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98results about How to "Larger surface area" patented technology

Preparation method of hierarchically porous zeolite molecular sieve

The invention relates to the technical field of molecular sieve preparation, and discloses a preparation method of a hierarchically porous zeolite molecular sieve. The specific surface area of a hierarchically porous EU-1 molecular sieve is improved. The method comprises the steps that a template agent part of EU-1 molecular sieve original powder is firstly removed through temperature controlling,then the processed EU-1 molecular sieve is placed in an acid solution to be reacted for 12-48 hours at the temperature of 100-150 DEG C, and finally the EU-1 molecular sieve is placed in an alkali solution where CTAB is dissolved to be reacted for 2-48 hours at the temperature of 80-180 DEG C to obtain the hierarchically porous EU-1 molecular sieve after sintering is conducted. The method has theadvantages that the hierarchically porous molecular sieve is prepared by the joint processing of desilicification and CTAB auxiliary secondary crystallization bonding through sintering temperature controlling and acid treatment, the method is simple, the outer specific surface area of the formed hierarchically porous EU-1 molecular sieve is increased, the dispersing performance of the molecular sieve is improved, and the catalytic activity is further improved.
Owner:TAIYUAN UNIV OF TECH

Preparation method of C10<+> heavyweight aromatic hydrocarbon transalkylation catalyst

ActiveCN104368373AHigh intragranular diffusion rateIncrease profitMolecular sieve catalystsHydrocarbonsSolventMetal salts
The invention discloses a preparation method of a C10<+> heavyweight aromatic hydrocarbon transalkylation catalyst. The preparation method is characterized in that firstly, the catalyst is prepared from a main active component named a HY molecular sieve with the mass percentage of 50-80% and the grain size of 30-100 nanometers, an adhesion agent named aluminum oxide of 15-40% and a modifying agent component named metal or a metallic oxide of 1-8%; secondly, the catalyst is prepared by the following steps: 1) mixing the nano HY molecular sieve with aluminum oxide, adding a squeeze aid, a pore-enlarging agent or an intensity additive with the mass percentage of no more than 5%, carrying out extrusion molding with a dilute nitric acid solution with mass percentage concentration of 4%, airing naturally, drying at 100-120 DEG C for 10-15 hours, then carrying out temperature programming to 550 DEG C, and roasting for 4-6 hours, thereby preparing a semi-finished catalyst; and 2) adding the product in the step 1) into a metal salt solution of the modifying agent component, dipping at room temperature with the equal volume for 6-30 hours, drying at 100-120 DEG C for 10-15 hours, then carrying out temperature programming to 550 DEG C, and roasting for 4-6 hours, thereby obtaining the finished product of the catalyst.
Owner:CHINA NAT OFFSHORE OIL CORP +3

Method for preparing MFI catalyst carrying transition elements and MFI catalyst application

Disclosed are a method for preparing an MFI catalyst carrying transition elements and MFI catalyst application. Cationic gemini surfactant- dibromide-1-(dimethyl hexyl ammonium)-6-(dimethyl octodecyl ammonium) hexane is used as structure directing agent of the MFI catalyst, sodium silicate is used as a silicon source and is subjected to low-temperature hot crystallization under self-generated pressure in a rotationally dynamic manner, and after directional polycondensation, rearrangement, nucleation and growth of inorganic atom Si-Al-Na-O on a two-dimensional plane, and single-structure-cell nano-layer MFI catalytic materials which are in mesoporous and microporous structure with the thickness ranging from 2 nanometers to 5 nanometers only are synthetized. Activity center point number of the MFI catalyst is increased evidently by utilizing two-dimensional single-structure-cell nano MFI carrying transition elements of Fe and Mo, the thickness of the catalyst crystal is reduced effectively, diffusion path is shortened, and molecular diffusion is speeded up. In addition, according to the result of a test of utilizing the selective catalytic reduction (SCR) process to remove tail gas of automobiles, NOx removal rate reaches 99.5%.
Owner:TAIYUAN UNIV OF TECH

Method for protecting precious metal crucible by coating crucible with high temperature resistant coating

The invention relates to a method for protecting a precious metal crucible by coating the crucible with a high temperature resistant coating. The method comprises the following steps: carrying out surface pretreatment on the precious metal crucible: blasting the outer surface of the precious metal crucible by using aluminium oxide particles at a high speed in an airtight box, so that ultrafine pits are formed on the outer surface of the precious metal crucible so as to increase the outer specific surface area of the crucible; and carrying out high-temperature plasma spraying of fine zirconium oxide sand on the pretreated outer surface of the precious metal crucible so as to form a dense zirconium oxide protective layer. According to the method, the ultrafine pits are formed on the outer surface of the precious metal crucible by carrying out high-speed fine particle blasting on the outer surface of the precious metal crucible so as to increase the outer specific surface area of the crucible, so that the adsorption capacity between the protective layer and the outer surface of the crucible is increased; and the dense zirconium oxide protective layer is formed through plasma spraying, so that the volatilization of the precious metal crucible is reduced, the using loss is reduced, and the growth cost of crystals is saved.
Owner:SHANGHAI INST OF CERAMIC CHEM & TECH CHINESE ACAD OF SCI

Dual-function catalyst applied to isomerization of C8 aromatic hydrocarbon and preparation method of dual-function catalyst

The invention discloses a dual-function catalyst applied to isomerization of C8 aromatic hydrocarbons and a preparation method of the dual-function catalyst. The catalyst is prepared from the following components: 10-89.9wt% of H type hierarchical-pore structure EUO molecular sieve, 9.9-89.9wt% of matrix and 0.01-2.0wt% of metal active component. The preparation method comprises the following steps: mixing the hierarchical-pore EUO molecular sieve, the matrix and a pore-enlarging agent, then adding an acid solution, kneading and forming, drying and roasting to remove the components such as thepore-enlarging agent to form a carrier, then dipping the carrier in a mixed solution containing metal salt and activating to obtain a formed catalyst. The hierarchical-pore EUO molecular sieve is crystallized and synthesized by taking a long-chain silane compound as a crystallization promoting agent and taking biquaternary ammonium salt with an alkane structure substituted by a di-penta-heterocycle group as an organic template agent. The catalyst shows favorable activity and selectivity in hydroisomerization reaction of C8 aromatic hydrocarbon and has a good industrial application prospect and a good economic value.
Owner:CHINA CATALYST HLDG CO LTD

A kind of spherical heteroatom ni-sapo-34 molecular sieve and its preparation and application

The invention relates to a spherical heteroatom Ni-SAPO-34 molecular sieve, and a preparation method and an application thereof. The preparation method comprises the following synthesis steps: (1) dissolving nickel nitrate hexahydrate in deionized water, and dropwise adding a chelating agent at room temperature while stirring to obtain a Ni chelate solution A; (2) mixing an aluminum source, a phosphorous source, a silicon source, a template and deionized water, and heating and stirring the obtained mixture to obtain an initial sol B; (3) adding the solution A to the initial sol B, and heating and stirring the solution A and the initial sol B to obtain a sol C; and (4) filling a reaction kettle with the sol C, carrying out a crystallization reaction, filtering and washing a product obtained after the reaction is completed until the product is neutral, and drying, calcining and cooling the neutral product to obtain the spherical heteroatom Ni-SAPO-34 molecular sieve. The spherical heteroatom Ni-SAPO-34 molecular sieve with a high crystallinity is synthesized by a sol-hydrothermal synthesis technology, the pressure drop of an accumulated catalyst bed is effectively reduced, the introduction of metallic nickel provides many active sites for the reaction, and the molecular sieve has an important application in an NH3-SCR reaction. The synthesis method has the advantages of simple steps, and easiness in operation.
Owner:SHANTOU UNIV

Alkyl anthraquinone hydrogenation catalyst and preparation method thereof

The invention discloses an alkyl anthraquinone hydrogenation catalyst and a preparation method thereof. The alkyl anthraquinone hydrogenation catalyst is applied to a technology for producing hydrogen peroxide by an anthraquinone method. The alkyl anthraquinone hydrogenation catalyst is prepared from a catalyst carrier (a CNTs-TiO2 complex) and an active component (palladium atoms) by an equivalent-volume impregnation method, wherein in terms of the elementary palladium atoms, the active component accounts for 0.1-5% of the total weight of the alkyl anthraquinone hydrogenation catalyst; the CNTs-TiO2 complex is prepared from TiO2 and Ni(NO3)2 by a chemical vapor deposition method in the presence of a carbon source gas; the molar ratio of the TiO2 to the Ni(NO3)2 is (0.04-0.25): (0.015-0.2); CNTs accounts for 5-30% of the total weight of the CNTs-TiO2 complex. In the alkyl anthraquinone hydrogenation catalyst, the carrier CNTs-TiO2 complex has a relatively large external specific surface area, so that envelopment of the palladium atoms in the carrier can be effectively reduced, and thus the palladium atoms are fully utilized to improve the activity of the alkyl anthraquinone hydrogenation catalyst; meanwhile, the acidity of the CNTs-TiO2 complex is weaker than Al2O3, and under the action of the TiO2, occurrence of a degradation reaction in the reaction process can be effectively reduced, so that production of a degraded product in a working fluid is reduced. The alkyl anthraquinone hydrogenation catalyst has the characteristics of high hydrogenation efficiency, low anthraquinone degradation and the like in the process of producing the hydrogen peroxide by the anthraquinone method.
Owner:CHINA CATALYST HLDG CO LTD

Preparation method and application of hierarchical pore SAPO-11 molecular sieve and long-chain alkane isomerization catalyst

The invention relates to the technical field of alkane isomerization catalysts, in particular to a preparation method and application of a hierarchical pore SAPO-11 molecular sieve and a long-chain alkane isomerization catalyst. The preparation method comprises the following steps: adding water, low-carbon alcohol, a Gemini surfactant and an organic pore-forming agent into a reaction kettle; thenadding phosphoric acid, a template agent and silica sol, conducting stirring, then putting the stirred material into a kettle for crystallization, washing, drying and roasting a crystallization product, then adding a binder and a molding aid for extrusion molding, loading a certain amount of active components on a carrier obtained by extrusion molding, and conducting drying and roasting to obtainthe long-chain alkane isomerization catalyst. In the preparation process, the low-carbon alcohol, the Gemini surfactant and the organic pore-forming agent are introduced to obtain the hierarchical pore SAPO-11 molecular sieve with small particle size, and the alkane isomerization catalyst prepared by taking the hierarchical pore SAPO-11 molecular sieve as the carrier is developed in pore passage and excellent in mass transfer performance, and has good isomerization activity and selectivity when being used for isomerization of long-chain alkane.
Owner:QINGDAO TECHNOLOGICAL UNIVERSITY
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