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761results about "Calcium/strontium/barium chlorides" patented technology

Salt, alkali and calcium combined cycle production technology by the use of well mineral salt

The invention relates to a salt, alkali and calcium combined cycle production technology by the use of well mineral salt. Based on the exploitation of brine from well mineral salt, the salt, alkali and calcium combined cycle production technology by the use of well mineral salt is a cycle production technology, which focuses on the technology for making alkali from brine by the ammonia-soda process and takes account of the vacuum salt-making (including the brine refinement) and calcium-making technologies. Alkali-making wastewater replaces most fresh water to be injected into a salt mine well to collect brine, and the obtained high-calcium brine is taken as the raw material of the salt and calcium (including liquid calcium) co-production as well as the raw material for preparing alkali and other chemical production raw materials, wherein the liquid calcium can be used to produce liquid salt; alkali-making waste residues are injected into an underground dissolution cavern, namely a salt cavern which is formed by the exploitation of brine from well mineral salt, thus accomplishing the combined cycle production technology in which alkali-making and salt-making technologies are closely related with materials. The produced wastes are used as resources or undergo a harmless treatment, thus protecting the environment. In addition, the utilization rate of sodium chloride in rock salt reaches 100%, achieving maximum efficiency.
Owner:江苏苏盐井神股份有限公司 +1

System for producing anhydrous calcium chloride by using industrial waste hydrochloric acid, and technology thereof

The invention discloses a system for producing anhydrous calcium chloride by using industrial waste hydrochloric acid, and a technology thereof. The reaction system of the technology is connected to an evaporation system through a refined calcium chloride conveying device, and the evaporation system, a calcium chloride forming machine, a drying system, a finished calcium chloride conveying device and a finished calcium chloride bunker are sequentially connected; the reaction system is mutually connected with a reaction tail gas treatment system; and the refined calcium chloride conveying device is also connected with a dry tail gas washing device, and the gas outlet end of the drying system is connected to the inlet end of the evaporation system through the dry tail gas washing device. The reaction tail gas washing device adopts a clean calcium chloride solution as an absorbent, and the hydrogen chloride absorbed calcium chloride solution returns to a calcium chloride reactor, so the concentration of hydrochloric acid is not diluted, and the energy consumption of the evaporation system is reduced; and the calcium chloride solution is used to wash dust-containing tail gas with calories to make dusts not exist in vented tail gas, and a circulating absorption solution absorbing the calories in the tail gas returns to the evaporation system and is reused, so the energy consumption of the evaporation system is reduced.
Owner:LIAOCHENG LUXI CHEM ENG DESIGN

Method for recovering and separating potassium salt and sodium salt from waste incineration fly ash

The invention relates to a method for recovering and separating a potassium salt and a sodium salt from waste incineration fly ash, which comprises the following steps of: extracting the potassium salt, the sodium salt and a calcium salt from the waste incineration fly ash by quartz sand and water to obtain high-concentration salt-containing water, separating the quartz sand from the fly ash, returning the quartz sand for continue use; adjusting the pH value of the high-concentration salt-containing water to 5-7 with an acid, and conducting evaporating and concentrating to obtain potassium andsodium mixed salts and a residual calcium chloride saturated solution; conducting flotation separation on the potassium and sodium mixed salts in saturated potassium chloride and sodium chloride solutions, and conducting filtration, so as to obtain a foam product, namely potassium chloride, and tailings slurry, namely sodium chloride; respectively conducting stirring washing on the potassium chloride and sodium chloride obtained by flotation through corresponding saturated salt water, and conducting filtering to obtain industrial grade potassium chloride and sodium chloride products, whereina washing solution is a saturated potassium chloride and sodium chloride mixed solution and is returned to the flotation procedure as a supplement solution of a flotation medium. The method effectively separates soluble salts in the fly ash: potassium chloride, sodium chloride and calcium chloride without decalcification to obtain high purity or industrial grade potassium chloride and sodium chloride products; and the efficiency-cost ratio of the treatment process is greatly improved.
Owner:RESEARCH INSTITUTE OF TSINGHUA UNIVERSITY IN SHENZHEN

Method for manufacturing industrial phosphoric acid, industrial ammonium phosphate and food-grade phosphoric acid from medium and low-grade phosphorite by one-step extraction of hydrochloric acid method

The invention discloses a method for manufacturing industrial phosphoric acid, industrial ammonium phosphate and food-grade phosphoric acid from medium and low-grade phosphorite by one-step extraction of a hydrochloric acid method. The method is characterized by comprising the following steps of: decomposing any phosphorite (the P2O5 of which is more than or equal to 6 weight percent) by using hydrochloric acid, preparing calcium chloride dihydrogen phosphate CaClH2PO4.H2O (P-01 for short), adding dilute phosphoric acid, pulping, filtering and purifying the P-01, pulping and dissolving the P-01 with hydrochloric acid, performing extraction by using tributyl phosphate, performing concentration and decolorization to obtain the industrial phosphoric acid, adding ammonia into the industrial phosphoric acid to obtain the industrial ammonium phosphate, or adding P2S5 into the concentrated industrial phosphoric acid to remove arsenic and heavy metal, performing decolorization by using active carbon and hydrogen peroxide and removing easily oxidized substances to reach the index requirement of the food-grade phosphoric acid.
Owner:上海协达精细化工研发有限公司

Method for synchronously recovering mercuric chloride, metal salt and active carbon in spent catalyst

The invention discloses a method for synchronously recovering mercuric chloride, metal salt and active carbon in a spent catalyst. The method is orderly implemented through the steps of spent catalyst drying, mercuric chloride recovery, complex perforation of active carbon and metal salt recovery, wherein mercuric chloride in the spent catalyst is recovered through destructive distillation in combination with condensation and aqueous solution absorption; deposits in the micropores of the active salt are displaced through hot water soaking in combination with bubbling by introducing air, thereby realizing the purpose of recovering the pores of the active carbon; and then the active carbon is recovered through drying and the metal salt is recovered through filtering; in the whole process, no pollutant is generated and discharged and the utilization rate of water is also extremely high; valuable elements in the spent catalyst are all recovered; and the valuable elements in the spent catalyst which is used in production previously and contains mercuric chloride, metal salt and active carbon are utilized, thereby achieving the purposes of solving the problems of scarce raw materials for new catalyst production and environmental pollution caused by inappropriate spent catalyst disposal; as a result, the method is obvious in economic benefit, environmental benefit and social benefit.
Owner:那风换

Tail-gas comprehensive utilization method in mercuric chloride catalyst

The invention discloses a comprehensive utilization method for tail gas in the production of a mercuric chloride catalyst. The method comprises the following steps: the temperature of tail gas coming from a dryer in the production of the mercuric chloride catalyst is between 90 and 105 DEG C; the discharge temperature of the tail gas of which the waste heat is recovered is controlled to be not higher than 45 DEG C through a heat exchange device serially connected with the back of the dryer; the tail gas of which the waste heat is recovered and the tail gas which comes from the other processes in the production of the mercuric chloride catalyst are mixed together, and enters from the lower part of a filler countercurrent gas-washing tower; mixture liquid of BaCl2 and Ba(OH)2 is continuously sprayed down from the top of the filler tower to perform countercurrent gas washing; liquid after washing flows into an anticorrosion circulation tank on the bottom of the tower; washing liquid is continuously circulated and sprayed under the action of a circulating anticorrosion pump; and the tail gas after washing is adsorbed to remove foam through dry activated carbon in an activated-carbon device for adsorbing and removing foam, so as to obtain the tail gas reaching discharge standard. The method can ensure that the tail gas after purification treatment reaches the discharge standard, and both solid waste and liquid waste generated can be directly used for producing the mercuric chloride catalyst, so as to save energy and reduce consumption.
Owner:WANSHAN HONGJING MERCURY

Method for producing triple superphosphate and co-producing calcium chloride by middle-low grade phosphate rock

InactiveCN101456545AOvercoming the Prejudice of Not being able to Produce TSPLow grade requirementsCalcium/strontium/barium chloridesPhosphorus compoundsPhosphoric acidEvaporation
The invention relates to a method for producing concentrated superphosphate and coproducing calcium chloride through medium and low grade phosphorite, which comprises: firstly, using hydrochloric acid to perform acidolysis on powdered rock phosphate 1 which is medium and low grade powdered rock phosphate with the particle diameter of less than or equal to 1,165 mu m; secondly, performing partial extraction, namely performing countercurrent extraction on an acidolysis solution obtained in the first step, wherein P2O5 entering an organic phase accounts for 50 to 90 percent of the total mass of P2O5; thirdly, performing washing and back-extraction on the organic phase in the second step, and concentrating a back extract acid to prepare concentrated phosphoric acid; fourthly, performing neutralization reaction on a residual aqueous phase in the second step and lime cream, performing solid-liquid separation after the reaction is over, washing filter cakes to obtain calcium hydrophosphate, and performing evaporation, concentration and drying on filtrate to obtain the calcium chloride; and fifthly, using the concentrated phosphoric acid obtained in the third step to perform acidolysis on powdered rock phosphate 2 which is medium and low grade powdered rock phosphate with the particle diameter of less than or equal to 74 mu m, adding the calcium hydrophosphate prepared in the fourth step for reaction after the acidolysis reaction is over, and drying reaction products to obtain the concentrated superphosphate after the reaction is over.
Owner:SICHUAN UNIV

Method for separatingcalcium chloride and sodium chloride in ammonia distillation waste clear solution with nanofiltration technology and application of production by the method

The invention discloses a method for separating calcium chloride and sodium chloride in ammonia distillation waste clear liquid by using nanofiltration membrane technology and application of product thereof, relating to a chemical field of preparing calcined soda by using an ammonia-soda process or a union alkali method; the method comprises that the ammonia distillation waste clear liquid is separated through a nanofiltration membrane filtering equipment to obtain concentrated solution mainly containing calcium chloride solution and penetrant mainly containing sodium chloride solution. The penetrant can be recycled for salt dissolving technology. The concentrated solution containing high-concentration calcium chloride can be used for producing calcium chloride product by adopting methods of evaporation and crystallization. The method leaves out processes of repeated sunning, heating and vacuum pumping, and most moisture can be reused; the invention reduces energy consumption and area occupation, saves a large amount of water resource, which create good condition for technology of subsequent salt dissolving and the calcium chloride production.
Owner:王晓璐

Method for preparing ammonia water and calcium chloride solution through decomposition recovery of ammonium chloride waste liquor

The invention discloses a method for preparing ammonia water and calcium chloride solution through the decomposition recovery of ammonium chloride waste liquor. The method comprises the following steps: the waste liquor is pretreated, and ammonium chloride and calcium oxide or calcium hydroxide powder is added into the pretreated ammonium chloride waste liquor; ammonia is distilled from the treated ammonium chloride waste liquor and is transferred into an ammonia absorption tower after being condensed, and a reaction liquid flows out from the bottom of a distillation tower; ammonia is absorbed from the condensed ammonia in the absorption tower by using desalted water, and the tail gas is exhausted after residual ammonia is washed by a tail gas washing tower; reaction liquid out of the bottom of the distillation tower is subjected to flash vaporization for recycling the energy and then is transferred into a clarifying barrel, and the clarified calcium chloride supernatant is used as the target product. According to the invention, the method is particularly suitable for the transformation of ammonium chloride wastewater treatment technology of enterprises in the existing rare earth industry, potassium carbonate industry and baking soda industry, and is simple in process; the ammonia is recycled by using desalted water through multi-stage absorption, and the recovery rate is up to 99%; the high-concentration calcium chloride solution can be used for producing calcium chloride products and the products can be recycled so as to have better economic benefits.
Owner:江苏大江干燥设备有限公司

Preparation and comprehensive utilization method of magnesium bicarbonate solution

The invention relates to a preparation and comprehensive utilization method of a magnesium bicarbonate solution. The method is used to prepare the magnesium bicarbonate solution used for deposition, crystallization and recovery of rare earth ions, and comprehensive recovery of calcium-compound products and magnesium-compound products by taking dolomite as a raw material. The method specifically comprises: roasting dolomite to obtain a powder containing calcium oxide and magnesium oxide, directly mixing with a magnesium chloride solution for digestion and alkali transformation at the same time to prepare a magnesium hydroxide secondary-product and a calcium compound secondary-product, and further to realize effective separation of calcium and magnesium; performing slurry mixing on magnesium hydroxide, introducing carbon dioxide gas for a carbonization reaction to prepare the magnesium bicarbonate solution; applying obtained magnesium bicarbonate to deposition and crystallization of the rare earth ions to produce rare-earth carbonate or rare-earth oxide products; and recycling one part of the filtrate to prepare magnesium bicarbonate, and evaporating one part of the filtrate for crystallization to produce the magnesium compound product.
Owner:GRIREM ADVANCED MATERIALS CO LTD

Pollution-free processing method and system for tailings generated by chlorination-process titanium extraction

The invention provides a pollution-free processing method and system for tailings generated by chlorination-process titanium extraction. The method comprises the following steps: cooling high-temperature tailings generated by chlorination-process titanium extraction by using cold air to obtain hot air and hot tailings with temperature of 120-150 DEG C; orderly carrying out vacuum washing and filtering on the hot tailings for more than twice, wherein every time vacuum washing and filtering is carried out, the tailings are mixed and soaked with a scrubbing solution and then filtrate and washed tailings can be obtained through filtering, and in addition the filtrate in the last vacuum washing and filtering process is used as the scrubbing solution in the previous vacuum washing and filtering process; concentrating the filtrate obtained in the first vacuum washing and filtering process by using hot air, so as to obtain a concentrated solution; and carrying out spray drying on the concentrated solution to obtain calcium chloride. The system comprises a cooling unit, a vacuum washing and filtering unit, a concentrating unit, a spray drying unit and a cold air supply unit. The tailings which can be applied to the industries such as building materials and can meet the pollution-free requirements can be obtained and cyclic utilization of the scrubbing solution can be achieved; moreover, the pollution-free processing method and system can be effectively connected with the process of preparing titanium tetrachloride by the chlorination process.
Owner:PANZHIHUA IRON & STEEL RES INST OF PANGANG GROUP

System and methods for removing minerals from a brine using electrodialysis

A method includes treating a first brine stream including a plurality of minerals with an anti-scalant to produce a treated brine. The first brine stream is provided by a wastewater treatment system. The method also includes directing the treated brine to a first nanofiltration (NF) system disposed downstream from and fluidly coupled to the wastewater treatment system, generating a first NF permeate stream and a first NF non-permeate stream from the treated brine in the first NF system, directing the first NF non-permeate stream to a mineral removal system disposed downstream from and fluidly coupled to the first NF system, and removing the plurality of minerals from the first NF non-permeate stream to generate a first overflow stream in the mineral removal system. The first overflow stream comprises at least a portion of the plurality of minerals. The method also includes routing a first portion of the first overflow stream to a hydrochloric acid (HCl) and sodium hydroxide (NaOH) production system disposed downstream from and fluidly coupled to the mineral removal system. The HCl and NaOH production system includes a second NF system that may receive the first portion of the first overflow stream and may generate a second brine stream from the first portion of the first overflow stream. The method further includes directing the second brine stream to a first electrodialysis (ED) system disposed within the HCl and NaOH production system and fluidly coupled to the second NF system. The first ED system may generate HCl and NaOH from the second brine stream.
Owner:ENVIRO WATER MINERALS COMPANY
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