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296results about How to "Accelerated vulcanization" patented technology

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

Hydro-denitrification catalyst for coal tar and preparation method thereof

The invention discloses a hydro-denitrification catalyst for coal tar and a preparation method thereof. The catalyst is composed of an active component, an additive and a carrier, wherein the active component is composed of tungsten trioxide and nickel oxide, and through taking the total mass of the catalyst as a benchmark, the content of the tungsten trioxide accounts for 16-24 wt % of the catalyst, and the content of the nickel oxide accounts for 3-6 wt % of the catalyst; the additive is phosphorus, through taking the total mass of the catalyst as a benchmark, and in terms of an elementary substance, the phosphorus accounts for 1-2 wt % of the catalyst; through taking the total mass of the catalyst as a benchmark, and in terms of a carrier dry basis, the carrier accounts for 68-80 wt % of the catalyst; and the carrier is composed of activated carbon, alumina and a H beta molecular sieve, wherein the activated carbon accounts for 10-31 wt % of the carrier, the alumina accounts for 53-82 wt % of the carrier, and the H beta molecular sieve accounts for 8-16 wt % of the carrier. The catalyst disclosed by the invention is easy to vulcanize and relatively high in activity; and a pore structure of the activated carbon is adjustable, so that the conversion of colloid components and the removal of nitrogen impurities in coal tar are facilitated, thereby slowing the carbon deposition of the catalyst. Compared with conventional catalysts, the prepared catalyst has more excellent hydro-denitrification performance.
Owner:SHAANXI COAL & CHEM TECH INST

Low-volatility benzothiazolyl mercaptosilanes and preparation method thereof

The invention discloses a low-volatility benzothiazolyl mercaptosilane and a preparation method thereof. A molecular structural formula of the low-volatility benzothiazolyl mercaptosilane is shown in the patent specification. The preparation method of the low-volatility benzothiazolyl mercaptosilane comprises the following steps that 1, a polyether and a chloroalkyl silane undergo a reaction at a temperature of 30 to 180 DEG C in the presence of one or more catalysts; and R3-H is separated from the reaction products so that a silane semi-finished product is obtained; and 2, 2-mercaptobenzothiazole is added into an organic solvent; and one or more alkalis and semi-finished silane are added into the 2-mercaptobenzothiazole solution to undergo a reaction with stirring at a temperature of 20 to 120 DEG C in a nitrogen atmosphere for 0.5 to 24 hours; the reaction products are subjected to filtration, washing and reduced pressure distillation to produce a brown-red liquid desired product. The low-volatility benzothiazolyl mercaptosilane can release a small quantity of alcohols, can improve reinforcing effects, mechanical properties and dynamic mechanical properties of vulcanized rubbers, and rolling resistance and wet skid resistance of tread rubber, has long scorch time and fast sulfuration speed, and can improve greatly sulfuration performances of rubber materials.
Owner:JIANGSU QIXIANG HIGH NEW MATERIAL

Method for preparing residual oil hydro-demetallization catalyst

The invention discloses a method for preparing a residual oil hydro-demetallization catalyst. The method comprises the following steps: (1) utilizing a polyhydric alcohol and / or a monosaccharide water solution for impregnation of an alumina carrier, carrying out hydrothermal carbonization treatment in a sealed vessel after the impregnation, and carrying out drying; (2) utilizing hydrogen peroxide for surface modification treatment of the alumina carrier which is hydrothermally carbonized in step (1), carrying out drying, loading the modified alumina carrier with active constituents, and carrying out drying again; (3) utilizing the alumina carrier which is loaded with the active constituents in step (2) for calcination in a nitrogen atmosphere or an inertia atmosphere, and then for calcination again in an oxygen-containing atmosphere to obtain the residual oil hydro-demetallization catalyst. The prepared residual oil hydro-demetallization catalyst is characterized in that the functions of the active constituents and a carrier are relatively poor, and the active constituents are uniformly distributed on the carrier, so that the active constituents are easy to vulcanize, and the demetallization activity and the desulfurization activity of the residual oil hydro-demetallization catalyst are obviously improved.
Owner:CHINA PETROLEUM & CHEM CORP +1

Method for circularly and rapidly pre-vulcanizing sulfur tolerant shift catalyst and carrying out segmental pre-vulcanizing by utilizing sulfur tolerant shift catalyst

ActiveCN103657741AThe vulcanization method is simpleHeating up fastCatalyst activation/preparationSocial benefitsVulcanization
The invention relates to a segmental pre-vulcanizing method of a sulfur tolerant shift catalyst in a multi-segment conversion process, particularly relates to a method for rapidly pre-vulcanizing cobalt-molybdenum-series sulfur tolerant shift catalysts and belongs to the technical field of pretreatment of the sulfur tolerant shift catalyst. According to the method, aiming at the situations of the temperature raising and the slow vulcanizing speed caused due to insufficient vulcanizing conditions, a segmental vulcanizing method is utilized, namely the rapid pre-vulcanizing of a first-segment furnace is reinforced to raise the temperature of a subsequent second-segment furnace; first-segment vulcanizing conditions are reinforced to guarantee the vulcanization of the catalyst so as to realize the rapid, efficient and complete vulcanization, meanwhile, the temperature of a subsequent second-segment bed is raised by high-temperature vulcanized gas in a rapid vulcanizing process, and the subsequent working segments are similarly processed, so that the vulcanizing and temperature raising time is greatly shortened, and the vulcanizing cost is lowered; by utilizing a circular vulcanizing manner, the emptying quantity is few, the overtemperature is avoided, the vulcanizing process is convenient and safe, the pollution is light, and the method has remarkable economic and social benefits.
Owner:CHINA PETROLEUM & CHEM CORP

Heavy oil hydrogenation catalyst and preparation method thereof

The invention provides a heavy oil hydrogenation catalyst and a preparation method thereof. The preparation method comprises the following steps: introducing a phosphorus source in the preparation process of a Y molecular sieve to obtain a phosphorus-containing NaY molecular sieve; converting the phosphorus-containing NaY molecular sieve into a phosphorus-containing hydrogen-type Y molecular sieve; preparing a solution from a titanium precursor and an aluminum precursor; adding the phosphorus-containing hydrogen-type Y molecular sieve, and hydrolyzing the solution to obtain a micro-pore/meso-pore oxide composite carrier; adding cobalt salt or nickel salt into the solution for preparing the micro-pore/meso-pore oxide composite carrier, and hydrolyzing the solution to obtain a metal-modified micro-pore/meso-pore oxide composite carrier; dropwise adding a solution of active components of nickel-tungsten or nickel-molybdenum into the metal-modified micro-pore/meso-pore oxide composite carrier; and immersing, drying and roasting to obtain the heavy oil hydrogenation catalyst. The catalyst provided by the invention can meet requirements on diffusion, hydrogenolysis and hydrogenation reaction of heavy oil macro-molecules, and is excellent in hydrogenation-denitrification activity on heavy oil.
Owner:BC P INC CHINA NAT PETROLEUM CORP +1

CO sulfur tolerant shift catalyst in cobalt-molybdenum system and preparation method

The invention provides a CO sulfur tolerant shift catalyst in a cobalt-molybdenum system. The CO sulfur tolerant shift catalyst comprises a carrier and active components, wherein the carrier is aluminium-titanium-based surficial magnesium-aluminium spinel; the active components are cobalt and molybdenum. The catalyst is ball-shaped. A preparation method comprises the following steps: introducing titanium on aluminium oxide to prepare the aluminium-titanium composite carrier; uniformly introducing magnesium on the aluminium-titanium composite carrier, and carrying out roasting and phase inversion to form the aluminium-titanium-based surficial magnesium-aluminium spinel; introducing the active components into the aluminium-titanium-based surficial magnesium-aluminium spinel to prepare the catalyst. The CO sulfur tolerant shift catalyst provided by the invention has the advantages that the low-temperature activity and the low-sulfur activity are good, the stability is strong, the adaptability to the demanding conversion condition of synthesized gas with high CO content (more than or equal to 60%) is stronger, the difficulties of poor stability, easy inactivity and short service life when the existing industrial catalyst is used for shifting of the synthesized gas with high CO content as a shifting or pre-shifting catalyst are solved, and the application range of the traditional CO sulfur tolerant shift catalyst is greatly expanded.
Owner:SHANDONG QILU KELI CHEMICAL RESEARCH INSTITUTE CO LTD
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