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61results about How to "Low fluorine content" patented technology

Method for preparing lanthanum-enriched rare earth chloride from bastnaesite

The invention relates to a method for producing lanthanum-enriched rare earth chloride by using bastnaesite as a raw material. The method comprises the following steps of: mixing the bastnaesite and sodium hydroxide and then roasting, carrying out sodium hydroxide alkali conversion on the bastnaesite to remove fluorine, washing the bastnaesite subjected to alkali conversion with water, and carrying out hydrochloric acid optimum solution to obtain lanthanum-enriched rare earth chloride liquid. In the alkali conversion process, the ratio of NaOH to REO (Rare Earth Oxide) in the bastnaesite is (0.10-0.40):1, the alkali conversion is carried out at 300-600 DEG C, and then the bastnaesite subjected to the alkali conversion is washed with water 3-8 times of the bastnaesite by weight proportion. In the optimum solution process, the weight ratio of 31% of industrial hydrochloric acid by weight to the REO in the bastnaesite is (1-1.5):1. In the alkali conversion process, the fluorine in the enriched lanthanum is preferentially subjected to the alkali conversion to obtain lanthanum-enriched hydroxide which is dissolved with acid, acid-soluble lanthanum-enriched rare earth is dissolved in a solution, and cerium is reserved in slag with large amount of fluorine, therefore, the purpose of separating the cerium and non-cerium can be achieved easily. In the whole process, the step of solid-liquid separation is reduced, the consumption of auxiliary materials is lowered, the yield per unit of equipment and the yield of rare earth are improved, and the production process has less pollution.
Owner:CHINA MINMETALS BEIJING RES INST OF RE

Method for separating scheelite from fluorite

The invention relates to a method for separating scheelite from fluorite and belongs to the technical field of mineral dressing of metal mines. The method comprises the following steps of: preparing ore pulp from tungsten secondary concentrate ore containing 30 to 60 weight percent of tungsten trioxide; carrying out two stages of separation by adopting shaking tables; then making middlings of a first-stage shaking table enter a second-stage shaking table to be separated so as to produce special grade white tungsten concentrate ore products containing over 70 weight percent of tungsten trioxide; concentrating the middlings and tailings, which are separated by the shaking tables, to 50 to 60 weight percent in a centralizing mode, then adding water glass and TN into the concentrated middlings and tailings, and uniformly stirring the mixture in a stirring barrel for flotation; diluting flotation pulp to 20 to 30 weight percent, regulating the pH of the diluted flotation pulp to 9 to 10, and adding an inhibitor KJ and a collector YY to produce white tungsten concentrate ore containing over 65 weight percent of tungsten trioxide; and further carrying out flotation on the flotation tailings to obtain fluorite powder ore containing over 85 percent of calcium fluoride. The method has the advantages of high mineral dressing index, simple process, low production cost, environmental protection and capability of better solving the environmental problems of ammonium paratungstate manufacturing enterprises, which are caused by high fluorine content of raw materials.
Owner:YUNNAN TIN GROUP HLDG

Method for jointly treating high-fluorine sewage by utilizing waste slag

The invention provides a method for jointly treating high-fluorine sewage by utilizing waste slag, which comprises the following steps: (1) carbide slag, pulverized fuel ash and red mud are added into a treatment pond containing the high-fluorine sewage and sent into an overflow pond after being stirred and reacting for 10-20 minutes, and clear liquid in the overflow pond flows into a reaction pond; (2) the carbide slag is added into the reaction pond, and the pH is regulated to 9-10; after 10-20 minutes of reaction, a coagulating agent is added to the clear liquid, and the pH is regulated to 6-7.5; after 10-20 minutes of reaction, a coagulant aid is added to the clear liquid; and after 10-20 minutes of reaction, the clear liquid is filtered and drained. The method uses the industrial waste slag for treating the high-fluorine sewage so as to ensure that the fluorine content in the treated sewage conforms to an environmental protection standard specified by the nation, thus the pollution of the high-fluorine sewage to the environment is greatly reduced. Meanwhile, the harm of the industrial slag to the environment is also reduced, thus the method has higher economic benefit and social benefit.
Owner:河南未来铝业(集团)有限公司

Method of leaching valuable metal from waste lithium ion battery and synchronously conducting defluorination

InactiveCN111961857ALow fluorine contentIncrease the aging defluorination stepProcess efficiency improvementMetal leachingProcess engineering
The invention provides a method of leaching valuable metal from a waste lithium ion battery and synchronously conducting defluorination. The method specifically comprises the steps that the waste lithium ion battery is pretreated, electrode powder materials are obtained, the electrode powder materials, water and concentrated sulfuric acid are evenly mixed, curing treatment is conducted, the temperature of the curing treatment is controlled to range from 50 DEG C to 200 DEG C, the time of the curing treatment is controlled to range from 1.0h to 24.0h, a leaching agent is added to a cured material to conduct leaching operation after the curing treatment is accomplished, filtering operation is conducted after leaching operation is accomplished, and low-fluorine-content valuable metal leachateis obtained. According to the method, removal of fluorine in the electrode powder and leaching operation of the valuable metal are organically combined, the curing defluorination step is added beforeacid pickling operation of the electrode powder is conducted, namely, part of concentrated sulfuric acid is added to the electrode powder to conduct curing defluorination, then part of concentrated sulfuric acid is supplemented and added to the defluorinated electrode powder to conduct leaching operation, and the two processes are closely connected. Compared with a conventional acid pickling technology, the method has the advantages that the acid consumption is not increased, the technological cost is low, the operability is high, the fluorine content of the obtained valuable metal leachate is low, and the industrial production is easily achieved.
Owner:CHANGSHA RES INST OF MINING & METALLURGY

Technology and device for producing defluorinated phosphoric acid

PendingCN110980674AIncreased surface reaction areaIncreased fluorine release ratePhosphorus compoundsO-Phosphoric AcidPhysical chemistry
A technology for producing defluorinated phosphoric acid is characterized in that fluorine-containing phosphoric acid produced from wet-process phosphoric acid is divided into two parts, one part is used as a returned acid, and the other part is used as crude phosphoric acid; an injection pump A, a reaction kettle, an injection pump B, a gas-liquid separator and an absorption tower are sequentially connected through pipelines to form a circulating closed pipeline system which is in a micro-negative pressure state; the injection pump A and the injection pump B enable a gas in the system to circularly flow at a high speed, and the injection pump A sucks and mixes the returned acid and sulfuric acid, then sucks a reaction liquid and sulfuric acid in the reaction kettle, mixes the reaction liquid and sulfuric acid with gas flow and sprays the obtained mixture onto the liquid level of the reaction kettle; vacuum generated by the injection pump B makes the crude phosphoric acid and low-fluorine hot steam emitted from the reaction kettle be sucked and mixed and then enter the gas-liquid separator, a liquid led out from the gas-liquid separator is refined product defluorinated phosphoric acid, the gas is sent to the bottom of the absorption tower, and a defluorination tail gas led out from the top of the absorption tower enters the injection pump A and circularly flows; and a washing liquid is sprayed from the top of the absorption tower, and fluosilicic acid liquid is led out from the bottom of the absorption tower. The invention further discloses a device for producing defluorinated phosphoric acid.
Owner:HUANGGANG NORMAL UNIV +1

Alkali-free setting accelerator, preparation method and application thereof

ActiveCN112125558AGood adaptability to cementLow fluorine contentAluminium saltsMagnesium
The invention relates to the technical field of engineering materials, in particular to an alkali-free setting accelerator, a preparation method and application thereof. The alkali-free setting accelerator is prepared from, by mass, 40-55% of aluminum sulfate, 10-15% of aluminum nitrate, 5.2-10.8% of alkylol amine, 1-1.5% of magnesium fluosilicate, 1-5% of silicate, 0.5-1% of a stabilizer and thebalance water; wherein the stabilizer is a composition prepared by mixing any one or more of sepiolite, zeolite or diatomite according to any proportion. The alkali-free setting accelerator is mainlycomposed of aluminum sulfate, aluminum nitrate, alkylol amine, magnesium fluosilicate and silicate, is extremely low in fluorine content, does not contain other harmful substances, is green and environment-friendly, and does not cause harm to a human body; when the alkali-free setting accelerator is used for spraying concrete, the addition amount of the setting accelerator is small, the initial setting time, the final setting time, the mortar 1d compressive strength, the 28d compressive strength ratio, the 90day compressive strength retention rate and the like of neat paste of the alkali-freesetting accelerator can meet the construction requirements of different types of cement sprayed concrete, and the alkali-free setting accelerator has good cement adaptability.
Owner:北京厚德交通科技股份有限公司

Processing technology of low-fluoro-content Tibetan tea

The invention relates to the technical field of low-fluoro-content Tibetan tea processing, and discloses a processing technology of low-fluoro-content Tibetan tea. The processing technology of the low-fluoro-content Tibetan tea comprises the following steps: S1, picking tender tea leaves, namely selecting tea trees which are older than 25 years, picking tea leaves with one bud and four leaves or five leaves which are within a growth cycle of 20 days; S2, carrying out withering treatment, namely putting the picked tender leaves into a withering tank, and carrying out hot-air withering at 30-50DEG C for 2 hour; S3, carrying out high-temperature fixating, dewatering and stem-removing, namely putting the withered tea leaves into a special fixation machine so as to be subjected to continuous stir-frying at 280-320 DEG C for 450 minutes so as to control the water content at 25%, thereby separating leaves from stems; S4, removing thick stems, namely removing think stems separated from the leaves by using an air-selecting machine, and retaining 15% of thin stems; and S5, sequentially carrying out steaming and rolling, namely putting the tea leaves after the primary selection into a steamdrum at 130 DEG C, and carrying out steaming for 5-8 minutes. The processing technology of the low-fluoro-content Tibetan tea is capable of solving the problems of relatively high fluorine content oftraditional Tibetan tea and low quality of Tibetan tea prepared by conventional processing technologies.
Owner:洪雅县偏坡山茶叶专业合作社

Method for preparing lanthanum-enriched rare earth chloride from bastnaesite

The invention relates to a method for producing lanthanum-enriched rare earth chloride by using bastnaesite as a raw material. The method comprises the following steps of: mixing the bastnaesite and sodium hydroxide and then roasting, carrying out sodium hydroxide alkali conversion on the bastnaesite to remove fluorine, washing the bastnaesite subjected to alkali conversion with water, and carrying out hydrochloric acid optimum solution to obtain lanthanum-enriched rare earth chloride liquid. In the alkali conversion process, the ratio of NaOH to REO (Rare Earth Oxide) in the bastnaesite is (0.10-0.40):1, the alkali conversion is carried out at 300-600 DEG C, and then the bastnaesite subjected to the alkali conversion is washed with water 3-8 times of the bastnaesite by weight proportion.In the optimum solution process, the weight ratio of 31% of industrial hydrochloric acid by weight to the REO in the bastnaesite is (1-1.5):1. In the alkali conversion process, the fluorine in the enriched lanthanum is preferentially subjected to the alkali conversion to obtain lanthanum-enriched hydroxide which is dissolved with acid, acid-soluble lanthanum-enriched rare earth is dissolved in a solution, and cerium is reserved in slag with large amount of fluorine, therefore, the purpose of separating the cerium and non-cerium can be achieved easily. In the whole process, the step of solid-liquid separation is reduced, the consumption of auxiliary materials is lowered, the yield per unit of equipment and the yield of rare earth are improved, and the production process has less pollution.
Owner:CHINA MINMETALS BEIJING RES INST OF RE

Preparation method of low-fluorine high-purity tantalum pentoxide optical coating material

InactiveCN112592180AThe removal effect is ideal and sufficientUniform grain distributionTantalum compounds preparationCrystal systemElectron bunches
The invention discloses a preparation method of a low-fluorine high-purity tantalum pentoxide optical coating material, and particularly relates to the technical field of tantalum metal oxide preparation, which comprises the following steps: dissolving metal tantalum in a mixed acid of hydrofluoric acid and nitric acid, extracting and purifying to obtain a high-purity tantalum liquid, introducingthe high-purity tantalum liquid into a neutralization precipitation tank, adding liquid ammonia into the high-purity tantalum liquid at the same time, introducing a solution containing tantalum hydroxide precipitate into a filter press after the tantalum hydroxide precipitate appears, adding ammonia-containing hot pure water at the same time, then obtaining tantalum hydroxide, and then repeatedlyadding tantalum hydroxide into the filtering process for multiple times. According to the method, tantalum pentoxide is heated through electron beams, the purpose of heating calcination can be achieved without high temperature, grain distribution is uniform, the crystal system structure is more ideal, meanwhile, ammonia-containing hot pure water is repeatedly used for assisting the filtering process, it is guaranteed that the effect of removing fluorine in the tantalum hydroxide solution is more ideal and sufficient, and the fluorine content in the product is greatly reduced.
Owner:海宁拓材科技有限公司

Water-repellent fabric and manufacturing method thereof

The invention relates to water-repellent fabric and a manufacturing method of the water-repellent fabric. The water-repellent fabric is formed by weaving polyester industrial yarn used for the water-repellent fabric, the polyester industrial yarn used for the water-repellant fabric is made of modified polyester, and the water-repellant fabric is formed by arranging after water repellency. The modified polyester is composed of polyester and amino fatty acid glycol ester dispersed among molecular chains of the polyester, a hydrogen-bond interaction is achieved between the amino fatty acid glycol ester and the molecular chains of the polyester, and therefore the relative positions of the amino fatty acid glycol ester and the molecular chains of the polyester are fixed. According to the water-repellent fabric, at the temperature of 70 DEG C-130 DEG C, the free volume space between the molecular chains inside fibers is enlarged by 10 v/v%-30 v/v%, the breaking strength of the polyester industrial yarn used for the water-repellant fabric is larger than or equal to 7.2 cN/dtex, and the elongation at break is 20.0+/-2.0%. The washable performance of the water-repellant fabric is good. The water-repellant fabric can be used for industries such as tents and drapes.
Owner:JIANGSU HENGLI CHEM FIBER

Process for optimizing phosphoric acid reaction and separation by using active silicon dioxide

The invention discloses a process for optimizing phosphoric acid reaction and separation by using active silicon dioxide. The process comprises the following steps: adding active silicon dioxide, which is a byproduct of an enterprise for producing anhydrous hydrogen fluoride by a fluosilicic acid method, into a phosphoric acid digestion tank, mixing phosphogypsum with the active silicon dioxide and an extremely small amount of flocculant at 80 DEG C, and aging to form a co-crystal, so that the phosphogypsum crystallization rate of the digestion tank is improved, filtering by a phosphoric acidvacuum drum filter, so that the filter cake is uniformly distributed, the formed filter pore size is uniform and fine, the filtering speed is greatly improved, and the total phosphorus and fluorine content of the phosphogypsum are both at a lower level, and carrying out dilute phosphoric acid concentration, separation and water washing to prepare fluosilicic acid for fluorine hydride production. According to the invention, the process achieves harmless treatment of fluorine-containing silicon dioxide, and the recovery rate of fluosilicic acid in phosphorite is increased, and after the auxiliary agent is mixed into the phosphoric acid digestion tank, efficient separation of phosphogypsum and dilute phosphoric acid is achieved, so that the process is a new process of resource recycling, byproduct comprehensive treatment and efficient phosphoric acid separation and purification.
Owner:福建瓮福蓝天氟化工有限公司

Polyurethane heat-dissipating dustproof coating and preparation method and application thereof

The invention discloses a polyurethane heat-dissipating dustproof coating and a preparation method and application thereof. Raw materials of the polyurethane heat-dissipating dustproof coating include a component A and a component B. The component A comprises the following ingredient in parts by weight: 16-75 parts of isocyanate; the component B comprises the following ingredients in parts by weight: 1-3 parts of polytetrafluoroethylene, 40-100 parts of polyhydric alcohols and 300-600 parts of a solvent; the total parts by weight of the isocyanate and the polyhydric alcohols is 90-150; the average particle size of the polytetrafluoroethylene is 120-800 nm; the polyhydric alcohols comprise fluorine-containing dihydric alcohols; and on the basis of the total weight of the polyhydric alcohols, the weight percentage of the fluorine-containing dihydric alcohols is 15-30wt%. By the polyurethane heat-dissipating dustproof coating and the preparation method and application thereof, dust accumulation is reduced, and the problems that the surface heat resistance of a heat sink and the like is increased, the heat conduction coefficient is reduced and the heat transfer efficiency is reduced due to dust blockage are solved.
Owner:HISENSE VISUAL TECH CO LTD
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