, and cooling and filtering the obtained solution to obtain a biomass-based water glass solution; adding sulfuric acid to adjust the pH value to 1-2, and dropwise slowly adding the NaOH solution to make the pH value reach 7-8, carrying out continuous stirring standing, and cleaning the obtained material with deionized water to remove impurities in order to synthesize biomass-based hydrogel; exchanging the hydrogel with an anhydrous ethanol solvent; and freeze-drying the exchanged biomass-based hydrogel by using a vacuum freeze drying machine to obtain the biomass-based nano-silica aerogel. The obtained nano-silica aerogel has the advantages of high specific surface area, reasonable pore structure, low apparent density and excellent thermal performance, can be used in the fields of buildings, medicines and chemical engineering catalysis materials, and realizes waste recycling.
Owner:林扬东方(北京)科技有限公司

Preparation method capable of improving low-temperature activity of low-pressure cobalt-molybdenum sulfur-tolerant shift catalyst

The invention relates to a preparation method capable of improving the low-temperature activity of a low-pressure cobalt-molybdenum sulfur-tolerant shift catalyst. The sulfur-tolerant shift catalyst which contains nano-molybdenum oxide and nano-cobalt oxide is produced directly by utilizing a conventional process capable of producing a spherical activated alumina carrier by adopting a quick release method. An impregnation process is omitted; the preparation is simple; the cost is low; catalytic active components are uniform; a porous structure is reasonable; the specific surface area is increased remarkably; the low-temperature activity is high; through the detection at 160 DEG C according to a national chemical industry standard HG/T2779-2009, the CO conversion rate is greater than or equal to 90 percent, the activation temperature is 40 DEG C lower than that of an SB303Q-type cobalt-molybdenum sulfur-tolerant shift catalyst; the low-pressure cobalt-molybdenum sulfur-tolerant shift catalyst is particularly suitable for a depth conversion workshop section of an ammonia synthesis plant, namely the conversion process in which the CO at an outlet of a conversion system is less than equal to 0.3 percent; steam is saved by 300kg per ton of ammonia; the energy-saving effect is remarkable.
Owner:湖北双雄催化剂有限公司

A hydrocracking catalyst and a preparing method thereof

A hydrocracking catalyst and a preparing method thereof are disclosed. The catalyst comprises metal components with hydrogenation activity and a carrier comprising a beta molecular sieve, amorphous silicon aluminum and aluminum oxide, wherein properties of the beta molecular sieve are as follows: the specific surface area is 400-800 m2/g, the total pore volume is 0.4-0.55 mL/g, the SiO2/Al2O3 mole ratio is 30-60, the relative crystallinity is 120-140%, the infrared acid content is 0.55-1.0 mmol/g, the non-framework aluminum accounts for less than 1% of the total aluminum, the amount of medium-strong acids which is measured by a NH3-TPD method accounts for 70-85% of the total acid amount, and the percent of Na2O is not more than 0.15 wt%. The preparing method includes mixing the beta molecular sieve, the amorphous silicon aluminum and the aluminum oxide, kneading and forming to prepare the carrier; and loading the metal components with hydrogenation activity by a conventional method. The beta molecular sieve which is proper in silicon aluminum ratio, large in specific surface area, proper in acidity, reasonable in pore structure and low in content of non-framework aluminum, and the amorphous silicon aluminum are adopted as cracking components of the catalyst. The prepared catalyst is characterized by producing a clean diesel oil product with a low condensation point with the highest yield, improving properties of hydrogenation tail oil, and the like.
Owner:CHINA PETROLEUM & CHEM CORP +1

Hydrocracking catalyst and its preparation method

A hydrocracking catalyst and a preparing method thereof are disclosed. The catalyst comprises metal components with hydrogenation activity and a carrier comprising a beta molecular sieve, amorphous silicon aluminum and aluminum oxide, wherein properties of the beta molecular sieve are as follows: the specific surface area is 400-800 m2 / g, the total pore volume is 0.4-0.55 mL / g, the SiO2 / Al2O3 mole ratio is 30-60, the relative crystallinity is 120-140%, the infrared acid content is 0.55-1.0 mmol / g, the non-framework aluminum accounts for less than 1% of the total aluminum, the amount of medium-strong acids which is measured by a NH3-TPD method accounts for 70-85% of the total acid amount, and the percent of Na2O is not more than 0.15 wt%. The preparing method includes mixing the beta molecular sieve, the amorphous silicon aluminum and the aluminum oxide, kneading and forming to prepare the carrier; and loading the metal components with hydrogenation activity by a conventional method. The beta molecular sieve which is proper in silicon aluminum ratio, large in specific surface area, proper in acidity, reasonable in pore structure and low in content of non-framework aluminum, and the amorphous silicon aluminum are adopted as cracking components of the catalyst. The prepared catalyst is characterized by producing a clean diesel oil product with a low condensation point with the highest yield, improving properties of hydrogenation tail oil, and the like.
Owner:CHINA PETROLEUM & CHEM CORP +1
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