CN210934485U

CN210934485U - Liquid evaporation instrument for Texas red production

Info

Publication number: CN210934485U
Application number: CN201921538864.3U
Authority: CN
Inventors: 沈彬彬; 陈康; 岳欢
Original assignee: Nanjing Guhe Biology Co ltd
Current assignee: Nanjing Guhe Biology Co ltd
Priority date: 2019-09-17
Filing date: 2019-09-17
Publication date: 2020-07-07
Anticipated expiration: 2029-09-17

Abstract

The utility model discloses a liquid evaporation instrument is used in production of texas red, comprising a base plate, bottom plate upper right side fixed mounting has a infiltration section of thick bamboo, the fixed intercommunication in infiltration section of thick bamboo upper left end has charge-in pipeline, the fixed intercommunication in infiltration section of thick bamboo right side lower extreme has drainage pipe, the fixed intercommunication of lower extreme of infiltration section of thick bamboo left end has first conveying pipeline, first conveying pipeline extends to the inside of infiltration section of thick bamboo, the fixed intercommunication in first conveying pipeline left end has the evaporation box, the fixed intercommunication of lower extreme of evaporation box left end has the second conveying pipeline. This liquid evaporation instrument is used in Texas red production uses the infiltration principle to replace traditional heating crystallization through the osmotic membrane, has saved the resource greatly, and the material of osmotic membrane is the polymer semipermeable membrane, can get rid of and discharge the moisture majority in the raw materials, then when solution concentration is enough with the liquid level floater time-out, the defeated material is opened with first conveying pipeline automatically to liquid level floater switch, realizes that the material loading is automatic, has improved work efficiency greatly.

Description

Liquid evaporation instrument for Texas red production

Technical Field

The utility model relates to an evaporation equipment technical field specifically is a liquid evaporation instrument is used in red production of texas.

Background

Evaporation has several definitions and generally refers to the process of phase change of a substance from a liquid to a gas, the process of phase change of water from a liquid or solid to a gas, the vaporization that occurs at the surface of a liquid, the conversion of liquid water to gaseous water, the escape into the atmosphere, the escape of water vapor from the surface of water, ice or other water-containing substances at temperatures below the boiling point, etc.

With the continuous development of science and technology, people often need to extract high-purity crystals or high-concentration solution from the solution in the production and manufacturing process, and the method for obtaining the crystals or the high-concentration solution from the solution is evaporation, so that the water in the low-concentration solution is evaporated, and the crystals or the high-concentration solution is obtained.

SUMMERY OF THE UTILITY MODEL

An object of the utility model is to provide a texas red production is with liquid evaporation instrument to it is big to propose the waste of heat in solving above-mentioned background art, and the energy loss that causes is high, and can not control the process of evaporation constantly, problem that work efficiency is low.

In order to achieve the above object, the utility model provides a following technical scheme: a liquid evaporation instrument for Texas red production comprises a bottom plate, a permeation cylinder is fixedly arranged at the upper right part of the bottom plate, the left upper end of the infiltration cylinder is fixedly communicated with a feed pipeline, the right lower end of the infiltration cylinder is fixedly communicated with a drainage pipeline, the lower end of the left end of the infiltration cylinder is fixedly communicated with a first material conveying pipeline which extends to the inside of the infiltration cylinder, the left end of the first material conveying pipeline is fixedly communicated with an evaporation box body, the lower end of the left end of the evaporation box body is fixedly communicated with a second material conveying pipeline, a crystallization cylinder is fixedly communicated with the right end of the second material conveying pipeline, a crystallization vessel is fixedly arranged inside the upper end of the crystallization cylinder, the left end of the lower end of the crystallization cylinder is fixedly communicated with a cooling water inlet, the right end of the lower end of the crystallization cylinder is fixedly communicated with a cooling water outlet, and the lower ends of the permeation cylinder, the evaporation box body and the crystallization cylinder are all fixed to the upper end of the bottom plate through a support.

Preferably, the inside vertical fixed osmotic membrane that is provided with in central authorities of infiltration section of thick bamboo, the outside profile of osmotic membrane closely laminates with charge-in pipeline's inner wall, charge-in pipeline is located the upper left end of osmotic membrane, drainage pipe is located the osmotic membrane have the lower extreme, the inside front end fixed mounting who is located first conveying pipeline of infiltration section of thick bamboo has the liquid level floater.

Preferably, evaporation box upper end fixed mounting has the evaporation mouth, the inside lower extreme fixed mounting who is located first conveying pipeline of evaporation box has the evaporating plate, the outside profile of evaporating plate closely laminates with the inner wall of evaporation box, the fixed heating room that is provided with of lower extreme of evaporating plate, the inside bottom mounting that is located the evaporating plate between the heating is provided with the heating wire, the heating wire embedded with the evaporating plate lower extreme.

Preferably, the feeding pipeline, the drainage pipeline, the first material conveying pipeline, the second material conveying pipeline, the cooling water inlet and the cooling water outlet are all fixedly provided with valves.

Preferably, the crystallization cylinder is of a hollow structure, a cooling water tank is fixedly arranged in the crystallization cylinder, and the upper end of the cooling water tank extends to the side of the crystallization vessel.

Preferably, the height of the permeation cylinder is higher than that of the evaporation box body, and the height of the evaporation box body is higher than that of the crystallization cylinder.

Compared with the prior art, the beneficial effects of the utility model are that: according to the liquid evaporation instrument for Texas red production, the permeable membrane is made of a high-molecular semipermeable membrane, most of water in raw materials can be removed and discharged, then when the concentration of a solution is enough to float the liquid level floating ball, the liquid level floating ball switch automatically opens the first material conveying pipeline for conveying, so that the feeding automation is realized, and the working efficiency is greatly improved;

according to the liquid evaporation instrument for Texas red production, the solution after primary treatment is heated through the evaporation plate, most of residual moisture is removed, the solubility of the solution is increased along with the rise of temperature, the solution achieves the phenomenon of high solubility through heating, and the solution with high temperature and high solubility can be cooled through installing the cooling water tank, so that crystals are separated out, the cooling contact area is greatly increased by using the design of an internal crystallization vessel, the cooling effect is further improved, and the crystallization is accelerated;

this liquid evaporation instrument is used in Texas red production through the installation valve, can control the evaporation process at any time, the operation of being convenient for, and utilizes the linker principle, and whole device does not need external power device, and solution can flow down from top to bottom automatically, has saved the resource greatly, and the device is applicable to the solution crystallization of large amount simultaneously, and application range is wide.

Drawings

FIG. 1 is a schematic perspective view of the present invention;

FIG. 2 is a schematic view of the cross-sectional structure of the infiltration cylinder of the present invention;

FIG. 3 is a schematic view of the cross-sectional structure of the evaporation tank of the present invention;

fig. 4 is a schematic view of the sectional structure of the cooling water tank of the present invention.

In the figure: 1. a base plate; 2. a support; 3. a permeation cylinder; 4. a feed conduit; 5. a valve; 6. a water discharge pipeline; 7. a first delivery conduit; 8. evaporating the box body; 9. an evaporation port; 10. a second delivery pipeline; 11. a crystallization cylinder; 12. a crystallization dish; 13. a cooling water inlet; 14. a cooling water outlet; 15. an evaporation plate; 16. a heating chamber; 17. an electric heating wire; 18. a permeable membrane; 19. a liquid level floating ball; 20. and a cooling water tank.

Detailed Description

The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.

Referring to fig. 1-4, the present invention provides a technical solution: a liquid evaporation instrument for Texas red production comprises a bottom plate 1, a permeation cylinder 3 is fixedly arranged at the upper right side of the bottom plate 1, a feeding pipeline 4 is fixedly communicated with the upper left end of the permeation cylinder 3, a drainage pipeline 6 is fixedly communicated with the lower right end of the permeation cylinder 3, a first material conveying pipeline 7 is fixedly communicated with the lower end of the left end of the permeation cylinder 3, the first material conveying pipeline 7 extends into the permeation cylinder 3, an evaporation box body 8 is fixedly communicated with the left end of the first material conveying pipeline 7, a second material conveying pipeline 10 is fixedly communicated with the lower end of the left end of the evaporation box body 8, a crystallization cylinder 11 is fixedly communicated with the right end of the second material conveying pipeline 10, a crystallization vessel 12 is fixedly arranged inside the upper end of the crystallization cylinder 11, a cooling water inlet 13 is fixedly communicated with the left end of the crystallization cylinder 11, a cooling water outlet 14 is fixedly communicated with the, the lower ends of the evaporation box body 8 and the crystallization cylinder 11 are fixed at the upper end of the bottom plate 1 through a bracket 2.

Further, the inside vertical fixed osmotic membrane 18 that is provided with of central authorities of infiltration section of thick bamboo 3, the outside profile of osmotic membrane 18 closely laminates with charge-in pipeline 4's inner wall, charge-in pipeline 4 is located the upper left end of osmotic membrane 18, drainage pipe 6 is located osmotic membrane 18 has the lower extreme, 3 inside front end fixed mounting who is located first conveying pipeline 7 of an infiltration section of thick bamboo has liquid level floater 19, use the infiltration principle to replace traditional crystallization method of heating through osmotic membrane 18, the resource has been saved greatly, the material of osmotic membrane 18 is the polymer semipermeable membrane, can get rid of and discharge the moisture majority in the raw materials, then when solution concentration is enough with liquid level floater 19 floats, liquid level floater 19 switch is automatic to open first conveying pipeline 7 and is defeated the material, realize the material loading automation, work efficiency is greatly improved.

Further, 8 upper ends fixed mounting of evaporation box has

evaporation mouth

9, 8 inside lower extreme fixed mounting who is located first conveying pipeline 7 of evaporation box has evaporating plate 15, evaporating plate 15's external profile and evaporation box 8's inner wall closely laminate, 16 between the fixed heating that is provided with of lower extreme of evaporating

plate

15, 16 inside bottom mounting who is located evaporating plate 15 between the heating is provided with heating wire 17, heating wire 17 is embedded and 15 lower extremes of evaporating plate, solution heating after for preliminary treatment through evaporating plate 15, and get rid of remaining most moisture, the solubility of solution increases along with the temperature rise, through heating, make the solution reach the phenomenon of high solubility, be convenient for crystallization on next step.

Furthermore, the feeding pipeline 4, the drainage pipeline 6, the first material conveying pipeline 7, the second material conveying pipeline 10, the cooling water inlet 13 and the cooling water outlet 14 are all fixedly provided with valves 5, and the evaporation process can be controlled at any time by installing the valves 5, so that the operation is convenient.

Further, crystallization cylinder 11 is hollow structure, and its inside is fixed and has been seted up cooling water tank 20, and cooling water tank 20's upper end extends to the avris of crystallization ware 12, can be the solution cooling of high temperature, high solubility through installation cooling water tank 20 to make it appear the crystallization, the design that uses inside crystallization ware 12 has increased cooling contact area greatly, and then improves the cooling effect, accelerates the crystallization.

Furthermore, the height of the permeation cylinder 3 is higher than that of the evaporation box body 8, the height of the evaporation box body 8 is higher than that of the crystallization cylinder 11, the principle of a communicating vessel is utilized, the whole device does not need to be externally connected with a power device, and the solution can automatically flow down from top to bottom, so that resources are greatly saved.

The working principle is as follows: firstly, raw materials enter the permeation cylinder 3 from the feeding pipeline 4, under the action of the permeation membrane 18 and gravity, moisture in the raw materials can seep out of the permeation membrane 18 to the other side of the permeation membrane 18 and is discharged through the drainage pipeline 6, the concentration is higher and higher along with the discharge of the moisture, the density of the raw materials is increased, then the liquid level floating ball 19 floats and automatically opens, then concentrated solution enters the evaporation box body 8, then the heating wire 17 heats the concentrated solution, the concentrated solution is heated, most of residual moisture is evaporated, then the high-temperature concentrated solution enters the crystallization vessel 12 through the second material conveying pipeline 10, then cold water is injected into the cooling water inlet 13 to cool the high-temperature concentrated solution, the solubility of the high-temperature concentrated solution is reduced, crystals are separated.

It should be finally noted that the above only serves to illustrate the technical solution of the present invention, and not to limit the scope of the present invention, and that simple modifications or equivalent replacements performed by those skilled in the art to the technical solution of the present invention do not depart from the spirit and scope of the technical solution of the present invention.

Claims

1. A liquid evaporation instrument for Texas red production comprises a bottom plate and is characterized in that: the improved water-cooling crystallization device is characterized in that a penetration cylinder is fixedly mounted at the upper right side of the bottom plate, a feeding pipeline is fixedly communicated with the upper left end of the penetration cylinder, a drainage pipeline is fixedly communicated with the lower right end of the penetration cylinder, a first material conveying pipeline is fixedly communicated with the lower left end of the penetration cylinder, the first material conveying pipeline extends into the penetration cylinder, an evaporation box is fixedly communicated with the left end of the first material conveying pipeline, a second material conveying pipeline is fixedly communicated with the lower left end of the evaporation box, a crystallization cylinder is fixedly communicated with the right end of the second material conveying pipeline, a crystallization vessel is fixedly arranged in the crystallization cylinder, a cooling water inlet is fixedly communicated with the left end of the crystallization cylinder, a cooling water outlet is fixedly communicated with the right end of the crystallization cylinder, and the lower ends.

2. The apparatus of claim 1, wherein: the inside vertical fixed osmotic membrane that is provided with of central authorities of infiltration section of thick bamboo, the outside profile of osmotic membrane closely laminates with charge-in pipeline's inner wall, charge-in pipeline is located the upper left end of osmotic membrane, drainage pipe is located what the osmotic membrane has the lower extreme, the inside front end fixed mounting who is located first conveying pipeline of infiltration section of thick bamboo has the liquid level floater.

3. The apparatus of claim 1, wherein: the evaporation box is characterized in that an evaporation opening is fixedly arranged at the upper end of the evaporation box, an evaporation plate is fixedly arranged at the lower end, located in the first material conveying pipeline, of the evaporation box, the outer contour of the evaporation plate is tightly attached to the inner wall of the evaporation box, a heating chamber is fixedly arranged at the lower end of the evaporation plate, a heating wire is fixedly arranged at the bottom end, located in the evaporation plate, of the heating chamber, and the lower end of the evaporation plate is embedded in the heating wire.

4. The apparatus of claim 1, wherein: and valves are fixedly arranged on the feeding pipeline, the drainage pipeline, the first material conveying pipeline, the second material conveying pipeline, the cooling water inlet and the cooling water outlet.

5. The apparatus of claim 1, wherein: the crystallization cylinder is of a hollow structure, a cooling water tank is fixedly arranged in the crystallization cylinder, and the upper end of the cooling water tank extends to the side of the crystallization dish.

6. The apparatus of claim 1, wherein: the height of the permeation cylinder is higher than that of the evaporation box body, and the height of the evaporation box body is higher than that of the crystallization cylinder.