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Method for directly producing potassium nitrate end product from complex nitrate bittern

A technology of nitrate and potassium nitrate, applied in the directions of alkali metal nitrate preparation and energy input, can solve the problems of undiscovered high-quality potassium nitrate finished product, large water consumption, large potassium loss, etc., and achieves white color, energy efficiency and utilization rate. High, reduce potassium loss effect

Inactive Publication Date: 2013-08-14
CHANGSHA DESIGN & RES INST OF CHEM IND MIN
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The combination of the two is theoretically feasible as a method for preparing finished product potassium nitrate from natural complex nitrate-type brine, but the route is too long, the loss of potassium is relatively large, and the semi-finished product needs to continue to dissolve before it can be mixed with potassium to produce potassium nitrate, and the water consumption is also relatively high. Big
Through literature research, no method has been found to directly extract high-quality potassium nitrate products from the liquid phase of salt lake brine

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0022] The brine composition of a certain salt lake is K + 0.41%, Mg 2+ 0.30%, Ca 2+ 0.048%, Na + 10.19%, Cl - 15.57%, SO 4 2- 1.64%, NO 3 2- 0.64%, with this brine as raw material:

[0023] (1) Import the brine into the salt field, use solar energy to evaporate and crystallize the brine in sections, control the mass fraction of sulfuric acid radicals in the brine discharged from the frozen nitric acid pool to be 0.05%, and the content of potassium ions in the sodium salt pool to be 4.3% by mass; (2) import the brine into Settling tank, add sodium hydroxide at 50g per cubic meter of halogen, stir for 2 hours, heat to 55°C, add sodium carbonate at 2g per cubic meter of halogen, and settle for 12 hours; (3) Halogen formation and steps after removing impurities (6) The second-effect high-temperature salt discharge is brine according to the mass ratio: salt discharge = 4:1 countercurrent mixing, and the residual potassium in the high-temperature discharge salt is wa...

Embodiment 2

[0026] The brine composition of a certain salt lake is K + 0.35%, Mg 2+ 0.36%, Ca 2+ 0.04%, Na + 10.49%, Cl- 14.96%, SO 4 2- 2.34%, NO 3 2- 1.82%, with this brine as raw material:

[0027] (1) Import the brine into the salt field, use solar energy to evaporate and crystallize the brine in stages, control the mass fraction of sulfate radicals in the brine discharged from the frozen nitrification tank to be 0.4%, and the content of potassium ions in the brine to be 4.1% by mass; (2) Import the brine into the sedimentation tank , add sodium hydroxide by 50g per cubic meter of halogenation, stir for 2 hours, heat to 60°C, add sodium carbonate by 3g per cubic meter of halogenation, and settle for 18 hours; (3) halogenation and step (6) after removing impurities ) II effect high-temperature desalting according to the mass ratio into brine: desalting = 4.1:1 countercurrent mixing, using brine to wash out the residual potassium in the high-temperature desalting, so that ...

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PUM

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Abstract

The invention discloses a method for directly producing a potassium nitrate end product from complex nitrate bittern. The method comprises the following steps of 1, setting a mirabilite freezing tank, a primary sodium salt tank and a secondary sodium salt tank, feeding bittern into the mirabilite freezing tank, the primary sodium salt tank and the secondary sodium salt tank, and carrying out fractional crystallization and evaporation to obtain deposited halogens from a salt pan, 2, precipitating Ca<2+> and Mg<2+> impurities of the deposited halogens respectively through caustic soda and soda ash, 3, mixing the impurity-free deposited halogens and a salt which is discharged by an effect II evaporation unit and is obtained by a step 6, removing potassium of the removed salt, and carrying out centrifugal separation, 4, feeding washing liquid into a secondary reaction tank, and adding potassium chloride into the secondary reaction tank for a stirring reaction to obtain a transformed mother solution, 5, mixing the transformed mother solution and cold-separated liquid obtained by the step 8, 6, after halogen mixing, feeding the transformed mother solution mixture into a four-effect evaporation system, carrying out step-by-step evaporation precipitation to remove sodium salts, discharging the salt-free evaporated mother solution from an effect I evaporation unit, and the salt from the effect II evaporation unit, 7, after the salt-free evaporated mother solution discharged from the effect I evaporation unit enters into a three-level series vacuum cold separation system, and carrying out step-by-step crystallization salt precipitation, and 8, carrying out centrifugal separation of the cold-separated liquid, and carrying out solid washing and drying. The potassium nitrate end product prepared by the method has KNO3 content great than or equal to 98%.

Description

technical field [0001] The present invention relates to a kind of production method of industrial potassium nitrate, especially relate to a kind of using + 、Na + , Mg 2+ , Ca 2+ , SO 4 2- , Cl - , NO 3- A method for the direct production of potassium nitrate from complex nitrate-type brines by plasma. Background technique [0002] At present, the methods for industrial production of potassium nitrate mainly include the following categories: (1) ion exchange method, such as directly dissolving and recrystallizing the finished product sodium nitrate and potassium chloride; (2) double decomposition method: such as application number 200510094223 The Chinese patent of .X discloses a method for preparing potassium nitrate by double decomposition method. The raw material potassium chloride, ammonium nitrate and process water are mixed and cooled to obtain potassium nitrate, and the mother liquor is evaporated and concentrated, then cooled and crystallized to obtain ammoniu...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01D9/08
CPCY02P20/133
Inventor 冯跃华刘小力杨能红彭建忠
Owner CHANGSHA DESIGN & RES INST OF CHEM IND MIN