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65results about How to "Good catalytic activity at low temperature" patented technology

Sliver-based bimetallic catalyst for catalyzing oxidation of volatile organic contaminant, preparation method and application thereof

The invention claims a sliver-based bimetallic catalyst, a preparation method and application thereof, wherein the catalyst takes mesoporous molecular sieves such as SBA-15, MCM-41 or MCM-48 and etc. and oxides such as aluminium oxide, silicon oxide and cerium oxide and the like as carriers; the active ingredient of the catalyst is sliver, the second ingredient is M which is any one of transition metal selected from the group consisting of Cu, Co, Ce and Mn and etc. The synthetic method of the catalyst is characterized in that the operation is simple and easy, the synergistic effects of selected different transition metals selected to the sliver type are different, taking copper as an example, when Ag: Cu is more than 1: 2 but not more than 2: 1, the catalyst presents an obvious synergistic effect between metals, and the catalytic oxidation reactivity of volatile organic contaminant (VOC) is obviously improved. Simultaneously, the sliver-based bimetallic catalyst provided by the invention has the advantages that the price of transition metal which is used is low by comparing with platinum, palladium and gold and etc., the resource of the transition metal is rich, the catalyst is suitable for mass production and industrial application and the application value and the application prospect are good.
Owner:DALIAN UNIV OF TECH

Platinum/cerium aluminum-molecular sieve catalyst for catalytic oxidation of ammonia gas and preparation method thereof

The invention provides a platinum/cerium aluminum-molecular sieve catalyst for catalytic oxidation of an ammonia gas. Cordierite ceramic is utilized as a carrier for the platinum/cerium aluminum-molecular sieve catalyst, the surface of the carrier is coated with a catalyst layer, and the catalytic active site of the catalyst layer consists of a noble metal platinum, a cerium-aluminum composite oxide and a neodymium-modified molecular sieve; the mass ratio of the cerium-aluminum composite oxide to the neodymium-modified molecular sieve to the noble metal platinum is (20-80):(20-80):(0.01-0.1), and the mass ratio of cerium oxide and aluminum oxide in the cerium-aluminum composite oxide is (1-3):(1-5); the mass ratio of neodymium oxide and a molecular sieve in the neodymium-modified molecular sieve is (1-10):(90-100). The platinum/cerium aluminum-molecular sieve catalyst is also capable of achieving wide low-temperature activity window, good catalytic activity and high selectivity even at a high space velocity (SV), and is capable of effectively restraining generation of secondary pollutants of N2O, NO and NO2. The invention further provides a preparation method of the platinum/cerium aluminum-molecular sieve catalyst.
Owner:SINOCAT ENVIRONMENTAL TECH

Method for removing NOx in sintering flue gas through low-temperature SCR (Selective Catalytic Reduction) catalyst

InactiveCN105561781ASolve the purchaseSolve a series of problems such as transportation and warehousingGas treatmentDispersed particle separationWater vaporSorbent
The invention discloses a method for removing NOx in sintering flue gas through a low-temperature SCR (Selective Catalytic Reduction) catalyst based on a metallurgy coke nut adsorbent. The method comprises the following steps: (1) smashing and sieving defective coke to obtain metallurgy coke nut; (2) cleaning the metallurgy coke nut with clear water, draining, and placing the drained metallurgy coke nut into a drying oven of which the temperature is 120 DEG C to perform constant-temperature drying for 2 hours; (3) performing high-temperature water vapor activation on the dried metallurgy coke nut; (4) selecting V2O5 to serve as an active component of the low-temperature SCR catalyst, selecting an ammonium metavanadate solution to serve as a precursor of V2O5, and soaking the metallurgy coke nut into a solution of which the V2O5 concentration is 6 percent and a solution of which the V2O5 concentration is 10 percent respectively for 16 hours through a soaking process to obtain a metallurgy coke nut low-temperature SCR de-nitration catalyst; (5) taking out a sample, placing the sample into an air blast drying box to dry for 3 hours, then placing the sample into a resistance furnace, and calcining in a nitrogen atmosphere at the temperature of 600 DEG C for 2 hours in order that the ammonium metavanadate is fully decomposed to obtain a V2O5-loaded modified metallurgy coke nut catalyst.
Owner:CHONGQING UNIV

Method for preparing SCO denitration catalyst by virtue of plasma method

The invention discloses a method for preparing an SCO denitration catalyst by virtue of a plasma method. The method comprises the following steps: (1) sieving brown coal particles by virtue of a sieve, and roasting the brown coal particles in a tubular furnace, so as to obtain pyrolysis coke; (2) dipping the pyrolysis coke into a manganese nitrate solution by virtue of an equivalent-volume impregnation method, so as to obtain pyrolysis coke dipped with manganese nitrate; (3) dipping the pyrolysis coke dipped with manganese nitrate into a cobalt nitrate solution by virtue of the equivalent-volume impregnation method, so as to obtain pyrolysis coke dipped with manganese nitrate and cobalt nitrate; and (4) frying the pyrolysis coke dipped with manganese nitrate and cobalt nitrate by virtue of an electric furnace, putting the pyrolysis coke into a plasma reaction kettle, and carrying out low-temperature plasma roasting, so as to obtain the SCO denitration catalyst. By improving existing preparation methods of denitration catalysts, the catalyst is subjected to pyrolysis coke surface modification by utilizing a plasma method and changing background gas, so that the ratio of a surface pore structure of the catalyst is increased, and the catalytic performance of the SCO denitration catalyst is improved.
Owner:XIAN UNIV OF SCI & TECH

Preparation method and application of copper-cobalt composite oxide catalyst

InactiveCN110975870ALow costGood catalytic combustion activity of toluene volatile organic compoundsGas treatmentDispersed particle separationOXALIC ACID DIHYDRATEVolatile organic compound
The invention discloses a preparation method and application of a copper-cobalt composite oxide catalyst, belonging to the technical field of preparation of composite catalysts. The preparation methodcomprises the following steps: mixing and grinding a copper salt, a cobalt salt and a complexing agent to form a dry material; and roasting the dry material under the roasting condition that a temperature is raised to 300-550 DEG C at a heating rate of 10 DEG C/min, then performing roasting for 1-2 hours at a constant temperature of 300-550 DEG C, and taking out the dry material after the temperature drops to a normal temperature after roasting is finished so as to obtain the catalyst, wherein a molar ratio of the copper salt to the cobalt salt to the complexing agent is 1: 2: (0-5), and thecomplexing agent is oxalic acid. The copper-cobalt composite oxide catalyst prepared by the method disclosed by the invention shows good activity in catalytic combustion of toluene volatile organic compounds at low temperature. According to the method, the copper-cobalt composite oxide catalyst is prepared through a grinding method, so preparation process is simple, conditions are mild and are easy to control, safety and environmental protection are achieved, repeatability is good, and great industrial application value is achieved.
Owner:CHONGQING TECH & BUSINESS UNIV

Liquid-phase CO2 methanation catalyst, preparation method and application of catalyst

The invention relates to a liquid-phase CO2 methanation catalyst, a preparation method and application of the catalyst. The liquid-phase CO2 methanation catalyst comprises amphipathic ionic liquid and metal active components dispersed in the amphipathic ionic liquid in the state of stable colloid, the grain sizes of the metal active components range from 0.5nm to 20nm, the spherical metal active components include a first metal active component and a second metal active component, the first metal active component includes nickel, the second metal active component includes one or mixture of more than one of lanthanum, cerium, molybdenum, ruthenium, ytterbium, rhodium, palladium, platinum, potassium and magnesium, and the molar ratio of the first metal active component to the second metal active component is 10:0.1-2. The metal active components in the liquid-phase CO2 methanation catalyst are small in grain size, narrow in distribution, wide in application prospect, easy to separate and recyclable, CO2 methanation of low-temperature liquid phase can be realized at the temperature of 100-200 DEG C, the liquid-phase CO2 methanation catalyst has excellent low-temperature catalytic activity, methane selectivity and heat stability, and the preparation method is simple and practicable, low in cost and easy in popularization.
Owner:WUHAN KAIDI ENG TECH RES INST CO LTD

Low-temperature coke oven flue gas desulfurizing and denitrifying process

The invention discloses a low-temperature coke oven flue gas desulfurizing and denitrifying process. The low-temperature coke oven flue gas desulfurizing and denitrifying process comprises the following steps: firstly, preparing an SCR catalyst, wherein the catalyst is obtained by preparing clay, polymethyl methacrylate and sodium silicate into a carrier and then loading metal oxides of manganese and cerium, and the catalyst has good catalytic activity at low temperature and a large adsorption rate; then in a desulfurizing and denitrifying step, dedusting coke oven flue gas first and then injecting the coke oven flue gas into a desulfurizing adsorption zone for desulfurizing, wherein a desulfurized product is adsorbed by the SCR catalyst, and the catalyst can be recycled after desulfurization regeneration and activation treatment; injecting the dedusted and desulfurized coke oven flue gas into an SCR reaction zone, injecting cyanuric acid and ammonia gas into the SCR reaction zone in a mixing manner, contacting with the coke oven flue gas and the SCR catalyst, denitrifying, and discharging the desulfurized and denitrified flue gas after the catalyst is recycled. The low-temperature coke oven flue gas desulfurizing and denitrifying process has high desulfurizing and denitrifying efficiency and high SCR catalyst adsorbing rate, and can be recycled, so that the cost is reduced.
Owner:DONGGUAN LIANZHOU INTPROP OPERATION MANAGEMENT CO LTD

Novel ceramic catalytic electrode and preparation method thereof

The invention discloses a novel ceramic catalytic electrode and a preparation method thereof. The novel ceramic catalytic electrode comprises a catalytic electrode ceramic matrix and precious metals arranged in the catalytic electrode ceramic matrix and on the surface of the catalytic electrode ceramic matrix, the catalytic electrode ceramic matrix is porous ceramic with tiny three-dimensional pore channels in the interior and on the surface, and the precious metals are distributed in the porous ceramic in a three-dimensional net shape. One purpose of the invention is to provide a novel ceramic catalytic electrode with low cost and high performance. The number of three-phase interfaces among precious metal, porous solid electrolyte ceramic and oxygen is greatly increased due to the structure, so that the novel ceramic catalytic electrode also has excellent catalytic capability under the condition of using a small amount of precious metal, and the production cost is greatly reduced. Another purpose of the invention is to provide a preparation method of the novel ceramic catalytic electrode, and the ceramic electrode prepared by the method is simple in process operation, good in combinability of the electrode material and the ceramic substrate, and less in precious metal consumption.
Owner:苏州工业园区传世汽车电子有限公司
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