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336results about How to "Wide concentration range" patented technology

Catalyst for hydrolyzing carbonyl sulfur and preparation method thereof

The invention discloses a catalyst for hydrolyzing active carbon-based COS under the condition of low temperature and a preparation method thereof, wherein a carrier of the catalyst is active carbon, and active compositions of the catalyst are alkali materials and metal oxide. The catalyst can remove COS in air at a low temperature (between 30 and 100 DEG C) and remove H2S generated by hydrolysis together. The preparation method comprises the following steps: firstly, using running water and distilled water to wash the active carbon, and drying the active carbon for 2 to 4 hours at a temperature of between 110 and 180 DEG C, wherein the active carbon can be coal and coconut husks; secondly, using a 1 mol/L KOH solution to boil the washed active carbon for 1.5 to 2 hours, performing modification treatment, and using distilled water to wash the solution until the pH value is approximately 6.0; thirdly, selecting one or more metallic salt solutions to soak the active carbon, performing modification treatment, and performing ultrasonic soakage for 0.5 to 1 hour, wherein the content of a soaking liquid is 10 to 90 percent of the mass ratio of the active carbon, and the volume of the soaking liquid is as follows: 20 milliliters of the soaking liquid is added into 10 grams of the catalyst; fourthly, drying the soaked active carbon for 2 to 6 hours in a 120 DEG C constant-temperature drying cabinet, and activating the catalyst for 2 to 4 hours under the protection of 300 to 600 DEG C N2; and fifthly, performing ultrasonic soakage on the activated catalyst in the fourth step in an alkali solution for 0.5 to 1 hour.
Owner:KUNMING UNIV OF SCI & TECH

Absorbent charcoal based catalyst for hydrolyzation and catalysis of carbonyl sulphur in low-temperature and preparation method thereof

The invention provides an active carbon based catalyst for hydrolyzing and catalyzing carbonyl sulfur in low temperature, which is characterized in that the catalyst takes active carbon as a carrier and is prepared by the following method: washing the active carbon, drying the active carbon for 2-4 hours under 100-140 DEG C; impregnating the active carbon in the (A) step for 6-12 hours with the impregnation liquid of alkaline substances or metal oxides or organic alcohol amine, wherein, the mass content of the alkaline substances or the metal oxides or the organic alcohol amine accounts for 5-30 percent of that of the active carbon; drying the impregnated active carbon for 2-6 hours under the constant temperature of 100-140 DEG C and then activating the active carbon for 2-4 hours under the temperature of 300-500 DEG C and the protection of N2. The catalyst can be used for catalyzing and hydrolyzing COS and removing H2S; furthermore, the catalyst can remove the COS in the gas under the temperature of 30-100 DEG C, ensure the conversion rate of the COS to be larger than 90 percent and remove the H2S generated in hydrolysis at the same time. The COS concentration which is between 100-1500ppm has a wide adaptive range, high desulfurization accuracy and higher breakthrough sulfur capacity.
Owner:KUNMING UNIV OF SCI & TECH

Dynamic preparation device for standard gas of solid-phase or liquid-phase compounds and application thereof

The invention relates to the dynamic preparation of standard gas of solid-phase or liquid-phase compounds, in particular to a dynamic preparation device for the standard gas of the solid-phase or liquid-phase compounds and application thereof. The device comprises a sample cell, a constant temperature evaporation tank, a gas flow controller, a liquid flow controller, and a diluent gas source, wherein the sample cell is connected with a sample solution inlet formed on the side wall of the constant temperature evaporation tank via the liquid flow controller through a pipeline, the wall surface of one side, which is close to the sample solution inlet, of the constant temperature evaporation tank is provided with a diluent gas inlet, and the diluent gas source is connected with the diluent gas inlet via the gas flow controller through a pipeline; and the wall surface of another side, which is opposite to the sample solution inlet, of the constant temperature evaporation tank is provided with a sampling port and a tail gas port. The method is suitable to prepare standard gas of compounds (most of the compounds are the solid-phase or liquid-phase compounds) with low saturated vapor pressure at normal temperature, and different concentrations of mixed gas of various compounds.
Owner:DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI

Waste gas treatment process and fluidized-bed bioreactor used for same

The invention provides a waste gas treatment process and a fluidized-bed bioreactor used for the same. The waste gas treatment process comprises the processes such as waste gas pressurization, waste gas reaction, waste gas separate-circulation and waste gas separate-emission; and waste gas is subjected to circular fluidization and enforced mass transfer in the reactor to be fully reacted with microorganisms at the temperature of between 15 and 40 DEG C. The provided fluidized-bed bioreactor used for the waste gas treatment process consists of a shell, a gas distributor, a guiding cylinder, a cap, a gas-liquid separator, a seal cover, and longitudinal sampling ports at different positions of the shell; and the guiding cylinder and the cap separate the inner cavity of the reactor into a lifting area, a reduction area and a separation area, so that the waste gas is circularly fluidized between the lifting area and the reduction area, and three phases, namely gas, liquid and solid, strengthen the mass transfer function. The concentration range of pollutants treated by the process and the fluidized-bed bioreactor is wide, the reaction efficiency is high, the reaction time is short, and the reactor occupies small area, and is quick to start and difficult to block.
Owner:CHINA PETROCHEMICAL CORP +1

Gas particle concentration measurement method and device on basis of broadband linear frequency modulation ultrasound

The invention discloses a gas particle concentration measurement method and a gas particle concentration measurement device on basis of broadband linear frequency modulation ultrasound. The measurement method includes the following steps: constructing a measurement signal by using a linear frequency modulation (LFM) signal, performing digital-to-analogue conversion to the measurement signal and transmitting the converted measurement signal from a transmitting ultrasonic transducer array; detecting an ultrasonic signal by a receiving ultrasonic transducer array, so as to obtain a received signal; performing analog-to-digital conversion to the received signal, and further performing spectrum estimation to the received signal, so as to obtain an attenuation spectrum of the received signal; and moreover, analyzing the obtained attenuation spectrum, determining the linearity of corresponding particles on basis of the frequency, and determining the concentration of corresponding linear particles as per the frequency spectrum amplitude on basis of a mathematical model or an empirical formula. The device for realizing the method includes an operating module, a processing module, a transmitting/receiving module, an outputting module and a measurement cavity. The method and the device, disclosed by the invention, have the advantages of wide application range, high measurement accuracy, simple device, low cost, convenience in use and the like.
Owner:SOUTH CHINA UNIV OF TECH

Optical fiber refractive index and temperature sensor and measurement method thereof

The invention discloses an optical fiber refractive index and temperature sensor and a measurement method thereof. The optical fiber refractive index and temperature sensor comprises a broadband light source (1), an optical fiber sensing head (2), a spectrometer (3) and a computer (4), wherein the broadband light source (1) is connected to a first input port of the optical fiber sensing head (2) through an optical fiber; a first output port of the optical fiber sensing head (2) is connected with the spectrometer through an optical fiber. According to the measurement method, two light beams split in a Mach-Zehnder interferometer interfere with each other, the movements of the valley value wavelength and the Bragg wavelength of an interference fringe change with the refractive index or the temperature of a material to be measured where the optical fiber sensing head is positioned, the movement ranges of the valley value wavelength and the Bragg wavelength of the interference fringe are measured through the spectrometer, and the refractive index and the temperature of the material to be measured are obtained through calculation of the computer. The optical fiber refractive index and temperature sensor is capable of measuring the refractive index and the temperature in high-precision and real-time ways at the same time and is simple in structure and convenient to operate.
Owner:SOUTH CHINA NORMAL UNIVERSITY

Self-circulation anaerobic reactor

The invention discloses a self-circulation anaerobic reactor. The self-circulation anaerobic reactor comprises a tank body, a water distributor, a sewage return pipe, a marsh gas flow guide device, an isolating inner cylinder, a three-phase separator and the like. The tank body is internally divided into several regions which are a mixing region, a main reaction region, a main marsh gas separating region, an auxiliary reaction region and a solid, liquid and gas three-phase separating region (containing a setting region) through the devices. Inner circulation is automatically formed by sewage in the regions under the raising action of marsh gas. As inner circulation is formed, rising flow speed of the main reaction region is increased, the contact area between organic matter in the main reaction region and anaerobic biological bacteria is increased, and water quality purification speed is increased. The concentration of input water is reduced by the self circulation, the concentration gradient of organic acid in a reactor is reduced, the living environment of the anaerobic biological bacteria is improved, and the degradation rate of the anaerobic biological bacteria is increased. As the self-circulation reactor is ingenious in structure, the self-circulation amount can be several times that of an existing anaerobic reactor. Output water is high and stable in quality, the requirement for designing anaerobic water output can be met without multi-level arrangement.
Owner:北京迅世达环保科技有限公司

Rod-shaped nano iron oxide electrode material, and preparation method and application thereof

The invention discloses a rod-shaped nano iron oxide electrode material, and a preparation method thereof. The preparation method comprises the steps of carrying out a hydrothermal reaction by using FeCl3.6H2O, ammonium dihydrogen phosphate and water as raw materials; and washing produced precipitate to obtain the rod-shaped nano iron oxide. The nano iron oxide is in a rod shape, with an average diameter being 60-80 nm, length being 250-300 nanometers, purity higher than 99.9% and crystal phase being alpha-Fe2O3. The rod-shaped nano iron oxide electrode material can be used as both a positive electrode active material and a negative electrode active material for a lithium ion battery. Raw materials used in the preparation method are easily available, nontoxic and pollution-free to environment. A preparation process is simple; operation is convenient; and the preparation method is suitable for large-scale production. By using the rod-shaped nano iron oxide electrode material as the positive and negative electrode active materials for the lithium ion battery, cost is low; electrochemical performance is excellent; chemical stability of the electrode material is stable; specific capacity is high; and polarization of a charge and discharge platform is small.
Owner:ADVANCED TECHNOLOGY & MATERIALS CO LTD

In-situ adsorption-microelectrolysis-catalytic oxidation sewage treatment equipment and method

The invention discloses in-situ adsorption-microelectrolysis-catalytic oxidation sewage treatment equipment and method, belonging to the technical field of sewage treatment in environment engineering. The in-situ adsorption-microelectrolysis-catalytic oxidation sewage treatment equipment is characterized in that adsorption equipment, electrolysis equipment and catalytic oxidation equipment are integrated so as to gather enable pollutants to be gathered from a low-concentration water phase onto an adsorbent; by using the favorable electric conductivity, the adsorbent is used as a complexly polarized three-dimensional electrode to form countless micro electrolytic baths, so that the organic pollutants are electrolyzed while organic matters are adsorbed, and adsorption active sites are continuously regenerated; and by utilizing an electric insulation material, the three-dimensional electrode is complexly polarized and has a high-class oxidation catalyst function at the same time, so that a gas oxidant dissolved in water and an oxidant generated by side reaction of the electrode form a high-class oxidant to efficiently remove the organic pollutants. According to the equipment and the method, the problems of slow reaction speed, low space-time efficiency, low current efficiency and low pollutant degradation efficiency in the conventional electrolytic reactors are solved, and an excellent market prospect is provided.
Owner:DALIAN UNIV OF TECH

Method for NO oxidation and nitrogen oxide removal at room temperature through synergism of plasma and catalyst

The present invention discloses a method for NO oxidation and nitrogen oxide removal at a room temperature through synergism of plasma and a catalyst. The method comprises that: a prepared catalyst is filled in a plasma reactor, and a mixing gas containing NO, O2 and N2 is introduced, such that the NO in the mixing gas is quantitively oxidized into NO2 at a room temperature through synergism of plasma and a catalyst, wherein a plasma voltage is 3.0-7.0 kV, and frequency is 8-10 kHz; and the treated gas enters an alkaline liquid absorption bottle to be absorbed, wherein a NO purification rate after absorption is up to more than 95%. According to the present invention, operation is performed at a room temperature, and heating equipment is not required, such that an operation cost is low; other gas components are not required to be added, such that an economic cost is substantially reduced, easy leakage caused by gas addition and other secondary pollution problems can be reduced; the method has characteristics of low equipment investment, low operating cost, simple process, no secondary pollution and the like; and adverse affects due to other impurity components in industrial flue gas are low, spreading use is easily performed, and high application values are provided.
Owner:KUNMING UNIV OF SCI & TECH

Reaction for preparing hydroxyacetone by selectively dewatering natural glycerol and catalyst

The invention relates to a catalyst for selective dehydration and conversion of natural glycerin into acrolein and the corresponding reaction process. The catalyst is composed of an H-ZSM-5 molecular sieve and 0.05%-7% of an active metal component, or the H-ZSM-5 molecular sieve, 5%-30% of amorphous silicon aluminum gel and 0.05%-7% of the active metal component. The usage of the catalyst of the invention can realize the conversion of the glycerin into the acrolein with high conversion rate and high selectivity under the conditions of normal pressure, reaction temperature of 200 to 400 DEG C and liquid-space velocity (LHSV) of 0.01 to 0.60h, glycerin water solution with 10 to 60 percent is taken as the reaction raw material, and the reaction is directly carried out in a fixed bed flow reactor without the steps of preheating and gasification. The conversion rate of the glycerin is 100% and the selectivity of the acrolein is 75.2mol% under the optimized conditions. The catalyst and the reaction process of the invention are significantly characterized in that: the catalyst has high strength and difficult argillization; the activity and the selectivity of the catalyst are high; the concentration of the reaction raw material liquid and the range of the reaction liquid-space velocity are wide, the reaction temperature is lower, and the reaction process route is simple.
Owner:HUNAN UNIV

Carbon-based catalyst desulfurization and denitrification system and method

The invention provides a carbon-based catalyst desulfurization and denitrification system and method. The carbon-based catalyst desulfurization and denitrification system comprises a fume system (A), a desulfuration adsorption system (B), a denitrification adsorption system (C), a carbon-based catalyst conveyer system (E), a nitrogen system (F), an ammonia gasification dilution system (G), a cooling water system (I), a carbon-based catalyst regeneration system (D) and an air heating system (H), wherein all the systems are connected through a pipeline. Boiler fume enters a chimney to be discharged after reaching the standard by being processed through the carbon-based catalyst desulfurization and denitrification system, the adsorbed carbon-based catalyst is heated, desorbed and regenerated and then returns to an adsorption tower, and high-concentration SO2 obtained through desorption is used for resource recovery. According to the system, SO2 and NOx are removed through two-stage movement adsorption, adaptability to the fume condition characterized in high sulfur content, variable sulfur content and large fume amount change is high, and the foundation can be laid for large-scale application and popularization of the carbon-based catalyst fume purification technique in the thermal power industry.
Owner:GUODIAN SCI & TECH RES INST

Castanea henryi high-yielding regulator and application thereof

ActiveCN103360159AMake up for the disadvantages of short blooming period and low efficiency of pollination and fertilizationMake up for the disadvantages of low pollination and fertilization efficiencyFertilising methodsFertilizer mixturesPhosphateMonopotassium phosphate
The invention provides a Castanea henryi high-yielding regulator and application thereof. The Castanea henryi high-yielding regulator is composed of a Castanea henryi high-yielding regulator 1 and a Castanea henryi high-yielding regulator 2, wherein the Castanea henryi high-yielding regulator 1 contains the following components in parts by weight: 10-150 parts of potassium dihydrogen phosphate, 20-150 parts of calcium chloride, 50-100 parts of boric acid, 50-100 parts of sucrose, 0.5-3 parts of 2,4-dichlorphenoxyacetic acid, 20-70 parts of gibberellin and 1-4 parts of indolebutyric acid; and the Castanea henryi high-yielding regulator 2 contains the following components in parts by weight: 100-300 parts of urea, 10-70 parts of ammonium phosphate, 20-50 parts of potassium sulfate, 30-70 parts of magnesium chloride, 50-100 parts of calcium chloride, 50-100 parts of manganese chloride, 10-30 parts of zinc sulfate and 50-200 parts of ferrous sulfate. The Castanea henryi high-yielding regulator provided by the invention can obviously enhance the yield of the Castanea henryi, and ensure the high and stable yield of the Castanea henryi.
Owner:CENTRAL SOUTH UNIVERSITY OF FORESTRY AND TECHNOLOGY
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