CN205500802U - Wen peng pond - Google Patents
Wen peng pond Download PDFInfo
- Publication number
- CN205500802U CN205500802U CN201620283368.8U CN201620283368U CN205500802U CN 205500802 U CN205500802 U CN 205500802U CN 201620283368 U CN201620283368 U CN 201620283368U CN 205500802 U CN205500802 U CN 205500802U
- Authority
- CN
- China
- Prior art keywords
- pond
- pool wall
- cell body
- wen peng
- lithium carbonate
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Landscapes
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
The utility model relates to a wen peng pond, its characterized in that, this wen peng pond include the cell body and with this cell body sealing connection's printing opacity cover, this cell body includes pool wall and gradient bottom of the pool, this gradient bottom of the pool include a plurality of horizontal bottom of the pools and a plurality of and the inclined plane of a plurality of horizontal bottom of the pools slope.
Description
Technical field
This utility model relates to the device that salt develops, and particularly relates to a kind of Wen Peng pond.
Background technology
Utilizing solar pond is that current salt carries lithium as crystallizing pond crystallization lithium carbonate from carbonate type bittern
One of technique.
As it is shown on figure 3, tradition solar pond includes higher troposphere 1, non-convection layer 2 (salinity gradient from top to bottom
Layer), lower troposphere 3, higher troposphere 1 generally fresh water (or dilute salt), be used for keeping salt in pond
Salinity gradient and the effect of wind resistance force-disturbance;There is salinity gradient from top to bottom and temperature ladder in non-convection layer 2
Degree, is the heat-insulation layer of solar pond;Lower troposphere 3 is made up of the saline solution of high concentration, and Main Function is thermal-arrest
And accumulation of heat, it is used for gathering storage solar energy.In solar pond, due to the depositing of salinity gradient of non-convection layer 2
, the generation of thermal convection current will be stoped, and keep the heat stability of solar pond.In this case, lower convection current
The heat of layer 3 can only be delivered to pool surface in thermo-conducting manner, rather than troposphere 2 water layer is the thickest, typically
The degree of depth up to 1~1.5m, has preferable heat-proof quality, and the temperature in lower troposphere 3 can reach 50 DEG C.
Utilize tradition solar pond during crystallization lithium carbonate from carbonate type bittern, when come from the external world
Low temperature richness lithium carbonate brine imports lower troposphere 3, due to higher troposphere 1 and the effect of non-convection layer 2,
The rich lithium carbonate brine making lower troposphere 3 is maintained under higher temperature environment, due to lithium carbonate dissolubility
Negative temperature effect, thus gradually separate out crystallization of lithium carbonate body in lower troposphere 3.
But, utilize tradition solar pond from carbonate type bittern during crystallization lithium carbonate, exist with
Lower deficiency: firstly, since low temperature richness lithium carbonate brine relies in lower troposphere 3 in tradition solar pond
The effect of troposphere 1 and non-convection layer 2 carries out accumulation of heat, insulation, and the speed of separating out of such lithium carbonate is relatively slow,
Productivity is low.Secondly, tradition solar pond is not closed structure, when ambient temperature is relatively low, and higher troposphere 1
Can freeze, thus affect solar energy and transmit downwards, thus affect salinity gradient and the insulation effect of non-convection layer 2
Really, so descend troposphere 3 just can not maintain higher temperature, thus affect the crystallization of lithium carbonate.Again
Secondary, tradition solar pond is affected bigger by outside air temperature, it is impossible to whole year operation, limits the yield of lithium carbonate.
Thirdly, higher troposphere 1 is highly prone to strong wind, sand and dust affect and are destroyed, and loses insulation more or less
And with the salinity gradient effect of non-convection layer 2.
Therefore, improve the structure of solar pond, improve the solar pond crystallization rate to lithium carbonate, extend solar pond
Year run the time, thus the crystallizing cycle shortening lithium carbonate is lithium carbonate salt lake carries lithium process-technology-evolutions
One of direction.
Utility model content
This utility model aims to provide that a kind of running temperature is high, annual exercisable to be carried for sulphate lake salt
The Wen Peng pond of lithium.
A kind of Wen Peng pond includes cell body and the diffuser being tightly connected with this cell body, and this cell body includes pool wall and ladder
At the bottom of degree pond, include at the bottom of multiple horizontal pond at the bottom of this gradient pond and multiple and the plurality of horizontal pond slanted floor inclined-plane.
Alternatively, described cell body includes the second pool wall that the first pool wall is relative with this first pool wall, connecting should
First pool wall and two the 3rd pool walls of the second pool wall, the width of described first pool wall is more than described second pool wall
Width, the degree of depth of described second pool wall is more than the degree of depth of described first pool wall.
Alternatively, the degree of depth of described cell body gradually deepens to the direction of the second pool wall from the first pool wall.
Alternatively, described first pool wall arranges multiple water inlet, and described second pool wall arranges multiple outlet.
Alternatively, described cell body has the big by formed at the bottom of the horizontal pond of large area of multiple close water inlet region
The shallow pond of area, described cell body have multiple near water outlet section by being formed at the bottom of multiple little area levels ponds
The deep pond of little area.
Alternatively, the shallow pond of described large area is heat exchange pond, and the described deep pond of little area is thermal insulation pool.
Alternatively, the plurality of water inlet parallel interval is arranged at described first pool wall.
Alternatively, described second pool wall arranges two outlets, and each outlet is obliquely installed in the second pool wall
With the junction of the 3rd pool wall, these two outlets are arranged into " eight " font relative to the second pool wall.
Alternatively, described diffuser includes that printing opacity cover body and fixed mount, described fixed mount are fixed on described cell body
Edge, described printing opacity cover body is double-decker.
Alternatively, described printing opacity cover body includes outer layer, internal layer and the heat collector cavity between outer layer and internal layer,
This outer layer is light-passing board, for absorbing the sunlight in the external world;This internal layer is collecting plate, and this heat collector cavity is formed at
Between this light-passing board and collecting plate.
Compared with prior art, this utility model has the advantage that
First, Wen Peng pond of the present utility model is provided with gradient pond bottom structure, the multiple horizontal pond at the bottom of gradient pond
The end, is equivalent to multiple heat exchange area, and low temperature richness lithium carbonate type bittern can be along the length of cell body after entering cell body
Direction sequentially enters each heat exchange area from left to right, due to the area at the bottom of multiple horizontal ponds the most successively
It is gradually reduced, therefore, enters the low temperature richness lithium carbonate type bittern at the bottom of first horizontal pond and can carry out rapidly greatly
Area, large-scale heat exchange reaction, thus the temperature of low temperature richness lithium carbonate type bittern can raise rapidly, this
Sample lithium carbonate also can crystallization rapidly;Along with salt continues to flow along cell body length direction to outlet direction,
Brine temperature also can gradually rise, and lithium carbonate also can separate out at the bottom of each horizontal pond successively;When salt flows to
When the territory, base area, multiple horizontal pond of outlet, due to smaller near outlet multiple horizontal pond floor space,
And the degree of depth is relatively deep, the temperature in this region is higher and stablizes, therefore low temperature richness lithium carbonate type bittern major part
It is to carry out crystallization in this region.Obviously, the structure design at the bottom of such gradient pond so that low temperature richness lithium carbon
Hydrochlorate type salt enters quickly heat exchange behind Wen Peng pond, is rapidly heated, thus quickly obtains crystallization of lithium carbonate body,
It is greatly promoted the precipitation rate of lithium carbonate.
Secondly, Wen Peng pond is provided with diffuser, and its printing opacity cover body is double-decker, have good thermal-arrest,
Accumulation of heat effect, and the impurity such as outside dust storm can be avoided to introduce cell body, it is to avoid crystallization of lithium carbonate body introduces impurity.
Finally, due to the design of the structure at the bottom of ladder pond of cell body and being combined with of diffuser in Wen Peng pond,
Temperature higher relative to external world's holding in making Wen Peng pond, it is generally the case that in western part of China highlands
Arranging Wen Peng pond of the present utility model, no matter how season changes, and the temperature in Wen Peng pond is relative to extraneous temperature
Degree exceeds 30 DEG C~50 DEG C.Annual temperature in western part of China highlands, Wen Peng pond can maintain 20 DEG C
~between 80 DEG C.So, this Wen Peng pond is utilized to carry out the deposition work of lithium carbonate from rich lithium carbonate type bittern
Whenever skill can operate in 1 year, i.e. can be with whole year operation.
Accompanying drawing explanation
Fig. 1 is the schematic diagram in Wen Peng pond of the present utility model.
Fig. 2 is the cross sectional representation in Wen Peng pond of the present utility model.
Fig. 3 is the solar pond of prior art.
Wen Peng pond 1
Cell body 10
Diffuser 20
First pool wall 11
Second pool wall 12
3rd pool wall 13
At the bottom of horizontal pond 14
Inclined-plane 15
Water inlet 16
Outlet 17
Crystallization of lithium carbonate body 30
Detailed description of the invention
For making the purpose of this utility model, technical scheme and advantage clearer, below in conjunction with concrete real
Execute example, this utility model is described in detail.Only should be appreciated that specific embodiment described herein
In order to explain this utility model, it is not used to limit this utility model.
This utility model provides a kind of for carrying out extracting by beneficial element in carbonate-type boron lithium salts lake bittern water
Wen Peng pond 1.The operation principle in Wen Peng pond 1: salt lake bittern is in evaporation and crystal process, and various salt progressively reach
After its saturation solubility from salt crystallization.In carbonate-type boron lithium salts lake bittern water, lithium carbonate is
Having the salt of negative temperature effect dissolubility, other salt has positive temperature effect, therefore, and can will at lithium carbonate
When reaching its saturation solubility, salt is introduced temperature canopy makes its liter of high-temperature, at this time, no matter other salt
Whether class reaches saturated before liter high-temperature, all will raise, by dissolubility owing to temperature raises in salt more
Add away from its dissolubility, thus without crystallization;Lithium carbonate then reaches higher degree of supersaturation from saturated,
Thus mass crystallization separates out.In general, the temperature difference of 20~30 DEG C can cause the molten of lithium carbonate about 30%
Xie Du is poor, i.e. salt Tanaka close to saturated lithium carbonate salt, behind excess temperature canopy pond, by crystallization 30%
The lithium carbonate of left and right, and temperature difference is the biggest, the crystallization rate of lithium carbonate is the highest.Behind excess temperature canopy pond again
Its lithium carbonate of salt in entrance salt pan reduces due to temperature, and dissolubility increases, and only evaporates lithium carbonate in temperature
Just can again reach saturated after eduction rate part in canopy, and the evaporation and concentration mistake that other salt is after temperature reduces
Cheng Zhong, crystallization.Therefore, by repeatedly Wen Peng pond process, gathering in the crops lithium carbonate in temperature canopy, salt Tanaka receives
Obtain other salt such as Borax, potassium chloride.In theory, Wen Peng pond can obtain pure lithium carbonate, but due to
There is evaporation in temperature canopy, have part and salt out, reduce the grade of the lithium carbonate obtained.In terms of practice, temperature
The canopy system temperature difference outer with system is positively retained at 30 DEG C~50 DEG C throughout the year, and therefore, temperature canopy can be used for producing carbon the whole year
Acid lithium.Function and the effect in Wen Peng pond 1 are described in detail by the structure below in conjunction with Wen Peng pond 1.
As it is shown in figure 1, Wen Peng pond 1 includes cell body 10 for accommodating salt and for thermal-arrest, insulation
Diffuser 20, diffuser 20 seals the opening of cell body 10, thus, Wen Peng pond 1 forms a knot sealed
Structure.Cell body 10 has specific width and depth characteristic, i.e. along the length direction of cell body 10, cell body 10
Width be gradually reduced, and the degree of depth of this cell body 10 is gradually increased.In the present embodiment, cell body 10 substantially in
Trapezoidal, as shown in Figure 2.
In conjunction with Fig. 1 and Fig. 2, cell body 10 includes first pool wall the 11, second pool wall 12, connects the first pool wall
11 and second pool wall 12 two the 3rd pool walls 13, gradient ponds at the bottom of.Multiple and horizontal plane is included at the bottom of gradient pond
At the bottom of parallel horizontal pond 14 and multiple 14 inclined-planes 15 tilted at the bottom of with horizontal pond.First pool wall the 11, second pond
Wall the 12, the 3rd pool wall 13 encloses one continuous print tubular pool wall of formation, certainly, the first pool wall 11, second
Pool wall the 12, the 3rd pool wall 13 can be structure as a whole.Diffuser 20 seals the opening of cell body 10, thus,
Wen Peng pond 1 forms a structure sealed.
Fig. 2 is the cross sectional representation in Wen Peng pond 1, it is clear that the width of the first pool wall 11 is more than the second pool wall
The width of 12.The degree of depth of the second pool wall 12 is more than the degree of depth of the first pool wall 11, i.e. the degree of depth of cell body 10
Gradually deepen along himself length direction (i.e. direction from left to right in Fig. 1).Along cell body 10
Length direction, at the bottom of gradient pond in multiple horizontal pond at the bottom of 14 width taper into, i.e. multiple horizontal ponds
The area at the end 14 is gradually reduced.It is to say, along the length direction of cell body 10, cell body 10 has multiple
The shallow pond of large area (i.e. being formed by the bottom of the horizontal pond of multiple large area 14) and multiple deep pond of little area are (i.e. by multiple
At the bottom of little area levels pond, 14 are formed), these shallow ponds and Shen Chi together form at the bottom of the gradient pond of cell body 10.
The shallow pond of the plurality of large area is heat exchange pond, and the effect in the shallow pond of multiple large area is so that from outside low temperature
Salt is rapidly heated;The plurality of deep pond of little area is thermal insulation pool, and the effect in multiple deep ponds of little area is to maintain
Brine temperature, the precipitation of prolongation lithium carbonate and recrystallization are to obtain high-quality crystallization of lithium carbonate body 30.This reality
Executing in example, first shallow pond of large area (near the shallow pond of the first pool wall 11) is heat exchange pond, be used for so that
It is rapidly heated from outside low temperature salt;And follow-up each deep pond (being formed by the bottom of multiple horizontal ponds 14) is
Thermal insulation pool, is only to maintain brine temperature and extends the precipitation of lithium carbonate and recrystallization to obtain high-quality lithium carbonate
Crystalline solid 30.
During utilizing Wen Peng pond 1 to separate out lithium carbonate, theoretically, Wen Peng pond can reach to rise for 1 one days
Temperature separates out the primary condition of lithium carbonate: as long as the salt thickness in Wen Peng pond 1 is less than 10cm, every day is single
Plane amasss the solar energy of acquisition can make brine temperature deep for 10cm raise more than 20 DEG C.Salt is at Wen Peng
In pond 1, the thickness of the time of staying and salt is inversely proportional to, and the volume of salt is the product of the degree of depth and surface area, this
Sample can calculate the width of the first pool wall, the degree of depth and length by year brine treatment amount, it is also possible to constructs
Two pool walls and other pool wall.According to said method, (that is, the required year brine treatment amount being actually needed can be built
) Wen Peng pond 1.
Shown in Fig. 1, Fig. 2, the first pool wall 11 is provided with multiple water inlet 16, and the second pool wall 12 sets
There is multiple outlet 17.Such as, multiple water inlet 16 parallel interval are arranged at the first pool wall 11, and two go out
The mouth of a river 17 is respectively arranged at the two ends of the second pool wall 12, and each outlet 17 is obliquely installed in the second pool wall
12 and the 3rd pool wall 13 junction, two such outlet 17 is arranged into " eight " relative to the second pool wall 12
Font.
Again as it is shown in figure 1, diffuser 20 includes that printing opacity cover body 21 and fixed mount 22, fixed mount 22 are fixed
In the edge of cell body 10, cell body 10 is sealed by printing opacity cover body 21.Printing opacity cover body 21 can use tool
Having the sunlight light-passing board of heat collection function, such as, printing opacity cover body 21 is double-decker, and outer layer is light-passing board,
For absorbing the sunlight in the external world;Internal layer is collecting plate, leaves certain interval shape between light-passing board and collecting plate
Become heat collector cavity.Heat collector cavity can carry out, by the air in air-through holes road and Wen Peng pond 1, heat exchange of circulating,
So that keep higher temperature relative to the external world in Wen Peng pond 1.
It addition, diffuser 20 makes cell body 10 be in closed environment, miscellaneous from machineries such as extraneous dusts storm
Matter will not introduce in salt, thus avoids the crystallization of lithium carbonate body finally obtained to contain impurity.
Owing to the structure at the bottom of the ladder pond of cell body 10 in Wen Peng pond 1 designs and being combined with of diffuser 20,
Temperature higher relative to external world's holding in making Wen Peng pond 1, it is generally the case that in western part of China plateau
District arranges Wen Peng pond 1 of the present utility model, and no matter how season changes, the temperature in Wen Peng pond 1 relative to
Ambient temperature exceeds 30 DEG C~50 DEG C.Such as, the temperature in western part of China highlands, Wen Peng pond 1 is complete
Year can maintain between 20 DEG C~80 DEG C.So, utilize this Wen Peng pond 1 from rich lithium carbonate type bittern
Whenever the depositing operation carrying out lithium carbonate can operate in 1 year, i.e. can be with whole year operation.
Temperature canopy 1 of the present utility model is for carrying out the deposition of lithium carbonate from rich lithium carbonate type bittern.By
Temperature in Wen Peng pond 1 exceeds 30 DEG C~50 DEG C relative to ambient temperature, owing to the dissolubility of lithium carbonate is
Negative temperature effect, experiences after the rich lithium carbonate type bittern entrance Wen Peng pond 1 that the temperature next from the external world is relatively low
A series of heat transfer process.Due to the structure design of cell body 10 in above-mentioned Wen Peng pond 1, along the length of cell body 10
Degree direction, and from water inlet 16 to the direction of outlet 17, cell body 10 has the shallow pond of multiple large area (i.e.
Formed by the bottom of the horizontal pond of multiple large area 14) and multiple deep pond of little area (at the bottom of i.e. by multiple little area levels ponds
14 are formed).After the low temperature richness lithium carbonate type bittern come when the external world enters the shallow pond of multiple large area, Duo Ge great
The shallow pond of area is equivalent to multiple large-area heat exchange area so that low temperature richness lithium carbonate type bittern programming rate
Comparatively fast, thus quickly sink in the shallow pond of multiple large area (at the bottom of the multiple horizontal pond of water inlet 16 14)
Form sediment crystallization of lithium carbonate body 30.Rich lithium carbonate type bittern through heat exchange continues to multiple deep ponds of little area
Direction flowing (i.e. at the bottom of the multiple horizontal pond of outlet 17 14), is completely heat exchanged and reaches permanent
The rich lithium carbonate type bittern of fixed temperature deposits in a large number at multiple deep pool areas of little area, it is excellent to produce crystal formation
The crystallization of lithium carbonate body 30 changed.
This utility model compared with prior art, has the advantage that
First, Wen Peng pond 1 of the present utility model is provided with gradient pond bottom structure, the multiple levels at the bottom of gradient pond
At the bottom of pond, 14 are equivalent to multiple heat exchange area, and low temperature richness lithium carbonate type bittern can be along pond after entering cell body 10
The length direction of body 10 sequentially enters each heat exchange area from left to right, due to the face of 14 at the bottom of multiple horizontal ponds
Amass and be gradually reduced the most successively, therefore, enter the low temperature richness lithium carbonate-type of at the bottom of first horizontal pond 14
Salt can carry out rapidly large area, large-scale heat exchange is reacted, thus the temperature of low temperature richness lithium carbonate type bittern
Degree can raise rapidly, and such lithium carbonate also can crystallization rapidly;Along with salt continues along cell body 10 length side
Flowing to outlet 17 direction, brine temperature also can gradually rise, and lithium carbonate also can be at the bottom of each horizontal pond
14 separate out successively;When salt flows near 14 region at the bottom of the multiple horizontal pond of outlet 17, owing to leaning on
14 Area comparisons at the bottom of more than 17 horizontal ponds of nearly outlet are little, and the degree of depth is relatively deep, and the temperature in this region is higher
And stablize, therefore low temperature richness lithium carbonate type bittern major part is to carry out crystallization in this region.Obviously,
So structure design at the bottom of gradient pond so that low temperature richness lithium carbonate type bittern is fast quick change after entering Wen Peng pond 1
Heat, it is rapidly heated, thus quickly obtains crystallization of lithium carbonate body, be greatly promoted the precipitation rate of lithium carbonate.
Secondly, Wen Peng pond 1 is provided with diffuser 20, and its printing opacity cover body 21 is double-decker, has very well
Thermal-arrest, accumulation of heat effect, and the impurity such as outside dust storm can be avoided to introduce cell body 10, it is to avoid crystallization of lithium carbonate body
Middle introducing impurity.
Finally, due to the structure at the bottom of ladder pond of cell body 10 designs and the knot of diffuser 20 in Wen Peng pond 1
Close and utilize so that keep higher temperature relative to the external world in Wen Peng pond 1, it is generally the case that at Western China
Highlands, portion arranges Wen Peng pond 1 of the present utility model, and no matter how season changes, the temperature in Wen Peng pond 1
Degree exceeds 30 DEG C~50 DEG C relative to ambient temperature.Temperature in western part of China highlands, Wen Peng pond 1
Can maintain the whole year between 20 DEG C~80 DEG C.So, utilize this Wen Peng pond 1 from rich lithium carbonate type bittern
In carry out the depositing operation of lithium carbonate and whenever can operate in 1 year, i.e. can be with whole year operation.
The foregoing is only preferred embodiment of the present utility model, not in order to limit this utility model,
All any amendment, equivalent and improvement etc. made within spirit of the present utility model and principle, all should
Within being included in protection domain of the present utility model.
Claims (10)
1. a Wen Peng pond, it is characterised in that this Wen Peng pond includes cell body and saturating with what this cell body was tightly connected
Light shield, this cell body includes at the bottom of pool wall and gradient pond, includes at the bottom of multiple horizontal pond and multiple and institute at the bottom of this gradient pond
State the inclined-plane of multiple horizontal ponds slanted floor.
2. Wen Peng pond as claimed in claim 1, it is characterised in that: described cell body include the first pool wall and
The second pool wall that this first pool wall is relative, connect two the 3rd pool walls of this first pool wall and the second pool wall, institute
Stating the width of the first pool wall width more than described second pool wall, the degree of depth of described second pool wall is more than described the
The degree of depth of one pool wall.
3. Wen Peng pond as claimed in claim 2, it is characterised in that: the degree of depth of described cell body is from the first pool wall
Direction to the second pool wall gradually deepens.
4. Wen Peng pond as claimed in claim 2, it is characterised in that: described first pool wall arrange multiple enter water
Mouthful, described second pool wall arranges multiple outlet.
5. Wen Peng pond as claimed in claim 4, it is characterised in that: described cell body has multiple near entering water
Port area by the shallow pond of large area formed at the bottom of the horizontal pond of large area, described cell body has multiple near outlet
Region by the deep pond of little area formed at the bottom of multiple little area levels ponds.
6. Wen Peng pond as claimed in claim 5, it is characterised in that: the shallow pond of described large area is heat exchange pond,
The described deep pond of little area is thermal insulation pool.
7. Wen Peng pond as claimed in claim 4, it is characterised in that: the plurality of water inlet parallel interval sets
It is placed in described first pool wall.
8. Wen Peng pond as claimed in claim 4, it is characterised in that: described second pool wall arranges two water outlets
Mouthful, each outlet is obliquely installed in the second pool wall and the junction of the 3rd pool wall, and these two outlets are relative
It is arranged into " eight " font in the second pool wall.
9. Wen Peng pond as claimed in claim 1, it is characterised in that: described diffuser include printing opacity cover body and
Fixed mount, described fixed mount is fixed on the edge of described cell body, and described printing opacity cover body is double-decker.
10. Wen Peng pond as claimed in claim 1, it is characterised in that: described printing opacity cover body includes outer layer, interior
Layer and the heat collector cavity between outer layer and internal layer, this outer layer is light-passing board, for absorbing the sunlight in the external world;
This internal layer is collecting plate, and this heat collector cavity is formed between this light-passing board and collecting plate.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620283368.8U CN205500802U (en) | 2016-04-07 | 2016-04-07 | Wen peng pond |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620283368.8U CN205500802U (en) | 2016-04-07 | 2016-04-07 | Wen peng pond |
Publications (1)
Publication Number | Publication Date |
---|---|
CN205500802U true CN205500802U (en) | 2016-08-24 |
Family
ID=56737022
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201620283368.8U Active CN205500802U (en) | 2016-04-07 | 2016-04-07 | Wen peng pond |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN205500802U (en) |
-
2016
- 2016-04-07 CN CN201620283368.8U patent/CN205500802U/en active Active
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN103420400B (en) | Salt lake brine evaporation method and equipment thereof, and salt lake brine treatment method by utilizing salt lake brine evaporation method and device thereof | |
CN207483397U (en) | A kind of floatation type desalination plant based on photo-thermal evaporation | |
RU2013142931A (en) | SELECTIVE EXTRACTION OF SALTS FROM MIXED SALT BRINE | |
CN103332708B (en) | A kind of Salt-nitrate coproduction method | |
CN104030320A (en) | Process for producing salt through concentrating strong brine after sea water desalination adopting two-way cycle method and bromine extraction | |
CN102815727A (en) | Method for extracting lithium carbonate from carbonate brine | |
CN105177619A (en) | Device and method for preparing potassium sulphate | |
CN205500802U (en) | Wen peng pond | |
CN102795645B (en) | Brine crystallizing salt-manufacturing apparatus | |
CN208648765U (en) | A kind of equipment of uniformly evaporating brine | |
CN103482660A (en) | Method and system for preparing high-purity lithium carbonate | |
CN115159546B (en) | Method for improving evaporation efficiency of salt lake brine | |
Mabrouk et al. | Experimental evaluation of novel hybrid multi effect distillation–membrane distillation (MED-MD) driven by solar energy | |
CN102356862A (en) | Method and device for continuously preparing monosodium glutamate crystals | |
CN109824067B (en) | Extracting lithium concentrate by natural evaporation crystallization lithium precipitation, combined heating crystallization lithium precipitation and dissolution lithium washing | |
CN108285157A (en) | A kind of technique preparing lithium carbonate with carbonate type bittern | |
CN105154918A (en) | Electrolytic manganese production system capable of saving energy and reducing consumption | |
CN105883862B (en) | The method that lithium carbonate is prepared from the carbonate type bittern of plateau | |
CN106318619B (en) | Method for extracting grease in algae | |
CN105858693B (en) | The method that high-purity magnesium carbonate is prepared from the carbonate type bittern of plateau | |
CN103553065B (en) | Method for preparing boron ore from mixed brine by using natural energy | |
CN108217693B (en) | Salt field technology for separating components by using temperature difference | |
CN109336137A (en) | A kind of carnallite solarization system and method processed | |
CN202687994U (en) | Brine crystallizing salt-preparing device | |
CN1398786A (en) | Lithium carbonate crystal separating process from carbonate-type bittern by means of solar battery |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant |