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28820 results about "Molecular sieve" patented technology

A molecular sieve is a material with pores (very small holes) of uniform size. These pore diameters are similar in size to small molecules, and thus large molecules cannot enter or be adsorbed, while smaller molecules can. As a mixture of molecules migrate through the stationary bed of porous, semi-solid substance referred to as a sieve (or matrix), the components of highest molecular weight (which are unable to pass into the molecular pores) leave the bed first, followed by successively smaller molecules. Some molecular sieves are used in chromatography, a separation technique that sorts molecules based on their size. Other molecular sieves are used as desiccants (some examples include activated charcoal and silica gel).

Porous molecular-sieve catalyst for assembling carbide and its preparation

A meso-porous molecular sieve catalyst with carbide features that the carbide particles are assembled in the pores of meso-porous molecular sieve, resulting in high isolation and dispersion of active component particles and in turn high stability and activity.
Owner:BEIJING UNIV OF CHEM TECH

Composite molecular sieve and hydrodesulfurization catalyst prepared with composite molecular sieve as carrier

The invention provides a composite molecular sieve and a hydrodesulfurization catalyst prepared with the composite molecular sieve as a carrier. According to the composite molecular sieve and the hydrodesulfurization catalyst, the Beta-FDU-12 composite molecular sieve is of a bimodal porous structure, namely a Beta micropore and an FDU-12 mesoporous, the superficial area of the composite molecular sieve is 800-1000m<2>.g<-1>, the pore diameter is 14-25 nm, and the pore volume is 0.4-0.9 cm<3>.g<-1>.The hydrodesulfurization catalyst prepared with the Beta-FDU-12 composite molecular sieve as the carrier is outstanding in performance, the yield of FCC diesel oil can be higher than 99%, the denitrification percent can be higher than 98%, and the sulphur content is lower than 10 ppm.
Owner:CHINA UNIV OF PETROLEUM (BEIJING)

Process for manufacturing lubricating base oil with high monocycloparaffins and low multicycloparaffins

A process for manufacturing a lubricating base oil by: a) performing Fischer-Tropsch synthesis on syngas to provide a product stream; b) isolating from said product stream a substantially paraffinic wax feed having less than about 30 ppm total nitrogen and sulfur, and less than about 1 wt % oxygen; c) dewaxing said feed by hydroisomerization dewaxing using a shape selective intermediate pore size molecular sieve comprising a noble metal hydrogenation component, wherein the hydroisomerization temperature is between about 600° F. (315° C.) and about 750° F. (399° C.), to produce an is dimerized oil; and d) hydrofinishing said isomerized oil to produce a lubricating base oil having specific desired properties.
Owner:CHEVROU USA INC

Ultrastable Y-type RE molecular sieve active component and its prepn process

InactiveCN1506161AReasonable matching activityIncreased hydrogen transfer activityMolecular sieve catalystsMolecular sieveActive component
The active component of ultrastable Y-type RE molecular sieve is composite modified Y-zeolite containing RE oxide 8-25 wt%, P 0.1-3.0 wt% and sodium oxide 0.3-2.5 wt%, and with degree of crystallization 30-55 % and unit cell parameter 2.455-2.477 nm. It is prepared with Y-zeolite as material and through the steps of exchange with RE and the first roasting to obtain RE-Na Y-zeolite; reaction with RE, reaction with P-containing compound, and the second roasting. The ultrastable Y-type RE molecular sieve is used as the active component of cracking catalyst and has the obvious effect of lowering olefin content in gasoline and the features of resulting in moderate coke yield and high diesel oil yield. The preparation process is simple and high in the utilization of the modifying elements.
Owner:PETROCHINA CO LTD

Cracking catalyst for petroleum hydrocarbon, and preparation method

ActiveCN1727442AAvoid separate preparationShort processCatalytic crackingMolecular sieveGasoline
A cracking catalyst for petroleum hydrocarbon is proportionally prepared from clay, aluminum oxide prepared from alpha-AlO(OH), Y-type molecular sieve containing RE and P and silicon oxide. Its advantages are strong power to convert heavy oil and high output rate of diesel oil.
Owner:CHINA PETROLEUM & CHEM CORP +1

Isoreticular metal-organic frameworks, process for forming the same, and systematic design of pore size and functionality therein, with application for gas storage

The ability to design and construct solid-state materials with pre-determined structures is a grand challenge in chemistry. An inventive strategy based on reticulating metal ions and organic carboxylate links into extended networks has been advanced to a point that has allowed the design of porous structures in which pore size and functionality can be varied systematically. MOF-5, a prototype of a new class of porous materials and one that is constructed from octahedral Zn—O—C clusters and benzene links, was used to demonstrate that its 3-D porous system can be functionalized with the organic groups, —Br, —NH2, —OC3H7, —OC5H11, —H4C2, and —H4C4, and its pore size expanded with the long molecular struts biphenyl, tetrahydropyrene, pyrene, and terphenyl. The ability to direct the formation of the octahedral clusters in the presence of a desired carboxylate link is an essential feature of this strategy, which resulted in the design of an isoreticular (having the same framework topology) series of sixteen well-defined materials whose crystals have open space representing up to 91.1% of the crystal volume, and homogeneous periodic pores that can be incrementally varied from 3.8 to 28.8 angstroms. Unlike the unpredictable nature of zeolite and other molecular sieve syntheses, the deliberate control exercised at the molecular level in the design of these crystals is expected to have tremendous implications on materials properties and future technologies. Indeed, data indicate that members of this series represent the first monocrystalline mesoporous organic / inorganic frameworks, and exhibit the highest capacity for methane storage (155 cm3 / cm3 at 36 atm) and the lowest densities (0.41 to 0.21 g / cm3) attained to date for any crystalline material at room temperature.
Owner:RGT UNIV OF MICHIGAN

Hydrocracking catalyst and preparation method thereof

The invention discloses a hydrocracking catalyst and a preparation method thereof. The catalyst comprises hydrogenation active metals and a carrier containing modified Y molecular sieve, alumina and amorphous aluminium silicon, wherein, the Y molecular sieve is prepared by the following method: the Y molecular sieve undergone hydro-thermal treatment by mixed water solution of aluminium salt and acid is adopted; the performance of the Y molecular sieve is as follows: specific surface is 800m<2> / g-900m<2> / g, total aperture volume is 0.40ml / g-0.50ml / g, relative crystallinity is 90%-130%, cell parameter is 2.434-2.440nm, aluminium silicon mol ratio is 20-100, infrared acid volume is 0.3-0.8mmol / g, the mol ratio of acid B and acid L is above 7.0, sodium oxide content is less than or equal to 0.05wt%. The catalyst prepared by the invention has the advantages of high catalytic activity, good target product selectivity and can produce heavy naphtha, aviation fuel and diesel fuel, and the like, with high yield and good quality.
Owner:CHINA PETROLEUM & CHEM CORP +1

Method for preparing aromatic hydrocarbons and propylene simultaneously employing methanol/dimethyl ether

The invention discloses a method for preparing aromatic hydrocarbons and propylene simultaneously employing methanol / dimethyl ether, comprising the following steps: 1) placing raw materials containing methanol or / and dimethyl ether, metals and molecular sieve based catalyst which is modified through silanizing in a first fixed bed reactor to perform catalytic reaction; 2) separating the products obtained in step 1) to obtain propylene, then placing propylene in a second fixed bed reactor with molecular sieve based catalyst which is modified by using metals to react, then performing aromatization on the obtained product in step 1) and obtaining aromatic hydrocarbons; then separating to obtain toluene and sending toluene back to the outlet of the first fixed bed reactor as a raw material. In the method, methanol is converted and prepared to aromatic hydrocarbons while propylene is produced at the same time and the content of paraxylene in aromatic hydrocarbons is high. In the products prepared by the method, the content of propylene can reach above 20%, the content of aromatic hydrocarbons can reach above 58wt% and the content of paraxylene in aromatic hydrocarbons is more than 35wt%.
Owner:CHINA NAT OFFSHORE OIL CORP +2

Preparation method of ZSM-type molecular sieve without binding agent

The present invention relates to preparation process of adhesive-free ZSM type molecular sieve, and aims at solving the problem of adding adhesive causing decrease in effective surface area and limited diffusion. Technologically, the present invention is that adhesive silica in 5-50 wt% and ZSM type molecular sieve powder are made to form mixture, and the mixture is hydrothermally converted inside water solution or steam containing organic amine halide and alkyl diamine into integrated ZSM type molecular sieve. The process of the present invention may be used in the industrial preparation of ZSM type molecular sieve catalyst.
Owner:CHINA PETROLEUM & CHEM CORP +1

Hydrocracking catalyst for moderate oil and preparation thereof

The invention discloses a high-activity and high and medium oil type hydrocracking catalyst and a preparation method thereof. The catalyst comprises hydrogenation active metals and a carrier containing modified Y molecular sieves, amorphous silicon aluminum and alumina, wherein the modified Y molecular sieves have high crystallinity, large silicon aluminum ratio and proper total acid amount and acid distribution, and are obtained by treating Y molecular sieves after hydro-thermal treatment by a mixed aqueous solution of aluminum salts and an acid. The hydrocracking catalyst has high activity and good intermediate distillate oil selectivity and product quality, and is particularly suitable for hydrocracking technology for producing intermediate distillate oil.
Owner:CHINA PETROLEUM & CHEM CORP +1

Catalyst propane using aluminium oxide modified mesonore molecular sieve as carrier for dehydrogenation producing propylene

InactiveCN101125298AHigh propane conversionGood dehydrogenation stabilityMolecular sieve catalystsHydrocarbonsMolecular sievePlatinum
The invention relates to a catalyst to make the propene by dehydrogenation propane which takes the modifying alumina medium molecular sieve as the carrier. The catalyst takes the modifying medium molecular sieve by the Al2O3 as the carrier; the platinum and tin double metal catalyst has an alumina weight proportion of 5.0 to 30.0 percent. The active component of the catalyst is the platinum; the weight proportion of the platinum is 0.4 percent; and the weight proportion of the accessory ingredient Sn is 0.1 to 2.0 percent.
Owner:NANJING UNIV

Modified molecular sieve capable of improving coking performance

The invention relates to a modified molecular sieve capable of improving coking performance. The modified molecular sieve is prepared from a NaY type molecular sieve by the twice-crosslinking twice-roasting preparation method. According to the weight ratio, in the modified molecular sieve, the content of RE2O3 is 0.05 to 4 percent, the content of P is 0.05 to 5.0 percent; and the crystal cell of the modified molecular sieve is 2.430 to 2.440nm, and the crystallinity is between 35 and 55 percent. The modified molecular sieve has bigger hole volume of medium-and-large-sized holes and good stability; under the same condition of preparation process for catalyst, compared with the comparison molecular sieve, the modified molecular sieve has the advantages of reducing coke yield of the catalyst, simultaneously further improving the heavy oil cracking capability, further improving total liquid yield, and particularly facilitating the improvement of the yield of light oil.
Owner:PETROCHINA CO LTD

Process for the removal of nitrogen compounds from a fluid stream

At lower temperatures an acidic molecular sieve adsorbent preferentially adsorbs water and basic organic nitrogen compounds over weakly basic organic nitrogen compounds such as nitrites. Elevated temperatures improve the capacity of acidic molecular sieve adsorbents to adsorb nitrites in the presence of water.
Owner:UOP LLC

Preparation of hydrogenation catalyst

The invention discloses a preparation method of a hydrogenation catalyst. The final catalyst is prepared by impregnation method or coprecipitation method using a carrier material containing molecular sieve and amorphous silica-alumina. The carrier material is prepared by introducing molecular sieve slurry in the process of forming amorphous silica-alumina gel, which improves the distribution of molecular sieve in the silica-alumina carrier, improves the coordinated catalytic effect of the two carrier materials, and greatly improves the performance of the catalyst. The catalyst prepared by the method of the present invention can be used in various hydrogenation processes.
Owner:CHINA PETROLEUM & CHEM CORP +1

Hydrogenating and pour point depressing catalyst and its preparing method

The invention discloses a hydro dewaxing catalyst and the preparation method. In the method, compound with hydrogen active component is mixed with aluminum dry gel to prepare adhesive; and then the adhesive is mixed with shape-selective cracked zeolite and is pinched in shape; after drying and roasting, catalyst carrier is yielded; then the catalyst carrier is impregnated in the impregnating solution containing the rest active component and promoter; and after drying and roasting again, the catalyst of the invention is yielded. The invention is capable of taking full advantage of the alumina used as adhesive in the catalyst carrier under low hydrogen active component content conditions to prepare adhesive containing all the molybdenum and tungsten and part of the nickel, thereby keeping a certain amount of nickel oxide in the zeolite. The rest of the active metal component is distributed in the alumina, keeping the zeolite passage unobstructed with good hydro dewaxing effect and effectively improving the hydrogen addition and purification performance of the catalyst. The catalyst is especially suitable for hydro dewaxing of raw material containing wax and with high nitrogen impurity content and suitable for hydrogen addition and purification.
Owner:CHINA PETROLEUM & CHEM CORP +1

Method for recovering rare earth from rare earth-containing aluminum-silicon materials

The invention relates to a method for recovering rare earth from rare earth-containing aluminum-silicon materials, which comprises the following steps: taking the rare earth-containing aluminum-silicon materials including rare earth-loaded molecular sieves, catalyst wastes, and the like as raw materials, conducting prioritized selective leaching by acid so as to lead the majority of the rare earth and a small amount of aluminum to be dissolved and separated from silicon and other impurities, leading the rare earth to form precipitates and be separated from the aluminum by adopting a double salt precipitation or oxalate precipitation method, and then recovering and purifying the rare earth. The method has the advantages of directly realizing the extraction of the rare earth from the aluminum-silicon materials including the molecular sieves and the like, with over 98% purity of the obtained rare earth, and avoiding impurities such as aluminum, silicon and the like entering the rare earth; and meanwhile, the technology also has the characteristics of little fixed investment, low production cost and easiness for realizing industrialized production.
Owner:GRIREM ADVANCED MATERIALS CO LTD

Isomerization/dehazing process for base oils from Fischer-Tropsch wax

A method for producing lubricant base oils is provided comprising the steps of: (a) separating a feedstock into a light lubricant base oil fraction and a heavy fraction; (b) hydroisomerizing the fractions over a medium pore size molecular sieve catalyst under hydroisomerization conditions to produce an isomerized light lubricant base oil fraction having a pour point less than or equal to a target pour point of the lubricant base oils and an isomerized heavy fraction having a pour point of equal to or greater than the target pour point of the lubricant base oils and a cloud point greater than the target cloud point of the lubricant base oils; and (c) dehazing the isomerized heavy fraction to provide a heavy lubricant base oil having a pour point less than or equal to the target pour point of the lubricant base oils and a cloud point less than or equal to the target cloud point of the lubricant base oils.
Owner:CHEVROU USA INC
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