CN1557708A - Comprehensive process for recovering and treating indigo blue powder waste slag - Google Patents
Comprehensive process for recovering and treating indigo blue powder waste slag Download PDFInfo
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Abstract
The comprehensive indigo powder waste gangue slag recovering treatment process includes heating the mixture of waste gangue slag and water in a reactor to 4-80 deg.c for the waste gangue slag to dissolve fully; centrifugally separating to eliminate dreg and create mother liquid A; cooling mother liquid an in a crystallizing tank for 12-30 hr; press filtering or centrifuging to separate crystal as mixture of crystal carbonate and natron from crystallized liquid A; and calcining the crystal mixture to obtain anhydrous sodium carbonate. The said process can recover sodium hydroxide, potassium hydroxide, potassium carbonate, potassium salt and sodium carbonate in low cost and high yield.
Description
Technical Field
The invention relates to a method for extracting substances from waste gangue, in particular to a comprehensive recovery treatment process for indigo powder and waste gangue.
Background
At present, waste gangue slag generated in the production of indigo powder contains: sodium hydroxide, potassium carbonate, potassium salt and more than 40% of sodium carbonate. Because the waste gangue contains a lot of raw materials which are difficult to extract, the sodium carbonate is unfavorable for recycling and utilizing potassium hydroxide and sylvite, and the waste gangue is generally discarded or sold at low price, so that the expensive raw materials in the waste gangue cannot be fully utilized.
Disclosure of Invention
The invention mainly aims to solve the problem of extracting raw materials from waste gangue generated in the production of indigo blue powder, and provides a comprehensive recovery treatment process for the indigo blue powder waste gangue, which can fully recover substances such as sodium carbonate, potassium hydroxide, potassium salt and the like from the indigo blue powder waste gangue.
The technical scheme adopted by the invention for solving the technical problems is as follows:
adding 400 portions of waste slag and 700 portions of water at the temperature of between 60 and 80 ℃ into a melting pot, keeping the specific gravity of the materials at 1.31 to 1.38, preserving the heat for 10 to 30 minutes, fully stirring the materials, heating the materials to between 40 and 80 ℃, and centrifugally separating the materials to remove slag to generate a mother solution after the waste slag is fully dissolved. The mother liquid is injected into a crystallization tank for cooling crystallization, and the temperature is kept at 8-12 ℃ for cooling crystallization for 30-48 hours.
Weighing 400 portions of waste rock slag and 700 portions of water, placing the waste rock slag and 500 portions ofthe waste rock slag into a melting pot, adding 450 portions of water into the melting pot, starting a stirrer to fully stir, heating by burning fire, raising the temperature, pumping the waste rock slag into a centrifugal machine to centrifuge, and centrifuging to obtain mother liquor. The waste residue in the centrifuge drum can be discarded or used for other purposes, and the solution A is put into a crystallization tank. Crystallizing at natural temperature for more than 30-48 hr in late autumn, winter and early spring, indirectly cooling with 10 deg.C chilled water via coiled pipe in crystallizing tank for crystallizing for 12 hr, and press filtering or centrifuging to separate crystal slurry.
And (3) separating crystals from the mother liquor obtained by cooling crystallization by adopting a filter pressing or centrifuging mode, wherein the separated mixed crystals are sodium carbonate with crystal water, and the mixed crystals are calcined to prepare anhydrous sodium carbonate.
The filter pressing liquid is mother liquid, and the sodium carbonate with crystal water obtained by filter pressing is calcined to obtain the anhydrous sodium carbonate.
And (3) separating mother liquor of the mixed crystals to obtain solution A, injecting the solution A into a lime slaking pot, heating to 90-120 ℃, adding 90-120 parts of lime or 230 parts of 280-plus of barium hydroxide, fully stirring, keeping the temperature at 100 ℃, heating for 30-60 minutes, cooling to 70 ℃, performing pressure filtration, separating and deslagging to obtain solution B, wherein the solution B is mixed gangue solution of potassium hydroxide and sodium hydroxide.
A1Pumping the solution into lime slaking pot, heating to 90-120 deg.C. Opening the stirrer to stir, and adding 90-120 parts of the mixtureLime or barium hydroxide. Keeping the temperature in a lime slaking pot at 100 ℃ for slaking for1 hour. The barium hydroxide is adopted for the gram reaction and the reaction time is 30 minutes. Taking out of the pot and performing filter pressing, wherein the filter pressing liquid is A, and filter pressing residues are used for other purposes. A. the2The liquid is separated potassium hydroxide and sodium hydroxide waste rock liquid containing secondary recoveryThe collected sylvite can be used in sylvite plants.
Adding 400 portions of waste slag and 700 portions of water and 450 portions of waste slag into a melting pot, fully stirring, heating to 40-80 ℃, melting while concentrating, and crystallizing and precipitating sodium carbonate in waste slag liquid.
Evaporating to remove 25% of water, stopping heating, centrifuging to remove residue to obtain mother liquid A, and separating to obtain crystal B.
Weighing 400 portions of waste rock slag and 700 portions of water, placing the waste rock slag and the water into a melting pot, adding 450 portions of waste rock slag and the water, starting a stirrer for stirring, heating to 40-80 ℃ by burning, melting while concentrating, and crystallizing and precipitating sodium carbonate in the waste rock liquid. And (3) evaporating the water with the total volume of 1/4, stopping heating, pumping into a centrifuge by a pump for centrifugation, wherein the centrifuged mother liquor is solution A, and the crystals in the centrifuge drum can be used for other purposes.
Injecting the liquid B into a tank, adding 20% of water into the liquid B, fully stirring, performing centrifugal separation, injecting the separated separation liquid and the liquid A into a curdling pot, injecting the centrifuged crystals into a melting tank, and adding water to dissolve the crystals to prepare 30% waste rock liquid.
Putting the B crystal into iron pot, adding 1/10 water, stirring for five minutes, filtering, preferably centrifuging. And putting the centrifugal crystals and the liquid A into a melting tank, adding water to dissolve the centrifugal crystals and the liquid A into 30% waste rock liquid, and then directly preparing a crystallized product.
Adding 90-120 parts of lime or 230-280 parts of barium hydroxide into a retort, fully stirring and heating to 90-120 ℃, keeping the temperature at 100 ℃ for 30 minutes, taking out of the retort, performing pressure filtration and separation, wherein the pressure filtrate is mixed waste rock liquid of potassium hydroxide and sodium hydroxide, namely A1The solution can be repeatedly crystallized for improving the purification of the potassium hydroxide and the sodium hydroxide, and the filter pressing residue is calcium hydroxide g for other purposes.
Pumping the solution A into a lime kettle of 90-120 parts or a barium hydroxide kettle of 230-280 parts by a pump, starting a stirrer for stirring, heating to 90-120 ℃ by burning fire, keeping the temperature in the kettle at 100 ℃ for about 30 minutes, taking out of the kettle, performing pressure filtration and separation.
The press filtrate is A1The hydraulic filter residue is liquid B, the liquid B is packaged for sodium sulfite production plants, and A1The liquid is filled into a waste rock storage tank for a sylvite plant. A. the1The liquid is separated and recycled potassium carbonate and sodium hydroxide,and can be used for potassium salt manufacturers. To obtain potassium hydroxide of higher purification quality, A is added1The liquid is repeatedly crystallized by the method, and the quality is improved once every time the liquid is repeatedly crystallized.
And (3) injecting the mother liquor, namely the solution A, of which the mixed crystals are separated into a boiling pot, heating and concentrating, cooling when the volume of the mother liquor is 6/10-8/10 of the volume of the original solution A, injecting the concentrated solution into a crystallization tank, keeping the temperature at 12-18 ℃ for crystallization for 30-48 hours, performing filter pressing separation, wherein the centrifuged solution A is potassium hydroxide, sylvite, potassium carbonate and sodium hydroxide, and the centrifuged crystal is sodium carbonate.
Although the waste rock solution A contains potassium carbonate and sodium carbonate, the potassium salt is also reacted during the production, and simultaneously contains a certain amount of potassium hydroxide and sodium hydroxide, so that the potassium salt can be completely produced, and a certain amount of potassium salt can be recovered. In order to increase the content of potassium hydroxide and reduce sodium hydroxide, a secondary crystallization method can be adopted.
Putting the solution A into a decocting pot, heating, concentrating, stopping heating when the volume of the solution A is 6/10-8/10 of the volume of the original solution A, pouring the concentrated solution into a crystallizing tank, crystallizing at 12-18 ℃ for 30-48 hours, and performing filter pressing, wherein the mother solution is C waste rock solution for a potassium salt factory to replace KOH waste rock solution. The press-filtered crystals are also sodium carbonate containing water of crystallization.
Injecting the separated mixedwaste rock liquid B of potassium hydroxide and sodium hydroxide into a carbon dioxide absorption pool, releasing carbon dioxide into the dilute waste rock liquid in the pool through an arrangement pipeline at the bottom of the pool, and injecting the reacted dilute waste rock liquid into a heating pot for heating and concentrating after full reaction.
The dilute waste water separated from the production of the indigo blue powder is injected into Co2In the absorption tank (the bottom of the tank is provided with discharge Co2Tube array) of the flue gas introduction start, and the flue gas containing (Co) is utilized2) And (3) reacting the carbon dioxide with sodium hydroxide in the dilute waste water to react potassium hydroxide to generate sodium carbonate and potassium carbonate. Is beneficial to the complete separation of sodium salt and sodium gangue.
When the sodium hydroxide and the potassium hydroxide completely react with the carbon dioxide, the solution is determined by an analysis means, the solution is pumped into a heating pot by a pump, the heating and the concentration are carried out, when the content of the gangue is concentrated to 50 percent, the solution is determined by an assay means, the solution is pumped into a filter press by the pump to carry out filter pressing, the filtrate is solution A, and the crystal which is filtered by the filter pressing is crystal B.
Performing pressure filtration separation when the concentration is 50%, separating filtrate to obtain C liquid, and separating crystal to obtain C crystal1And (4) liquid.
C is to be1Injecting the crystal and water into a meltingpot at a ratio of 1: 1-1: 1.2, heating to 30-80 ℃, injecting into a crystallization tank for cooling crystallization after full dissolution, keeping the temperature at 8-12 ℃ for natural crystallization for 30-48 hours, and performing centrifugal separation in a centrifugal mode, wherein the centrifuged mother liquor is potassium carbonate liquor, and the centrifuged crystal is sodium carbonate.
C1The crystal and water are put into a melting pot according to the proportion of 1: 1-1: 1.2, heated to 30-80 ℃ for dissolution and then put into a crystallization tank, and the temperature is kept at 8-12 ℃ for natural crystallization for 30-48 hours. If the natural temperature is higher than 15 ℃, the cooling pipe in the crystallization tank is cooled by using the freezing water with the temperature of 10 ℃. Crystallizing for 8-20 h, discharging from the tank, pumping into a centrifuge, and centrifuging to obtain mother liquor as potassium carbonate solution. Centrifuged outThe crystals are sodium carbonate.
A and A1Separating waste rock liquid containing potassium carbonate and potassium salt, and supplying the waste rock liquid to a potassium salt factory for use. B is1The crystal can be used as a crystallization finished product, and can also be dissolved into gangue water by water to be used as a product.
The invention relates to a comprehensive recovery treatment process for indigo blue powder waste gangue. The process design is reasonable, the preparation method is simple and feasible, raw materials of sodium hydroxide, potassium carbonate, potassium salt and sodium carbonate can be fully recovered from the indigo powder waste slag, the preparation cost is low, and the effect is high.
Detailed Description
Example 1 (high metering)
Adding 600kg of waste rock residues and 700kg of water with the temperature of 60-80 ℃ into a melting pot by the weight of 1kg of the waste rock residues and the water, keeping the specific gravity at 1.38, preserving the heat for 10-30 minutes, fully stirring, heating to 40-80 ℃, and after the waste rock residues are fully dissolved, carrying out centrifugal separation and deslagging to generate mother liquor.
The mother liquid is injected into a crystallization tank for cooling crystallization, and the temperature is kept at 8-12 ℃ for cooling crystallization for 30-48 hours.
And (3) carrying out crystal separation on the cooled and crystallized mother liquor by adopting a filter pressing or centrifuging mode, wherein the separated crystal is sodium carbonate with crystal water, and the crystal is calcined to prepare anhydrous sodium carbonate.
Separating the mother liquor of the mixed crystals to obtain solution A, injecting the solution A into a lime slaking pot, heating to 90-120 ℃, adding 120kg of lime, fully stirring, keeping the temperature at 100 ℃, heating for 30-60 minutes, cooling to 70 ℃, performing pressure filtration and separation to remove residues to generate solution B, wherein the solution B is the mixed waste liquor of potassium hydroxide and sodium hydroxide, and is shown in figure 1.
Example 2 (Low metering)
Adding 400kg of waste rock residues and 450kg of water with the temperature of 60-80 ℃ into a melting pot by the weight of 1kg of the waste rock residues and the water, keeping the specific gravity at 1.31, preserving the temperature for 10-30 minutes, fully stirring, heating to 40-80 ℃, and after the waste rock residues are fully dissolved, carrying out centrifugal separation and deslagging to generate mother liquor.
The mother liquid isinjected into a crystallization tank for cooling crystallization, and the temperature is kept at 8-12 ℃ for cooling crystallization for 30-48 hours.
And (3) carrying out crystal separation on the cooled and crystallized mother liquor by adopting a filter pressing or centrifuging mode, wherein the separated crystal is sodium carbonate with crystal water, and the crystal is calcined to prepare anhydrous sodium carbonate.
And (3) separating a mother liquor of the crystals to obtain a liquor A, injecting the liquor A into a lime slaking pot, heating to 90-120 ℃, adding 90kg of lime, fully stirring, keeping the temperature at 100 ℃, heating for 30-60 minutes, cooling to 70 ℃, performing pressure filtration, separating and removing residues to generate a liquor B, wherein the liquor B is a mixed waste liquor of potassium hydroxide and sodium hydroxide, and is shown in figure 1.
Example 3 (Medium gauge)
Adding 500kf of waste gangue and 575kg of water with the temperature of 60-80 ℃ into a melting pot by the weight of 1kg of each part, keeping the specific gravity of 1.345, preserving the temperature for 10-30 minutes, fully stirring, heating to 40-80 ℃, after the waste gangue is fully dissolved, carrying out centrifugal separation and deslagging to generate mother liquor.
The mother liquid is injected into a crystallization tank for cooling crystallization, and the temperature is kept at 8-12 ℃ for cooling crystallization for 30-48 hours.
And (3) carrying out crystal separation on the cooled and crystallized mother liquor by adopting a filter pressing or centrifuging mode, wherein the separated crystal is sodium carbonate with crystal water, and the crystal is calcined to prepare anhydrous sodium carbonate.
And (3) separating a mother solution of the mixed crystals to obtain a solution A, injecting the solution A into a lime slaking pot, heating to 90-120 ℃, adding 105kg of lime, fully stirring, keeping the temperature at 100 ℃, heating for 30-60 minutes, cooling to 70 ℃, performing pressure filtration, separating and removing residues to generate a solution B, wherein the solution B is a mixed waste solution of potassium hydroxide and sodium hydroxide, and is shown in figure 1.
Example 4 (high metering)
Adding 600kg of waste rock residues and 700kg of water with the temperature of 60-80 ℃ into a melting pot by the weight of 1kg of the waste rock residues and the water, keeping the specific gravity at 1.38, preserving the heat for 10-30 minutes, fully stirring, heating to 40-80 ℃, and after the waste rock residues are fully dissolved, carrying out centrifugal separation and deslagging to generate mother liquor.
The mother liquid is injected into a crystallization tank for cooling crystallization, and the temperature is kept at 8-12 ℃ for cooling crystallization for 30-48 hours.
And (3) carrying out crystal separation on the cooled and crystallized mother liquor by adopting a filter pressing or centrifuging mode, wherein the separated crystal is sodium carbonate with crystal water, and the crystal is calcined to prepare anhydrous sodium carbonate.
And (3) separating a mother liquor of the crystals to obtain a liquor A, injecting the liquor A into a lime slaking pot, heating to 90-120 ℃, adding 280kg of barium hydroxide, fully stirring, keeping the temperature at 100 ℃, heating for 30-60 minutes, cooling to 70 ℃, performing pressure filtration, separating and removing residues to generate a liquor B, wherein the liquor B is a mixed waste liquor of potassium hydroxide and sodium hydroxide, and is shown in figure 1.
Example 5 (Low metering)
Adding 400kg of waste rock residues and 450kg of water with the temperature of 60-80 ℃ into a melting pot by the weight of 1kg of the waste rock residues and the water, keeping the specific gravity at 1.31, preserving the temperature for 10-30 minutes, fully stirring, heating to 40-80 ℃, and after the waste rock residues are fully dissolved, carrying out centrifugal separation and deslagging to generate mother liquor.
The mother liquid is injected into a crystallization tank for cooling crystallization, and the temperature is kept at 8-12 ℃ for cooling crystallization for 30-48 hours.
And (3) carrying out crystal separation on the cooled and crystallized mother liquor by adopting a filter pressing or centrifuging mode, wherein the separated crystal is sodium carbonate with crystal water, and the crystal is calcined to prepare anhydrous sodium carbonate.
And (3) separating a mother solution of the mixed crystals to obtain a solution A, injecting the solution A into a lime slaking pot, heating to 90-120 ℃, adding 230kg of barium hydroxide, fully stirring, keeping the temperature at 100 ℃, heating for 30-60 minutes, cooling to 70 ℃, performing pressure filtration, separating and removing residues to generate a solution B, wherein the solution B is a mixed waste solution of potassium hydroxide and sodium hydroxide, and is shown in figure 1.
Example 6 (Medium gauge)
Adding 500kf of waste gangue and 575kg of water with the temperature of 60-80 ℃ into a melting pot by the weight of 1kg of each part, keeping the specific gravity of 1.345, preserving the temperature for 10-30 minutes, fully stirring, heating to 40-80 ℃, after the waste gangue is fully dissolved, carrying out centrifugal separation and deslagging to generate mother liquor.
The mother liquid is injected into a crystallization tank for cooling crystallization, and the temperature is kept at 8-12 ℃ for cooling crystallization for 30-48 hours.
And (3) carrying out crystal separation on the cooled and crystallized mother liquor by adopting a filter pressing or centrifuging mode, wherein the separated crystal is sodium carbonate with crystal water, and the crystal is calcined to prepare anhydrous sodium carbonate.
And (3) separating a mother solution of the mixed crystals to obtain a solution A, injecting the solution A into a lime slaking pot, heating to 90-120 ℃, adding 255kg of barium hydroxide, fully stirring, keeping the temperature at 100 ℃, heating for 30-60 minutes, cooling to 70 ℃, performing pressure filtration, separating and removing residues to generate a solution B, wherein the solution B is a mixed waste solution of potassium hydroxide and sodium hydroxide, and is shown in figure 1.
Example 7 (high metering)
Adding 600kg of waste slag and 700kg of water into a melting pot, fully stirring, heating to 40-80 ℃, melting while concentrating, and crystallizing and precipitating sodium carbonate in waste slag liquid.
Evaporating to remove 25% of water, stopping heating, centrifuging to remove residue to obtain mother liquid A, and separating to obtain crystal B.
And injecting the liquid B into a tank, adding 20% of water into the liquid B, fully stirring, performing centrifugal separation, injecting the separated separation liquid and the liquid A into a curdling pot, injecting the centrifuged crystals into a melting tank, and adding water to dissolve the crystals to prepare 30% waste rock liquid.
Adding 120kg lime into a retort, stirring thoroughly, heating to 90-120 deg.C, maintaining at 100 deg.C for 30 min, taking out, press filtering, and separating to obtain a filtrate A1Filtering the residue by pressing, and mixing A1The liquid recrystallization improves the quality of the potassium hydroxide, as shown in fig. 1.
Example 8 (Low metering)
Adding 400kg of waste slag and 450kg of water into a melting pot, fully stirring, heating to 40-80 ℃, melting while concentrating, and crystallizing and precipitating sodium carbonate in waste slag liquid.
Evaporating to remove 25% of water, stopping heating, centrifuging to remove residue to obtain mother liquid A, and separating to obtain crystal B.
Injecting the liquid B into a tank, adding 20% of water into the liquid B, fully stirring, performing centrifugal separation, injecting the separated separation liquid and the liquid A into a curdling pot, injecting the centrifuged crystals into a melting tank, and adding water to dissolve the crystals to prepare 30% waste rock liquid;
adding 90kg of lime into a chalking pan,stirring thoroughly, heating to 90-120 deg.C, maintaining at 100 deg.C for 30 min, taking out, press filtering, separating to obtain filtrate A1The liquid and filter residue are calcium carbonate which can be used as other materials, A1The liquid recrystallization improves the quality of the potassium hydroxide, as shown in fig. 1.
Example 9 (Medium gauge)
Adding 500kg of waste slag and 575kg of water into a melting pot, fully stirring, heating to 40-80 ℃, melting while concentrating, and crystallizing and precipitating sodium carbonate in waste slag liquid.
Evaporating to remove 25% of water, stopping heating, centrifuging to remove residue to obtain mother liquid A, and separating to obtain crystal B.
And injecting the liquid B into a tank, adding 20% of water into the liquid B, fully stirring, performing centrifugal separation, injecting the separated separation liquid and the liquid A into a curdling pot, injecting the centrifuged crystals into a melting tank, and adding water to dissolve the crystals to prepare 30% waste rock liquid.
Adding 105kg of lime barium hydroxide into a retort, fully stirring and heating to 90-120 ℃, keeping the temperature at 100 ℃ for 30 minutes, taking out of the retort, performing pressure filtration and separation, wherein the pressure filtrate is a mixed waste rock liquid A of potassium hydroxide and sodium hydroxide1The liquid and filter residue are calcium hydroxide which can be used for other purposes, A1The liquid recrystallization improves the quality of the potassium hydroxide, as shown in fig. 1.
Example 10 (high metering)
Adding 600kg of waste slag and 700kg of water into a melting pot, fully stirring, heating to 40-80 ℃, melting while concentrating, and crystallizing and precipitating sodium carbonate in waste slag liquid.
Evaporating to remove 25% of water, stopping heating, centrifuging to remove residue to obtain mother liquid A, and separating to obtain crystal B.
And injecting the liquid B into a tank, adding 20% of water into the liquid B, fully stirring, performing centrifugal separation, injecting the separated separation liquid and the liquid A into a curdling pot, injecting the centrifuged crystals into a melting tank, and adding water to dissolve the crystals to prepare 30% waste rock liquid.
Adding 280kg of barium hydroxide into a retort, fully stirring and heating to 90-120 ℃, keeping the temperature at 100 ℃ for 30 minutes,taking out of the pot, performing filter pressing and separation, wherein the filter pressing liquid is mixed waste rock liquid of potassium hydroxide and sodium hydroxide, namely A1Filtering the residue by pressing, and mixing A1The liquid recrystallization improves the quality of the potassium hydroxide, as shown in fig. 1.
Example 11 (Low metering)
Adding 400kg of waste slag and 450kg of water into a melting pot, fully stirring, heating to 40-80 ℃, melting while concentrating, and crystallizing and precipitating sodium carbonate in waste slag liquid.
Evaporating to remove 25% of water, stopping heating, centrifuging to remove residue to obtain mother liquid A, and separating to obtain crystal B.
And injecting the liquid B into a tank, adding 20% of water into the liquid B, fully stirring, performing centrifugal separation, injecting the separated separation liquid and the liquid A into a curdling pot, injecting the centrifuged crystals into a melting tank, and adding water to dissolve the crystals to prepare 30% waste rock liquid.
Adding 230kg of barium hydroxide into a retort, fully stirring and heating to 90-120 ℃, and keeping the temperature at 100 DEG CTaking the mixture out of the pot for filter pressing separation after 30 minutes, wherein the filter pressing liquid is a mixed waste liquid A of potassium hydroxide and sodium hydroxide1The liquid and filter residue are calcium hydroxide which can be used for other purposes, A1The liquid recrystallization improves the quality of the potassium hydroxide, as shown in fig. 1.
Example 12 (Medium gauge)
Adding 500kg of waste slag and 575kg of water into a melting pot, fully stirring, heating to 40-80 ℃, melting while concentrating, and crystallizing and precipitating sodium carbonate in waste slag liquid.
Evaporating to remove 25% of water, stopping heating, centrifuging to remove residue to obtain mother liquid A, and separating to obtain crystal B.
And injecting the liquid B into a tank, adding 20% of water into the liquid B, fully stirring, performing centrifugal separation, injecting the separated separation liquid and the liquid A into a curdling pot, injecting the centrifuged crystals into a melting tank, and adding water to dissolve the crystals to prepare 30% waste rock liquid.
Adding 255kg of barium hydroxide into a retort, fully stirring and heating to 90-120 ℃, keeping the temperature at 100 ℃ for 30 minutes, taking out of the retort, performing pressure filtration and separation, wherein the pressure filtrate is potassium hydroxide and oxyhydrogenSodium dissolving mixed waste rock liquid A1The liquid and filter residue are calcium hydroxide which can be used for other purposes, A1The liquid recrystallization improves the quality of the potassium hydroxide, as shown in fig. 1.
Example 13 (high metering)
Adding 600kg of waste rock residues and 700kg of water with the temperature of 60-80 ℃ into a melting pot by the weight of 1kg of the waste rock residues and the water, keeping the specific gravity at 1.38, preserving the heat for 10-30 minutes, fully stirring, heating to 40-80 ℃, and after the waste rock residues are fully dissolved, carrying out centrifugal separation and deslagging to generate mother liquor.
The mother liquid is injected into a crystallization tank for cooling crystallization, and the temperature is kept at 8-12 ℃ for cooling crystallization for 30-48 hours.
And (3) carrying out crystal separation on the cooled and crystallized mother liquor by adopting a filter pressing or centrifuging mode, wherein the separated crystal is sodium carbonate with crystal water, and the crystal is calcined to prepare anhydrous sodium carbonate.
And (3) separating a mother solution of the mixed crystals to obtain a solution A, injecting the solution A into a lime slaking pot, heating to 90-120 ℃, adding 120kg of lime, fully stirring, keeping the temperature at 100 ℃, heating for 30-60 minutes, cooling to 70 ℃, performing pressure filtration, separating and removing residues to generate a solution B, wherein the solution B is a mixed waste rock solution of potassium hydroxide and sodium hydroxide.
Injecting the separated crystal A into a decocting pot, heating and concentrating, cooling when the crystal A is concentrated to 6/10-8/10 of the volume of the original crystal A, injecting the concentrated solution into a crystallizing tank, keeping the temperature at 12-18 ℃ for crystallizing for 30-48 hours, performing filter pressing separation, centrifuging to obtain a solution A which is potassium hydroxide, sodium hydroxide and potassium carbonate, and centrifuging to obtain a crystal which is potassium carbonate; as shown in fig. 1.
Example 14 (Low metering)
Adding 400kg of waste rock residues and 450kg of water with the temperature of 60-80 ℃ into a melting pot by the weight of 1kg of the waste rock residues and the water, keeping the specific gravity at 1.31, preserving the temperature for 10-30 minutes, fully stirring, heating to 40-80 ℃, and after the waste rock residues are fully dissolved, carrying out centrifugal separation and deslagging to generate mother liquor.
The mother liquid is injected into a crystallization tank for cooling crystallization, and the temperature is kept at 8-12 ℃ for cooling crystallization for 30-48 hours.
And (3) carrying out crystal separation on the cooled and crystallized mother liquor by adopting a filter pressing or centrifuging mode, wherein the separated crystal is sodium carbonate with crystal water, and the crystal is calcined to prepare anhydrous sodium carbonate.
And (3) separating a mother solution of the mixed crystals to obtain a solution A, injecting the solution A into a lime slaking pot, heating to 90-120 ℃, adding 90kg of lime, fully stirring, keeping the temperature at 100 ℃, heating for 30-60 minutes, cooling to 70 ℃, performing pressure filtration, separating and removing residues to generate a solution B, wherein the solution B is a mixed waste rock solution of potassium hydroxide and sodium hydroxide.
Injecting mother liquor, namely A liquid, of which mixed crystals are separated into a boiling pot, heating and concentrating, cooling when the mother liquor is concentrated to 6/10-8/10 of the volume of the original A liquid, injecting the concentrated liquid into a crystallization tank, keeping the temperature at 12-18 ℃ for crystallization for 30-48 hours, performing filter pressing separation, wherein the centrifuged A liquid is potassium hydroxide, sodium hydroxide and potassium carbonate, and the centrifuged crystal is potassium carbonate; as shown in fig. 1.
Example 15 (Medium gauge)
Adding 500kf of waste gangue and 575kg of water with the temperature of 60-80 ℃ into a melting pot by the weight of 1kg of each part, keeping the specific gravity of 1.345, preserving the temperature for 10-30 minutes, fully stirring, heating to 40-80 ℃, after the waste gangue is fully dissolved, carrying out centrifugal separation and deslagging to generate mother liquor.
The mother liquid is injected into a crystallization tank for cooling crystallization, and the temperature is kept at 8-12 ℃ for cooling crystallization for 30-48 hours.
And (3) carrying out crystal separation on the cooled and crystallized mother liquor by adopting a filter pressing or centrifuging mode, wherein the separated crystal is sodium carbonate with crystal water, and the crystal is calcined to prepare anhydrous sodium carbonate.
And (3) separating a mother solution of the mixed crystals to obtain a solution A, injecting the solution A into a lime slaking pot, heating to 90-120 ℃, adding 105kg of lime, fully stirring, keeping the temperature at 100 ℃, heating for 30-60 minutes, cooling to 70 ℃, performing pressure filtration, separating and removing residues to generate a solution B, wherein the solution B is a mixed waste rock solution of potassium hydroxide and sodium hydroxide.
And (2) injecting the mother liquor, namely the solution A, of the separated mixed crystals into a decocting pot, heating and concentrating, cooling when the volume of the mother liquor is 6/10-8/10 of the volume of the original solution A, injecting the concentrated solution into a crystallizing tank, keeping the temperature at 12-18 ℃ for crystallizing for 30-48 hours, performing filter pressing separation, wherein the centrifuged solution A is potassium hydroxide, sodium hydroxide and potassium carbonate, and the centrifuged crystal is potassium carbonate as shown in figure 1.
Example 16 (high metering)
Adding 600kg of waste rock residues and 700kg of water with the temperature of 60-80 ℃ into a melting pot by the weight of 1kg of the waste rock residues and the water, keeping the specific gravity at 1.38, preserving the heat for 10-30 minutes, fully stirring, heating to 40-80 ℃, and after the waste rock residues are fully dissolved, carrying out centrifugal separation and deslagging to generate mother liquor.
The mother liquid is injected into a crystallization tank for cooling crystallization, and the temperature is kept at 8-12 ℃ for cooling crystallization for 30-48 hours.
And (3) carrying out crystal separation on the cooled and crystallized mother liquor by adopting a filter pressing or centrifuging mode, wherein the separated crystal is sodium carbonate with crystal water, and the crystal is calcined to prepare anhydrous sodium carbonate.
And (3) separating a mother solution of the mixed crystals to obtain a solution A, injecting the solution A into a lime slaking pot, heating to 90-120 ℃, adding 280kg of barium hydroxide, fully stirring, keeping the temperature at 100 ℃, heating for 30-60 minutes, cooling to 70 ℃, performing pressure filtration, separating and removing residues to generate a solution B, wherein the solution B is a mixed waste solution of potassium hydroxide and sodium hydroxide, and is shown in figure 1.
Example 17 (Low metering)
Adding 400kg of waste rock residues and 450kg of water with the temperature of 60-80 ℃ into a melting pot by the weight of 1kg of the waste rock residues and the water, keeping the specific gravity at 1.31, preserving the temperature for 10-30 minutes, fully stirring, heating to 40-80 ℃, and after the waste rock residues are fully dissolved, carrying out centrifugal separation and deslagging to generate mother liquor.
The mother liquid is injected into a crystallization tank for cooling crystallization, and the temperature is kept at 8-12 ℃ for cooling crystallization for 30-48 hours.
And (3) carrying out crystal separation on the cooled and crystallized mother liquor by adopting a filter pressing or centrifuging mode, wherein the separated crystal is sodium carbonate with crystal water, and the crystal is calcined to prepare anhydrous sodium carbonate.
And (3) separating a mother solution of the mixed crystals to obtain a solution A, injecting the solution A into a lime slakingpot, heating to 90-120 ℃, adding 230kg of barium hydroxide, fully stirring, keeping the temperature at 100 ℃, heating for 30-60 minutes, cooling to 70 ℃, performing pressure filtration, separating and removing residues to generate a solution B, wherein the solution B is a mixed waste solution of potassium hydroxide and sodium hydroxide.
And (2) injecting the mother liquor, namely the solution A, of the separated mixed crystals into a decocting pot, heating and concentrating, cooling when the volume of the mother liquor is 6/10-8/10 of the volume of the original solution A, injecting the concentrated solution into a crystallizing tank, keeping the temperature at 12-18 ℃ for crystallizing for 30-48 hours, performing filter pressing separation, wherein the centrifuged solution A is potassium hydroxide, sodium hydroxide and potassium carbonate, and the centrifuged crystal is potassium carbonate as shown in figure 1.
Example 18 (Medium gauge)
Adding 500kf of waste gangue and 575kg of water with the temperature of 60-80 ℃ into a melting pot by the weight of 1kg of each part, keeping the specific gravity of 1.345, preserving the temperature for 10-30 minutes, fully stirring, heating to 40-80 ℃, after the waste gangue is fully dissolved, carrying out centrifugal separation and deslagging to generate mother liquor.
The mother liquid is injected into a crystallization tank for cooling crystallization, and the temperature is kept at 8-12 ℃ for cooling crystallization for 30-48 hours.
And (3) carrying out crystal separation on the cooled and crystallized mother liquor by adopting a filter pressing or centrifuging mode, wherein the separated crystal is sodium carbonate with crystal water, and the crystal is calcined to prepare anhydrous sodium carbonate.
And (3) separating a mother solution of the mixed crystals to obtain a solution A, injecting the solution A into a lime slaking pot, heating to 90-120 ℃, adding 255kg of barium hydroxide, fully stirring, keeping the temperature at 100 ℃, heating for 30-60 minutes, cooling to 70 ℃, performing pressure filtration, separating and removing residues to generate a solution B, wherein the solution B is a mixed waste rock solution of potassium hydroxide and sodium hydroxide.
And (2) injecting the mother liquor, namely the solution A, of the separated mixed crystals into a decocting pot, heating and concentrating, cooling when the volume of the mother liquor is 6/10-8/10 of the volume of the original solution A, injecting the concentrated solution into a crystallizing tank, keeping the temperature at 12-18 ℃ for crystallizing for 30-48 hours, performing filter pressing separation, wherein the centrifuged solution A is potassium hydroxide, sodium hydroxide and potassium carbonate, and the centrifuged crystal is potassium carbonate as shown in figure 1.
Example 19 (high metering)
Adding 600kg of waste rock residues and 700kg of water with the temperature of 60-80 ℃ into a melting pot by the weight of 1kg of the waste rock residues and the water, keeping the specific gravity at 1.38, preserving the heat for 10-30 minutes, fully stirring, heating to 40-80 ℃, and after the waste rock residues are fully dissolved, carrying out centrifugal separation and deslagging to generate mother liquor.
The mother liquid is injected into a crystallization tank for cooling crystallization, and the temperature is kept at 8-12 ℃ for cooling crystallization for 30-48 hours.
And (3) carrying out crystal separation on the cooled and crystallized mother liquor by adopting a filter pressing or centrifuging mode, wherein the separated crystal is sodium carbonate with crystal water, and the crystal is calcined to prepare anhydrous sodium carbonate.
And (3) separating a mother solution of the mixed crystals to obtain a solution A, injecting the solution A into a lime slaking pot, heating to 90-120 ℃, adding 120kg of lime, fully stirring, keeping the temperature at 100 ℃, heating for 30-60 minutes, cooling to 70 ℃, performing pressure filtration, separating and removing residues to generate a solution B, wherein the solution B is a mixed waste rock solution of potassium hydroxide and sodium hydroxide.
And injecting the separated mixed waste rock liquid A into a carbon dioxide absorption pool, releasing carbon dioxide into the dilute waste rock liquid in the pool through an arrangement pipeline at the bottom of the pool, and injecting the reacted mixed waste rock liquid of potassium carbonate and sodium carbonate into a heating pot for heating and concentrating after full reaction.
Performing pressure filtration separation when the concentration is 50%, separating filtrate to obtain C liquid, and separating crystal to obtain C crystal1And (4) liquid.
C is to be1Injecting the liquid and water into a melting pot at a ratio of 1: 1-1: 1.2, heating to 30-80 deg.C, dissolving completely, injecting into a crystallization tank, cooling for crystallization, maintaining at 8-12 deg.C for natural crystallization for 12-30 hr, centrifuging to obtain mother liquid of potassium carbonate solution and crystal of sodium carbonate as shown in FIG. 1.
Example 20 (Low metering)
Adding 400kg of waste rock residues and 450kg of water with the temperature of 60-80 ℃ into a melting pot by the weight of 1kg of the waste rock residues and the water, keeping the specific gravity at 1.31, preserving the temperature for 10-30 minutes, fully stirring, heating to 40-80 ℃, and after the waste rockresidues are fully dissolved, carrying out centrifugal separation and deslagging to generate mother liquor.
The mother liquid is injected into a crystallization tank for cooling crystallization, and the temperature is kept at 8-12 ℃ for cooling crystallization for 30-48 hours.
And (3) separating crystals from the mother liquor obtained by cooling crystallization by adopting a filter pressing or centrifuging mode, wherein the separated mixed crystals are sodium carbonate with crystal water, and the mixed crystals are calcined to prepare anhydrous sodium carbonate.
And (3) separating a mother solution of the crystals to obtain a solution A, injecting the solution A into a lime slaking pot, heating to 90-120 ℃, adding 90kg of lime, fully stirring, keeping the temperature at 100 ℃, heating for 30-60 minutes, cooling to 70 ℃, performing pressure filtration, separating and removing residues to generate a solution B, wherein the solution B is a mixed waste solution of potassium hydroxide and sodium hydroxide.
And injecting the separated waste rock liquid A into a carbon dioxide absorption pool, releasing carbon dioxide into the dilute waste rock liquid in the pool through an arrangement pipeline at the bottom of the pool, and injecting the mixed waste rock liquid of potassium carbonate and sodium carbonate after reaction into a heating pot for heating and concentrating after full reaction.
Performing pressure filtration separation when the concentration is 50%, separating filtrate to obtain C liquid, and separating crystal to obtain C crystal1And (4) liquid.
C is to be1Injecting the liquid and water into a melting pot at a ratio of 1: 1-1: 1.2, heating to 30-80 deg.C, dissolving completely, injecting into a crystallization tank, cooling for crystallization, maintaining at 8-12 deg.Cfor natural crystallization for 12-30 hr, centrifuging to obtain mother liquid of potassium carbonate solution and crystal of sodium carbonate as shown in FIG. 1.
Example 21 (Medium gauge)
Adding 500kf of waste gangue and 575kg of water with the temperature of 60-80 ℃ into a melting pot by the weight of 1kg of each part, keeping the specific gravity of 1.345, preserving the temperature for 10-30 minutes, fully stirring, heating to 40-80 ℃, after the waste gangue is fully dissolved, carrying out centrifugal separation and deslagging to generate mother liquor.
The mother liquid is injected into a crystallization tank for cooling crystallization, and the temperature is kept at 8-12 ℃ for cooling crystallization for 30-48 hours.
And (3) carrying out crystal separation on the cooled and crystallized mother liquor by adopting a filter pressing or centrifuging mode, wherein the separated crystal is sodium carbonate with crystal water, and the crystal is calcined to prepare anhydrous sodium carbonate.
And (3) separating a mother solution of the crystals to obtain a solution A, injecting the solution A into a lime slaking pot, heating to 90-120 ℃, adding 105kg of lime, fully stirring, keeping the temperature at 100 ℃, heating for 30-60 minutes, cooling to 70 ℃, performing pressure filtration, separating and removing residues to generate a solution B, wherein the solution B is a mixed waste solution of potassium hydroxide and sodium hydroxide.
And injecting the separated mixed waste rock liquid A into a carbon dioxide absorption pool, releasing carbon dioxide into the dilute waste rock liquid in the pool through an arrangement pipeline at the bottom of the pool, and injecting the reacted mixed waste rock liquid of potassium carbonate and sodium carbonate into a heating pot for heating and concentrating after full reaction.
Performing pressure filtration separation when the concentration is 50%, separating filtrate to obtain C liquid, and separating crystal to obtain C crystal1And (4) liquid.
C is to be1Injecting the liquid and water into a melting pot at a ratio of 1: 1-1: 1.2, heating to 30-80 deg.C, dissolving completely, injecting into a crystallization tank, cooling for crystallization, maintaining at 8-12 deg.C for natural crystallization for 12-30 hr, centrifuging to obtain mother liquid of potassium carbonate solution and crystal of sodium carbonate as shown in FIG. 1.
Example 22 (high metering)
Adding 600kg of waste rock residues and 700kg of water with the temperature of 60-80 ℃ into a melting pot by the weight of 1kg of the waste rock residues and the water, keeping the specific gravity at 1.38, preserving the heat for 10-30 minutes, fully stirring, heating to 40-80 ℃, and after the waste rock residues are fully dissolved, carrying out centrifugal separation and deslagging to generate mother liquor.
The mother liquid is injected into a crystallization tank for cooling crystallization, and the temperature is kept at 8-12 ℃ for cooling crystallization for 30-48 hours.
And (3) carrying out crystal separation on the cooled and crystallized mother liquor by adopting a filter pressing or centrifuging mode, wherein the separated crystal is sodium carbonate with crystal water, and the crystal is calcined to prepare anhydrous sodium carbonate.
And (3) separating a mother solution of the mixed crystals to obtain a solution A, injecting the solution A into a lime slaking pot, heating to 90-120 ℃, adding 280kg of barium hydroxide, fully stirring, keeping the temperature at 100 ℃, heating for 30-60 minutes, cooling to 70 ℃, performing pressure filtration, separating and removing residues to generate a solution B, wherein the solution B is a mixed waste rock solution of potassium hydroxide and sodium hydroxide.
And injecting the separated mixed waste rock liquid A into a carbon dioxide absorption pool, releasing carbon dioxide into the dilute waste rock liquid in the pool through an arrangement pipeline at the bottom of the pool, and injecting the reacted mixed waste rock liquid of potassium carbonate and sodium carbonate into a heating pot for heating and concentrating after full reaction.
Performing pressure filtration separation when the concentration is 50%, separating filtrate to obtain C liquid, and separating crystal to obtain C crystal1And (4) liquid.
C is to be1Injecting the liquid and water into a melting pot at a ratio of 1: 1-1: 1.2, heating to 30-80 deg.C, dissolving completely, injecting into a crystallization tank, cooling for crystallization, maintaining at 8-12 deg.C for natural crystallization for 12-30 hr, centrifuging to obtain mother liquid of potassium carbonate solution and crystal of sodium carbonate as shown in FIG. 1.
Example 23 (Low metering)
Adding 400kg of waste rock residues and 450kg of water with the temperature of 60-80 ℃ into a melting pot by the weight of 1kg of the waste rock residues and the water, keeping the specific gravity at 1.31, preserving the temperature for 10-30 minutes, fully stirring, heating to 40-80 ℃, and after the waste rock residues are fully dissolved, carrying out centrifugal separation and deslagging to generate mother liquor.
The mother liquid is injected into a crystallization tank for cooling crystallization, and the temperature is kept at 8-12 ℃ for cooling crystallization for 30-48 hours.
And (3) carrying out crystal separation on the cooled and crystallized mother liquor by adopting a filter pressing or centrifuging mode, wherein the separated crystal is sodium carbonate with crystal water, and the crystal is calcined to prepare anhydrous sodium carbonate.
And (3) separating a mother solution of the mixed crystals to obtain a solution A, injecting the solution A into a lime slaking pot, heating to 90-120 ℃, adding 230kg of barium hydroxide, fully stirring, keeping the temperature at 100 ℃, heating for 30-60 minutes, cooling to 70 ℃, performing pressure filtration, separating and removing residues to generate a solution B, wherein the solution B is a mixed waste solution of potassium hydroxide and sodium hydroxide.
And injecting the separated mixed waste rock liquid A into a carbon dioxide absorption pool, releasing carbon dioxide into the dilute waste rock liquid in the pool through an arrangement pipeline at the bottom of the pool, and injecting the reacted mixed waste rock liquid of potassium carbonate and sodium carbonate into a heating pot for heating and concentrating after full reaction.
Performing pressure filtration separation when the concentration is 50%, separating filtrate to obtain C liquid, and separating crystal to obtain C crystal1And (4) liquid.
C is to be1Injecting the liquid and water at a ratio of 1: 1-1: 1.2 into a melting pot, heating to 30-80 deg.C, dissolving completely, injecting into a crystallization tank, and coolingAnd (3) cooling and crystallizing, keeping the temperature at 8-12 ℃ for natural crystallization for 12-30 hours, and performing centrifugal separation in a centrifugal mode, wherein the centrifuged mother liquor is potassium carbonate solution, and the centrifuged crystal is sodium carbonate, as shown in figure 1.
Example 24 (Mediumgauge)
Adding 500kf of waste gangue and 575kg of water with the temperature of 60-80 ℃ into a melting pot by the weight of 1kg of each part, keeping the specific gravity of 1.345, preserving the temperature for 10-30 minutes, fully stirring, heating to 40-80 ℃, after the waste gangue is fully dissolved, carrying out centrifugal separation and deslagging to generate mother liquor.
The mother liquid is injected into a crystallization tank for cooling crystallization, and the temperature is kept at 8-12 ℃ for cooling crystallization for 30-48 hours.
And (3) carrying out crystal separation on the cooled and crystallized mother liquor by adopting a filter pressing or centrifuging mode, wherein the separated crystal is sodium carbonate with crystal water, and the crystal is calcined to prepare anhydrous sodium carbonate.
And (3) separating a mother solution of the mixed crystals to obtain a solution A, injecting the solution A into a lime slaking pot, heating to 90-120 ℃, adding 255kg of barium hydroxide, fully stirring, keeping the temperature at 100 ℃, heating for 30-60 minutes, cooling to 70 ℃, performing pressure filtration, separating and removing residues to generate a solution B, wherein the solution B is a mixed waste rock solution of potassium hydroxide and sodium hydroxide.
And injecting the separated mixed waste rock liquid A into a carbon dioxide absorption pool, releasing carbon dioxide into the dilute waste rock liquid in the pool through an arrangement pipeline at the bottom of the pool, and injecting the reacted mixed waste rock liquid of potassium carbonate and sodium carbonate into a heating pot for heating and concentrating after full reaction.
Performing filter-pressing separation when the concentration is 50%, separating filtrate to obtain C liquid, and separating crystal mush toobtain C liquid1And (4) liquid.
C is to be1Injecting the liquid and water into a melting pot at a ratio of 1: 1-1: 1.2, heating to 30-80 deg.C, dissolving completely, injecting into a crystallization tank, cooling for crystallization, maintaining at 8-12 deg.C for natural crystallization for 12-30 hr, centrifuging to obtain mother liquid of potassium carbonate solution and crystal of sodium carbonate as shown in FIG. 1.
Claims (4)
1. A comprehensive recovery treatment process for indigo blue powder waste slag is characterized in that 400 portions of waste slag and 700 portions of water with the temperature of 60-80 ℃ and 450 portions of waste slag are added into a melting pot, the specific gravity is 1.31-1.38, the temperature is kept for 10-30 minutes, the mixture is fully stirred and heated to 40-80 ℃, and after the waste slag is fully dissolved, the mother solution is generated by centrifugal separation and deslagging; injecting the mother liquor into a crystallization tank for cooling crystallization, keeping the temperature at 8-12 ℃ and cooling crystallization for 30-48 hours; separating crystals from the mother liquor obtained by cooling crystallization by adopting a filter pressing or centrifugation mode, wherein the separated mixed crystals are sodium carbonate with crystal water, and the mixed crystals are calcined to prepare anhydrous sodium carbonate; and (3) separating mother liquor of the mixed crystals to obtain solution A, injecting the solution A into a lime slaking pot, heating to 90-120 ℃, adding 90-120 parts of lime or 230 parts of 280-plus of barium hydroxide, fully stirring, keeping the temperature at 100 ℃, heating for 30-60 minutes, cooling to 70 ℃, performing pressure filtration, separating and deslagging to obtain solution B, wherein the solution B is mixed gangue solution of potassium hydroxide and sodium hydroxide.
2. The process according to claim 1, wherein the process comprises adding 400-600 parts of waste slag and 450-700 parts of water into a melting pot, stirring, heating to 40-80 ℃, melting while concentrating to crystallize and precipitate sodium carbonate in the waste slag; evaporating water with a volume of about 25% of the total volume, stopping heating, centrifuging to remove residue to obtain a mother solution A, and separating to obtain a crystal B; injecting the liquid B into a tank, adding 20% of water into the liquid B, fully stirring, performing centrifugal separation, injecting the separated separation liquid and the liquid A into a curdling pot, injecting the centrifuged crystals into a melting tank, and adding water to dissolve the crystals to prepare 30% waste rock liquid; adding 90-120 parts of lime or 230-280 parts of barium hydroxide into a retort, fully stirring and heating to 90-120 ℃, keeping the temperature at 100 ℃ for 30 minutes, taking out of the retort, performing pressure filtration and separation, wherein the pressure filtrate is mixed waste rock liquid of potassium hydroxide and sodium hydroxide, namely A1The filter residue is sodium hydroxide, namely B liquid, A is filtered1The quality of the potassium hydroxide is improved by liquid recrystallization.
3. The process of claim 1, wherein the mother liquor, i.e. the solution A, from which the mixed crystals are separated is poured into a decocting pot, heated to raise the temperature for concentration, and when the mixed crystals are concentrated to 6/10-8/10 of the volume of the original solution A, the mixed crystals are cooled, the concentrated solution is poured into a crystallizing tank, the temperature is kept at 12-18 ℃ for crystallization for 30-48 hours, and the concentrated solution is subjected to filterpressing separation, wherein the centrifuged solution A is potassium carbonate, potassium salt and sodium carbonate, and the centrifuged crystals are sodium carbonate; .
4. The process according to claim 1, wherein the separated mixed waste rock liquid B of potassium hydroxide and sodium hydroxide is injected into a carbon dioxide absorption tank, carbon dioxide is released into the dilute waste rock liquid in the tank through a pipeline arranged at the bottom of the tank, and the reacted mixed waste rock liquid of potassium hydroxide and sodium hydroxide is injected into a heating pot for heating and concentration after full reaction; performing pressure filtration separation when the concentration is 50%, separating filtrate to obtain C liquid, and separating crystal to obtain C crystal1Liquid; c is to be1Injecting the liquid and water into a melting pot at a ratio of 1: 1-1: 1.2, heating to 30-80 ℃, injecting into a crystallization tank for cooling crystallization after full dissolution, keeping the temperature at 8-12 ℃ for natural crystallization for 12-30 hours, and performing centrifugal separation in a centrifugal mode, wherein the centrifuged mother liquid is potassium carbonate liquid, and the centrifuged crystal is sodium carbonate.
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101323577B (en) * | 2007-06-14 | 2011-04-13 | 重庆达华砼外加剂科技发展有限公司 | Method for extracting aniline and sodium carbonate and potassium carbonate from mixed alkaline residue in bipseudoindoxyl production |
| CN102127307A (en) * | 2010-12-29 | 2011-07-20 | 梅剑平 | Recovered mixed alkali solution from production of indigo, and recovering method and use thereof |
| CN103827037A (en) * | 2011-09-16 | 2014-05-28 | 沙特基础创新塑料Ip私人有限责任公司 | Method to remove carbonate from caustic scrubber waste stream |
| CN104692423A (en) * | 2015-02-13 | 2015-06-10 | 内蒙古泰兴泰丰化工有限公司 | Mixed alkaline residue treatment device in indigo blue production |
| CN104692422A (en) * | 2015-02-13 | 2015-06-10 | 内蒙古泰兴泰丰化工有限公司 | Mixed alkaline residue treatment device and method in indigo blue production |
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2004
- 2004-01-19 CN CN 200410018621 patent/CN1266043C/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101323577B (en) * | 2007-06-14 | 2011-04-13 | 重庆达华砼外加剂科技发展有限公司 | Method for extracting aniline and sodium carbonate and potassium carbonate from mixed alkaline residue in bipseudoindoxyl production |
| CN102127307A (en) * | 2010-12-29 | 2011-07-20 | 梅剑平 | Recovered mixed alkali solution from production of indigo, and recovering method and use thereof |
| CN103827037A (en) * | 2011-09-16 | 2014-05-28 | 沙特基础创新塑料Ip私人有限责任公司 | Method to remove carbonate from caustic scrubber waste stream |
| US9364794B2 (en) | 2011-09-16 | 2016-06-14 | Sabic Global Technologies B.V. | Method to remove carbonate from a caustic scrubber waste stream |
| CN104692423A (en) * | 2015-02-13 | 2015-06-10 | 内蒙古泰兴泰丰化工有限公司 | Mixed alkaline residue treatment device in indigo blue production |
| CN104692422A (en) * | 2015-02-13 | 2015-06-10 | 内蒙古泰兴泰丰化工有限公司 | Mixed alkaline residue treatment device and method in indigo blue production |
| CN104692422B (en) * | 2015-02-13 | 2016-03-30 | 内蒙古泰兴泰丰化工有限公司 | Its Future about Alkaline Residue Treatment Unit and treatment process is mixed in indigo production |
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| CN1266043C (en) | 2006-07-26 |
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