CN103145194B - A kind of method utilizing by-product of white titanium pigment to prepare iron oxide yellow - Google Patents
A kind of method utilizing by-product of white titanium pigment to prepare iron oxide yellow Download PDFInfo
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Abstract
The invention provides a kind of method that byproduct ferrous sulfate of titanium dioxide prepares iron oxide yellow, belong to chemical field.The method comprises refining, neutralization reaction, JZPD capsule, the oxidative synthesis of ferrous sulfate, it adopts the method controlling solution ph when ferrous sulfate is refined, effective removal impurity manganese, magnesium, zinc, neutralization reaction process and seed crystal production process is divided into, by Fe (OH) additionally by by seed crystal production process
2separately, the shape effectively controlling crystal seed is fusiformis or aciculiform, and improves the dispersiveness of crystal seed for the preparation process of suspensoid and oxidising process.The present invention has good impurity removing effect, and the shape that effectively can control crystal seed is fusiformis or aciculiform, and improves the dispersiveness of crystal seed, and it is good that the sulfuric acid iron oxide yellow prepared by the method has form and aspect, tinting strength advantages of higher.
Description
Technical field
The present invention relates to a kind of method that byproduct ferrous sulfate of titanium dioxide prepares ferric oxide yellow pigment, belong to the preparation method field of pigment.
Background technology
Titanium white is a kind of white inorganic pigment of high-grade high-quality, mainly contains anatase titanium dioxide and rutile-type two kinds of crystal formations.Because its density, specific inductivity and specific refractory power are all very superior, be considered to a kind of white pigment that performance is in the world best, be widely used in the industry such as coating, plastics, papermaking, printing, ink and rubber.At present, the production method of titanium dioxide has sulfuric acid process and chlorination process two kinds, and because Production By Sulfuric Acid Process technique is relatively simple, and can produce with the lower ilmenite concentrate of taste, current China mainly Titanium White Production By Sulfuric Acid Process, its ratio accounts for 98%.
Titanium White Production By Sulfuric Acid Process is often produced 1 ton of titanium white and is about by-product 3.5 ~ 4 tons of ferrous sulfate.Titanium white output in 2010 reaches 160 ~ 1,800,000 tons according to statistics, and useless by-product ferrous sulfate during (hereinafter referred to as ferrous sulfate as side product) output is then up to 640 ~ 7,200,000 tons.So a large amount of ferrous sulfate as side product is as still adopted original bulk mode, and shared place is big and the impact of environment is all seriously constrained to the development of titanium dioxide industry.
In order to recycle fully ferrous sulfate as side product, also there is people to be used for doing iron catalyst, water purification agent, fodder additives, soil improvement agent etc. by titanium white ferrous sulfate as side product in the past, the amount of the titanium white ferrous sulfate as side product of relative output, the consumption of these process approach is all very little, a large amount of ferrous sulfate as side product is still had urgently to fully utilize, not so will cause serious environmental pollution, and waste precious resources.And to utilize titanium white ferrous sulfate as side product to prepare iron oxide pigment be comprehensive utilization, the better approach that turns waste into wealth.
China produces iron oxide yellow based on " liquid and solid phase reaction " method, and main raw material is enamel plant's scrap iron (scrap stock), data presentation, often produces one ton of iron oxide yellow and just needs about 900 kilograms low-carbon (LC) sheet irons.At present, iron sheet price increase, source of goods shortage, in order to reduce costs, so to find new raw material sources just very necessary.And utilize titanium white ferrous sulfate as side product to prepare ferric oxide yellow pigment, ferrous sulfate as side product can be consumed in a large number, iron oxide pigment about per ton can consume 4 tons of ferrous sulfate as side product, namely the problem that the ferrous sulfate as side product produced in Producing Titanium Dioxide process hoards environmental pollution is in a large number solved, ferric oxide yellow pigment production cost can be reduced again, realize the comprehensive utilization of resource.
At present, in prior art, there is the method utilizing titanium white ferrous sulfate as side product to prepare ferric oxide yellow pigment.Such as Chinese patent ZL02148429C discloses a kind of method that titanium white ferrous sulfate as side product produces ferric oxide yellow pigment, and the method specifically comprises the steps:
(1) ferrous sulfate is refining, first titanium white ferrous sulfate as side product is dissolved, with sulfuric acid adjust pH for 1.0 ~ 1.5, add a certain amount of iron sheet, control temperature is at 50 ~ 70 DEG C, and it is 3.0 ~ 4.5 that hydrolysis 6 ~ 10h reaches pH value, being diluted to iron vitriol concentration is 350 ~ 450g/L, add flocculation agent, stirring, standing sedimentation 4 ~ 6h, supernatant liquid is POV ferrous iron solution; (2) JZPD capsule, in traditional seed tank, ammonia and above-mentioned POV ferrous iron (initial pH value is 6.0 ~ 8.0) solution, at 10 ~ 40 DEG C, with air reaction, through 18 ~ 36h, system pH reaches 5.0 ~ 7.0, and namely obtains needle-like oyster ferric oxide crystal seed; (3) oxidizing reaction, in conventional oxidation bucket, add above-mentioned crystal seed, be warming up to 60 ~ 95 DEG C, constant temperature, adjust pH to 2.0 ~ 5.0, add above-mentioned refining copperas solution, air and ammonia continuously, maintenance system pH value is 2.0 ~ 5.0, and iron vitriol concentration is at 10 ~ 45g/L, oxidation 40 ~ 130h, i.e. obtained iron oxide yellow slurry; (4) filter, wash, dry, pulverize, pack i.e. obtained finished product ferric oxide yellow pigment.
In above-mentioned technology, in the treating process of ferrous sulfate, by controlling the conditions such as the pH value of solution and temperature, the impurity titanium in ferrous sulfate effectively can be removed; Because the deposition condition of magnesium, zinc, mn ion must be greater than 7, under above-mentioned pH value condition, so then cannot remove impurity magnesium, zinc and the manganese in ferrous sulfate, and the existence of magnesium, zine ion can cause the color of iron oxide yellow product partially white, the existence of mn ion can cause the color of iron oxide yellow product partially black, direct impact is caused on product ferric oxide yellow, and color is the important indicator of iron oxide yellow product.If pH value be adjusted to and be greater than 7, then Fe can be made simultaneously
2+precipitate, affect the productive rate of subsequent oxidation iron oxide yellow.
In addition, in the above-described techniques, to ferrous sulfate carry out impurity elimination refining after, in the ferrous sulfate after refining, add ammoniacal liquor directly generate ferric oxide crystal seed through single step reaction under blowing air condition, in above-mentioned reaction process, first ferrous sulfate and ammoniacal liquor react and generate Fe (OH)
2suspensoid, the existence of air makes this part product be oxidised with air to alpha-feooh (i.e. hydrous iron oxide) immediately while generation, when alpha-feooh reaches the minimum supersaturation concentration of nucleation requirement, nucleus nucleation in solution, nucleus is once be formed, first the alpha-feooh then generated can make the nucleus formed grow up rapidly, and not easily generate new nucleus, this mode easily causes the alpha-feooh crystal seed reacting generation few, established crystal seed growth rate is too fast, shape is wayward, generate based on needle-like or fusiformis seed shape, and mix the product having cylindrical crystal seed, wherein cylindrical crystal seed is iron oxide red, and the existence of this part cylindrical crystal seed makes the transmittance of alpha-feooh, absorb light rate and refracted light rate receive impact, thus directly cause the ferric oxide yellow of generation partially dark.
Summary of the invention
First technical problem to be solved by this invention be in prior art ferrous sulfate is carried out refining after, ammoniacal liquor is added in the ferrous sulfate after refining, ferric oxide crystal seed is directly generated through single step reaction under blowing air condition, cause the crystal seed that generates in reaction process few and effectively can not control the nucleation of crystal seed and the growth of nucleus, cause in crystal seed to mix and have cylindrical crystal seed, make the finished product ferric oxide yellow prepared be subject to direct impact.
Second technical problem to be solved by this invention is impurity magnesium, zinc and the manganese that pH value condition when carrying out refining to ferrous sulfate in prior art cannot remove in ferrous sulfate, the existence of magnesium, zine ion causes direct impact to product ferric oxide yellow, if pH value be adjusted to and be greater than 7, then Fe can be made simultaneously
2+precipitate, affect the productive rate of subsequent oxidation iron oxide yellow.
In order to solve the problems of the technologies described above, the invention provides a kind of method utilizing byproduct ferrous sulfate of titanium dioxide to prepare iron oxide yellow, comprising the steps:
(1) ferrous sulfate is refining
Utilize byproduct ferrous sulfate of titanium dioxide to prepare iron vitriol solution, regulate the pH value of this solution to be 1 ~ 2.5, byproduct ferrous sulfate of titanium dioxide is carried out to the hydrolysis treatment of titanium;
Iron powder or iron sheet is added, to the Fe in solution in the iron vitriol solution after titanium hydrolysis treatment
3+carry out reduction treatment and the pH value of regulator solution is 6.0 ~ 6.5, byproduct ferrous sulfate of titanium dioxide is carried out to the precipitation process of magnesium, manganese, zinc;
In the solution after titanium hydrolysis treatment and magnesium, manganese, zinc precipitation process, add flocculation agent, stir, filter after standing sedimentation, filtrate be refining after copperas solution;
(2) Fe (OH)
2generation
In the copperas solution after described refining, add alkaline solution, at 10 ~ 39 DEG C, carry out neutralization reaction, hierarchy of control pH value is 6.0 ~ 7.5, and when the white precipitate of the generation in solution becomes blackish green, neutralization reaction terminates;
(3) iron oxide yellow JZPD capsule
Reacted system solution in step (2) is diluted, passes into air wherein and react, when system pH reaches 3 ~ 4, i.e. obtained needle-like oyster iron oxide yellow crystal seed;
(4) oxidative synthesis
The iron oxide yellow crystal seed prepared in step (3) is diluted, slowly be warming up to 75 ~ 85 DEG C, pass into air wherein, control air capacity is 2 ~ 5 times of the air capacity passed in step (3), maintenance system pH value is 2 ~ 3.5, is oxidized and namely obtains iron oxide yellow slurries in more than 40 hours;
(5) aftertreatment
Iron oxide yellow slurries after step (4) process are filtered successively, wash, dry the iron oxide yellow that gets product.
In described step (1), at 10 ~ 80 DEG C, prepare described iron vitriol strength of solution is 350 ~ 490g/L.
In described step (1), the pH value regulating iron vitriol solution with sulfuric acid is 2.
In described step (1), the add-on of described flocculation agent is 0.05% of iron vitriol quality.
In described step (1), before adding flocculation agent, the solution after titanium hydrolysis treatment and magnesium, manganese, zinc precipitation process is lowered the temperature, reduces to room temperature to system temperature.
In step (1), the time of standing sedimentation is 1 ~ 2h.
In step (2), hierarchy of control pH value is 6.5 ~ 7.2.
The mass ratio of described alkaline solution and iron vitriol is 0.05 ~ 0.09.
In described step (3), reacted system solution in step (2) is diluted to 200 ~ 300g/L.
In described step (3), after 2.5 ~ 11 hours, system pH reaches 3 ~ 4.
In described step (3), in 4 ~ 8 hours, be warming up to 75 ~ 85 DEG C.
In described step (3), per minute pass into that described air capacity is reactor volume 1/40 ~ 1/10.
In described step (4), in the solution after dilution, add excessive iron sheet, maintenance system pH value is 2 ~ 3.5.
In described step (4), 100 ~ 150g/L is diluted to the iron oxide yellow crystal seed prepared in step (3).
The method utilizing byproduct ferrous sulfate of titanium dioxide to prepare iron oxide yellow of the present invention, first need to utilize byproduct ferrous sulfate of titanium dioxide to prepare iron vitriol solution, and control ph is 1 ~ 2.5, titanium impurity in iron vitriol solution is hydrolyzed under this pH value condition, generates and namely can be changed into the rapid sedimentation of floss and the Ti decomposed after adding flocculation agent
2oH
2o; When iron vitriol solution preparation, preferably preparing at 50 ~ 80 DEG C, is the dissolved efficiency that ensure that byproduct ferrous sulfate of titanium dioxide considering stability of solution while; In order to remove the Fe in byproduct ferrous sulfate of titanium dioxide
3+, to through except adding iron powder or iron sheet in the iron vitriol solution after titanium process to Fe
3+reduce, removing Fe
3+; Further, in order to improve the purity of the ferrous sulfate prepared, pass through the interpolation of iron powder or iron sheet in method of the present invention, and adjust ph is 6.0 ~ 6.5, thus achieves the precipitate reduction to the magnesium in iron vitriol solution, manganese, zine ion.In the solution after carrying out above-mentioned process, add flocculation agent, thus fully realize titanyl hydrate, magnesium, manganese, zinc precipitation remove, be convenient to its carry out effectively filtering obtain refining after copperas solution.
Then, in the copperas solution after refining, add alkaline solution, hierarchy of control pH value is 6.0 ~ 7.5, at 10 ~ 39 DEG C, carry out neutralization reaction, thus generates Fe (OH)
2precipitation, when precipitation to be generated transfers to blackish green by white, neutralization reaction terminates; In above-mentioned neutralization reaction, Fe be ensured
2+react fully, first Fe
2+reaction generates the Fe (OH) of white
2precipitation, but, due to Fe (OH)
2instability, newly-generated Fe (OH)
2very soon by a small amount of dioxygen oxidation be dissolved in air in solution, be converted into the intermediate product of ironic hydroxide, i.e. the flocks of some greyish-green, when white precipitate changes into blackish green in ie in solution, show that neutralization reaction terminates, reaction should be terminated immediately and avoid Fe (OH)
2be further oxided.But, generally speaking, in neutralization reaction process, mainly still generate a large amount of Fe (OH)
2suspensoid, Fe (OH)
2the oxidized alpha-feooh obtained of suspensoid is little, and concentration not yet reaches the minimum supersaturation concentration that nucleation requires, now in solution, nucleus does not generate.
Because the ferrous hydroxide prepared after this neutralization reaction is precipitated as flocculent substance, so it is dense, if directly to wherein passing into air, air then cannot precipitate with ferrous hydroxide and carry out contact reacts fully, so when preparing iron oxide yellow crystal seed, needing first to dilute the system solution after neutralization reaction, then passing into air wherein and react, when system pH reaches 3 ~ 4, i.e. obtained needle-like oyster iron oxide yellow crystal seed; In this preparation process, in the solution after neutralization reaction, pass into air, due in now solution containing Fe (OH)
2suspensoid, after passing into enough air, the oxygen in air can Oxidation of Fe (OH)
2, generate alpha-feooh.In addition, owing to containing a large amount of Fe (OH) in solution
2, so the speed that now oxidation obtains alpha-feooh can be very fast, after the concentration of the solute alpha-feooh in solution meets and exceeds the one-tenth nuclear concentration of crystal seed, nucleus will be formed fast and be evenly distributed.In above-mentioned two-step reaction, first simple neutralization reaction is carried out to the copperas solution after refining, and do not pass into air when neutralization reaction, the Fe (OH) that in solution, main generation is a large amount of
2suspensoid; After neutralization reaction terminates, then pass into air in solution, carry out oxidative synthesis iron oxide yellow crystal seed.
Finally, the iron oxide yellow crystal seed prepared is diluted, be warming up to 80 ~ 83 DEG C, pass into air wherein, control air capacity is 2 ~ 5 times of the air capacity passed in step (3), maintenance system pH value is 2 ~ 3.5, and further namely oxidation obtains iron oxide yellow slurries in more than 40 hours, carries out aftertreatment and to get product iron oxide yellow.In above-mentioned iron oxide yellow slurry production process, along with the carrying out of oxidizing reaction, H in solution
+concentration constantly increase, solution ph decline, amorphous substance Fe (OH)
2transform to amorphous material FeOOH gradually, Fe
2+gradually become Fe
3+, solution becomes yellow; In iron oxide yellow slurry production process, when solution pH lower than 2 time, FeOOH dissolves, and can have influence on the productive rate of iron oxide yellow, so in oxidising process, controls the pH value of slurry system in 2 ~ 3.5 scopes, after oxidation enough time, obtains iron oxide yellow slurries.
The present invention compared with prior art tool has the following advantages:
Seed crystal production process in prior art is divided into Fe (OH) by the present invention
2generative process and iron oxide yellow seed crystal production process, preparing a large amount of Fe (OH)
2after suspensoid, carry out iron oxide yellow JZPD capsule passing into air, can generate and generate a large amount of iron oxide yellow crystal seed within a short period of time, and effectively can control the nucleation of crystal seed and the growth of nucleus, and then the shape effectively controlling crystal seed is fusiformis or aciculiform, and improve the dispersiveness of crystal seed.
In addition, the pH value of solution when ferrous sulfate is refined can be controlled more accurately by adding iron powder or iron sheet in preparation method of the present invention, thus under optimum pH condition, the reduction to magnesium, manganese, zine ion is realized by reduction reaction, thus realize the object removing impurity magnesium, manganese, zine ion, obtain high-purity mangesium oxide iron oxide yellow.It is good that the sulfuric acid iron oxide yellow prepared by the method has form and aspect, tinting strength advantages of higher.
Accompanying drawing explanation
The TEM characterization test picture of the iron oxide yellow prepared in Fig. 1 embodiment 1.
Embodiment
Below in conjunction with embodiment, the present invention is further described in detail.
embodiment 1
(1) ferrous sulfate is refining
Under normal temperature, the iron vitriol solution 500ml utilizing byproduct ferrous sulfate of titanium dioxide compound concentration to be 350g/L, regulates the pH value of this solution to be 1 with sulfuric acid, carries out titanium hydrolysis treatment to byproduct ferrous sulfate of titanium dioxide; 26g iron powder reducing Fe is added again in the iron vitriol solution after titanium hydrolysis treatment
3+and adjust ph is 6.0, the precipitation obtaining magnesium, manganese, zinc simple substance reduced to magnesium, manganese, zine ion, 0.09g polyacrylamide flocculant is added in the solution after titanium hydrolysis treatment and magnesium, manganese, zinc precipitation process, filter after stirring, standing sedimentation 5h, product after the hydrolysis of removing titanium and magnesium, manganese, zinc precipitation, filtrate is the copperas solution after refining;
(2) Fe (OH)
2generation
Get the copperas solution 375ml after described refining, add the NaOH solution of 9g30wt% wherein, at 10 DEG C, carry out neutralization reaction, hierarchy of control pH value is 6.0, and when the white precipitate generated in solution becomes blackish green, neutralization reaction terminates;
(3) iron oxide yellow JZPD capsule
Being diluted to concentration to reacted system solution in step (2) is 200g/L, passes into air wherein and reacts, and the speed passing into air is 60ml/min, namely per minute pass into that air capacity is reactor volume 1/40; When system pH reaches 3.0, i.e. obtained needle-like oyster iron oxide yellow crystal seed;
(4) oxidative synthesis
Being diluted to concentration to the iron oxide yellow crystal seed prepared in step (3) is 150g/L, controlling the heating-up time is that 4h is slowly warming up to 75 DEG C, air is passed in the solution after dilution, control air capacity is 2 times of the air capacity passed in step (3), and add the iron sheet of 40g, maintenance system pH value is 3.5, is oxidized and namely obtains iron oxide yellow slurries in more than 40 hours;
(5) aftertreatment
Iron oxide yellow slurries after step (4) process are filtered successively, wash, dry the iron oxide yellow that gets product.
After testing, the finished product iron oxide yellow total iron of preparation is with Fe
2o
3meter, content is 98%.
embodiment 2
(1) ferrous sulfate is refining
At 50 DEG C, the iron vitriol solution 500ml utilizing byproduct ferrous sulfate of titanium dioxide compound concentration to be 370g/L, regulates the pH value of this solution to be 1.5 with sulfuric acid, carries out titanium hydrolysis treatment to byproduct ferrous sulfate of titanium dioxide; 28g iron powder reducing Fe is added again in the iron vitriol solution after titanium hydrolysis treatment
3+and regulate pH to be 6.1, the precipitation obtaining magnesium, manganese, zinc simple substance reduced to magnesium, manganese, zine ion, when solution is cooled to room temperature, 0.09g polyacrylamide flocculant is added in the solution after titanium hydrolysis treatment and magnesium, manganese, zinc precipitation process, filter after stirring, standing sedimentation 2h, product after the hydrolysis of removing titanium and magnesium, manganese, zinc precipitation, filtrate is the copperas solution after refining;
(2) Fe (OH)
2generation
Get the copperas solution 375ml after described refining, add the NaOH solution of 9.5g30wt% wherein, at 20 DEG C, carry out neutralization reaction, hierarchy of control pH value is 6.5, and when the white precipitate generated in solution becomes blackish green, neutralization reaction terminates;
(3) iron oxide yellow JZPD capsule
Being diluted to concentration to reacted system solution in step (2) is 250g/L, passes into air wherein and reacts, and the speed passing into air is 80ml/min, namely per minute pass into that air capacity is reactor volume 1/30; When system pH reaches 3.5, i.e. obtained needle-like oyster iron oxide yellow crystal seed;
(4) oxidative synthesis
Being diluted to concentration to the iron oxide yellow crystal seed prepared in step (3) is 130g/L, controlling the heating-up time is that 8h is slowly warming up to 83 DEG C, air is passed in the solution after dilution, control air capacity is 3 times of the air capacity passed in step (3), and to add 42g iron sheet maintenance system pH value be 2, be oxidized and namely obtain iron oxide yellow slurries in more than 40 hours;
(5) aftertreatment
Iron oxide yellow slurries after step (4) process are filtered successively, wash, dry the iron oxide yellow that gets product.
After testing, the finished product iron oxide yellow total iron of preparation is with Fe
2o
3meter, content is 98%.
embodiment 3
(1) ferrous sulfate is refining
At 60 DEG C, the iron vitriol solution 500ml utilizing byproduct ferrous sulfate of titanium dioxide compound concentration to be 400g/L, regulates the pH value of this solution to be 2.0 with sulfuric acid, carries out titanium hydrolysis treatment to byproduct ferrous sulfate of titanium dioxide; 30g iron powder reducing Fe is added again in the iron vitriol solution after titanium hydrolysis treatment
3+and regulate pH to be 6.0, the precipitation obtaining magnesium, manganese, zinc simple substance reduced to magnesium, manganese, zine ion, when solution is cooled to room temperature, 0.1g polyacrylamide flocculant is added in the solution after titanium hydrolysis treatment and magnesium, manganese, zinc precipitation process, filter after stirring, standing sedimentation 1.5h, product after the hydrolysis of removing titanium and magnesium, manganese, zinc precipitation, filtrate is the copperas solution after refining;
(2) Fe (OH)
2generation
Get the copperas solution 375ml after described refining, add the NaOH solution of 12g30wt% wherein, at 30 DEG C, carry out neutralization reaction, hierarchy of control pH value is 7.0, and when the white precipitate of the generation in solution becomes blackish green, neutralization reaction terminates;
(3) iron oxide yellow JZPD capsule
Being diluted to concentration to reacted system solution in step (2) is 300g/L, passes into air wherein and reacts, and the speed passing into air is 100ml/min, namely per minute pass into that air capacity is reactor volume 1/25; When system pH reaches 4.0, i.e. obtained needle-like oyster iron oxide yellow crystal seed;
(4) oxidative synthesis
Being diluted to concentration to the iron oxide yellow crystal seed prepared in step (3) is 150g/L, controlling the heating-up time is that 5h is slowly warming up to 80 DEG C, air is passed in the solution after dilution, control air capacity is 3 times of the air capacity passed in step (3), and to add 45g iron powder maintenance system pH value be 2.5, be oxidized and namely obtain iron oxide yellow slurries in more than 40 hours;
(5) aftertreatment
Iron oxide yellow slurries after step (4) process are filtered successively, wash, dry the iron oxide yellow that gets product.
After testing, the finished product iron oxide yellow total iron of preparation is with Fe
2o
3meter, content is 99%.
embodiment 4
(1) ferrous sulfate is refining
At 70 DEG C, the iron vitriol solution 500ml utilizing byproduct ferrous sulfate of titanium dioxide compound concentration to be 490g/L, regulates the pH value of this solution to be 2.5 with hydrochloric acid, carries out titanium hydrolysis treatment to byproduct ferrous sulfate of titanium dioxide; 36g iron powder reducing Fe is added again in the iron vitriol solution after titanium hydrolysis treatment
3+and regulate pH to be 6.3, the precipitation obtaining magnesium, manganese, zinc simple substance reduced to magnesium, manganese, zine ion, when solution is cooled to room temperature, 0.12g polyacrylamide flocculant is added in the solution after titanium hydrolysis treatment and magnesium, manganese, zinc precipitation process, filter after stirring, standing sedimentation 1h, product after the hydrolysis of removing titanium and magnesium, manganese, zinc precipitation, filtrate is the copperas solution after refining;
(2) Fe (OH)
2generation
Get the copperas solution 375ml after described refining, add the NaOH solution of 16g30wt% wherein, at 39 DEG C, carry out neutralization reaction, hierarchy of control pH value is 7.2, and when the white precipitate of the generation in solution becomes blackish green, neutralization reaction terminates;
(3) iron oxide yellow JZPD capsule
Being diluted to concentration to reacted system solution in step (2) is 300g/L, passes into air wherein and reacts, and the speed passing into air is 150ml/min, namely per minute pass into that air capacity is reactor volume 1/20; When system pH reaches 3.5, i.e. obtained needle-like oyster iron oxide yellow crystal seed;
(4) oxidative synthesis
Being diluted to concentration to the iron oxide yellow crystal seed prepared in step (3) is 100g/L, be warming up to 81 DEG C, pass into air wherein, control air capacity is 5 times of the air capacity passed in step (3), and to add 55g iron sheet maintenance system pH value be 3.5, be oxidized and namely obtain iron oxide yellow slurries in more than 40 hours;
(5) aftertreatment
Iron oxide yellow slurries after step (4) process are filtered successively, wash, dry the iron oxide yellow that gets product.
After testing, the finished product iron oxide yellow total iron of preparation is with Fe
2o
3meter, content is 98%.
embodiment 5
(1) ferrous sulfate is refining
At 80 DEG C, the iron vitriol solution 500ml utilizing byproduct ferrous sulfate of titanium dioxide compound concentration to be 400g/L, regulates the pH value of this solution to be 2.0 with sulfuric acid, carries out titanium hydrolysis treatment to byproduct ferrous sulfate of titanium dioxide; 30g iron sheet reduction Fe is added again in the iron vitriol solution after titanium hydrolysis treatment
3+and regulate pH to be 6.5, the precipitation obtaining magnesium, manganese, zinc simple substance reduced to magnesium, manganese, zine ion, when solution is cooled to room temperature, 0.1g polyacrylamide flocculant is added in the solution after titanium hydrolysis treatment and magnesium, manganese, zinc precipitation process, filter after stirring, standing sedimentation 1.0h, product after the hydrolysis of removing titanium and magnesium, manganese, zinc precipitation, filtrate is the copperas solution after refining;
(2) Fe (OH)
2generation
Get the copperas solution 375ml after described refining, add the NaOH solution of 12g30wt% wherein, at 30 DEG C, carry out neutralization reaction, hierarchy of control pH value is 7.5, and when the white precipitate of the generation in solution becomes blackish green, neutralization reaction terminates;
(3) iron oxide yellow JZPD capsule
Being diluted to concentration to reacted system solution in step (2) is 300g/L, passes into air wherein and reacts, and the speed passing into air is 100ml/min, namely per minute pass into that air capacity is reactor volume 1/10; When system pH reaches 4.0, i.e. obtained needle-like oyster iron oxide yellow crystal seed;
(4) oxidative synthesis
Being diluted to concentration to the iron oxide yellow crystal seed prepared in step (3) is 100g/L, controlling the heating-up time is that 5h is slowly warming up to 85 DEG C, air is passed in the solution after dilution, control air capacity is 3 times of the air capacity passed in step (3), and to add 45g iron powder maintenance system pH value be 2.5, be oxidized and namely obtain iron oxide yellow slurries in more than 40 hours;
(5) aftertreatment
Iron oxide yellow slurries after step (4) process are filtered successively, wash, dry the iron oxide yellow that gets product.
After testing, the finished product iron oxide yellow total iron of preparation is with Fe
2o
3meter, content is 97%.
The finished product iron oxide yellow total iron prepared in above-described embodiment is with Fe
2o
3meter, content all 96 ~ 99%, and maximumly reaches 99%.
Produce the detection method of iron oxide yellow in particle-size analyzer and GB/T1863-2008 obtained in above-described embodiment and carry out the detections such as form and aspect, meet the iron oxide pigment national standard of GB/T1863-2008.
experimental example
The present invention has also carried out TEM characterization test to the iron oxide yellow prepared in above-described embodiment 1, and as shown in Figure 1, as we can see from the figure, the crystalline form of the iron oxide yellow of generation is fusiformis and aciculiform to test picture, does not exist cylindrical.
Obviously, above-described embodiment is only for clearly example being described, and the restriction not to embodiment.For those of ordinary skill in the field, can also make other changes in different forms on the basis of the above description.Here exhaustive without the need to also giving all embodiments, and thus the apparent change of extending out or variation be still among the protection domain of the invention claim.
Claims (14)
1. utilize byproduct ferrous sulfate of titanium dioxide to prepare a method for iron oxide yellow, comprise the steps:
(1) ferrous sulfate is refining
Utilize byproduct ferrous sulfate of titanium dioxide to prepare iron vitriol solution, regulate the pH value of this solution to be 1 ~ 2.5, byproduct ferrous sulfate of titanium dioxide is carried out to the hydrolysis treatment of titanium; Iron powder or iron sheet is added, to the Fe in solution in the iron vitriol solution after titanium hydrolysis treatment
3+carry out reduction treatment and the pH value of regulator solution is 6.0 ~ 6.5, byproduct ferrous sulfate of titanium dioxide is carried out to the precipitation process of magnesium, manganese, zinc; In the solution after titanium hydrolysis treatment and magnesium, manganese, zinc precipitation process, add flocculation agent, stir, filter after standing sedimentation, filtrate be refining after copperas solution;
(2) Fe (OH)
2generation
In the copperas solution after described refining, add alkaline solution, at 10 ~ 39 DEG C, carry out neutralization reaction, hierarchy of control pH value is 6.0 ~ 7.5, and when the white precipitate of the generation in solution becomes blackish green, neutralization reaction terminates;
(3) iron oxide yellow JZPD capsule
Reacted system solution in step (2) is diluted, passes into air wherein and react, when system pH reaches 3 ~ 4, i.e. obtained needle-like oyster iron oxide yellow crystal seed;
(4) oxidative synthesis
The iron oxide yellow crystal seed prepared in step (3) is diluted, slowly be warming up to 75 ~ 85 DEG C, pass into air wherein, control air capacity is 2 ~ 5 times of the air capacity passed in step (3), maintenance system pH value is 2 ~ 3.5, is oxidized and namely obtains iron oxide yellow slurries in more than 40 hours;
(5) aftertreatment
Iron oxide yellow slurries after step (4) process are filtered successively, wash, dry the iron oxide yellow that gets product.
2. the method utilizing byproduct ferrous sulfate of titanium dioxide to prepare iron oxide yellow according to claim 1, is characterized in that, in described step (1), at 10 ~ 80 DEG C, prepare described iron vitriol strength of solution is 350 ~ 490g/L.
3. the method utilizing byproduct ferrous sulfate of titanium dioxide to prepare iron oxide yellow according to claim 1 and 2, is characterized in that, in described step (1), the pH value regulating iron vitriol solution with sulfuric acid is 2.
4. the method utilizing byproduct ferrous sulfate of titanium dioxide to prepare iron oxide yellow according to claim 3, is characterized in that, in described step (1), the add-on of described flocculation agent is 0.05% of iron vitriol quality.
5. the method utilizing byproduct ferrous sulfate of titanium dioxide to prepare iron oxide yellow according to claim 4, it is characterized in that, in described step (1), before adding flocculation agent, solution after titanium hydrolysis treatment and magnesium, manganese, zinc precipitation process is lowered the temperature, reduces to room temperature to system temperature.
6. the method utilizing byproduct ferrous sulfate of titanium dioxide to prepare iron oxide yellow according to claim 5, is characterized in that, in step (1), the time of standing sedimentation is 1 ~ 2h.
7. the method utilizing byproduct ferrous sulfate of titanium dioxide to prepare iron oxide yellow according to claim 6, is characterized in that, in step (2), hierarchy of control pH value is 6.5 ~ 7.2.
8. prepare the method for iron oxide yellow according to the arbitrary described byproduct ferrous sulfate of titanium dioxide that utilizes of claim 5-7, it is characterized in that, the mass ratio of described alkaline solution and iron vitriol is 0.05 ~ 0.09.
9. the method utilizing byproduct ferrous sulfate of titanium dioxide to prepare iron oxide yellow according to claim 8, is characterized in that, in described step (3), reacted system solution in step (2) is diluted to 200 ~ 300g/L.
10. the method utilizing byproduct ferrous sulfate of titanium dioxide to prepare iron oxide yellow according to claim 9, is characterized in that, in described step (3), after 2.5 ~ 11 hours, system pH reaches 3 ~ 4.
11. methods utilizing byproduct ferrous sulfate of titanium dioxide to prepare iron oxide yellow according to claim 10, is characterized in that, in described step (4), be warming up to 75 ~ 85 DEG C in 4 ~ 8 hours.
12. prepare the method for iron oxide yellow according to the arbitrary described byproduct ferrous sulfate of titanium dioxide that utilizes of claim 9-11, it is characterized in that, in described step (3), per minute pass into that described air capacity is reactor volume 1/40 ~ 1/10.
13. methods utilizing byproduct ferrous sulfate of titanium dioxide to prepare iron oxide yellow according to claim 12, is characterized in that, in described step (4), in the solution after dilution, add excessive iron sheet, maintenance system pH value is 2 ~ 3.5.
14. methods utilizing byproduct ferrous sulfate of titanium dioxide to prepare iron oxide yellow according to claim 13, it is characterized in that, in described step (4), 100 ~ 150g/L is diluted to the iron oxide yellow crystal seed prepared in step (3).
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| CN105502512B (en) * | 2016-02-04 | 2017-06-20 | 天津大学 | A kind of method that iron oxide yellow is prepared by iron and steel pickling waste liquid |
| CN107352585A (en) * | 2017-08-02 | 2017-11-17 | 浙江神光材料科技有限公司 | The preparation method of transparent zinc-iron yellow pigment |
| CN108455681B (en) * | 2018-02-05 | 2020-07-14 | 吉林建筑大学 | Method for preparing iron oxide yellow pigment by using iron and aluminum-containing industrial wastewater |
| CN113061730A (en) * | 2021-03-23 | 2021-07-02 | 北京佰利格瑞资源科技有限公司 | Method for removing iron in waste ternary lithium battery recovery process |
| CN113104901B (en) * | 2021-04-13 | 2024-02-09 | 江西理工大学 | Method for preparing iron oxide yellow from rare earth waste acid leaching slag |
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