At above-mentioned situation, the invention provides a kind of according to ammonium nitrate, Repone K and saltpetre, ammonium chloride quaternary salt-water system phasor, select reasonable process conditions, the composition of control reaction feed liquid, make it be in the crystallizing field of saltpetre, ammonium chloride successively, to reach the purpose of separating saltpetre and ammonium chloride, mother liquor restock Repone K and ammonium nitrate behind separation saltpetre and the ammonium chloride, carry out potassium nitrate crystal and ammonium chloride crystals, and the replacement(metathesis)reaction that recycles of feed liquid is produced the method for saltpetre and ammonium chloride. The reaction takes place in a boiling solution. Aqueous ammonium nitrate and aqueous potassium chloride … The present invention adopts under 110 ℃ temperature, with ammonium nitrate and Repone K, according to ammonium ion and chlorion be 1: 2 ratio water-soluble after, continue to add Repone K and water, heating while stirring, reach the hypersaturated state of saltpetre, stopping heating making solution ℃ separate out potassium nitrate crystals at vacuum cooling crystallizer internal cooling to 38, the whizzer of putting into the liner filter cloth gets thick saltpetre, isolating mother liquor I is a saltpetre, the common saturation point of another of ammonium chloride, thick saltpetre is got finished product saltpetre with the cold water washing after drying, in mother liquor I and washings, add ammonium nitrate, adjust the state of saturation that strength of solution reaches ammonium chloride, in vacuum concentrating apparatus, carry out negative pressure evaporation, the centrifugal ammonium chloride of separating out that leaches, obtain the solid ammonium chloride product, the scheme of feed liquid circulating reaction has overcome higherly and resource is nervous with the SODIUMNITRATE price, and the byproduct sodium chloride utility value is low, open type direct evaporation container, consume a large amount of steam, thermo-efficiency is very low, and the ion exchange method equipment requirements is higher, need to use the titanium material, Ti-Mo-Ni alloy or other synthetic materials, defect of high cost. It is also found around some types of volcanic vents. 3+KCI→KNO The heat of reaction is utilized for evaporation and 80–83% ammonium nitrate solution is obtained. Potassium Nitrate is insoluble in ethanol while Calcium Chloride and Ammonium Chloride are somewhat soluble. The reaction proceeds as follows: KOH + NH4Cl → KCl + NH4OH It is a double replacement reaction, however upon heating will evolve ammonia gas (NH3). What is happening in terms of chemistry is a double displacement reaction is taking place between the potassium chloride and ammonium nitrate producing potassium nitrate and ammonium chloride: KCl + NH 4 NO 3 → KNO 3 + NH 4 Cl. 6. magnesium nitrate reacts in solution with potassium hydroxide to yield a magnesium hydroxide precipitate and soluble potassium nitrate magnesium nitrate + potassium hydroxide magnesium hydroxide + potassium nitrate Mg(NO 3) 2 … While there is no difference between the chloride, sulfate and nitrate salts of potassium insofar as the potassium ion is concerned, there may be a difference on plant response due to the associated ion. Anonymous. 3, mother liquor II evaporating concentration process system lock, continuously-running, operational condition is improved, the level of automation height. BPR regulation aims to improve the functioning of the biocidal products market in the EU, while ensuring a high level of protection for humans and the environment. Method for preparing potassium nitrate and ammonium chloride employing double decomposition reaction, Application filed by 湖南丹化农资有限公司, 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Method for producing sodium chromate from potassium chromate, Waste steam heat recycling method in potassium nitrate production, A method of production of potassium nitrate by electrodialysis and apparatus for making the same, Continuous triple-effect falling-film concentration and vacuum crystallization system and method in potassium nitrate production through double-decomposition method, System and method for producing potassium nitrate by adopting continuous double-decomposition method, Ammonium chloride forced circulating continuous triple-effect concentration and vacuum crystallization system and ammonium chloride forced circulating continuous triple-effect concentration and vacuum crystallization process in production of potassium nitrate by double decomposition method, Wastewater recycling system and wastewater recycling method in coproduction of potassium nitrate and ammonium chloride, Control method for granularity of potassium nitrate product produced through double decomposition, Fully-automatic rapid separation and washing processing device for potassium nitrate, A kind of method being produced high-quality potassium nitrate with ammonium nitrate double decomposition circulation process by potassium chloride, Method for production of potassium nitrate and co-production of potassium ammonium chloride by non-cyclic double decomposition, A kind of preparation method of potassium nitrate, The high yield preparation method of potassium nitrate, A kind of impurity-removing method for the waste nitric acid potassium producing chemically reinforced glass, The joint process of saltpetre and ammonium chloride, Process for preparing potassium nitrate by double decomposition method, The continuous triple effect falling film concentration of ammonium chloride, vacuum crystallization system and method in a kind of double decomposition Production of Potassium Nitrate, A kind of system and method for continous way preparing potassium nitrate by means of double decomposition, Concentrated, the vacuum crystallization system of the continuous triple effect of ammonium chloride pump circulation and technique in a kind of double decomposition Production of Potassium Nitrate, A kind of method of acyclic preparing potassium nitrate by means of double decomposition combined producting ammonium chloride potassium, A kind of recovery and treatment method of high-salt wastewater, Method and System for Quickly Extracting Lithium Carbonate from Saline Lake Water, Application of MVR (mechanical vapor recompression) crystallizing evaporator in sodium sulfate and sodium chloride separation technology, Multifunctional multiple-effect automatic continuous evaporative crystallization technique and crystallization device, A kind of efficient method preparing cyanamide solution, Method for directly preparing battery grade lithium carbonate from salt lake brine with high magnesium-to-lithium ratio, Method for extracting amber acid in fermentation liquor by cationic resin exchange, Method for recovery utilization of mother solution hydrochloric acid for ADC foaming agent production, A kind of recovery system and recovery process for reclaiming salt from desulfurization wastewater, A kind of function of mechanical steam recompression continuous evaporative crystallization system and method, Production process of lithium hydroxide monohydrate, A kind of preparation method of LITHIUM BATTERY lithium hydroxide, Method for preparing electronic grade phosphoric acid through liquid membrane crystallization, Process method for recovering ammonium chloride and sodium chloride from waste water containing ammonium chloride and sodium chloride, Process for preparing calcium chloride solution by utilizing ammonia soda filtration mother liquor, Production method for co-production of mirabilite and salt and production device thereof, A kind of method and its device for preparing methionine and reclaiming accessory substance carbon dioxide, Crystallization treatment method and device of high salt wastewater, Method for processing battery-level lithium carbonate mother liquor, Evaporative crystallization is adopted to realize the device of Coal Chemical Industry height strong brine recycling, A kind of be raw material production barium chloride with witherite technique, A kind of crystallization treatment device of high slat-containing wastewater, A kind of preparation method of potassium sulfate, A kind of beta naphthal high-concentration organic substance wastewater process for reclaiming with high salt and system, Entry into force of request for substantive examination, Termination of patent right due to non-payment of annual fee, Termination of patent right or utility model.

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