370 results about "Weight space" patented technology

The invention relates to a method for preparing olefin by conversion of methanol by using Zn-SAPO-34 molecular sieve and bonding agent as the catalyst for alkene production through methanol converstion, and employing a reaction temperature of 300-500 deg. C, a reaction pressure of atmospheric pressure, methanol weight space velocity of 1.0-10hr-1, the prepared low carbon alkene can be used in the industrial production of alkene from methanol.

The invention relates to a method for preparing alcohols by selectively hydrogenating aldehydes, belonging to hydrogenation technologies. In order to meet the requirements of people on two aspects, i.e. the improving of the selectivity on preparing the alcohols by hydrogenating the aldehydes and the prolonging of the service life of a catalyst currently, the method proposes that: the aldehydes are taken as raw materials; the reaction temperature is 20-300 DEG C; the reaction pressure is 0.1-7.0 MPa; the weight space velocity of the aldehydes is 0.02-20 h<-1>; the aldehydes and hydrogen gas are in contact with a hydrogenation catalyst; and the aldehydes are produced into corresponding alcohols through selectively hydrogenating. In the method, the hydrogenation catalyst comprises a carrier, a metal active component and silane groups; the silane groups are grafted through a silylanizing treatment; and the content of the silane groups in the total weight of the catalyst is 0.05 wt% to 25 wt%. Compared with the existing method, with the adoption of the catalyst in the method provided by the invention, the selectivity is high, the amount of byproducts, such as ethers, esters and acetals is greatly lowered; and meanwhile, the generation amount of carbon deposit is little, so that the catalyst has longer service life.

The invention relates to a method for improving reaction selectivity of isomerization of double bonds of butylene. The method mainly solves the problem of poor reaction selectivity in the prior art. Through a technical proposal that butylenes-1, butylenes-2 or a mixture which contains the butylenes-1 and butylenes-2 and does not meet a thermodynamic equilibrium value is used as a raw material; carbon-predeposited aluminosilicate is used as a catalyst, wherein the amount of predeposited carbon is 0.01 to 5 percent counted by the weight of the catalyst; and under the conditions of reaction temperature of between 50 and 480 DEG C, reaction pressure of between -0.08 and 10MPa and weight space velocity of between 0.1 and 100 hours<-1>, the raw material and the catalyst contact and have the isomerization reaction of the double bonds of the butylene to generate an effluent substance with the molar ratio of butylenes-1 to butylenes-2 close to the thermodynamic equilibrium value, and the method well solves the problems and can be applied to industrial production of isomerization of double bonds of butylene.

The invention provides an inverse-kinematics universal solving method of a robot with multi-degree of freedom. The common space theory is used for setting a universal kinematical equation of an nR robot, the weighted space vector projection method is used for analyzing the relationship between space vector projection values and revolute joint angles of a space robot, projection weighted values of joint vectors on robot tail end vectors are used as the basis for regulating the tail end pose of the robot, and projection weighted values of joint vectors are determined to achieve half-analytic solution of the inverse kinematics. The method achieves kinematical salvation of the nR robot and also finishes the space obstacle avoidance task. The method can be widely applied to series type space nR robots, has the advantages of being high in calculation speed and high in solving precision, provides control input parameters for series type robots, and meets the requirement for robot kinematics solving operation on industrial sites.

The invention relates to a method for preparing light olefins through the fluid catalytic cracking of naphtha and mainly solves the technical problems of the existing catalytic cracking method such as low conversation rate of naphtha and low yields of ethylene and propylene. The method uses naphtha and water as raw materials and comprises the following step: contacting the raw materials and a catalyst under the conditions that the temperature is 600-750 DEG C, the weight space velocity is 0.1-2.0h<-1> and the weight ratio of water to oil is 0.2-8.0:1, to react and obtain ethylene and propylene, wherein the catalyst comprises the following components by weight percent: 15.0-60.0% of kaolin, 10.0-30.0% of at least one of silicon oxide and aluminum oxide, 0.5-15% of at least one of phosphorus and rare earth oxide or alkaline earth metal oxide and 25.0-70.0% of 200-1000nm of ZSM-5 zeolite. The technical scheme in the invention better solves the problems and can be used in the catalytic cracking industrial production for preparing ethylene and propylene.

The invention relates to a method for producing glycol, which mainly solves the problem that catalysts in the prior art are poor in stability and short in regeneration period. By adopting a technical proposal of taking oxalate as raw material, taking polar or nonpolar solvent as thinner and allowing the raw material to be in contact with and react with a copper-bearing catalyst so as to form glycol-containing effluent at a temperature between 120 and 300 DEG C, at a weight space velocity between 0.01 and 10 hours, with the hydrogen/ester molar ratio of 5-300:1, under the reaction pressure between 0.1 and 10.0 MPa, under the condition that the mass fraction of the oxalate is between 0.1 and 100 percent, the method solves the problem well, and can be used in the industrial production of glycol.

The invention relates to a catalyst for preparing propylene from methanol and a method for preparing the same, which mainly solve the problems that in the prior art, the objective product propylene has low yield and the ratio of P/E (mass ratio of the propylene to ethylene) is low. The method adopts a technical proposal in which small-grain high silicon ZSM-5 zeolite synthesized in an extremely-dense system is used, and an inorganic acid selected from nitric acid, hydrochloric acid, phosphoric acid or sulfuric acid is adopted for exchange and calcination to prepare obtain the required catalyst, and the technical proposal better solves the problems. The obtained catalyst has partial pressure of 50 kPa in the methanol and reaction temperature of 470 DEG C; under the condition that the weight space velocity of the methanol is 1, the yield of the propylene reaches 42 weight percent, and the weight ratio of the propylene to the ethylene reaches more than 8, thus the catalyst can be used in the industrial production of preparing the propylene from the methanol.

The present invention discloses a method of adaptive weighting space-time transmit diversity, comprising: symbols to be transmitted at a transmitting end being output after being space-time encoded according to certain regulation, and the current transmission powers of the two antennae being real-timely adjusted according to the given transmission power weight values; after the transmission powers are determined, the space-time encoded output signals being sent out at two independent antennas by transmitting antenna array in terms of the current transmission power; the fading characters of two wireless channels being estimated by the receiver at a receiving end according to the present received signals and then fed back to the transmitting end; the transmitting end receiving and obtaining the fading amplitude characters of two wireless channels through feedback channel, calculating new adaptive weight values of transmission powers, and adjusting transmission powers according to these weight values. The present invention also discloses a system for implementing the above method of adaptive weighting Space-time Transmit Diversity. In term of the method and structure, the transmission powers can be dynamically adjusted in adaptive weighting manner, in order to boost system performance gain.

The invention relates to a reaction method for transferring high selectivity alkyl aromatic hydrocarbon and increasing the yield of xylene through dealkylation. The invention mainly solves the problems that the reaction product has high content of by-product of phenylethane, thereby causing that the xylene of compound C6 product has low selectivity, and has no selection to the dealkylation of lateral chain alkyl aromatic hydrocarbon in the prior art. The invention has the technical proposal that the catalyst is made of 40 to 90 proportions of hydrogen zeolite with the SiO2AL2O3 mole ratio of 12 to 70, 10 to 60 proportions of adhesive agent, oxide which is selected from at least one of molybdenum, palladium or nickel, zeolite which is selected from at least one of iron, bismuth, stannum ormolybdenum and oxide which is selected from at least one of lanthanum, cerium, magnesium or titanuium; the xylene product is generated through a catalytic reaction at the weight space velocity of 1.0to 3.5 hours<-1>, the reaction temperature of 350 to 460 DEG C, the reaction pressure of 1.5 to 3.5 MPa and the hydrogen-hydrocarbon molecule rate of 2.0 to 8.0. The invention preferably solves the technical problems mentioned above, and the invention can be applied to the industrial production of transferring C9 and more than C9 heavy aromatic hydrocarbon and toluol alkyl and the dealkylation reaction.

The present invention adopts benzene and C9 and higher aromatic hydrocarbons as raw material for reaction, in the fixed bed reactor and under the condition of hydrogenation uses the composition formed from zeolite in which the silicon-aluminium ratio is 3-500 and alumina as catalyst, on the zeolite metal molybdenum or/and its oxide and non-forced-added at least one metal selected from Fe, Co, Ni,Cr, W, Bi, La, Zr and Ag or/and oxide are loaded, under the conditions of that reaction temp. is 300-600 deg.C, pressure is 1.0-6.0 MPa, hydrogen and hydrocarbon mole ratio of 1-15 and weight space velocity WHSV is 0.5-5.0 hr.(-1) makes the above-mentioned materials produce reaction to produce methylbenzene and C8 aromatics.

The invention relates to a method for preparing propylene through C4 disproportionation and mainly solves the problems of the past technologies such as the consumption of ethylene and low catalyst activity. In the technical scheme in the method, C4 is used as the raw material and the method comprises the following step: under the conditions that the reaction temperature is 300-520 DEG C, the reaction pressure is 0-2MPa and the weight space velocity is 1-10h<-1>, the raw material passes through a catalyst bed to generate propylene. The catalyst used in the method comprises the following components in parts by weight: 4-30 parts of at least one of tungsten oxide, molybdenum oxide and rhenium oxide and 70-96 parts of SiO2 carrier. By adopting the technical scheme, the problems can be better solved and the method can be used in the propylene industrial production adopting C4 disproportionation.

The invention relates to a method for producing ethylbenzene by performing vapor phase alkylation on ethanol and benzene and mainly solves the problem of low ethylbenzene selectivity in the prior art. The problem is solved by adopting the technical scheme that ethanol and benzene which are used as reaction raw materials and a catalyst contact under the conditions that the reaction temperature is 300 to 460 DEG C, the reaction pressure is 0.5 to 2.8MPa, the weight space velocity of ethanol is 0.1 to 5.0 hours<-1>, and the molar ratio of benzene to ethanol is 2 to 10 to perform vapor phase alkylation reaction so as to generate ethylbenzene; the used catalyst contains the following components in percentage by weight: 90 to 99.9 percent of adhesive-free ZSM-5 molecular sieve of which the silicon-to-aluminum (SiO2/Al2O3) molar ratio is 30 to 400 and the grain diameter is 5 to 350 nanometers, and 0.1 to 10 percent of rare-earth metallic oxide. The method can be used for industrial production of preparing ethylbenzene by performing vapor phase alkylation on ethanol and benzene.

The invention relates to a method for preparing ethylene propylene by light oil through catalytic cracking, which mainly solves the problems of low catalyst activity, low ethylene propylene yield and high reaction temperature of the current ethylene propylene preparing technique by catalytic cracking. The invention properly solves the problems by adopting the technical proposals that: a ZSM-5/mordenite/analcime intergrown molecular sieve, a ZSM-5/mordenite/zeolite beta intergrown molecular sieve, a ZSM-5/mordenite/zeolite Y intergrown molecular sieve, a ZSM-5/mordenite/MCM-22intergrown molecular sieve or a mixture thereof serves as a catalyst, the light oil with the compositions of C4 to C10 hydrocarbon is adopted as a raw material, and the material is in contact reaction with a catalyst under the conditions of a reaction temperature of between 600 and 700 DEG C, a reaction pressure of between 0.001 and 0.5MPa, a reaction weight space velocity of between 0.1 and 4/h, and water/light oil being present in a weight ratio of 0.5-6: 1, and the method of preparation can be used for the industrial production of preparing the ethylene propylene by the light oil through catalytic cracking.

The invention discloses a brain tumor image segmentation method based on depth learning and weight space integration, comprising the following steps: S1, acquiring a multimodal MRI image of the braintumor, and preprocessing the acquired multimodal MRI image; S2, constructing a first network model and a second network model; S3, inputting the preprocessed multimodal MRI image into the second network model, passing through the weight space, and updating the average weight; training it and storing the average value of weights into the first network model; S4, inputting the multimodal MRI image to be tested into the first network model, and outputting the segmentation result of the brain tumor image. The segmentation method of the invention is conducive to improving the accuracy and reliability of the brain tumor segmentation result, and the parallel network can obtain the positioning information while segmenting the lesion, and meanwhile, the method integrates the weight space collection, thereby improving the efficiency and the accuracy of the brain tumor segmentation.

The invention relates to a control method of a light-type direct-current transmission system converter of an offshore wind power station, belonging to the technical field of power transmission. In the invention, a PID (Piping and Instruments Diagram) neural network controller is designed based on a particle group optimizing method, the traditional PI (Piping and Instruments) regulator is substituted, step input is used to train a neural network, that is to say, multi-group particles are set to search in the neural network weight space of searching, and the position and speed of the particles are continuously updated according to an adaptive value function of the neural network to obtain the optimum weight of the neural network. The invention adopts the method of using the optimum weight value obtained by training in combination with the error forward broadcast of the neural network to substitute the traditional PI regulator to control the operation of the system, thereby reducing the parameter to be regulated and improving the transient response performance of the system; the neural network weight value is obtained by training a nonlinear model of a controlled system so as to approach to a true system. Only the forward broadcast process of the PID neural network is controlled in the operation process of the system. The method is relatively simple and is easy to achieve.

This invention relates to a method of lighting heavy aromatic hydrocarbon and alkyl transfer. Mainly to solve existing technologies problems, such as low conversion rate and needing precious metal when use solo pure zeolite molecular sieve catalyst, and raw materials and components demanding. This invention takes carbon 9 and above aromatic hydrocarbon as raw material, in the fixed-bed reactor, use symbiotic molecular sieve that contains 10 ~ 80% (weight) of beta zeolite and Mordenite, and 20 ~ 90% (weight) inorganic binder composition of the catalyst that at least one selected from the gamma-Al2O3, thin diaspore, silica, silicon oxide, alumina oxide, bentonite, kaolin, diatomite or montmorillonite. Take reaction under the conditions of the reaction temperature 300 to 500 deg, pressure of 1.0 to 3.5MPa, raw materials weight space velocity of 1.5 ~ 6 .0 per hour, hydrogen and hydrocarbon molar ratio of 2.0 to 6.0 to obtain product containing benzene, toluene and xylene.

The invention relates to a method for preparing ethylene and propylene through catalytic cracking, mainly solving the problems of the prior catalyst used for preparing ethylene and propylene through catalytic cracking of high service temperature and low yields of ethylene and propylene. Through taking naphtha the compositions of which are C4 to C10 hydrocarbons as raw material, catalytic cracking reaction of the raw material is carried out through a catalyst bed so as to generate ethylene and propylene at a temperature of between 550 and 700 DEG C, under the pressure of between 0.001 and 0.5MPa, at the weight space velocity of between 0.1 and 4 hour<-1> and in the water/naphtha weight ratio of between 0.5 and 4 to 1, wherein the catalyst is at least two of rare earth elements, VA group elements, IIIA group elements, IB group elements or IIB group elements, IA group elements or IIA group elements loaded on ZSM-5/mordenite intergrowth molecular sieve, ZSM-5/Beta zeolite intergrowth molecular sieve or ZSM-5/Y zeolite intergrowth molecular sieve; and the technical proposal solves the problems better, and can be used in the industrial production for preparing ethylene and propylene through catalytic cracking of naphtha.

The invention relates to a method for preparing glycol from oxalate, which mainly solves the problems of easy catalyst deactivation and low selectivity of glycol serving as a target product caused by large temperature difference in a reactor in the prior art. The technical scheme of the invention is that: oxalate and hydrogen are used as raw materials, a molar ratio of the hydrogen to the oxalateis 40-200:1, fatty alcohol having 1 to 4 carbon atoms is used as a solvent, the weight ratio of the solvent to the oxalate in the raw materials is 0-0.9:1, and at least one of the oxalate, hydrogen, solvent and water is used as a cooling medium; and the cooling medium passes through a tube nest in a shell and tube fixed bed reactor at the temperature of 160 and 280 DEG C, under the pressure of between 1.0 and 6.0 MPa and under the conditions that the weight space velocity is between 0.1 and 10 hours<-1> on the basis of the weight of a mixture of the oxalate and the solvent and the molar ratioof the hydrogen to the oxalate is 40-200:1, a catalyst bed is positioned outside the tube nest, and after entering the reactor, the mixture of the raw materials and the solvent contacts a copper-containing catalyst outside the tube nest for reacting to form the glycol, wherein the flow direction of the cooling medium is the same or opposite to that of the mixture of the raw materials and the solvent, and the oxalate accounts for more than or equal to 10 weight percent of the mixture. By adopting the technical scheme, the problems are solved better. The method can be used for the industrial production of the glycol.

The invention provides a gasoline desulfurization catalyst, a preparation method of the gasoline desulfurization catalyst, and a gasoline desulfurization method. On the basis of the total weight of the gasoline desulfurization catalyst, the gasoline desulfurization catalyst comprises the following components: 10 to 30% of nickel oxide, 30 to 60% of zinc oxide, 0.1 to 5% of potassium oxide, 5 to 20% of SAPO-11 (Silicoaluminophosphate) molecular sieve and/or ZSM (Zeolite Socony Mobil) molecular sieve, and the balance of alumina. The preparation method of the gasoline desulfurization catalyst comprises the following steps of: mixing raw materials; forming; drying; and roasting for 0.5 to 4 hours at 400 to 600 DEG C, thus obtaining the gasoline desulfurization catalyst. The gasoline desulfurization method comprises the following step of: contacting sulfur-containing gasoline with the gasoline desulfurization catalyst at a critical hydrogen condition in which the weight space velocity is 2 to 8h<-1>, the temperature ranges from 350 to 500 DEG C, the pressure is 1 to 3MPa, and the molar ratio of hydrogen/sulfur-containing gasoline is 0.1 to 0.8, thus obtaining the gasoline with ultra-low sulfur content. The gasoline desulfurization catalyst provided by the invention is a catalyst with two functions, namely, proper hydrogenation activity and adsorption capacity.