CN217418236U - Coal industry strong brine evaporation crystallization device - Google Patents
Coal industry strong brine evaporation crystallization device Download PDFInfo
- Publication number
- CN217418236U CN217418236U CN202221418212.8U CN202221418212U CN217418236U CN 217418236 U CN217418236 U CN 217418236U CN 202221418212 U CN202221418212 U CN 202221418212U CN 217418236 U CN217418236 U CN 217418236U
- Authority
- CN
- China
- Prior art keywords
- liquid storage
- storage tank
- reserve tank
- liquid reserve
- screw rod
- 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.)
- Expired - Fee Related
Links
- 238000002425 crystallisation Methods 0.000 title claims abstract description 41
- 230000008025 crystallization Effects 0.000 title claims abstract description 41
- 230000008020 evaporation Effects 0.000 title claims abstract description 27
- 238000001704 evaporation Methods 0.000 title claims abstract description 27
- 239000012267 brine Substances 0.000 title claims abstract description 24
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 title claims abstract description 24
- 239000003245 coal Substances 0.000 title claims abstract description 22
- 239000007788 liquid Substances 0.000 claims abstract description 51
- 238000010438 heat treatment Methods 0.000 claims abstract description 17
- 238000003756 stirring Methods 0.000 claims abstract description 9
- 239000000126 substance Substances 0.000 claims description 11
- 238000007599 discharging Methods 0.000 claims description 9
- 238000009413 insulation Methods 0.000 claims description 6
- 239000011550 stock solution Substances 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 4
- 239000013078 crystal Substances 0.000 description 10
- 239000000463 material Substances 0.000 description 7
- 238000000034 method Methods 0.000 description 3
- 230000005540 biological transmission Effects 0.000 description 2
- 238000012993 chemical processing Methods 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 125000003118 aryl group Chemical group 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000002309 gasification Methods 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000011253 protective coating Substances 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000004449 solid propellant Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model provides a coal industry strong brine evaporation crystallization device, includes the liquid reserve tank, the liquid reserve tank outside is equipped with the zone of heating, be equipped with the heating piece in the zone of heating, the zone of heating outside is equipped with the insulating layer, the liquid reserve tank internal rotation is equipped with the transfer line, the liquid reserve tank top is equipped with drive transfer line pivoted motor one, be equipped with a plurality of stirring vane on the transfer line, be equipped with the screw rod in the liquid reserve tank, the liquid reserve tank top is equipped with drive screw rod pivoted motor two, be equipped with annular scraper blade on the screw rod, annular scraper blade bottom contacts with the liquid reserve tank inner wall. Compared with the prior art, the utility model the advantage lie in: the stirring blades are arranged, so that the strong brine can be conveniently and fully heated, and the evaporation and crystallization effects are good; be equipped with screw rod and annular scraper blade, be convenient for collect the crystallization on the liquid reserve tank inner wall, the efficiency of evaporation crystallization is higher.
Description
Technical Field
The utility model relates to an evaporation crystallization device technical field specifically indicates a coal industry strong brine evaporation crystallization device.
Background
Coal chemical refers to the process of converting coal into gas, liquid and solid fuels and chemicals by chemical processing using coal as a raw material. Mainly comprises coal gasification, liquefaction, dry distillation and the like. Coal chemical processing. The chemical structure of organic matter in coal is a macromolecular structure with aromatic condensed rings as core units, bridge bonds for mutual connection and various functional groups, and can convert coal into various fuels and chemical products by thermal processing and catalytic processing
In the process of evaporation crystallization, strong brine needs to be heated, and the existing evaporation crystallization device is not uniformly heated and has poor evaporation crystallization effect; and in the strong brine evaporation crystallization process of coal chemical industry, can make some crystallization remain in the evaporation crystallization device side, the inconvenient crystallization on the side of current evaporation crystallization device is collected, leads to the evaporation crystallization efficiency lower.
SUMMERY OF THE UTILITY MODEL
The to-be-solved technical problem of the utility model is to overcome above technical defect, provide a coal industry strong brine evaporation crystallization device convenient to strong brine even heating, be convenient for collect the crystallization on the side.
In order to solve the technical problem, the utility model provides a technical scheme does: the utility model provides a coal industry strong brine evaporation crystallization device, includes the liquid reserve tank, the liquid reserve tank outside is equipped with the zone of heating, be equipped with the heating piece in the zone of heating, the zone of heating outside is equipped with the insulating layer, the liquid reserve tank internal rotation is equipped with the transfer line, the liquid reserve tank top is equipped with drive transfer line pivoted motor one, be equipped with a plurality of stirring vane on the transfer line, be equipped with the screw rod in the liquid reserve tank, the liquid reserve tank top is equipped with drive screw rod pivoted motor two, be equipped with annular scraper blade on the screw rod, annular scraper blade bottom contacts with the liquid reserve tank inner wall.
As an improvement, a limiting rod is arranged on one side, far away from the screw, in the liquid storage tank, and the annular scraper is connected with the limiting rod in a sliding mode.
As an improvement, a liquid inlet is formed in the top end of the liquid storage tank.
As an improvement, the bottom end in the liquid storage tank is provided with material guide plates, a material discharge pipe is arranged between the two material guide plates, and a control valve is arranged on the material discharge pipe.
As an improvement, U-shaped clamping grooves are symmetrically formed in the heat insulation layer, and a crystallization collecting disc located below the discharge pipe is clamped between the U-shaped clamping grooves.
As an improvement, support columns are symmetrically arranged at the bottom end of the heat insulation layer.
Compared with the prior art, the utility model the advantage lie in: the stirring blades are arranged, so that the strong brine can be conveniently and fully heated, and the evaporation and crystallization effects are good; the screw and the annular scraper are arranged, so that crystals on the inner wall of the liquid storage tank can be conveniently collected, and the evaporation crystallization efficiency is high; the heat insulation layer is arranged, so that the device is convenient to prevent the device from scalding workers; the limiting rod is arranged, so that the annular scraper plate can be limited conveniently, and the free rotation of the annular scraper plate is avoided, so that the moving stability of the annular scraper plate is ensured; the material guide plate is arranged to facilitate the crystallization to move towards the discharging pipe, and the control valve is arranged to facilitate the discharging control of the discharging pipe; the U-shaped clamping groove is arranged, so that the crystallization collecting disc can be conveniently installed and detached; and a crystallization collecting tray is arranged, so that evaporative crystals can be collected conveniently.
Drawings
Fig. 1 is a schematic structural diagram of the concentrated brine evaporation crystallization device in the coal chemical industry of the present invention.
As shown in the figure: 1. a liquid storage tank; 2. a heating layer; 3. a heating block; 4. a thermal insulation layer; 5. a transmission rod; 6. a first motor; 7. a stirring blade; 8. a screw; 9. a second motor; 10. an annular scraper; 11. a limiting rod; 12. a liquid inlet; 13. a material guide plate; 14. a discharge pipe; 15. a control valve; 16. a U-shaped clamping groove; 17. a crystallization collection tray; 18. and (4) a support column.
Detailed Description
In order to make the content of the present invention more clearly understood, the technical solution in the embodiment of the present invention will be clearly and completely described below with reference to the attached drawings in the embodiment of the present invention.
It should be noted that as used in the following description, the terms "front," "back," "left," "right," "upper" and "lower" refer to directions in the drawings, and the terms "inner" and "outer" refer to directions toward and away from, respectively, the geometric center of a particular component.
Combine the figure, a coal industry strong brine evaporation crystallization device, including liquid reserve tank 1, 1 outside of liquid reserve tank is equipped with zone of heating 2, be equipped with heating block 3 in the zone of heating 2, the 2 outside of zone of heating is equipped with insulating layer 4, 1 internal rotation of liquid reserve tank is equipped with transfer line 5, 1 top of liquid reserve tank is equipped with drive transfer line 5 pivoted motor 6, be equipped with a plurality of stirring vane 7 on the transfer line 5, be equipped with screw rod 8 in the liquid reserve tank 1, 1 top of liquid reserve tank is equipped with drive screw rod 8 pivoted motor two 9, be equipped with annular scraper blade 10 on the screw rod 8, annular scraper blade 10 bottom contacts with 1 inner wall of liquid reserve tank.
Keep away from one side of screw rod 8 in the liquid reserve tank 1 and be equipped with gag lever post 11, annular scraper blade 10 and gag lever post 11 sliding connection are convenient for carry on spacingly to annular scraper blade 10, avoid annular scraper blade 10 free rotation to guarantee the stability that annular scraper blade 10 removed.
The top end of the liquid storage tank 1 is provided with a liquid inlet 12, so that strong brine can be conveniently added into the liquid storage tank 1.
The inside bottom of liquid storage tank 1 is equipped with stock guide 13, two be equipped with discharging pipe 14 between the stock guide 13, be convenient for crystallization to discharging pipe 14 removal, be equipped with control valve 15 on the discharging pipe 14, be convenient for control discharging pipe 14 ejection of compact.
The thermal-protective coating 4 is symmetrically provided with U-shaped clamping grooves 16, so that the crystallization collecting tray 17 can be conveniently mounted and dismounted. And a crystallization collecting disc 17 positioned below the discharge pipe 14 is clamped between the two U-shaped clamping grooves 16, so that evaporative crystals can be collected conveniently.
The bottom end of the heat insulation layer 4 is symmetrically provided with support columns 18, so that the use stability of the device is ensured.
When the utility model is implemented specifically, strong brine is added into the liquid storage tank 1 through the liquid inlet 12 on the liquid storage tank 1, the heating block 3 is started to heat the strong brine in the liquid storage tank 1, the first motor 6 is started, the first motor 6 drives the transmission rod 5 to rotate, the stirring blade 7 stirs the strong brine, so that the strong brine is uniformly heated, and the evaporation crystallization effect is better; after crystallization is completed, a second motor 9 is started, the second motor 9 drives a screw rod 8 to rotate to drive an annular scraper 10 to move towards a discharge pipe 14, the annular scraper 10 scrapes crystals on the inner wall of the liquid storage tank 1 to be collected, the annular scraper 10 is in sliding connection with a limiting rod 11 to ensure that the annular scraper 10 stably moves, the crystals move towards the discharge pipe 14 through a material guide plate 13, a crystal collecting disc 17 is installed below the discharge pipe 14 through two U-shaped clamping grooves 16, a control valve 15 is opened, the discharge pipe 14 discharges the crystals to the crystal collecting disc 17, and the crystal collecting disc 17 is taken out from the U-shaped clamping grooves 16 so as to obtain evaporative crystals.
The present invention and the embodiments thereof have been described above, but the description is not limited thereto, and the embodiment shown in the drawings is only one of the embodiments of the present invention, and the actual structure is not limited thereto. In summary, it should be understood that those skilled in the art should also understand the scope of the present invention without inventively designing the similar structure and embodiments of the present invention without departing from the spirit of the present invention.
Claims (6)
1. The utility model provides a coal industry strong brine evaporation crystallization device, includes liquid reserve tank (1), its characterized in that: the utility model discloses a liquid storage tank, including liquid storage tank (1), zone of heating (2) outside is equipped with insulating layer (4), liquid storage tank (1) internal rotation is equipped with transfer line (5), liquid storage tank (1) top is equipped with drive transfer line (5) pivoted motor (6), be equipped with a plurality of stirring vane (7) on transfer line (5), be equipped with screw rod (8) in liquid storage tank (1), liquid storage tank (1) top is equipped with drive screw rod (8) pivoted motor two (9), be equipped with annular scraper blade (10) on screw rod (8), annular scraper blade (10) bottom contacts with liquid storage tank (1) inner wall.
2. The concentrated brine evaporation and crystallization device for coal chemical industry according to claim 1, characterized in that: one side of the liquid storage box (1) far away from the screw rod (8) is provided with a limiting rod (11), and the annular scraper (10) is connected with the limiting rod (11) in a sliding manner.
3. The concentrated brine evaporation and crystallization device for coal chemical industry according to claim 1, characterized in that: the top end of the liquid storage tank (1) is provided with a liquid inlet (12).
4. The concentrated brine evaporation and crystallization device for coal chemical industry according to claim 1, characterized in that: stock solution tank (1) inside bottom is equipped with stock guide (13), two be equipped with discharging pipe (14) between stock guide (13), be equipped with control valve (15) on discharging pipe (14).
5. The concentrated brine evaporation and crystallization device for coal chemical industry according to claim 1, characterized in that: the thermal-insulating layer (4) is symmetrically provided with U-shaped clamping grooves (16), and a crystallization collecting disc (17) located below the discharge pipe (14) is clamped between the U-shaped clamping grooves (16).
6. The concentrated brine evaporation and crystallization device for coal chemical industry according to claim 1, characterized in that: support columns (18) are symmetrically arranged at the bottom end of the heat insulation layer (4).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202221418212.8U CN217418236U (en) | 2022-06-08 | 2022-06-08 | Coal industry strong brine evaporation crystallization device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202221418212.8U CN217418236U (en) | 2022-06-08 | 2022-06-08 | Coal industry strong brine evaporation crystallization device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN217418236U true CN217418236U (en) | 2022-09-13 |
Family
ID=83170713
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202221418212.8U Expired - Fee Related CN217418236U (en) | 2022-06-08 | 2022-06-08 | Coal industry strong brine evaporation crystallization device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN217418236U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115487517A (en) * | 2022-09-24 | 2022-12-20 | 广州市合利源食品有限公司 | Five-effect evaporation system for starch sugar concentration |
-
2022
- 2022-06-08 CN CN202221418212.8U patent/CN217418236U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115487517A (en) * | 2022-09-24 | 2022-12-20 | 广州市合利源食品有限公司 | Five-effect evaporation system for starch sugar concentration |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20220913 |