CN209865341U - High-efficient dehydration tower - Google Patents
High-efficient dehydration tower Download PDFInfo
- Publication number
- CN209865341U CN209865341U CN201920472707.0U CN201920472707U CN209865341U CN 209865341 U CN209865341 U CN 209865341U CN 201920472707 U CN201920472707 U CN 201920472707U CN 209865341 U CN209865341 U CN 209865341U
- Authority
- CN
- China
- Prior art keywords
- pipe
- tower body
- reboiler
- efficient
- tower
- 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
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a high-efficient dehydration tower relates to high-efficient dehydration tower technical field, for solving the current high-efficient dehydration tower's that provides extravagant material distillation composition and the not good problem of heating distillation effect. The below of tower body is provided with the mount, the below of mount is provided with the supporting legs, and the supporting legs is provided with two, the inside of tower body is provided with high-efficient whirl dehydrator, the below of high-efficient whirl dehydrator is provided with PMKD, the top of high-efficient whirl dehydrator is provided with the filler plate, be provided with the overflow pipe between filler plate and the high-efficient whirl dehydrator, the top of filler plate is provided with backward flow condensation mechanism, be provided with the outlet duct between tower body and the condensation mechanism, the opposite side of tower body is provided with the reboiler, one side of reboiler is provided with the drain pump, be provided with the waste pipe between reboiler and the drain pump, one side of drain pump is provided with.
Description
Technical Field
The utility model relates to a high-efficient dehydration tower technical field specifically is a high-efficient dehydration tower.
Background
The dehydration tower is a tower type vapor-liquid contact device for rectification, also called as a distillation tower, and can be divided into a continuous dehydration tower and an intermittent dehydration tower according to the operation mode, the basic principle of the dehydration tower is that vapor enters from the bottom of the tower and is in countercurrent contact with descending liquid, volatile components in the descending liquid are continuously transferred into the vapor in two-phase contact, and the components which are difficult to volatilize in the vapor are continuously transferred into the descending liquid, the more the vapor is close to the top of the tower, the higher the concentration of the volatile components is, and the more the descending liquid is close to the bottom of the tower, the more the volatile components are enriched, so that the purpose of separating the components is achieved, and therefore, the efficient dehydration tower is more and more widely used.
At present, the high-efficient dehydration tower on the market, when distilling and dehydrating, can waste the material distillation composition of a lot, work efficiency is low moreover, often can not reach the standard of dehydration, still can cause the waste on the resource, can't carry out the circulation distillation to it is not good to heat the distillation effect, has influenced the dehydration effect, can not satisfy user's demand, therefore the market is urgently needed to develop a high-efficient dehydration tower and helps people to solve current problem.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide a high-efficient dehydration tower to solve the not good problem of the extravagant material distillation composition and the heating distillation effect of the current high-efficient dehydration tower that provides in the above-mentioned background art.
In order to achieve the above object, the utility model provides a following technical scheme: a high-efficiency dehydration tower comprises a tower body, wherein a fixed frame is arranged below the tower body, supporting legs are arranged below the fixed frame, two supporting legs are arranged on the supporting legs, a high-efficiency rotational flow dehydrator is arranged inside the tower body, a fixed bottom plate is arranged below the high-efficiency rotational flow dehydrator, a partition plate is arranged below the fixed bottom plate, a heater is arranged above the partition plate, a liquid phase outlet pipe is arranged below the fixed bottom plate, a feeding pipe is arranged above the liquid phase outlet pipe, a condensing mechanism is arranged on one side of the tower body, a tank body is arranged on one side of the condensing mechanism, a production pipe is arranged on one side of the tank body, a connecting pipe is arranged between the condensing mechanism and the tank body, a packing plate is arranged above the high-efficiency rotational flow dehydrator, an overflow pipe is arranged between the, the top of packing plate is provided with backward flow condensation mechanism, be provided with the outlet duct between tower body and the condensation mechanism, the opposite side of tower body is provided with the reboiler, one side of reboiler is provided with the drain pump, be provided with the waste pipe between reboiler and the drain pump, one side of drain pump is provided with the drain pipe.
Preferably, the high-efficiency cyclone dehydrator comprises a rotary cylinder, a rotary base and a rotary shaft, wherein the rotary shaft is positioned above the rotary base, the rotary cylinder is positioned above the rotary shaft, and the rotary shaft is rotatably connected with the rotary cylinder.
Preferably, one end of the liquid phase outlet pipe penetrates through the partition plate, one end of the liquid phase outlet pipe extends to the outside of the tower body, and one end of the overflow pipe penetrates through and extends to the outside of the packing plate.
Preferably, the inside of condensation mechanism is provided with the spiral catch bar, the below of spiral catch bar is provided with the drain pipe, one side of condensation mechanism is provided with the motor.
Preferably, the condensing mechanism is connected with the tank body in a sealing manner through a connecting pipe, the tower body is connected with the condensing mechanism in a sealing manner through an air outlet pipe, and the liquid phase outlet pipe is connected with the reboiler in a sealing manner.
Preferably, the supporting legs are welded to the fixing frame, and the tower body is fixedly connected with the partition plate and the fixing bottom plate.
Compared with the prior art, the beneficial effects of the utility model are that:
1. this high-efficient dehydration tower is through setting up high-efficient whirl dehydrator, and it is rotatory to drive the rotation axis through the inside actuating mechanism of high-efficient whirl dehydrator, and the rotation axis drives rotatory section of thick bamboo rotatory, with the moisture discharge in the material to get into condensation mechanism and reboiler through the liquid phase outlet pipe, can reach the effect of recirculation, thereby avoided the waste on the resource, reach resources are saved, reuse's purpose has solved the problem of the extravagant material distillation composition of traditional high-efficient dehydration tower.
2. This high efficiency dehydration tower is through setting up the heater, and the heater heats, under the effect of wind-heat, has accelerated the distillation process of material to through the liquid phase of high-efficient whirl dehydrator backward flow, get into the internal rectification of dehydration tower once more, the last waste water of coming out passes through reboiler steam reflux effect, and partly converges into the outlet duct, and another part is under the drain pump effect, discharges from the drain pipe, has solved the not good problem of traditional high efficiency dehydration tower heating distillation effect.
Drawings
Fig. 1 is a front view of the present invention;
FIG. 2 is a schematic structural view of the high-efficiency cyclone dehydrator of the present invention;
fig. 3 is a schematic structural diagram of the condensing mechanism of the present invention.
In the figure: 1. supporting legs; 2. a fixed mount; 3. a screw pushing rod; 4. a motor; 5. a feed pipe; 6. a tower body; 7. a liquid phase outlet pipe; 8. a drain pipe; 9. a reboiler; 10. a waste pipe; 11. draining pump; 12. a condensing mechanism; 13. a connecting pipe; 14. a tank body; 15. a pipe is extracted; 16. an air outlet pipe; 17. a high-efficiency rotational flow dehydrator; 18. a heater; 19. a reflux condensing mechanism; 20. a filler sheet; 21. a rotary drum; 22. a partition plate; 23. fixing the bottom plate; 24. rotating the base; 25. a rotating shaft; 26. an overflow pipe; 27. a liquid outlet pipe.
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.
Referring to fig. 1-3, the present invention provides an embodiment: a high-efficiency dehydration tower comprises a tower body 6, a fixing frame 2 is arranged below the tower body 6, two supporting feet 1 are arranged below the fixing frame 2, two supporting feet 1 are arranged on the supporting feet 1, a high-efficiency rotational flow dehydrator 17 is arranged inside the tower body 6, a fixing bottom plate 23 is arranged below the high-efficiency rotational flow dehydrator 17, a partition plate 22 is arranged below the fixing bottom plate 23, a heater 18 is arranged above the partition plate 22, a distillation process of materials is accelerated under the wind-heat effect, a liquid phase outlet pipe 7 is arranged below the fixing bottom plate 23, a feeding pipe 5 is arranged above the liquid phase outlet pipe 7, a condensing mechanism 12 is arranged on one side of the tower body 6, a tank body 14 is arranged on one side of the condensing mechanism 12, a sampling outlet pipe 15 is arranged on one side of the tank body 14, a connecting pipe 13 is arranged between the condensing mechanism 12 and the, be provided with overflow pipe 26 between filled plate 20 and the high-efficient whirl dehydrator 17, filled plate 20's top is provided with backward flow condensation mechanism 19, be provided with outlet duct 16 between tower body 6 and the condensation mechanism 12, the opposite side of tower body 6 is provided with reboiler 9, one side of reboiler 9 is provided with drain pump 11, be provided with waste pipe 10 between reboiler 9 and the drain pump 11, one side of drain pump 11 is provided with drain pipe 8, the effect of recirculation can be reached, thereby the waste on the resource has been avoided, reach resources are saved, reuse's purpose.
Further, the high-efficiency cyclone dehydrator 17 comprises a rotary cylinder 21, a rotary base 24 and a rotary shaft 25, wherein the rotary shaft 25 is positioned above the rotary base 24, the rotary cylinder 21 is positioned above the rotary shaft 25, and the rotary shaft 25 is rotatably connected with the rotary cylinder 21, so that the connection between the structures is more stable and the operation is more efficient.
Further, one end of the liquid phase outlet pipe 7 penetrates through the partition plate 22, one end of the liquid phase outlet pipe 7 extends to the outside of the tower body 6, one end of the overflow pipe 26 penetrates through and extends to the outside of the packing plate 20, and the recycling effect can be achieved, so that waste of resources is avoided, and the purposes of saving resources and recycling are achieved.
Further, the inside of condensation mechanism 12 is provided with spiral catch bar 3, and the below of spiral catch bar 3 is provided with drain pipe 27, and one side of condensation mechanism 12 is provided with motor 4, can accelerate the outflow of distillate.
Further, condensation mechanism 12 and jar body 14 pass through connecting pipe 13 sealing connection, and tower body 6 passes through outlet duct 16 sealing connection with condensation mechanism 12, and liquid phase outlet pipe 7 and reboiler 9 sealing connection for the leakproofness between the structure is better.
Furthermore, supporting legs 1 and mount 2 welded connection, tower body 6 and division board 22 and the equal fixed connection of PMKD 23 for the relation of connection between the structure is safer, reliable.
The working principle is as follows: when in use, firstly, materials are put in through the feeding pipe 5 and enter the rotary drum 21 in the high-efficiency cyclone dehydrator 17, the high-efficiency cyclone dehydrator 17 drives the rotary base 24 to rotate through the driving mechanism, the rotation of the rotary base 24 drives the rotary shaft 25 to rotate, the rotary shaft 25 drives the rotary drum 21 to rotate, in high-speed rotation, a heater 18 connected with the bottom end of the high-efficiency cyclone dehydrator 17 is added to distill out partial components of the materials, the heater 18 heats the materials to accelerate the outflow of liquid-phase distillate, the liquid-phase distillate reflows through the high-efficiency cyclone dehydrator 17 passes through the overflow pipe 26 and enters the reflux condensing mechanism 19 for condensation and filtration, after the reflux condensing mechanism 19 carries out condensation and filtration, the liquid-solid mixture in the air outlet pipe 16 enters the condensing mechanism 12 for secondary condensation and filtration, after the gas-solid mixture in the air outlet, liquid flows out from the liquid outlet pipe 27, the other part of solid materials enter the tank body 14 through the connecting pipe 13 under the pushing of the spiral pushing rod 3, finally, the materials are extracted from the extraction pipe 15, meanwhile, the wastewater generated by the spiral flow of the high-efficiency spiral flow dehydrator 17 flows into the liquid phase outlet pipe 7 at the lower part, the wastewater flowing out of the liquid phase outlet pipe 7 passes through the reboiler 9, the effect of recirculation can be achieved, thereby the waste on resources is avoided, the purposes of saving resources and recycling are achieved, the reboiler 9 generates steam backflow again, because the pipe diameter of the liquid phase outlet pipe 7 is larger than that of the wastewater pipe 10, and the wastewater is accumulated in the reboiler 9, therefore, under the work of the reboiler 9, a part of steam directly gathers into the gas outlet pipe 16 with a one-way valve, the steam enters the condensing mechanism 12 again, and the other part of wastewater is discharged from the water discharge pipe 8 under the action of, has high efficiency and circulation effect.
It is obvious to a person skilled in the art that the invention is not restricted to details of the above-described exemplary embodiments, but that it can be implemented in other specific forms without departing from the spirit or essential characteristics of the invention. The present embodiments are therefore to be considered in all respects as illustrative and not restrictive, the scope of the invention being indicated by the appended claims rather than by the foregoing description, and all changes which come within the meaning and range of equivalency of the claims are therefore intended to be embraced therein. Any reference sign in a claim should not be construed as limiting the claim concerned.
Claims (6)
1. An efficient dehydration tower comprises a tower body (6), and is characterized in that: the device is characterized in that a fixing frame (2) is arranged below the tower body (6), supporting legs (1) are arranged below the fixing frame (2), two supporting legs (1) are arranged, a high-efficiency cyclone dehydrator (17) is arranged inside the tower body (6), a fixing bottom plate (23) is arranged below the high-efficiency cyclone dehydrator (17), a partition plate (22) is arranged below the fixing bottom plate (23), a heater (18) is arranged above the partition plate (22), a liquid phase outlet pipe (7) is arranged below the fixing bottom plate (23), an inlet pipe (5) is arranged above the liquid phase outlet pipe (7), a condensing mechanism (12) is arranged on one side of the tower body (6), a tank body (14) is arranged on one side of the condensing mechanism (12), an extraction pipe (15) is arranged on one side of the tank body (14), and a connecting pipe (13) is arranged between the condensing mechanism (12) and the tank body (14), the top of high-efficient whirl dehydrator (17) is provided with packing plate (20), be provided with overflow pipe (26) between packing plate (20) and high-efficient whirl dehydrator (17), the top of packing plate (20) is provided with backward flow condensation mechanism (19), be provided with outlet duct (16) between tower body (6) and condensation mechanism (12), the opposite side of tower body (6) is provided with reboiler (9), one side of reboiler (9) is provided with drain pump (11), be provided with between reboiler (9) and drain pump (11) waste pipe (10), one side of drain pump (11) is provided with drain pipe (8).
2. The high efficiency dehydration column according to claim 1, characterized in that: the high-efficiency cyclone dehydrator (17) comprises a rotary barrel (21), a rotary base (24) and a rotary shaft (25), wherein the rotary shaft (25) is positioned above the rotary base (24), the rotary barrel (21) is positioned above the rotary shaft (25), and the rotary shaft (25) is rotatably connected with the rotary barrel (21).
3. The high efficiency dehydration column according to claim 1, characterized in that: one end of the liquid phase outlet pipe (7) penetrates through the partition plate (22), one end of the liquid phase outlet pipe (7) extends to the outside of the tower body (6), and one end of the overflow pipe (26) penetrates through and extends to the outside of the packing plate (20).
4. The high efficiency dehydration column according to claim 1, characterized in that: the inside of condensation mechanism (12) is provided with spiral catch bar (3), the below of spiral catch bar (3) is provided with drain pipe (27), one side of condensation mechanism (12) is provided with motor (4).
5. The high efficiency dehydration column according to claim 1, characterized in that: condensation mechanism (12) and jar body (14) are through connecting pipe (13) sealing connection, tower body (6) and condensation mechanism (12) are through outlet duct (16) sealing connection, liquid phase outlet pipe (7) and reboiler (9) sealing connection.
6. The high efficiency dehydration column according to claim 1, characterized in that: the supporting legs (1) are welded with the fixing frame (2), and the tower body (6) is fixedly connected with the partition plate (22) and the fixed bottom plate (23).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201920472707.0U CN209865341U (en) | 2019-04-10 | 2019-04-10 | High-efficient dehydration tower |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201920472707.0U CN209865341U (en) | 2019-04-10 | 2019-04-10 | High-efficient dehydration tower |
Publications (1)
Publication Number | Publication Date |
---|---|
CN209865341U true CN209865341U (en) | 2019-12-31 |
Family
ID=68959015
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201920472707.0U Active CN209865341U (en) | 2019-04-10 | 2019-04-10 | High-efficient dehydration tower |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN209865341U (en) |
-
2019
- 2019-04-10 CN CN201920472707.0U patent/CN209865341U/en active Active
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN209865341U (en) | High-efficient dehydration tower | |
CN205516576U (en) | Washing type stills is exempted from in saving | |
CN201500467U (en) | Double-layered sleeve heat collecting Soxhlet extractor | |
CN108192794A (en) | A kind of list using energy source formula alcohol distillation extracting system | |
CN207270743U (en) | A kind of efficient dehydrating tower | |
CN212575660U (en) | Film flash distillation rectifying tower | |
CN212575657U (en) | Rectifying tower device for efficient backflow distribution of essence and spice | |
CN113636707A (en) | Industrial wastewater recycling high-efficiency treatment equipment | |
CN209020382U (en) | Reaction kettle with vapor collection device | |
CN208825182U (en) | A kind of solid-state waste mineral oil disposal system | |
CN208843757U (en) | Portable type sea water desalination equipment | |
CN201578873U (en) | Rectifying device | |
CN218774325U (en) | High-efficient chemical industry extraction rectifying column | |
CN206492242U (en) | A kind of efficient ultrasonic extractor | |
CN206544988U (en) | A kind of glycol recycling system for polyester industrial | |
CN221254372U (en) | Catalytic oxidation treatment facility for livestock-raising industry manure | |
CN210409568U (en) | High-efficiency reboiler | |
CN218793899U (en) | Energy-efficient low temperature draws concentrator group | |
CN219429873U (en) | Oily sludge drying and solidifying treatment device | |
CN214551280U (en) | Rectifying column waste heat utilization device | |
CN215232198U (en) | Ethylene-chlorotrifluoroethylene rectification purification device | |
CN216191714U (en) | High-efficient industry waste acid water treatment facilities | |
CN212383207U (en) | A raw materials enrichment facility for pharmaceutical production | |
CN217724619U (en) | Rotary evaporator convenient for feeding and discharging | |
CN218923817U (en) | Multilayer rectifying column |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant |