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235results about "Calcium/strontium/barium nitrates" patented technology

Process and equipment for nitrogen oxide waste conversion to fertilizer

The present invention describes a process for converting vapor streams from sources containing at least one nitrogen-containing oxidizing agent therein to a liquid fertilizer composition comprising the steps of: a) directing a vapor stream containing at least one nitrogen-containing oxidizing agent to a first contact zone, b) contacting said vapor stream with water to form nitrogen oxide(s) from said at least one nitrogen-containing oxidizing agent, c) directing said acid(s) as a second stream to a second contact zone, d) exposing said second stream to hydrogen peroxide which is present within said second contact zone in a relative amount of at least 0.1% by weight of said second stream within said second contact zone to convert at least some of any nitrogen oxide species or ions other than in the nitrate form present within said second stream to nitrate ion, e) sampling said stream within said second contact zone to determine the relative amount of hydrogen peroxide within said second contact zone, f) adding hydrogen peroxide to said second contact zone when a level of hydrogen peroxide less than 0.1 % by weight in said second stream is determined by said sampling, g) adding a solution comprising potassium hydroxide to said second stream to maintain a pH between 6.0 and 11.0 within said second stream within said second contact zone to form a solution of potassium nitrate, and h) removing said solution of potassium nitrate from said second contact zone.
Owner:NAT AERONAUTICS & SPACE ADMINISTATION U S GOVERNMENT AS REPRESENTED BY THE ADMINISTATOR

Comprehensive soda ash producing process and product application thereof

The invention relates to the technical field of soda ash production, and especially relates to a comprehensive soda ash producing process and product applications thereof; the process comprises the following process steps: introducing ammonia gas into a saturated sodium chloride solution to prepare ammoniacal brine; introducing carbon dioxide generated in limestone calcination into the ammoniacal brine to generate a mixture of sodium bicarbonate, sodium chloride and ammonium chloride; filtering the mixture to obtain sodium bicarbonate, sodium chloride and ammonium chloride; calcining the sodium bicarbonate to generate soda ash and carbon dioxide, recycling the carbon dioxide; adding sodium chloride fine powder and ammonia gas into the mixed filtrate of ammonium chloride and sodium chloride to generate ammonium chloride and sodium chloride solutions; separating impurities from the sodium chloride solution by a membrane filter, recycling the sodium chloride solution. The process has the advantages of low production cost, high soda ash whiteness, high sodium chloride utilization rate, no water waste or solid waste generation, environment protection, safety, simple processes, full use of geographic advantages in our country, low raw material purchase cost, waste change into things of value, high economic benefits, and good social benefits.
Owner:GUANGDONG DAZHONG AGRI SCI CO LTD

Recycling method of circuit board tin stripping wastewater

The invention provides a recycling method of circuit board tin stripping wastewater and the method can be used in the resource treatment of the tin stripping wastewater of the circuit board factory, belonging to the technical field of environmental protection. The method has the following process flows: adding refined lime slurry in the tin stripping wastewater to adjust the pH value to be alkaline and ensure that a part of beta-stannic acid sol with positive charges is coagulated, another part of beta-stannic acid sol is converted to beta-stannic acid sol with negative charges, and adding the tin stripping wastewater to adjust the pH value to be neutral and ensure that the beta-stannic acid sol with negative charges performs charge neutralization with the beta-stannic acid sol particles with positive charges and is completely coagulated, performing solid-liquid separation, and rinsing to obtain solid beta-stannic acid precipitate which is used as the raw material of tin smelting to produce metal tin. The separated solution is mixed with the same rinse water and then the mixture is evaporated and concentrated to obtain a calcium nitrate tetrahydrate product. The recycling method is characterized by low treatment cost, simple treatment process, good treatment effect, high treatment efficiency, total recycling, zero emission and the like and is suitable for the resource treatment of the tin stripping wastewater of the circuit board factory.
Owner:HUIZHOU DAYAWAN HUILU ENVIRONMENT PROTECTION SERVICE +1

Method for producing less-barium fine strontium salts from celestite

The invention mainly aims to provide a method for producing less-barium fine strontium salts from celestite, and the method is low in cost, which comprises the steps: refining: crushing or grinding the celestite to particles of less than 200 mesh; acid washing: reacting diluted hydrochloric acid with the levigated celestite, and removing a carbonate component in the celestite to obtain high-purity refined celestite; and double decomposition: adding the refined celestite to an ammonium carbonate aqueous solution, uniformly stirring, then reacting in an airtight condition at a reaction pressure of 0.2-0.3MPa and a reaction material temperature of 100-115 DEG C, stopping heating after the reaction is finished, filtering and washing obtained solid to obtain a strontium carbonate crude product, and further refining the strontium carbonate crude product to obtain a product. The method has the advantages that during the double decomposition reaction, when reacting with the celestite, ammonium carbonate only reacts with strontium sulfate in the celestite without reacting with barium sulfate, so that the barium content of the obtained strontium carbonate crude product is very low and lower than 0.05%; and the method is low in production cost and has wide market prospect.
Owner:CHONGQING YUANHE FINE CHEM

Method for treating calcium in high-calcium fly ash

The invention discloses a method for treating calcium in high-calcium fly ash, which comprises the steps of phase inversion reaction, decalcification reaction and calcium compound preparation. The technique principle comprises the following steps: converting calcium sulfate in fly ash into calcium compounds capable of reacting with hydrochloric acid and nitric acid by a phase inversion process, treating the fly ash with hydrochloric acid or nitric acid to convert the calcium compounds in the fly ash into soluble calcium chloride or calcium nitrate, and separating to collect a calcium chloride or calcium nitrate solution and a decalcified fly ash filter cake; and concentrating the calcium chloride or calcium nitrate solution, and crystallizing to collect the calcium chloride or calcium nitrate product. The decalcified fly ash filter cake is sent to a subsequent procedure and subjected to acid hydrolysis and alkaline hydrolysis, the acid leach solution is used for preparing aluminum ammonium sulfate, aluminum oxide, cryolite, aluminum fluoride, high-purity iron oxide or iron oxide red, the water glass is used for preparing silica white other silicon compounds, and the decomposition residues are mixed with coal to be used as a boiler fuel.
Owner:河南省睿博环境工程技术有限公司

Method for producing water-soluble calcium nitrate dihydrate and phosphoric acid by decomposing phosphorite through nitric acid

The invention relates to a water-soluble calcium nitrate production method, and especially relates to a method for producing water-soluble calcium nitrate dihydrate and phosphoric acid by decomposing phosphorite through nitric acid. The method comprises the following steps: decomposing phosphorite by nitric acid to prepare an acidolysis liquid, carrying out freezing crystallization of the acidolysis liquid to separate a calcium nitrate crystal and phosphoric acid, dissolving the calcium nitrate crystal, carrying out deep impurity removal of the obtained calcium nitrate solution, carrying out evaporative concentration of the calcium nitrate solution, removing water from the obtained crystal, and carrying out ammonium nitrate wrapping granulation to prepare calcium nitrate dihydrate having a water solubility of not less than 99.9%. The method avoids the insufficient utilization of sulfate radicals residual in phosphogypsum of sulfuric acid methods when wet phosphoric acid is simultaneously produced, and the production of the high-added-value calcium nitrate dihydrate through the combination of nitrate radicals with calcium ions has the advantages of widening of the product chains of phosphoric acid or nitric phosphate enterprises, economic utilization of the nitrogen element in nitric acid, and improvement of the competition advantages of the enterprises.
Owner:云天化集团有限责任公司 +2

Method for extracting phosphate concentrate from phosphate tailings and cooperatively producing calcium ammonium nitrate and magnesium ammonium sulphate

The invention discloses a method for extracting phosphate concentrate from phosphate tailings and cooperatively producing calcium ammonium nitrate and magnesium ammonium sulphate. Phosphate tailings are calcined under high temperature, hot water is added into the calcined material for digestion treatment, an ammonium nitrate solution is added to the calcined material, the mixture is stirred, calcium is extracted under a certain temperature, calcium-containing leaching liquid and leaching residues are obtained, phosphate concentrate and magnesium-containing leaching liquid are obtained after magnesium is extracted from the leaching residues with an ammonium sulfate solution, and calcium ammonium nitrate and magnesium ammonium sulphate are obtained after the calcium-containing leaching liquid and the magnesium-containing leaching liquid are concentrated and dried. According to the method, phosphate concentrate, calcium ammonium nitrate and magnesium ammonium sulphate are prepared with phosphate tailings as the main raw materials, large-scale treatment can be carried out on the phosphate tailings, the problem that because phosphate tailings pile up in quantity, the phosphate tailings occupy a lot of land and pollute the environment is solved, and the obtained phosphate concentrate, calcium ammonium nitrate and magnesium ammonium sulphate can bring certain economic interests.
Owner:GUIZHOU RES INST OF CHEM IND
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