CN207941232U - A kind of device of control salt flash evaporation tank degree of supersaturation - Google Patents
A kind of device of control salt flash evaporation tank degree of supersaturation Download PDFInfo
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- CN207941232U CN207941232U CN201721829635.8U CN201721829635U CN207941232U CN 207941232 U CN207941232 U CN 207941232U CN 201721829635 U CN201721829635 U CN 201721829635U CN 207941232 U CN207941232 U CN 207941232U
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- tank
- support
- supersaturation
- conduit
- tank body
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Abstract
The utility model discloses a kind of devices of control salt flash evaporation tank degree of supersaturation, including supporting rack and tank body, tank body is set to above supporting rack, support frame bottom is equipped with several support columns, support plate is equipped at the top of support column, fixed plate is equipped with below support plate between support column, it is surrounded by fixed frame at the top of support plate, temperature control layer is equipped with outside tank body, one side bottom of tank body is equipped with into halogen pipe, it is equipped with solenoid valve into halogen pipe, top of the tank side is equipped with woven hose, water tank is equipped at the top of fixed plate, tank top side is equipped with conduit, conduit is equipped with water pump, it is connect with temperature control layer through support plate at the top of conduit, temperature control layer top side is equipped with return duct, return duct one end is connect with tank top.The utility model is simple in structure, convenient to use, can realize the double control to brine liquid inlet volume and brine solubility, and then realize the control to degree of supersaturation in tank, and control effect is good, can extend manufacture cycle, and increases product yield.
Description
Technical field
The utility model is related to salt making equipment technical field more particularly to a kind of dresses of control salt flash evaporation tank degree of supersaturation
It sets.
Background technology
Salt manufacturing is exactly to make salt (or industrial salt).Salt industry occupies important economic status in national economy,
It is the important component of national economy.Salt is the necessity of human lives, is the base stock of chemical industry, in other industry
Also it was once the important fiscal revenues of many countries to have extensive use, salt tax in department and farming, animal husbandry and fishery.The explored salt in the world
The total reserves of resource be about 64 × 10,700,000,000 tons, wherein seawater (including bottom sediment) salt content be 43 × 10,700,000,000 tons, rock
Salt is 21 × 10,700,000,000 tons, and salt lake and underground natural bittern are 310,000,000,000 tons, and new halite bed is also constantly being found.Salt purposes
Extensively, be life it is edible product and basic chemical industry raw material, main component is sodium chloride, and when production carries out bittern water net
Change, is made using being crystallized after steam heating evaporation.In normal production, since flash evaporation tank (EV302) shwoot is too fast, solution is caused
Middle sodium chloride content supersaturation, causes sodium chloride nucleus easily to adhere to tank skin, causes flash evaporation tank shwoot space to become low current and increases, causes
Make the production cycle that must just stop production at 10-15 days processing, to influence product yield.
Utility model content
Purpose of the utility model is to solve some problems in the prior art, and a kind of control salt shwoot proposed
The device of tank degree of supersaturation.
To achieve the goals above, the utility model uses following technical solution：
A kind of device of control salt flash evaporation tank degree of supersaturation, including supporting rack and tank body, the tank body are set to the support
Above frame, support frame as described above bottom is equipped with several support columns, and support plate, the support plate lower section are equipped at the top of the support column
It is equipped with fixed plate between the support column, the fixed frame to match with the tank body, institute are surrounded by the top of the support plate
It states and is equipped with temperature control layer outside tank body, one side bottom of the tank body is equipped with into halogen pipe, described to be equipped with solenoid valve, the tank into halogen pipe
Body top side is equipped with woven hose, and water tank is equipped at the top of the fixed plate, and the tank top side is equipped with conduit, the conduit
It is equipped with water pump, the conduit bottom is through the tank top shell and extends to the water tank inside bottom, the conduit
Top is connect through the support plate with the temperature control layer, and the temperature control layer top side is equipped with return duct, the return duct one
End is connect with the temperature control layer, and the return duct other end is connect with the tank top.
Preferably, the support column bottom is equipped with non-slip mat.
Preferably, the support column side is equipped with the accessory plate to match with the water tank.
Preferably, support frame as described above is loop configuration.
Preferably, the conduit and the return duct are equipped with geometrical clamp with temperature control layer junction.
Compared with prior art, the utility model provide it is a kind of control salt flash evaporation tank degree of supersaturation device, have with
Lower advantageous effect：
1, the device of the control salt flash evaporation tank degree of supersaturation, by the way that into solenoid valve is arranged on halogen pipe, brine can be controlled
Liquid inlet volume, can in tank when degree of supersaturation reduce brine liquid inlet volume, balance bittern concentration；
2, the device of the control salt flash evaporation tank degree of supersaturation can by the way that temperature control layer, water tank, conduit and return duct is arranged
Temperature control effect is realized to tank body, by controlling tank body heating and cooling, realization controls the solubility of brine, and then realization pair
The control of degree of supersaturation, convenient and efficient in tank, energy conservation and environmental protection.
It is not directed to part in the device to be the same as those in the prior art or can be realized by using the prior art, the utility model
It is simple in structure, it is convenient to use, it can realize the double control to brine liquid inlet volume and brine solubility, and then realize to tank
The control of interior degree of supersaturation, control effect is good, can extend manufacture cycle, and increases product yield.
Description of the drawings
Fig. 1 be the utility model proposes a kind of control salt flash evaporation tank degree of supersaturation device structural schematic diagram；
Fig. 2 be the utility model proposes a kind of control salt flash evaporation tank degree of supersaturation device vertical view.
In figure：1 supporting rack, 2 tank bodies, 3 support columns, 4 support plates, 5 fixed plates, 6 fixed frames, 7 temperature control layers, 8 are into halogen pipe, 9
Solenoid valve, 10 woven hoses, 11 water tanks, 12 conduits, 13 water pumps, 14 return ducts.
Specific implementation mode
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.
In the description of the present invention, it should be understood that term "upper", "lower", "front", "rear", "left", "right",
The orientation or positional relationship of the instructions such as "top", "bottom", "inner", "outside" is to be based on the orientation or positional relationship shown in the drawings, and is only
The utility model and simplifying describes for ease of description, do not indicate or imply the indicated device or element must have it is specific
Orientation, with specific azimuth configuration and operation, therefore should not be understood as limiting the present invention.
Referring to Fig.1-2, a kind of device of control salt flash evaporation tank degree of supersaturation, including supporting rack 1 and tank body 2, the tank body 2
Above support frame as described above 1,1 bottom of support frame as described above is equipped with several support columns 3, and 3 top of the support column is equipped with support
Plate 4, the lower section of the support plate 4 are equipped with fixed plate 5 between the support column 3,4 top of the support plate be surrounded by with it is described
The fixed frame 6 that tank body 2 matches, 2 outside of the tank body are equipped with temperature control layer 7, and 2 one side bottom of the tank body is equipped with into halogen pipe 8, institute
It states into halogen pipe 8 and is equipped with solenoid valve 9,2 top side of the tank body is equipped with woven hose 10, and 5 top of the fixed plate is equipped with water tank
11,11 top side of the water tank is equipped with conduit 12, and the conduit 12 is equipped with water pump 13, and 12 bottom of the conduit is through described
11 top shell of water tank simultaneously extends to 11 inside bottom of the water tank, the top of the conduit 12 through the support plate 4 with it is described
Temperature control layer 7 connects, and 7 top side of temperature control layer is equipped with return duct 14, and 14 one end of the return duct connects with the temperature control layer 7
It connects, 14 other end of the return duct is connect with 11 top of the water tank.
3 bottom of the support column is equipped with non-slip mat, and 3 side of the support column is equipped with the auxiliary to match with the water tank 11
Plate, support frame as described above 1 are that loop configuration, the conduit 12 and the return duct 14 are equipped with admittedly with 7 junction of temperature control layer
Clamp.
The utility model is simple in structure, convenient to use, can realize pair to brine liquid inlet volume and brine solubility
It controls again, and then realizes the control to degree of supersaturation in tank, control effect is good, can extend manufacture cycle, and increases product yield.
Herein, relational terms such as first and second and the like be used merely to by an entity or operation with it is another
One entity or operation distinguish, and without necessarily requiring or implying between these entities or operation, there are any this reality
Relationship or sequence.Moreover, the terms "include", "comprise" or its any other variant are intended to the packet of nonexcludability
Contain, so that the process, method, article or equipment including a series of elements includes not only those elements, but also includes
Other elements that are not explicitly listed, or further include for elements inherent to such a process, method, article, or device.
In the absence of more restrictions, the element limited by sentence "including a ...", it is not excluded that including the element
Process, method, article or equipment in there is also other identical elements.
While there has been shown and described that the embodiments of the present invention, for the ordinary skill in the art,
It is appreciated that can these embodiments be carried out with a variety of variations in the case where not departing from the principles of the present invention and spirit, repaiied
Change, replace and modification, the scope of the utility model are defined by the appended claims and the equivalents thereof.
The preferable specific implementation mode of the above, only the utility model, but the scope of protection of the utility model is not
Be confined to this, any one skilled in the art within the technical scope disclosed by the utility model, according to this practicality
Novel technical solution and its utility model design are subject to equivalent substitution or change, should all cover the protection model in the utility model
Within enclosing.
Claims (5)
1. a kind of device of control salt flash evaporation tank degree of supersaturation, including supporting rack (1) and tank body (2), which is characterized in that the tank
Body (2) is set to above support frame as described above (1), and support frame as described above (1) bottom is equipped with several support columns (3), the support column (3)
Top is equipped with support plate (4), and fixed plate (5), the support are equipped between the support column (3) below the support plate (4)
It is surrounded by the fixed frame (6) to match with the tank body (2) at the top of plate (4), temperature control layer (7) is equipped with outside the tank body (2),
(2) one side bottom of the tank body is equipped with into halogen pipe (8), described to be equipped with solenoid valve (9), tank body (2) top into halogen pipe (8)
Side is equipped with woven hose (10), and water tank (11) is equipped at the top of the fixed plate (5), and water tank (11) top side is equipped with conduit
(12), the conduit (12) is equipped with water pump (13), and conduit (12) bottom is through the water tank (11) top shell and prolongs
The water tank (11) inside bottom is extended to, is connected through the support plate (4) and the temperature control layer (7) at the top of the conduit (12)
It connecing, temperature control layer (7) top side is equipped with return duct (14), and described return duct (14) one end is connect with the temperature control layer (7),
It is connect at the top of return duct (14) other end and the water tank (11).
2. a kind of device of control salt flash evaporation tank degree of supersaturation according to claim 1, which is characterized in that the support column
(3) bottom is equipped with non-slip mat.
3. a kind of device of control salt flash evaporation tank degree of supersaturation according to claim 1, which is characterized in that the support column
(3) side is equipped with the accessory plate to match with the water tank (11).
4. a kind of device of control salt flash evaporation tank degree of supersaturation according to claim 1, which is characterized in that support frame as described above
(1) it is loop configuration.
5. a kind of device of control salt flash evaporation tank degree of supersaturation according to claim 1, which is characterized in that the conduit
(12) and the return duct (14) is equipped with geometrical clamp with temperature control layer (7) junction.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721829635.8U CN207941232U (en) | 2017-12-25 | 2017-12-25 | A kind of device of control salt flash evaporation tank degree of supersaturation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721829635.8U CN207941232U (en) | 2017-12-25 | 2017-12-25 | A kind of device of control salt flash evaporation tank degree of supersaturation |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207941232U true CN207941232U (en) | 2018-10-09 |
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ID=63704249
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721829635.8U Active CN207941232U (en) | 2017-12-25 | 2017-12-25 | A kind of device of control salt flash evaporation tank degree of supersaturation |
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| CN (1) | CN207941232U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113482577A (en) * | 2021-07-21 | 2021-10-08 | 江苏淮盐矿业有限公司 | Bittern purification and collection method |
-
2017
- 2017-12-25 CN CN201721829635.8U patent/CN207941232U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113482577A (en) * | 2021-07-21 | 2021-10-08 | 江苏淮盐矿业有限公司 | Bittern purification and collection method |
| CN113482577B (en) * | 2021-07-21 | 2023-01-17 | 江苏淮盐矿业有限公司 | Bittern purification and collection method |
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