CN106986367A - A kind of method that atlapulgite spent acid mother liquor prepares soda alum - Google Patents
A kind of method that atlapulgite spent acid mother liquor prepares soda alum Download PDFInfo
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- CN106986367A CN106986367A CN201710241636.9A CN201710241636A CN106986367A CN 106986367 A CN106986367 A CN 106986367A CN 201710241636 A CN201710241636 A CN 201710241636A CN 106986367 A CN106986367 A CN 106986367A
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- Prior art keywords
- soda alum
- mother liquor
- spent acid
- alum
- acid mother
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01F—COMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
- C01F7/00—Compounds of aluminium
- C01F7/68—Aluminium compounds containing sulfur
- C01F7/74—Sulfates
- C01F7/76—Double salts, i.e. compounds containing, besides aluminium and sulfate ions, only other cations, e.g. alums
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2006/00—Physical properties of inorganic compounds
- C01P2006/80—Compositional purity
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Inorganic Chemistry (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The invention discloses a kind of method that atlapulgite spent acid mother liquor prepares soda alum, belong to atlapulgite wastewater treatment and inorganic salts preparing technical field.The present invention is to utilize sulfuric acid, the aluminum sulfate in atlapulgite spent acid mother liquor, is reacted with aluminium hydroxide and sodium hydroxide, and through flocculation, pure soda alum is made after the steps such as removal of impurities, crystallization, press filtration, dehydration.The present invention uses polyaluminium sulfate as flocculant, pass through further optimize technique simultaneously, so that the alum purity obtained by the method for the present invention reaches more than 99.86%, increase rate must be measured and reach more than 15.89%, " a kind of utilization activated clay production waste prepares the method (publication number of soda alum than prior art：CN105271588A it is) " high.
Description
【Technical field】
The present invention relates to atlapulgite wastewater treatment and inorganic salts preparation field, and in particular to a kind of atlapulgite spent acid is female
The method that liquid prepares soda alum.
【Background technology】
Atlapulgite is mainly used in the decolorizing and refining of mineral oil, vegetable oil and animal fat, is a kind of important oil
Work and daily-use chemical industry raw material.Atlapulgite is, using bentonite as raw material, mainly to be processed using wet method acidification technique.It is produced
Process includes：Bentonite aquation plus sulfuric acid activated, washing, dry, crushing., need to be through washing repeatedly just because its product acid content is big
Acid content can be made to be less than 0.2%, to reach the requirement of HG/T2569-94 product standards.It is different according to method, what water-washing process was produced
Wastewater flow rate has different, but the wastewater flow rate that production 1t atlapulgites are produced typically is no less than 30-40t.Mainly contain in the waste water
There are aluminum sulfate and unreacted sulfuric acid that bentonite acidification reaction is produced etc., if directly discharging, not only waste substantial amounts of resource,
And serious pollution can be caused to environment.
In recent years, the improvement and recycling for activated clay production waste have pointed out certain methods, and such as lime is neutralized
Method, carbide slag neutralisation, time acid activation method, and china clay is decomposed with process industry water treatment agent aluminum sulfate with it, dissolve iron filings
Manufacture green vitriol etc..These methods, what is had preferably solves the governing problem of activated clay production waste, and such as lime neutralisation is led to
Crossing addition lime can be neutralized the acidity in waste water, make the formation such as sulfate ion, aluminium ion and iron ion calcium sulfate, hydrogen
Aluminum oxide, iron hydroxide etc. are precipitated and removed, but these sediments turn into new solid waste because that can not be utilized；What is had is preferable
Ground solves the problems, such as the recycling of resource in activated clay production waste, such as decomposes china clay with it with process industry water process
The method of agent aluminum sulfate is exactly to decompose china clay using the sulfuric acid in waste water, and the aluminium in china clay is leached to solution, then passes through
Purification and impurity removal, evaporative crystallization, separation drying, crushing packing obtain aluminum sulfate, and the method is although efficiently utilize activated clay production
Resources such as sulfuric acid, aluminum sulfate in waste water, but because the impurity such as iron ion can influence the quality of product aluminum sulfate, thus must be through
Purification and impurity removal process is removed.At present frequently with activated manganese dioxide method except iron is, it is necessary to which expensive manganese salt, causes processing
Cost is higher.
Soda alum chemical name aluminum sodium sulfate, is white particulate or powdery.Met generation carbon dioxide with sodium acid carbonate, so
Food additives yeast powder is commonly used for, mordant, waterproofing agent are used as in textile industry, ceramics, tanning is may be additionally used for, makes
The industries such as paper, match, ink, purified water, refined sugar.The current main production process of the product is made with sulfuric acid treatment bauxite
Aluminum sulfate, then with sodium sulphate react, then purified, evaporation, crystallisation by cooling, filtering, drying and obtain.
" a kind of utilization activated clay production waste prepares the method (publication number of soda alum to patent：CN105271588A) ",
A kind of open method for preparing soda alum of knowing clearly, but this method is the problem of have purity and relatively low yield..
【The content of the invention】
The present invention provides a kind of method that atlapulgite spent acid mother liquor prepares soda alum, white to solve activity in the prior art
Native spent acid mother liquor prepares the problem of soda alum has purity and relatively low yield.The present invention uses polyaluminium sulfate as flocculation
Agent, while passing through further optimize technique so that the alum purity obtained by method of the invention reaches more than 99.86%, obtains
Amount increase rate reaches more than 15.89%, than prior art " a kind of method that utilization activated clay production waste prepares soda alum
(publication number：CN105271588A it is) " high.
To solve above technical problem, the present invention uses following technical scheme：
A kind of method that atlapulgite spent acid mother liquor prepares soda alum, comprises the following steps：
S1：Aluminium hydroxide is added to atlapulgite spent acid mother liquor, the stirring and dissolving aluminium hydroxide in the case where temperature is 91-94 DEG C,
Sodium hydroxide is added to above-mentioned solution, makes Na in solution+:Al3+:SO4 2-Mol ratio be 1-1.01:1:2-2.04, and regulation pH
It is worth for 4-4.3, adds after flocculant, coacervation soda alum, be then filtered to remove impurity, resulting solution crystallisation by cooling, then press filtration
Obtain the thick soda alum of filter cake；
S2：Thick soda alum is put into water, heating and stirring makes thick soda alum add flocculant, coacervation sodium after being completely dissolved
After alum, impurity is then removed again, press filtration obtains filter cake to resulting solution after crystallisation by cooling again, and gained filter cake is put into centrifugation
Moisture is removed in machine, that is, pure soda alum is made.
Preferably, the temperature of stirring and dissolving aluminium hydroxide is 94 DEG C in step S1.
Preferably, Na in step S1+:Al3+:SO4 2-Mol ratio be 1:1:2.
Preferably, flocculant described in step S1 and step S2 is polyaluminium sulfate.
Preferably, the temperature of crystallisation by cooling is less than 9 DEG C in step S1 and step S2.
Preferably, the pressure of press filtration is 0.92-0.97Mpa in step S1 and step S2.
Preferably, the pressure of the press filtration is 0.97Mpa.
Preferably, water is put into step S2 makes concentration of polymer solution be 57%-59%.
Preferably, the dewatered rotating speed of centrifuge is 4000-5000r/min in step S2, and the time of water removal is 8-
10min。
Preferably, the dewatered rotating speed of centrifuge is 5000r/min, and the time of water removal is 8min.
The invention has the advantages that：
The present invention uses polyaluminium sulfate as flocculant, and polyaluminium sulfate is composite polymer polymer, molecule knot
Structure is huge, high adsorption capacity, and the floccule body formed after input water is big, and settling velocity is fast, and activity is high, and filterability is good, passes through simultaneously
Further optimize technique so that the alum purity obtained by method of the invention reaches more than 99.86%, and the amount of obtaining increase rate reaches
More than 15.89%, than prior art, " a kind of utilization activated clay production waste prepares the method (publication number of soda alum：
CN105271588A it is) " high.
【Brief description of the drawings】
Fig. 1 is the process chart that atlapulgite spent acid mother liquor of the present invention prepares soda alum.
【Embodiment】
For ease of more fully understanding the present invention, it is illustrated by following examples, these embodiments belong to the present invention's
Protection domain, but do not limit the scope of the invention.
In embodiment, the method that the atlapulgite spent acid mother liquor prepares soda alum comprises the following steps：
S1：Aluminium hydroxide is added to atlapulgite spent acid mother liquor, the stirring and dissolving aluminium hydroxide in the case where temperature is 91-94 DEG C,
Sodium hydroxide is added to above-mentioned solution, makes Na in solution+:Al3+:SO4 2-Mol ratio be 1-1.01:1:2-2.04, and regulation pH
It is worth for 4-4.3, adds after polyaluminium sulfate, coacervation soda alum, be then filtered to remove impurity, resulting solution chilling temperature is 9 DEG C
Crystallization below, then in the case where pressure is 0.92-0.97Mpa, press filtration obtains the thick soda alum of filter cake；
S2：Thick soda alum is put into water, heating and stirring makes thick soda alum make the concentration of polymer solution be after being completely dissolved
57%-59%, adds after polyaluminium sulfate, coacervation soda alum, impurity is then removed again, chilling temperature is resulting solution again
After 9 DEG C of crystallization below, in the case where pressure is 0.92-0.97Mpa, press filtration obtains filter cake, and gained filter cake is put into rotating speed for 4000-
Moisture is removed in 5000r/min centrifuges, the time of water removal is 8-10min, that is, pure soda alum is made.
Embodiment 1
A kind of method that atlapulgite spent acid mother liquor prepares soda alum, comprises the following steps：
S1：Aluminium hydroxide is added to atlapulgite spent acid mother liquor, the stirring and dissolving aluminium hydroxide in the case where temperature is 93 DEG C, upwards
State solution and add sodium hydroxide, make Na in solution+:Al3+:SO4 2-Mol ratio be 1:1:2.02, and regulation pH value is 4, is added
After polyaluminium sulfate, coacervation soda alum, impurity is then filtered to remove, resulting solution chilling temperature is 8 DEG C of crystallizations, then in pressure
The thick soda alum of filter cake is obtained for press filtration under 0.96Mpa；
S2：Thick soda alum is put into water, heating and stirring makes thick soda alum make the concentration of polymer solution be after being completely dissolved
57%, add after polyaluminium sulfate, coacervation soda alum, impurity is then removed again, chilling temperature is 8 DEG C to resulting solution again
After crystallization, in the case where pressure is 0.95Mpa, press filtration obtains filter cake, and gained filter cake is put into rotating speed to remove in 5000r/min centrifuges
Moisture is removed, the time of water removal is 8min, that is, pure soda alum is made.
Embodiment 2
A kind of method that atlapulgite spent acid mother liquor prepares soda alum, comprises the following steps：
S1：Aluminium hydroxide is added to atlapulgite spent acid mother liquor, the stirring and dissolving aluminium hydroxide in the case where temperature is 94 DEG C, upwards
State solution and add sodium hydroxide, make Na in solution+:Al3+:SO4 2-Mol ratio be 1.01:1:2.04, and regulation pH value is 4.2,
Add after polyaluminium sulfate, coacervation soda alum, be then filtered to remove impurity, resulting solution chilling temperature is 7 DEG C of crystallizations, Ran Hou
Pressure obtains the thick soda alum of filter cake for press filtration under 0.97Mpa；
S2：Thick soda alum is put into water, heating and stirring makes thick soda alum make the concentration of polymer solution be after being completely dissolved
57%, add after polyaluminium sulfate, coacervation soda alum, impurity is then removed again, chilling temperature is 7 DEG C to resulting solution again
After crystallization, in the case where pressure is 0.92Mpa, press filtration obtains filter cake, and gained filter cake is put into rotating speed to remove in 40000r/min centrifuges
Moisture is removed, the time of water removal is 10min, that is, pure soda alum is made.
Embodiment 3
A kind of method that atlapulgite spent acid mother liquor prepares soda alum, comprises the following steps：
S1：Aluminium hydroxide is added to atlapulgite spent acid mother liquor, the stirring and dissolving aluminium hydroxide in the case where temperature is 91 DEG C, upwards
State solution and add sodium hydroxide, make Na in solution+:Al3+:SO4 2-Mol ratio be 1.01:1:2.01, and regulation pH value is 4.2,
Add after polyaluminium sulfate, coacervation soda alum, be then filtered to remove impurity, resulting solution chilling temperature is 9 DEG C of crystallizations, Ran Hou
Pressure obtains the thick soda alum of filter cake for press filtration under 0.97Mpa；
S2：Thick soda alum is put into water, heating and stirring makes thick soda alum make the concentration of polymer solution be after being completely dissolved
59%, add after polyaluminium sulfate, coacervation soda alum, impurity is then removed again, chilling temperature is 7 DEG C to resulting solution again
After crystallization, in the case where pressure is 0.92Mpa, press filtration obtains filter cake, and gained filter cake is put into rotating speed to remove in 4500r/min centrifuges
Moisture is removed, the time of water removal is 9min, that is, pure soda alum is made.
Comparative example 1-3, using " a kind of utilization activated clay production waste prepares the method (publication number of soda alum：
CN105271588A the embodiment 1-3 methods in) " prepare soda alum.
Soda alum purity in embodiment and comparative example, it increase rate result must be measured see the table below, wherein setting bright by sodium in comparative example
It is 0 that alum, which must measure increase rate, and other must measure increase rate in contrast.
| Soda alum purity (%) | Soda alum must measure increase rate (%) | |
| Embodiment 1 | 99.89 | 16.57 |
| Embodiment 2 | 99.92 | 15.89 |
| Embodiment 3 | 99.86 | 16.16 |
| Comparative example 1 | 99.5 | 0 |
| Comparative example 2 | 99.6 | 0.52 |
| Comparative example 3 | 99.8 | 0.68 |
As seen from the above table, the soda alum purity obtained by method of the invention reaches more than 99.86%, and the amount of obtaining increase rate reaches
More than 15.89%, it is higher than prior art, it is seen that not only purity is high and yield is also high for soda alum made from present invention process.
Embodiments of the invention are the foregoing is only, are not intended to limit the invention, it is all in the spirit and principles in the present invention
Within any modification, equivalent substitution and improvements made etc., should be included in the scope of the protection.
Claims (10)
1. a kind of method that atlapulgite spent acid mother liquor prepares soda alum, it is characterised in that：Comprise the following steps：
S1：Aluminium hydroxide is added to atlapulgite spent acid mother liquor, the stirring and dissolving aluminium hydroxide in the case where temperature is 91-94 DEG C, upwards
State solution and add sodium hydroxide, make Na in solution+:Al3+:SO4 2-Mol ratio be 1-1.01:1:2-2.04, and regulation pH value be
4-4.3, adds after flocculant, coacervation soda alum, is then filtered to remove impurity, resulting solution crystallisation by cooling, then press filtration is obtained
The thick soda alum of filter cake；
S2：Thick soda alum is put into water, heating and stirring makes thick soda alum add flocculant, coacervation soda alum after being completely dissolved
Afterwards, impurity is then removed again, press filtration obtains filter cake to resulting solution after crystallisation by cooling again, and gained filter cake is put into centrifuge
Moisture is removed, that is, pure soda alum is made.
2. the method that atlapulgite spent acid mother liquor according to claim 1 prepares soda alum, it is characterised in that：In step S1
The temperature of stirring and dissolving aluminium hydroxide is 94 DEG C.
3. the method that atlapulgite spent acid mother liquor according to claim 1 prepares soda alum, it is characterised in that：In step S1
Na+:Al3+:SO4 2-Mol ratio be 1:1:2.
4. the method that atlapulgite spent acid mother liquor according to claim 1 prepares soda alum, it is characterised in that：Step S1 and
Flocculant described in step S2 is polyaluminium sulfate.
5. the method that atlapulgite spent acid mother liquor according to claim 1 prepares soda alum, it is characterised in that：Step S1 and
The temperature of crystallisation by cooling is less than 9 DEG C in step S2.
6. the method that atlapulgite spent acid mother liquor according to claim 1 prepares soda alum, it is characterised in that：Step S1 and
The pressure of press filtration is 0.92-0.97Mpa in step S2.
7. the method that atlapulgite spent acid mother liquor according to claim 6 prepares soda alum, it is characterised in that：The press filtration
Pressure be 0.97Mpa.
8. the method that atlapulgite spent acid mother liquor according to claim 1 prepares soda alum, it is characterised in that：In step S2
Input water makes concentration of polymer solution be 57%-59%.
9. the method that atlapulgite spent acid mother liquor according to claim 1 prepares soda alum, it is characterised in that：In step S2
The dewatered rotating speed of centrifuge is 4000-5000r/min, and the time of water removal is 8-10min.
10. the method that atlapulgite spent acid mother liquor according to claim 9 prepares soda alum, it is characterised in that：Centrifuge
Dewatered rotating speed is 5000r/min, and the time of water removal is 8min.
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| CN101671048A (en) * | 2009-09-30 | 2010-03-17 | 合肥工业大学 | Method for recovering and preparing alum from activated clay production waste liquid |
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