Summary of the invention
The object of the invention is for the deficiencies in the prior art, thus a kind of preparation method of industrial alum is provided.
To achieve these goals, the technical solution adopted in the present invention is: a kind of preparation method of industrial alum, comprises the following steps:
Step 1, getting feldspar in powder and Neutral ammonium fluoride, is that 1:1.1 ~ 1.2 mix according to mass ratio, and at the temperature of 250 ~ 270 DEG C constant temperature 0.5 ~ 4 hour so that mixed feldspar in powder and Neutral ammonium fluoride fully react;
Step 2, in step 1, add Fluorspar Powder and the vitriol oil in reacted solid mixture, the mass ratio of solid mixture, Fluorspar Powder and the vitriol oil is 1:0.4 ~ 0.5:1, be reaction constant temperature 0.5 ~ 4 hour under the condition of 270 ~ 290 DEG C in temperature, the solid generated after reaction comprises calcium sulfate, potassium sulfate and Tai-Ace S 150;
Step 3, solid step 2 being reacted rear generation are pulverized, and then add in the water of 85 ~ 95 DEG C and leach, temperature keeps 2 hours, and water is 5:1 with the ratio of solid masses, and object is dissolved in water by the potassium sulfate in solid and Tai-Ace S 150;
Step 4, in step 3 leaching after mixed solution in plate-and-frame filter press press filtration to obtain leaching liquid;
Step 5, the leaching liquid of step 4 gained added in crystallization kettle and carry out initial concentration crystallization under the condition of vacuum tightness-0.08MPa and temperature 70 C, and sampling analysis chemical examination, make potassium ion and aluminum ions mol ratio meet 1:1 according to result of laboratory test interpolation moderate amount of sulfuric acid aluminium or potassium sulfate;
Step 6, proceed condensing crystal, filter and obtain alum crystal.
Based on above-mentioned, the reaction of step 1 and step 2 is all carried out in converter.
Based on above-mentioned, the condensing crystal in step 6, adopts first to heat and to be concentratedly stops heating when reaching 50 ~ 60% to alum concentration, and then cooling continues the mode of crystallization, until filter after meeting setting crystallization requirement.
Based on above-mentioned, the mixed gas generated in step 1 and step 2 all absorbs with aqueous ethanolic solution, the silicon tetrafluoride gas in mixed gas and hydrogen fluoride is made to be dissolved in aqueous ethanolic solution, then ammonia solution is carried out to the liquid after absorption, after pH value reaches 8 ~ 9, obtain white carbon black by filter pressing, evaporative crystallization is carried out to filtrate and obtains Neutral ammonium fluoride.
Based on above-mentioned, described ammonia solution is carried out in ammonia solution groove.
Based on above-mentioned, in described aqueous ethanolic solution, the volume ratio of ethanol and aqueous ethanolic solution is 1:10.
The invention provides a kind of method utilizing potassium felspar sand to produce industrial alum, add the production ways of alum, simultaneously, extend the utilization of potassium felspar sand resource, preparation method of the present invention, step is simple, and the extraction yield of alum is high, production efficiency is high, by two-step approach decomposing of potassium feldspar, i.e. step 1 and step 2, substantially increase the rate of decomposition of potassium felspar sand, decrease the consumption of fluorite, Neutral ammonium fluoride can also reclaim Posterior circle utilization simultaneously.
Further, the process of ammonia solution is carried out to the gas collected, can also white carbon black be obtained, decrease the waste of environmental pollution and resource.
Embodiment
Below by embodiment, technical scheme of the present invention is described in further detail.
The embodiment of a kind of preparation method of industrial alum
Embodiment 1
As shown in Figure 1, comprise the following steps:
Step 1, getting feldspar in powder and Neutral ammonium fluoride, is that 1:1.1 ~ 1.2 mix according to mass ratio, and at the temperature of 250 ~ 270 DEG C constant temperature 0.5 ~ 4 hour so that mixed feldspar in powder and Neutral ammonium fluoride fully react;
Step 2, in step 1, add Fluorspar Powder and the vitriol oil in reacted solid mixture, the vitriol oil is the vitriol oil of 98%, the mass ratio of solid mixture, Fluorspar Powder and the vitriol oil is 1:0.4 ~ 0.5:1, be reaction constant temperature 0.5 ~ 4 hour under the condition of 270 ~ 290 DEG C in temperature, the solid generated after reaction comprises calcium sulfate, potassium sulfate and Tai-Ace S 150;
Step 3, solid step 2 being reacted rear generation are pulverized, and then add in the water of 85 ~ 95 DEG C and leach, temperature keeps 2 hours, and water is 5:1 with the ratio of solid masses, and object is dissolved in water by the potassium sulfate in solid and Tai-Ace S 150;
Step 4, in step 3 leaching after mixed solution in plate-and-frame filter press press filtration to obtain leaching liquid;
Step 5, the leaching liquid of step 4 gained added in crystallization kettle and carry out initial concentration crystallization under the condition of vacuum tightness-0.08MPa and temperature 70 C, and sampling analysis chemical examination, make potassium ion and aluminum ions mol ratio meet 1:1 according to result of laboratory test interpolation moderate amount of sulfuric acid aluminium or potassium sulfate;
Step 6, proceed condensing crystal, filter and obtain alum crystal.
Wherein, the reaction of step 1 and step 2 is all carried out in converter, and solid mixture comprises feldspar in powder, aluminum fluoride and Potassium monofluoride.
A kind of method utilizing potassium felspar sand to produce industrial alum of the present embodiment, adds the production ways of alum, simultaneously, extend the utilization of potassium felspar sand resource, preparation method of the present invention, step is simple, and the extraction yield of alum is high, production efficiency is high, by two-step approach decomposing of potassium feldspar, i.e. step 1 and step 2, substantially increase the rate of decomposition of potassium felspar sand, decrease the consumption of fluorite, Neutral ammonium fluoride can also reclaim Posterior circle utilization simultaneously.
Embodiment 2
As different from Example 1, the condensing crystal in step 6, adopts first to heat and to be concentratedly stops heating when reaching 50 ~ 60% to alum concentration, and then cooling continues the mode of crystallization, until filter after meeting setting crystallization requirement.
Embodiment 3
With embodiment 1,2 unlike, the mixed gas generated in step 1 and step 2 all absorbs with aqueous ethanolic solution, the silicon tetrafluoride gas in mixed gas and hydrogen fluoride is made to be dissolved in aqueous ethanolic solution, then ammonia solution is carried out to the liquid after absorption, after pH value reaches 8 ~ 9, obtain white carbon black by filter pressing, evaporative crystallization is carried out to filtrate and obtains Neutral ammonium fluoride, described ammonia solution is carried out in ammonia solution groove, and in aqueous ethanolic solution, the volume ratio of ethanol and aqueous ethanolic solution is 1:10.
The process of ammonia solution is carried out to the gas collected, can also white carbon black be obtained, decrease the waste of environmental pollution and resource.
Embodiment 4
With embodiment 1-3 unlike, step 1, get feldspar in powder and Neutral ammonium fluoride, be that 1:1.1 mixes according to mass ratio, and at the temperature of 250 DEG C constant temperature 0.5 hour; Fluorspar Powder and the vitriol oil is added in reacted solid mixture in step 1, the mass ratio of solid mixture, Fluorspar Powder and the vitriol oil is 1:0.4:1, be reaction constant temperature 0.5 hour under the condition of 270 DEG C in temperature, the solid generated after reaction comprises calcium sulfate, potassium sulfate and Tai-Ace S 150;
In step 3, solid step 2 being reacted rear generation is pulverized, and then adds in the water of 85 DEG C and leaches.
Embodiment 5
With embodiment 1-4 unlike, step 1, get feldspar in powder and Neutral ammonium fluoride, be that 1:1.15 mixes according to mass ratio, and at the temperature of 260 DEG C constant temperature 2 hours; Fluorspar Powder and the vitriol oil is added in reacted solid mixture in step 1, the mass ratio of solid mixture, Fluorspar Powder and the vitriol oil is 1:0.45:1, be reaction constant temperature 2 hours under the condition of 280 DEG C in temperature, the solid generated after reaction comprises calcium sulfate, potassium sulfate and Tai-Ace S 150;
In step 3, solid step 2 being reacted rear generation is pulverized, and then adds in the water of 90 DEG C and leaches.
Embodiment 6
With embodiment 1-5 unlike, step 1, get feldspar in powder and Neutral ammonium fluoride, be that 1:1.2 mixes according to mass ratio, and at the temperature of 270 DEG C constant temperature 4 hours; Fluorspar Powder and the vitriol oil is added in reacted solid mixture in step 1, the mass ratio of solid mixture, Fluorspar Powder and the vitriol oil is 1:0.5:1, be reaction constant temperature 4 hours under the condition of 290 DEG C in temperature, the solid generated after reaction comprises calcium sulfate, potassium sulfate and Tai-Ace S 150; In step 3, solid step 2 being reacted rear generation is pulverized, and then adds in the water of 95 DEG C and leaches.
Finally should be noted that: above embodiment is only in order to illustrate that technical scheme of the present invention is not intended to limit; Although with reference to preferred embodiment to invention has been detailed description, those of ordinary skill in the field are to be understood that: still can modify to the specific embodiment of the present invention or carry out equivalent replacement to portion of techniques feature; And not departing from the spirit of technical solution of the present invention, it all should be encompassed in the middle of the technical scheme scope of request of the present invention protection.