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55 results about "Strontium sulfide" patented technology

Strontium sulfide is the inorganic compound with the formula SrS. It is a white solid. The compound is an intermediate in the conversion of strontium sulfate, the main strontium ore called celestite, to other more useful compounds.

Preparation of red strontium sulphide long afterglow material

The invention discloses a method for preparing a red strontium sulphide long afterglow material, comprising a hydrothermal coprecipitation method which comprises the following steps that: (a) water-solubility strontium salt, water-solubility europium salt, water-solubility dysprosium salt, carbamide and water are weight according to the mol ratio of 1: between 0.01 and 0.05: between 0.01 and 0.05: between 4 and 6: between 28 and 32 and are put inside a container to be stirred and dissolved, the mixture is insulated in a sealing state at a temperature of between 80 and 160 DEG C for 5 to 24 hours so that a precursor is obtained; (b) the precursor is subject to filtering and annealing at a temperature of between 900 and 1200 DEG C in the reaction environment for 0. 5 to 2 hours so that the red strontium sulphide long afterglow material is prepared; the water-solubility strontium salt is strontium nitrate or strontium chloride or strontium acetate, the water-solubility europium salt is europium nitrate, europium chloride or polyimide, the water-solubility dysprosium salt is dysprosium nitrate or dysprosium chloride or dysprosium acetate, and a surface active agent is added according to the mol ratio of the water-solubility strontium salt to the surface active agent of 1: between 0.0001 and 0.0003. The method is widely applied to the fields such as building decoration, traffic transportation, military facilities, fire emergency service and goods for everyday consumption.
Owner:HEFEI INSTITUTES OF PHYSICAL SCIENCE - CHINESE ACAD OF SCI

Method of forming a thick film dielectric layer in an electroluminescent laminate

A patterned phosphor structure, and EL laminate containing same, forming red, green and blue sub-pixel phosphor elements for an AC electroluminescent display. The patterned phosphor structure includes at least a first and a second phosphor emitting light in different ranges of the visible spectrum, but with combined emission spectra contains red, green and blue light, the first and second phosphors being in a layer, arranged in adjacent, repeating relationship to each other to provide a plurality of repeating first and second phosphor deposits. The phosphor structure also includes one or more means associated with one or more of the first and second phosphor deposits, and which together with the first and second phosphor deposits, form the red, green and blue sub-pixel phosphor elements, for setting and equalizing the threshold voltages of the red, green and blue sub-pixel phosphor elements, and for setting the relative luminosities of the red, green and blue sub-pixel phosphor elements so that they bear set ratios to one another at each operating modulation voltage used to generate the desired luminosities for red, green and blue. Photolithographic methods for producing the patterned phosphor structure are also provided. Also provided is an improved dielectric layer for use in an EL laminate, including a pressed, sintered ceramic material having, compared to an unpressed, sintered dielectric layer of the same composition, improved dielectric strength, reduced porosity and uniform luminosity in an EL laminate. Also provided are combined substrate and dielectric layer components or EL laminates containing the pressed thick film dielectric layer, and methods of forming the pressed thick film dielectric layer. A process is also provided for synthesizing strontium sulfide phosphors by providing a source of high purity strontium carbonate in a dispersed form, heating the strontium carbonate in a reactor with gradual heating up to a maximum temperature in the range of 800 to 1200° C., contacting the heated strontium carbonate with a flow of sulfur vapours formed by heating elemental sulfur in the reactor to at least 300° C. in an inert atmosphere; and terminating the reaction by stopping the flow of sulfur at a point when sulfur dioxide or carbon dioxide in the reaction gas reaches an amount which correlates with an amount of oxygen in oxygen-containing strontium compounds in the reaction product which is in the range of 1 to 10 atomic percent.
Owner:IFIRE IP CORP

Process for producing strontium carbonate and barium carbonate without continuous carbonization of hydrogen sulfide gas holder

InactiveCN107140670ASubsequent production process is stableBarium carbonatesStrontium carbonatesStrontium carbonateStrontium sulfide
The application of the present invention discloses a process for continuously carbonizing strontium carbonate and barium carbonate without hydrogen sulfide gas tank, which includes the following process steps: the first step is to pass the strontium sulfide or barium sulfide liquid through the liquid feed pipe first from the first carbonization tower The upper part is sprayed down; the second step is to adjust the flow rate to maintain a stable liquid level in the first carbonization tower; the third step is to adjust the flow rate to maintain a stable liquid level in the second carbonization tower, and so on; The fourth step is to completely react carbon dioxide with strontium sulfide or barium sulfide solution, and the hydrogen sulfide gas produced is discharged from the exhaust pipe at the top of the first carbonization tower into the subsequent production process; the fifth step is to discharge strontium sulfide or barium strontium sulfide slurry , and then adjust the flow rate to maintain a stable liquid level in the last carbonization tower; the sixth step is to start the car and start continuous production according to the above process. By adopting the process of the invention, the hydrogen sulfide gas tank can be eliminated, and at the same time, the production stability of the follow-up process using hydrogen sulfide as a raw material can be guaranteed.
Owner:CHONGQING KINGLONG FINE STRONTIUM CHEM

Process for producing barium sulfate byproduct in process of removing barium from yellow water

The invention relates to a process for producing a barium sulfate byproduct in the process of removing barium from yellow water. The process comprises the following steps of: (1) obtaining the yellow water, namely calcining celestite and reducing coal to obtain black ash, and leaching the black ash by using water to obtain an aqueous solution of strontium sulfide, namely the yellow water; and performing natural sedimentation on the yellow water at the temperature of between 80 and 85 DEG C to remove impurities, namely acid-insoluble substances and calcium ions so as to obtain clear yellow water; (2) performing barium removal reaction, namely adding industrial dilute sulfuric acid into the clear yellow water, and performing barium removal reaction; and continuously stirring for 2 to 5 hours to convert barium ions into barium sulfate; (3) adding a flocculating agent, namely a polyacrylamide solution into the yellow water subjected to barium removal reaction, stirring, and filtering to obtain a filter cake and filtrate yellow water; and (4) carbonizing the filtrate yellow water by the conventional process to produce strontium carbonate; and washing the filter cake for one to two times, drying, and grinding to obtain the barium sulfate byproduct. The process is simple and low in cost, the clarity of the yellow water can be effectively improved, the content of the barium ions in the yellow water is reduced, and the environment-friendly barium sulfate byproduct is obtained.
Owner:QINGHAI INST OF SALT LAKES OF CHINESE ACAD OF SCI

Process for reducing celestine in rotary hearth furnace to produce strontium sulfide

The invention relates to a production process for reducing celestine concentrate pellets with carbon in a rotary hearth furnace to produce strontium sulfide. The process comprises the following steps: subjecting celestine concentrate powder and anthracite duff or petroleum coke powder, used as main raw materials, to batching according to a certain ratio, weighing and mixing, adding a binder and water and carrying out blending so as to obtain a wet material; pressing the wet material with a ball press machine to obtain cold-bonded pellets with certain sizes; drying the pellets in a chain grate, then conveying the dried pellets to the rotary hearth furnace with a highest reduction temperature of 1200 to 1300 DEG C to convert strontium sulfate in celestine into strontium sulfide; and discharging the reduced hot pellets out from the rotary hearth furnace and directly quenching the hot pellets in a water leaching pool, wherein the waste heat of the pellets can be used for increasing water temperature so as to facilitate acceleration of a series of chemical reactions for subsequent preparation of strontium carbonate. The process for production of strontium sulfide via the rotary hearth furnace has the advantages of simple operation, high efficiency, great output, low cost, no pollution, etc. Detection results show that the conversion rate of strontium sulfate in celestine reaches 95% or above through reduction of celestine with carbon in the rotary hearth furnace.
Owner:JIANGSU UNIV

Continuous carbonization reaction system and production process for producing high-purity large-particle-size strontium carbonate

The invention discloses a continuous carbonization reaction system and production process for producing high-purity large-particle-size strontium carbonate. The production process comprises the following steps of: carrying out high-temperature reduction on celestite to obtain strontium sulfide; soaking the strontium sulfide in hot water; performing filtering, impurity removing, cooling and crystallizing to obtain strontium hydroxide crystals; dissolving the strontium hydroxide crystals to remove impurities, thereby obtaining a strontium hydroxide reaction solution; introducing the strontium hydroxide reaction solution into a continuous carbonization reaction tower which is provided with three reaction towers communicated with one another; introducing the strontium hydroxide reaction solution and carbon dioxide gas into the reaction towers; and keeping the liquid level of each reaction tower stable, thereby obtaining the high-purity large-particle-size strontium carbonate, The production process of the invention is simple; a continuous production mode is adopted; the strontium sulfide is directly used for producing the large-particle-size strontium carbonate, and barium hydroxide can also be used for producing barium carbonate; and high stability of the liquid level in the reaction process is guaranteed by controlling the concentration and impurity content of the reaction solution, and the produced high-purity strontium carbonate or barium carbonate product is large in particle size and stable in quality; large-scale production is facilitated.
Owner:CHONGQING KINGLONG FINE STRONTIUM CHEM

A kind of beneficiation method of antimony sulfide ore

ActiveCN106733210BStrong flotation collection capacityImprove recycling effectFlotationLead nitrateSulfide minerals
The invention relates to a mineral processing method of antimony sulfide ore. The mineral processing method comprises the following steps: crushing raw antimony sulfide ore, carrying out ore grinding, adding water, stirring, carrying out size mixing, recycling antimony sulfide minerals by adopting a flotation method, and carrying out roughing once, scavenging for three times and concentration for three times to obtain antimony concentrate, wherein lead nitrate is taken as an activating agent, xanthogenate mixture and B sulfur nitrogen are taken as a combined collecting agent and new coniferyl oil is taken as a foaming agent during the roughing, and the lead nitrate is taken as the activating agent and the xanthogenate mixture is taken as a collecting agent during primary scavenging and secondary scavenging. The method provided by the invention has the advantages that floatation collecting capability on the antimony sulfide minerals is strong, recycling effect is good, antimony recovery rate is more than or equal to 93.2% and is increased by 0.98% compared with the prior art, lead-antimony ratio in the antimony concentrate is reduced by more than or equal to 26.8%, and antimony concentrate grade is more than or equal to 50.0%; reaction conditions of the method provided by the invention are neutral, corrosive effect on mineral processing equipment is alleviated, operation safety is improved, and production cost is reduced; and the method provided by the invention is easy to operate, efficient and environmentally friendly.
Owner:锡矿山闪星锑业有限责任公司
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