CN208883501U - A kind of deep refining system of complexity brine - Google Patents
A kind of deep refining system of complexity brine Download PDFInfo
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- CN208883501U CN208883501U CN201821618926.7U CN201821618926U CN208883501U CN 208883501 U CN208883501 U CN 208883501U CN 201821618926 U CN201821618926 U CN 201821618926U CN 208883501 U CN208883501 U CN 208883501U
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Abstract
The utility model discloses a kind of deep refining systems of complicated brine comprising the oblique choline pond of circle, muddy lye heat exchanger, muddy lye flocculation settling tank, primary purification brine overflow ladle, primary purification brine pump, brine precoat filter, secondary refining brine storage tank.The utility model is in trona production process of sodium bicarbonate, the system for carrying out deep refining for the poor tailing complexity brine of trona, iron content in suspension content, brine turbidity, brine in reduction brine, improves the whiteness index of sodium bicarbonate product, it is made to meet production requirement.
Description
Technical field:
The utility model relates to a kind of deep refining systems of complicated brine, more particularly to a kind of economic and practical poor tailing
The deep refining system of complicated brine.
Background technique:
Brine refining mainly includes the technical indicators such as insoluble suspended matter, soluble impurity element in removal brine, is
The main technical process of the industries such as chemical industry, food directly determines the quality of production method and product, such as ammonia-soda process, union soda, chlorine
The purification of raw material sodium chloride brine in alkali industry, purification, purification of some industrial chemicals liquid of brine etc. in natural alkaline process.
Existing Brine Purification Process technology has membrane filter method, sand filtration method, absorption method and chemical precipitation method etc., main according to not
With material source, various processes technology, the Brine Purification Process using each self application is needed.
In natural alkaline process production technology, especially lake Hunan deposits alkali mine, and processing technology is different from ammonia-soda process and connection alkali
Method is broadly divided into standby making from brine and refinement, brine carbonization workshop section, mother liquor hygroscopic water solution, filtration drying packing department, in choline
In the brine of preparation, brine composition is complicated, and impurity content is higher in material, and suspended matter partial size is smaller, using traditional membrane filter method
Fenestra road can be blocked quickly；When using sand filtration method, since the suspended matter partial size in brine is too small, it is difficult to filter out by sandstone；
Absorption method is mainly to use the removal of trace suspension object and solvent borne ion in water, and the suspended matter in the brine of this system is too many,
It cannot use；And chemical precipitation method mainly uses some coagulant, and it is stringenter to the pH value requirement of material, it needs between 5-9,
Alkaline brine is greater than 9 in alkalinity and pH；Therefore it can not use.
Utility model content:
The purpose of this utility model is to provide a kind of deep refining systems of complicated brine.
The utility model is implemented by following technical solution: a kind of deep refining system of complexity brine comprising circle obliqueization
Alkali pool, muddy lye heat exchanger, muddy lye flocculation settling tank, primary purification brine overflow ladle, primary purification brine pump, brine precoating
The discharge port of filter, secondary refining brine storage tank, the oblique choline pond of circle is connected to the outer comb of impurity, the oblique choline pond of circle
Liquid outlet be connected to the cold medium entrance of the muddy lye heat exchanger, the outlet of the cold medium of the muddy lye heat exchanger with it is described
The discharge port of the feed inlet connection of muddy lye flocculation settling tank, the muddy lye flocculation settling tank is connected to alkali mud outlet pipeline,
The liquid outlet of the muddy lye flocculation settling tank is connected to the feed inlet of the primary purification brine overflow ladle, the primary purification
The overflow port of brine overflow ladle is connected to the feed inlet of the primary purification brine pump, the discharge port of the primary purification brine pump
It is connected to the feed inlet of the brine precoat filter, the liquid outlet of the brine precoat filter and the secondary refining brine
Storage tank connection, the discharge port of the brine precoat filter are connect with waste residue outlet pipeline.
It further, further include steam pipe, the steam pipe is connected to the thermal medium entrance of the muddy lye heat exchanger,
The thermal medium outlet of the muddy lye heat exchanger is connected to the feed inlet in the oblique choline pond of the circle.
It further, further include muddy lye pump, the oblique choline pond of circle is connected to the feed inlet of the muddy lye pump, institute
The discharge port for stating muddy lye pump is connected to the cold medium entrance of the muddy lye heat exchanger.
It further, further include diatomite precoating pump, the discharge port and the brine of the diatomite precoating pump precoat
The feed inlet of filter is connected to.
It further, further include filter aid pump, the discharge port and the primary purification brine pump of the filter aid pump
Feed inlet connection.
It further, further include flocculant pump, the discharge port of the flocculant pump and the muddy lye flocculation settling tank
Inlet connection.
The utility model is to carry out depth for the poor tailing complexity brine of trona in trona production process of sodium bicarbonate
The system of purification reduces suspension content, brine turbidity, iron content in brine in brine, improves the whiteness of sodium bicarbonate product
Index makes it meet production requirement.
Utility model has the advantages that (1) uses flocculation sedimentation technology for poor tailing complexity brine in alkali producing process
Flocculant 40-100ppm is added in the muddy lye of solid content 10-20wt%, obtains primary purification brine suspension content 100-
500mg/l, turbidity 20-50NTU；(2) precoat filtration technology is used, filter aid is added to 200- in primary purification brine
600ppm obtains secondary refining brine, suspension content≤35mg/l, turbidity≤15NTU after filtering.(3) in circle obliqueization
Vulcanized sodium is added during muddy lye is made in alkali, generates ferrous sulfide precipitating and is adsorbed by alkali mud, removes during flocculation sedimentation,
The iron content in brine is reduced, iron rate >=60% is removed.(4) it by the complicated brine after deep refining, is carbonized to obtain small
Soda product whiteness >=85 are up-to-standard, and quality is greatly improved.
Detailed description of the invention:
In order to illustrate the embodiment of the utility model or the technical proposal in the existing technology more clearly, below will be to embodiment
Or attached drawing needed to be used in the description of the prior art is briefly described, it should be apparent that, the accompanying drawings in the following description is only
It is some embodiments of the utility model, for those of ordinary skill in the art, in the premise not made the creative labor
Under, it is also possible to obtain other drawings based on these drawings.
Fig. 1 is a kind of schematic diagram of the deep refining system of complicated brine in present embodiment；
Specific embodiment:
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are without creative efforts
Every other embodiment obtained, fall within the protection scope of the utility model.
A kind of deep refining system of complexity brine comprising the oblique choline pond 1 of circle, muddy lye pump 2, muddy lye heat exchanger 3,
It is diatomite precoating pump 4, filter aid pump 5, flocculant pump 6, muddy lye flocculation settling tank 7, primary purification brine overflow ladle 8, primary
Refine brine pump 9, brine precoat filter 10, secondary refining brine storage tank 11, the discharge port and impurity outlet in the oblique choline pond 1 of circle
Pipe 12 is connected to, and the liquid outlet in the oblique choline pond 1 of circle is connected to the feed inlet of muddy lye pump 2, the discharge port and muddy lye of muddy lye pump 2
The cold medium entrance of heat exchanger 3 is connected to, the cold medium outlet of muddy lye heat exchanger 3 and the feed inlet of muddy lye flocculation settling tank 7
The discharge port of connection, muddy lye flocculation settling tank 7 is connected to alkali mud outlet pipeline 13, the liquid outlet of muddy lye flocculation settling tank 7
It is connected to the feed inlet of primary purification brine overflow ladle 8, the overflow port and primary purification brine pump of primary purification brine overflow ladle 8
9 feed inlet connection, the discharge port of primary purification brine pump 9 are connected to the feed inlet of brine precoat filter 10, brine precoating
The liquid outlet of filter 10 is connected to secondary refining brine storage tank 11, the outer comb of the discharge port and waste residue of brine precoat filter 10
Line 14 connects.
The discharge port of diatomite precoating pump 4 is connected to the feed inlet of brine precoat filter 10, the discharge port of filter aid pump 5
It is connected to the feed inlet of primary purification brine pump 9, the discharge port of flocculant pump 6 and the inlet of muddy lye flocculation settling tank 7 connect
It is logical.
It further includes steam pipe 15, and steam pipe 15 is connected to the thermal medium entrance of muddy lye heat exchanger 3, muddy lye heat exchanger
3 thermal medium outlet is connected to the feed inlet in the oblique choline pond 1 of circle.
System process is described as follows:
Winter production work pattern,
(1) it is added in the oblique choline pond 1 of circle from the mined trona raw material d in lake region, from hygroscopic water solution workshop section
Complete liquid c, the vulcanized sodium solid b being added in oblique 1 central draft tube of choline pond of circle and the steaming from muddy lye heat exchanger
Vapor condensed water recycles choline by muddy lye pump 2 and obtains total alkali concentration 100g/l, 60 DEG C, the muddy lye of solid content 10-20wt%；
(2) the muddy lye of qualified is sent by muddy lye pump 2 to muddy lye flocculation settling tank 7, is added on feed-line
Enter the flocculant solution h of a ten thousandth concentration in muddy lye to 40-100ppm, carries out flocculation clarification；
(3) muddy lye flocculation 7 supernatant liquor overflow of settling tank enters primary purification brine overflow ladle 8, and lower layer alkali mud i passes through alkali
13 outflow system of mud outlet pipeline；
(4) primary purification brine is sent by primary purification brine pump 9 to brine precoat filter 10, is added on export pipeline
Enter filter aid slurry g to about 200-600ppm, brine precoat filter 10 needs to precoat the 10wt% from diatomite precoating pump 4
Diatomite slurry f, precoating amount about 0.5kg/m2, the waste residue j of filtering is by 14 outflow system of waste residue outlet pipeline, and filtered two
Secondary purification brine flows into secondary refining brine storage tank 11, is raw material-secondary refining brine k that lower C1 chemical industry section uses.
Spring, summer, autumn production operation mode,
(1) it is added in the oblique choline pond 1 of circle from the mined trona raw material d in lake region, from lake region and washes mud day
Shine evaporation brine c, the vulcanized sodium solid b being added in oblique 1 central draft tube of choline pond of circle and from muddy lye heat exchanger
3 steam condensation water, by muddy lye pump 2 recycle choline obtain total alkali concentration 100g/l, 60 DEG C, solid content 10-20wt% it is muddy
Lye；
(2) the muddy lye of qualified is sent by muddy lye pump 2 to muddy lye flocculation settling tank 7, is added on feed-line
Enter the flocculant solution h of a ten thousandth concentration in muddy lye to 40-100ppm, carries out flocculation clarification；
(3) muddy lye flocculation 7 supernatant liquor overflow of settling tank enters primary purification brine overflow ladle 8, and lower layer alkali mud i passes through alkali
13 outflow system of mud outlet pipeline；
(4) primary purification brine is sent by primary purification brine pump 9 to brine precoat filter 10, is added on export pipeline
Enter filter aid slurry g to about 200-600ppm, brine precoat filter 10 needs to precoat the 10wt% from diatomite precoating pump 4
Diatomite slurry f, precoating amount about 0.5kg/m2, the waste residue j of filtering is by 14 outflow system of waste residue outlet pipeline, and filtered two
Secondary purification brine flows into secondary refining brine storage tank 11, is raw material-secondary refining brine k that lower C1 chemical industry section uses.
Since the insoluble solid content in trona raw material is very high, 20wt% is reached by solid content after water-soluble choline, because
This can only realize the primary purification of brine by flocculation sedimentation technology, implement secondary brine refining according to sand filtration method, using stone
Sand filter, 2 meters of bed height, bed layer flow speed 5m/h.A brine turbidity into sand filter is greater than 35NTU, total suspended matter
Content is greater than 300mg/l, and the secondary refining brine turbidity of sand filter is greater than 20NTU out, and suspension content is greater than 200mg/l, greatly
Partial suspended thing is not filtered, and causes the whiteness of product less than 85.Same brine implements brine two using precoat filtration method
Secondary purification, by diatomite precoat filter, is realized by adding the super-cell of 200-600ppm in a brine
The secondary refining of brine, brine turbidity≤15NTU, total suspended matter≤35mg/l, product whiteness >=85.
The above is only the preferred embodiment of the utility model only, is not intended to limit the utility model, all at this
Within the spirit and principle of utility model, any modification, equivalent replacement, improvement and so on should be included in the utility model
Protection scope within.
Claims (6)
1. a kind of deep refining system of complexity brine, which is characterized in that it includes the oblique choline pond (1) of circle, muddy lye heat exchanger
(3), muddy lye flocculation settling tank (7), primary purification brine overflow ladle (8), primary purification brine pump (9), brine precoat filtration
Device (10), secondary refining brine storage tank (11),
The discharge port of the oblique choline pond (1) of circle and impurity outer comb (12) be connected tos, the liquid outlet of the oblique choline pond (1) of circle and
The cold medium entrance of the muddy lye heat exchanger (3) is connected to, cold medium outlet and the muddy alkali of the muddy lye heat exchanger (3)
The feed inlet connection of liquid flocculation settling tank (7), the discharge port and alkali mud outlet pipeline (13) of muddy lye flocculation settling tank (7)
The liquid outlet of connection, muddy lye flocculation settling tank (7) is connected to the feed inlet of the primary purification brine overflow ladle (8),
The overflow port of the primary purification brine overflow ladle (8) is connected to the feed inlet of the primary purification brine pump (9), described primary
The discharge port of purification brine pump (9) is connected to the feed inlet of the brine precoat filter (10), the brine precoat filter
(10) liquid outlet is connected to the secondary refining brine storage tank (11), the discharge port of the brine precoat filter (10) and useless
Slag outlet pipeline (14) connection.
2. a kind of deep refining system of complicated brine according to claim 1, which is characterized in that it further includes steam pipe
(15), the steam pipe (15) is connected to the thermal medium entrance of the muddy lye heat exchanger (3), the muddy lye heat exchanger (3)
Thermal medium outlet be connected to the feed inlet of the oblique choline pond (1) of the circle.
3. a kind of deep refining system of complicated brine according to claim 1, which is characterized in that it further includes muddy lye pump
(2), the oblique choline pond (1) of the circle is connected to the feed inlet of the muddy lye pump (2), the discharge port of the muddy lye pump (2) with
The cold medium entrance of the muddy lye heat exchanger (3) is connected to.
4. a kind of deep refining system of complicated brine according to claim 1, which is characterized in that it further includes that diatomite is pre-
Pump (4) is applied, the discharge port of the diatomite precoating pump (4) is connected to the feed inlet of the brine precoat filter (10).
5. a kind of deep refining system of complicated brine according to claim 1, which is characterized in that it further includes filter aid pump
(5), the discharge port of the filter aid pump (5) is connected to the feed inlet of the primary purification brine pump (9).
6. a kind of deep refining system of complicated brine according to claim 1, which is characterized in that it further includes flocculant pump
(6), the discharge port of the flocculant pump (6) is connected to the inlet of muddy lye flocculation settling tank (7).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821618926.7U CN208883501U (en) | 2018-09-29 | 2018-09-29 | A kind of deep refining system of complexity brine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821618926.7U CN208883501U (en) | 2018-09-29 | 2018-09-29 | A kind of deep refining system of complexity brine |
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| Publication Number | Publication Date |
|---|---|
| CN208883501U true CN208883501U (en) | 2019-05-21 |
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ID=66515017
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| Application Number | Title | Priority Date | Filing Date |
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| CN201821618926.7U Active CN208883501U (en) | 2018-09-29 | 2018-09-29 | A kind of deep refining system of complexity brine |
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| Country | Link |
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2018
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