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35results about How to "Coarse particles" patented technology

Mixed salt process to preparing in-situ reinforced Mg-based composite material

The present invention relates to material technology and is mixed salt process to prepare in-situ reinforced Mg-base composite material. The process includes determining the alloy element components in the composite material, selecting the reinforcing phase based on the wettability between the substrate and the reinforcing phase whith ic controlled in 2-15 wt%, compounding and pretreating mixed salt system, smelting the magnesium substrate material and adding the pretreated mixed salt into the magnesium melt at proper temperature via stirring, and final casting after being let stand to form. The reinforcing phase is fine, homogeneously distributed and excellent in interface bindnig, and the Mg-base composite material has excellent mechanical and physical performance and may be used widely.
Owner:SHANGHAI JIAO TONG UNIV

Preparation method of high-stability high-purity extra-coarse tungsten carbide powder

A preparation method of a high-stability high-purity extra-coarse tungsten carbide powder contains the following steps of: (1) grinding a high-purity extra-coarse tungsten carbide powdered raw material with its chemical purity being greater than or equal to 99.98 wt%, and carrying out size grading to obtain the required average granularity and a high-purity extra-coarse tungsten powder according to the particle size distribution; (2) carrying out carbon addition by the use of carbon black according to the total carbon content of the obtained tungsten carbide powder being 6.13+ / -0.05%, followed by ball milling and mixing to obtain a ball-milling mixture; (3) filling the obtained ball-milling mixture into a graphite boat and a carbide furnace, and carrying out high-temperature carbonization at 1600-2500 DEGC for the carbonization time of 1-10 hours; and (4) carrying out coarse crushing on the obtained carbonized material, followed by grinding and crushing, and carrying out size grading to obtain the high-purity extra-coarse tungsten carbide powder. The method provided by the invention can be adopted to produce the high-purity extra-coarse tungsten carbide powder with good crush resistance, morphology and structure and excellent thermal stability. The high-purity extra-coarse tungsten carbide powder is used to prepare an extra-coarse crystal cemented carbide product with high performance.
Owner:江西耀升钨业股份有限公司 +1

Method for preparing rare-earth phosphorate

The invention belongs to the technical field of rare earth chemical engineering and particularly relates to a method for preparing rare-earth phosphorate. The method for preparing rare-earth phosphorate comprises the following steps that firstly, a rare-earth carbonate or rare-earth oxide suspension with the concentration of 10-1000 g / L is prepared; secondly, a precipitator is added into the suspension under continuous stirring at the room temperature until the pH value is smaller than or equal to 5; thirdly, stirring continues for 5-30 min, the reaction endpoint is reached when it is observed that the pH does not rise any more, if in the stirring process, the pH rises to 2 or above, the precipitator is supplemented until the pH is smaller than or equal to 5, and stirring and observation are carried out until the reaction endpoint is reached; fourthly, precipitation, dehydration and washing are carried out, and rare-earth phosphorate is obtained. According to the method, rare-earth phosphorate obtained through precipitation is large in particle size and easy to filter and wash with water; compared with preparation with a hydrothermal reaction and a solid-phase reaction, the method is relatively easy to implement, and certain industrial popularization meaning is achieved.
Owner:淄博包钢灵芝稀土高科技股份有限公司

Crystallization method of ammonium paratungstate

The invention discloses a crystallization method of ammonium paratungstate and relates to a production method of ammonium tungstate by adopting hydrometallurgy. The method is characterized in that the invention has a crystallization process that ammonium paratungstate crystal seeds are added into ammonium tungstate solution when the solution is evaporated and concentrated to appear microcrystalline particles for isothermal crystallization under the solution temperature of 90-95 DEG C for 20-40mins; the solution is then heated up to boil and added with weak aqua ammonia to adjust the pH value of the ammonium tungstate solution to 8.0-8.5 and then treated with feeding and filtering when the density of mother liquor reaches 10.8 to 1.10 g / cm <3>; the solution is again washed with the weak aqua ammonia and deionized water and dried to obtain the ammonium paratungstate crystals with large particle size and uniform distribution. The method of the invention effectively controls the crystallization of the ammonium paratungstate through the measures of removing fine crystals through the weak aqua ammonia, adding the crystal seeds, controlling the evaporation speed, etc.; in addition, the produced ammonium paratungstate crystals with large and controllable particle size are uniform and smooth; and the technology is simple and easy to be operated.
Owner:JINDUICHENG MOLYBDENUM CO LTD

Method for converting neodymium oxide into neodymium acetate crystal

The invention relates to a method for converting neodymium oxide into a neodymium acetate crystal. The method is characterized by comprising the following steps of: pumping analytically-pure glacial acetic acid and deionized water into a reaction kettle according to the volume ratio of 1:1, uniformly stirring and heating until the mixture is boiled; rotating a stirring paddle, and slowly adding the weighted neodymium oxide into the reaction kettle, wherein the mole rate of the addition of the neodymium oxide to the addition of acetic acid is 1:3.9; after the reaction is ended completely, heating a liquid material to 110-125 DEG C, and then, stopping heating to enable the liquid material in the reaction kettle to naturally cool and crystallize; when the liquid material is cooled to the temperature below 50 DEG C, enabling the stirring paddle to stop stirring, filtering a liquid through a filter tank, and centrifugally dewatering; and airing the dewatered reactant in a dust-free room to realize natural evaporation. The rare earth neodymium oxide is used for manufacturing the neodymium acetate crystal, so that the method is simple in process flow, high in production efficiency, low in energy consumption and capable of reducing the production cost and environment pollution; and the neodymium acetate crystal product is high in purity and total rare earth quantity, large in crystal particle and pure in color and luster, and the added value of a product can be increased.
Owner:YIXING XINWEI LEESHING RARE EARTH +1

Gypsum crystallization regulator suitable for wet type calcium-based flue gas desulphurization poisoning slurry

The invention discloses a gypsum crystallization modifier suitable for wet type calcium-based desulphurization of a thermal power generating unit, and the gypsum crystallization modifier can effectively eliminate the impact of heavy metal ions and oil contaminations in gypsum slurry on gypsum crystallization process to obtain gypsum crystals with coarse and large particles and low water content, increases stability of the desulfurization system, and belongs to the technical field of environmental protection. The gypsum crystallization modifier comprises the following components by weight: 0.1-5% of an oil-removing agent, 85-95% of a metal complexing agent and 5-10% of a surfactant, and is characterized in that the gypsum crystallization modifier can be directly added into an absorption tower or an absorption tower filtrate pit, then mixed evenly and dissolved for pumping. The gypsum crystallization modifier can accelerate the oxidation of sulfites and the gypsum crystallization process, is appropriate to improve the efficiency of the desulfurization system. In the embodiment, the gypsum crystallization modifier concentration is increased from 0% to 0.1%, the by-product gypsum purity is improved from 78% to 93%, the gypsum water content is reduced from 19% to 10%, the crystal size distribution is more uniform, acicular gypsum crystals are decreased, rhombic crystal share and columnar crystal share increase, the crystal specific surface area increases, and the gypsum dewatering performance is better.
Owner:NANJING INST OF TECH

Method for treating wastewater containing heavy metal ions through phase transformation of MgCO3.3H2O

The invention provides a method for treating wastewater containing heavy metal ions through phase transformation of MgCO3.3H2O, and belongs to the technical field of wastewater treatment. The method comprises the following steps: taking wastewater solution containing heavy metal ions, regulating the temperature to 50-60 DEG C, regulating the pH value to 4-8, adding MgCO3.3H2O into the wastewater solution containing the heavy metal ions, and oscillating the solution at constant temperature, so as to obtain wastewater turbid liquid containing the heavy metal ions; heating the wastewater turbid liquid to 55-90 DEG C, stirring at constant temperature for 30-90min, standing, aging, and filtering obtained mixed solution containing precipitation, so as to obtain clear liquid and a filter cake, wherein the mass ratio of MgCO3.3H2O to the heavy metal ions is (4-50):(0.01-1); the heavy metal ion(s) is / are one or more heavy metal ions of Cr<3+>, Pb<2+>, Ni<2+>, Cu<2+>, Zn<2+> and Cd<2+>. According to the method, the wastewater containing the heavy metal ions is treated, the treatment cost is lowered, and the secondary resource recycling of heavy metals can be realized.
Owner:SHENYANG LIGONG UNIV

Synthetic method of citric acid gypsum

The invention belongs to the field of dihydrate gypsum synthesis and relates to a synthetic method of citric acid gypsum. The method comprises the following steps: preparing a suspension from calcium hydrogen citrate, calcium sulphate dihydrate seed crystal and water; heating the suspension until the temperature of the suspension is 20-80 DEG C, stirring the suspension and simultaneously adding a sulfuric acid solution into the suspension until sulfuric acid and calcium hydrogen citrate completely react; standing and taking a bottom solid after the reaction, cooling and washing and drying. By the technical scheme, the problem of low strength of building gypsum powder due to fine citric acid gypsum particles and irregular crystal structure is solved.
Owner:JIANGSU EFFUL SCIENCE AND TECHNOLOGY CO LTD

Process for improving quality of phosphorus chemical industry waste smoke desulfurization gypsum

The invention discloses a process for improving the quality of phosphorus chemical industry waste smoke desulfurization gypsum, and the process comprises the following steps: mixing a desulphurized absorbent with slag washing water; stirring to form an even slag slurry; carrying out rotational flow separation on the slag slurry; removing bottom flow slag to obtain an overflowing liquid; configuring additive mixed liquor; mixing and stirring the additive mixed liquor and the overflowing liquid to obtain even size; contacting the size with the phosphorus chemical industry smoke; adsorbing sulfur dioxide and phosphorus compound in the phosphorus chemical industry smoke; carrying out airoxidation to form a gypsum liquid; carrying out the rotational flow separation on the gypsum to obtain top flow liquid and bottom flow desulfurization gypsum liquid; reusing the top flow liquid; and dewatering the bottom flow desulfurization gypsum liquid to obtain the desulfurization gypsum. According to the process disclosed by the invention, the problems of small desulfurization gypsum crystalline particle and difficulty in separation in the phosphorus chemical industry waste smoke desulfurization system are solved, gypsum crystal with big particle and low moisture content is obtained, and the filtering performance of the gypsum is improved.
Owner:ZHEJIANG TIANLAN ENVIRONMENTAL PROTECTION TECH

Method for decontaminating potassium sub-molten salt soluble crystal liquid and preparing chromic oxide

The invention discloses a method for decontaminating potassium sub-molten salt soluble crystal liquid and preparing chromic oxide. The method comprises the following steps: (1) introducing CO2 to potassium sub-molten salt soluble crystal liquid, neutralizing potassium hydroxide in the solution, then adding seed crystals, controlling the temperature of the solution at 30-90 DEG C and removing aluminum and silicon; (2) introducing CO2 to the solution obtained in the step (1) to carry out room-temperature pre-carbonation; (3) adding a reducing agent to pre-carbonated feed liquid obtained in the step (2), heating to 120-170 DEG C, and carrying out heat preservation and solid-liquid separation after reaction is ended, so as to obtain a chromium hydroxide filter cake; and (4) drying and calcining the chromium hydroxide filter cake obtained in the step (3), so as to obtain a chromium sesquioxide product. By adopting a pre-acidification mode, the reducing agent is not added in pre-carbonation; no CO2 is introduced after the pre-carbonated feed liquid and the reducing agent are mixed; the method is high in conversion rate of hydrothermal reduction, fewer in intermediate products, high in total yield of chrome, high in purity of the sintered chromic oxide and fewer in impurities by controlling a proper pre-carbonation condition.
Owner:INST OF PROCESS ENG CHINESE ACAD OF SCI

Preparation technology of zinc sulfate heptahydrate by cold liquid hot flushing method

The invention discloses a preparation technology of zinc sulfate heptahydrate by a cold liquid hot flushing method. The preparation technology comprises the following steps of quickly cooling a saturated zinc sulfate solution for the first time, crystallizing, quickly cooling for the second time, adding a hot saturated solution, quickly cooling for the third time, cooling by cooling water, and crystallizing, so as to obtain a zinc sulfate heptahydrate product. The preparation technology has the advantages that when the zinc sulfate heptahydrate is applied to the industrial production, the large-particle zinc sulfate crystal can be obtained; the content of free water in the product is obviously reduced, the crystallizing time is shortened, and the production efficiency and the product quality are improved.
Owner:SHANDONG DAZHENG ENERGY SAVING ENVIRONMENTAL PROTECTION TECH CO LTD

Method of water treatment process

The invention belongs to the technical field of sewage treatment in zinc hydrometallurgy process, and provides a method of water treatment process. The method comprises the following steps: (1) addinga neutralizing agent to acidic wastewater containing heavy metals to adjust the pH value to 7.0 to 8.0 till the reaction stops and precipitates are generated, and then filtering to separate the precipitates to obtain first filtrate with residue at the bottom; (2) adding a neutralizing agent to the first filtrate again to adjust the pH value to 8.0 to 9.0 till the reaction stops and precipitates are generated, then adding Na2S to the filtrate till the reaction stops and precipitates are generated, wherein the weight ratio of Na2S added to heavy metals in the first filtrate is (1.2-1.5) to 1, and finally, filtering to separate the precipitates in the first filtrate, so as to obtain second filtrate with residue at the bottom. The method is highly efficient, the consumption of a precipitatingagent is small, the degree of purification is deep, and the amount of residue is small, and thus the method is suitable for large-scale industrial treatment.
Owner:四川四环锌锗科技有限公司

Treatment method of high-fluorine-chlorine secondary zinc oxide slag

The invention provides a treatment method of high-fluorine-chlorine secondary zinc oxide slag. The treatment method comprises the following steps: S1) washing the high-fluorine-chlorine secondary zinc oxide slag with water to obtain washing slag and washing water; S2) mixing and stirring the washing slag, zinc electrolysis waste liquid and a sulfuric acid-containing solution, and filtering to obtain a zinc sulfate-containing solution and slag; and S3) performing cooling crystallization on the zinc sulfate-containing solution to obtain zinc sulfate and crystallization mother liquor. Compared with the prior art, the treatment method has the advantages that the secondary zinc oxide waste slag is washed with water, fluorine and chlorine in part of secondary zinc oxide can be removed in advance, and a foundation is laid for fluorine and chlorine purity control of subsequent zinc sulfate crystallization; then the washing slag of secondary zinc oxide, which is obtained after washing, the zinc electrolysis waste liquid and the sulfuric acid-containing solution are mixed and stirred, and the temperature is controlled to improve the saturation of zinc sulfate in the solution, thereby laying a foundation for subsequent induced crystallization and precipitation of zinc sulfate; and finally, zinc sulfate crystals generated through cooling induced crystallization are coarse in particle and high in purity, only a small amount of fluorine and chlorine are adsorbed on the surfaces of the crystals, and the recycling quality requirement can be met.
Owner:湖南中金岭南康盟环保科技有限公司

Method for manufacturing specified nickel powder for welding electrode by machinery crushing method

The invention is an electric welding rod special nickel powder production technique by machine fragmenting. Fragment an oxidating production with brittle nickel oxide surfacing layer outside and nickel inside which obtained by dynamically continuously oxidating the foam nickel raw material, with multi-level fragmenting machine. Secondary oxidating the fragmented powder obtaining large particle nickel oxide powder and then take the powder into phasing deoxidation so to obtain high performance nickel powder with high purity and large particles which is also the advantages of the invention and the powder is a fine material of electric welding rod coating. The production technique is simple, of low cost and high efficiency which adapted to mass production. The preparation processes is without any additions and any pollutions which is environmetal.
Owner:长沙市维优金属材料有限公司

Method for producing holmium acetate crystal

InactiveCN103360234AHigh purityHigh Total Rare EarthCarboxylic acid salt preparationAcetic acidHolmium
The invention relates to a method for producing a holmium acetate crystal. The method is characterized by comprising the following steps of: pumping analytically pure glacial acetic acid and deionized water at the volume ratio of 1:0.5 into a reactor, stirring uniformly, and heating to the temperature of 50 DEG C; rotating a stirring paddle, and adding the weighed holmium carbonate into the reactor slowly, wherein the molar ratio of the added holmium carbonate to the glacial acetic acid is 1:3.3; heating a liquid material to the temperature of 110-125 DEG C after the materials react completely, and stopping heating to naturally cool the liquid material in the reactor to crystallize; cooling the liquid material to the temperature below 50 DEG C, discharging the liquid material into a filtering box, removing liquid by filtering, and dehydrating centrifugally; and airing the dehydrated product of reaction in a dust-free room to evaporate naturally. The method for producing the holmium acetate crystal from the carbonate holmium (rear earth) is simple in technological process, high in production efficiency and low in production cost, consumes less energy and causes less pollution to the environment. In addition, the holmium acetate crystal is high in purity, high in content of rear earth, high in additional value, large in particle size and pure in color.
Owner:YIXING XINWEI LEESHING RARE EARTH +1

An ionic membrane salt separation concentration crystallization freeze crystallization salt production device and process

The invention discloses a device and a process for preparing salt through ionic membrane salt separation, concentration crystallization and freezing crystallization. The device for preparing salt through ionic membrane salt separation, concentration crystallization and freezing crystallization comprises a monovalent ionic membrane salt separation device, a heating and heat exchanging device with a water inlet connected with a concentrated water outlet of the monovalent ionic membrane salt separation device, a concentration crystallization device with a water inlet connected with a water outlet of the heating and heat exchanging device, a special ionic membrane salt concentration device with a water inlet connected with a fresh water outlet of the monovalent ionic membrane salt separation device, a cooling and heat exchanging device with a water inlet connected with a concentrated water outlet of the special ionic membrane salt concentration device as well as a freezing crystallization device with a water inlet connected with a water outlet of the cooling and heat exchanging device. The system recovery rate is increased, the salt separation effect is enhanced, high-purity NaCl crystal salt and mirabilite are obtained according to different qualities, the system is stable and reliable, the operation cost is low, and the investment cost is low.
Owner:岳阳锦能环境绿色能源有限公司

Sodium chromate alkali solution impurity removal method and preparation method of chromic oxide

The invention discloses a sodium chromate alkali solution impurity removal method and a preparation method of chromic oxide. According to sodium chromate alkali solution impurity removal, CO2 with rich resources and low cost serves as acidulant, aluminium and silicon are removed by continuous carbonating decomposition, and the removal rates of the aluminium and the silicon are high; new impurities are not introduced; and aluminium mud after sedimentation has thick and large particles, is low in chromium belt loss, and can be used in alumina industries after being filtered and washed, thus having a high added value. Impurities and sodium chromate solution are separated to obtain solution, cheap and rich starch and derivatives of the starch serve as reductants, and hydrated chromium hemitrioxide is prepared under a hydrothermal reducing condition, and then pigment-level chromium hemitrioxide is generated after dehydration and calcination. The reducing condition is mild, the conversion rate is higher than 90%, slurry easy to filter and wash, and final filtrate and alkaline rinse in production process can be returned to mix with chromite to enter a calcination process, thereby recycling sodium carbonate. According to the invention, the process adopted for generating the chromium hemitrioxide is simple and environment-friendly, the cost is low, and industrialization is easy to realize.
Owner:INST OF PROCESS ENG CHINESE ACAD OF SCI

Method for analyzing lithium ion battery electrolyte salt LiBF4

The invention relates to a method for analyzing lithium ion battery electrolyte salt LiBF4. The method includes steps of preparing and calibrating a Na2S2O3 5H2O standard solution; preparing and calibrating a K13 standard solution; preparing and calibrating a (C6H5) As4Cl standard solution; preparing 1mol / L of a LiBF4 solution; preparing 0.01 mol of mol / L of the LiBF4 solution; determining a main content four fluorine boric acid roots by a weighting method: placing the LiBF4 solution in a water bath thermostatic bath, adding the (C6H5) As4Cl solution dropwise after 15 minutes to 30 minutes, mixing the mixture during dropwise adding, and obtaining sediment (C6H5) 4AsBF4 after dropwise adding; and ageing the sediment (C6H5) 4AsBF4 in a constant temperature water bath for 30 minutes to 60 minutes and then performing leaching, cleaning and drying to a constant weight, and performing content calculation. According to the method, the operation is simple and rapid, and defects that errors are increased for the increase of the sample dilution ratio as the ion selective electrode method is used are effectively overcome.
Owner:QINGHAI INST OF SALT LAKES OF CHINESE ACAD OF SCI

Method for converting yttrium oxide into yttrium acetate crystal

The invention relates to a method for converting yttrium oxide into an yttrium acetate crystal. The method is characterized by comprising the following steps of: pumping analytically-pure glacial acetic acid and deionized water into a reaction kettle according to the volume ratio of 1:1, uniformly stirring and heating until the mixture is boiled; rotating a stirring paddle, and slowly adding the weighted yttrium oxide into the reaction kettle, wherein the mole rate of the addition of the yttrium oxide to the addition of acetic acid is 1:3.9; after the reaction is ended completely, heating a liquid material to 110-125 DEG C, and then, stopping heating to enable the liquid material in the reaction kettle to naturally cool and crystallize; when the liquid material is cooled to the temperature below 50 DEG C, enabling the stirring paddle to stop stirring, filtering a liquid through a filter tank, and centrifugally dewatering; and airing the dewatered reactant in a dust-free room to realize natural evaporation. The rare earth yttrium oxide is used for manufacturing the yttrium acetate crystal, so that the method is simple in process flow, high in production efficiency, low in energy consumption and capable of reducing the production cost and environment pollution; and the yttrium acetate crystal product is high in purity and total rare earth quantity, large in crystal particle and pure in color and luster, and the added value of a product can be increased.
Owner:YIXING XINWEI LEESHING RARE EARTH +1

A method for removing impurities and preparing chromium oxide in a potassium-based sub-molten salt solution

The invention discloses a method for decontaminating potassium sub-molten salt soluble crystal liquid and preparing chromic oxide. The method comprises the following steps: (1) introducing CO2 to potassium sub-molten salt soluble crystal liquid, neutralizing potassium hydroxide in the solution, then adding seed crystals, controlling the temperature of the solution at 30-90 DEG C and removing aluminum and silicon; (2) introducing CO2 to the solution obtained in the step (1) to carry out room-temperature pre-carbonation; (3) adding a reducing agent to pre-carbonated feed liquid obtained in the step (2), heating to 120-170 DEG C, and carrying out heat preservation and solid-liquid separation after reaction is ended, so as to obtain a chromium hydroxide filter cake; and (4) drying and calcining the chromium hydroxide filter cake obtained in the step (3), so as to obtain a chromium sesquioxide product. By adopting a pre-acidification mode, the reducing agent is not added in pre-carbonation; no CO2 is introduced after the pre-carbonated feed liquid and the reducing agent are mixed; the method is high in conversion rate of hydrothermal reduction, fewer in intermediate products, high in total yield of chrome, high in purity of the sintered chromic oxide and fewer in impurities by controlling a proper pre-carbonation condition.
Owner:INST OF PROCESS ENG CHINESE ACAD OF SCI
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