CN207575817U - A kind of destilling tower - Google Patents
A kind of destilling tower Download PDFInfo
- Publication number
- CN207575817U CN207575817U CN201721570489.1U CN201721570489U CN207575817U CN 207575817 U CN207575817 U CN 207575817U CN 201721570489 U CN201721570489 U CN 201721570489U CN 207575817 U CN207575817 U CN 207575817U
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- CN
- China
- Prior art keywords
- destilling tower
- distributary division
- mixing part
- chuck
- tower according
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- 238000002156 mixing Methods 0.000 claims abstract description 37
- 238000012546 transfer Methods 0.000 claims abstract description 5
- 239000000463 material Substances 0.000 claims description 28
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 claims description 8
- 238000003756 stirring Methods 0.000 claims description 7
- 239000006210 lotion Substances 0.000 abstract description 31
- 239000007789 gas Substances 0.000 abstract description 6
- 239000012159 carrier gas Substances 0.000 abstract description 3
- 230000000694 effects Effects 0.000 description 13
- 238000004821 distillation Methods 0.000 description 6
- 239000000498 cooling water Substances 0.000 description 5
- 239000005416 organic matter Substances 0.000 description 5
- 238000000926 separation method Methods 0.000 description 5
- 239000000839 emulsion Substances 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 238000001816 cooling Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000009835 boiling Methods 0.000 description 1
- 210000000481 breast Anatomy 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses destilling towers, including superposed distributary division and positioned at the mixing part of lower part, several isocons are vertically provided in the distributary division, connecting tube is provided in the mixing part, the upper end of connecting tube and the lower end of distributary division connect, and lower end is less than the outlet port being arranged on the side wall of mixing part；The destilling tower sets the connector and Matter Transfer pipe, isocon of a variety of carrier gas, lotion is made to be mixed into mixed gas to shunt from isocon and recycle between destilling tower and circulating line, the VOC in lotion can efficiently be detached, the content of VOC in lotion is greatly reduced, improve the quality of lotion, and the destilling tower is simple in structure, and operating cost is low.
Description
Technical field
The utility model is related to the separating-purifying engineering device technique field of coating, more particularly to a kind of destilling tower.
Background technology
More and more with the type of product emulsion, application is also increasingly extensive, but one in product emulsion on the market
As contain more volatile organic matter（VOC）, the requirement of environmental protection is not met, is unfavorable for the health of human body yet；The prior art
Perfect not enough to the treatment technology of volatile organic matter in product emulsion, traditional VOC disengagings technique is not only of high cost, consumption
Duration, and the effect being detached from is undesirable, greatly limits the exploitation of high-quality product emulsion.
The function of destilling tower is primarily to separating mixed liquids, using different liquids at different conditions, such as temperature not
Together, volatility（Boiling point）Different principles carries out liquid separation, so as to reach refining effect.
At present, the destilling tower of column plate type is flowed between pedal by material, is flowed back in a distillation column, reaches the effect of separation
Fruit；When destilling tower on the market is used to detach volatile organic matter in lotion, the contact area of lotion and working environment is limited,
Separating capacity is insufficient, and the standard of environmental protection is not achieved in product.
As it can be seen that the prior art could be improved and improve.
Utility model content
Part in view of above-mentioned deficiencies of the prior art, the purpose of this utility model is to provide a kind of destilling tower, Neng Gougao
Volatile organic matter in effect ground separation lotion, it is intended to solve the treatment technology of volatile organic matter in lotion in the prior art
It is not perfect, the problem of ecological requirements are not achieved.
In order to achieve the above object, the utility model takes following technical scheme：
A kind of destilling tower, including superposed distributary division and in the mixing part of lower part, the distributary division vertically
It is provided with several isocons；Connecting tube is provided in the mixing part, the upper end of connecting tube and the lower end of distributary division connect,
Lower end is less than the outlet port being arranged on the side wall of mixing part.
In the destilling tower, the destilling tower further includes chuck, and the chuck is wrapped in the lower part of mixing part, chuck
Bottom and side wall on be respectively arranged with the first thermometer connector and second temperature meter connector, the first thermometer connection
Mouth is extended in mixing part, the second temperature meter connector is extended to through the side wall of chuck inside chuck through chuck.
In the destilling tower, the connecting tube is in circular, the internal diameter size one of the distributary division of internal diameter and destilling tower
It causes.
In the destilling tower, the top and lower end of the distributary division are respectively fixed with one piece of fixed plate, fixed plate
Diameter is consistent with the internal diameter of distributary division, and the both ends of isocon are separately fixed in fixed plate.
In the destilling tower, the lower end of the mixing part is provided with the first material being connect with first material circulation pipe
Tube connection ports are recycled, the upper end of distributary division is provided with the second material cycle tube connection ports being connect with second material circulation pipe.
In the destilling tower, the upper end of the distributary division is additionally provided with steam tube connection ports and recirculated water water outlet,
The lower end of distributary division is provided with recirculated water water inlet.
In the destilling tower, several baffle plates are longitudinally disposed in the distributary division, the baffle plate is equidistantly
Heterogeneous Permutation is distributed between two fixed plates.
In the destilling tower, the lower end of the mixing part is additionally provided with inlet port and outlet port.
In the destilling tower, agitating device is provided in the mixing part, the agitating device is located at mixing part
Lower end, for material to be uniformly mixed.
In the destilling tower, the agitating device includes upper agitating paddle and lower stirring paddle, upper agitating paddle and lower stirring
Paddle is connected by rotating bar with motor, and the motor is located at the lower section of agitating paddle.Advantageous effect：
The utility model provides a kind of destilling tower, by setting the interface of a variety of carrier gas and Matter Transfer pipe, isocon,
Lotion is made to be mixed into mixed gas, shunted from isocon and is recycled in destilling tower and pipeline, increases connecing for lotion and environment
Contacting surface is accumulated, and improves the separative efficiency of VOC, and the VOC isolated is discharged from outlet port immediately, reduces destilling tower
In air pressure, so as to which VOC be promoted to be detached from lotion, and avoid VOC and mixed again with lotion；Distillation tower bottom, which uses, to be stirred
It mixes device stirring and hot water is added in chuck and lotion is preheated, all accelerate the separation of VOC in lotion；The destilling tower knot
Structure is simple, and operating cost is low, can efficiently detach the VOC in lotion, the content of VOC in lotion is greatly reduced, improves
The quality of lotion.
Description of the drawings
Fig. 1 is the structure diagram of destilling tower provided by the utility model.
Fig. 2 is sectional view of the destilling tower along A-A ' described in Fig. 1.
Specific embodiment
The utility model provides a kind of destilling tower, for make the purpose of this utility model, technical solution and effect it is clearer,
Clearly, the utility model is further described in the embodiment that develops simultaneously referring to the drawings.It should be appreciated that tool described herein
Body embodiment only to explain the utility model, is not used to limit the utility model.
It please refers to Fig.1 with 2, the utility model provides a kind of destilling tower, including superposed distributary division 1 and positioned at lower part
Mixing part 2, be vertically provided with several isocons 11 in the distributary division 1；Connecting tube is provided in the mixing part 2
21, the upper end of connecting tube 21 is connect with the lower end of distributary division 1, and lower end is less than the exhaust gas discharge being arranged on 2 side wall of mixing part
Mouth 22.
The isocon 11 is equidistantly distributed, and isocon 11 described in present embodiment forms the shape of regular hexagon,
Make isocon 11 as more as possible and be evenly dispersed in distributary division 1, certainly, the arrangement of isocon can also be octagon,
The shapes such as regualr decagon, as long as the energy for reaching the heat transfer effect of target and using reaches a best state.
During above-mentioned destilling tower work, the lotion of reflux enters from the upper end of distributary division 1 in destilling tower, with entering in destilling tower
Mixed gas mixing, flowed down from isocon 11, then fall on the bottom of mixing part 2 by connecting tube 21, lotion is from shunting
Same form is still maintained after flowing out in pipe 11 to fall, the surface area ratio of lotion is not provided with isocon 11 and is flowed directly to destilling tower
Bottom is much bigger, can effectively improve the separating effect of VOC in lotion.The outlet port 22 is connected with exhaust fan,
Exhaust gas is extracted out from destilling tower, the lower end of connecting tube 21 is arranged to that lotion can be avoided in whereabouts less than outlet port 22
Destilling tower is taken out of by air-flow when passing through outlet port 22 in the process, causes unnecessary waste.
Further, the destilling tower further includes chuck 3, and the chuck 3 is wrapped in the lower part of mixing part 2, chuck 3
The first thermometer connector 31 and second temperature meter connector 32 are respectively arranged in bottom and side wall, first thermometer connects
Interface 31 runs through chuck 3, extends in mixing part 2, and the second temperature meter connector 32 extends to folder through the side wall of chuck 3
Inside set 3.
The chuck 3 plays the role of heat preservation to the material in destilling tower, can also be by being passed through heat medium to distillation
Material in tower is heated；The bottom of chuck 3 and the upper end of side are respectively arranged with heat medium inflow entrance and heat medium
Outflux；First thermometer connector 31 and second temperature meter connector 32 have internal thread, and the first thermometer connector 31 connects
Jointing temp meter is used to test the temperature of the bottom of the mixing part 2 of destilling tower, and second temperature meter connector 32 connects thermometer and is used for
The temperature of medium in chuck is tested, when the temperature for detecting the material in destilling tower mixing part 2 is too low, needs to heat, and is detected
To chuck 2 in medium temperature be insufficient for the requirement of heating again when, it is necessary to be passed through that temperature is higher to meet heating requirements
Medium.
Preferably, the connecting tube 21 is in circular, and the internal diameter of the distributary division 1 of internal diameter and destilling tower is in the same size, is protected
The material flowed down in card isocon 11 is all fallen from connecting tube 21, is not influenced by air-flow.
Preferably, the top of the distributary division 1 and lower end are respectively fixed with one piece of fixed plate 12, the diameter of fixed plate 12
Consistent with the internal diameter of distributary division 1, the both ends of isocon 11 are separately fixed in fixed plate 12.The fixed plate 12 is circular hole
Plate, isocon 11 are passed through from the hole of fixed plate 12 in fixed fixed plate 12.
Further, the lower end of the mixing part 2 is provided with the first material cycle being connect with first material circulation pipe
Tube connection ports 23, the upper end of distributary division are provided with the second material cycle tube connection ports 13 being connect with second material circulation pipe.Object
Material is flowed out from the first material tube connection ports 23 of 2 lower end of mixing part, passes through second material tube connection ports after circulating line
13 are again introduced into destilling tower, so recycle, until the separating effect of material reaches the requirement of standard.
Further, the upper end of the distributary division 1 is additionally provided with steam tube connection ports 14 and recirculated water water outlet 15, point
The lower end in stream portion is provided with recirculated water water inlet 16.Steam mixes, so after steam tube connection ports 14 enter destilling tower with lotion
It is flowed down from isocon 11 afterwards, there is certain gap between isocon 11, recirculated water works as distillation from the gap flowing between isocon 11
Material overheat in tower, when needing cooling, cooling water flows into distributary division from recirculated water water inlet 16, then from recirculated water water outlet
15 outflows, the effect that the flow direction of material and cooling water on the contrary, can improve exchanges heat make full use of the cooling effect of cooling water.
Further, several baffle plates 17 have been longitudinally disposed in the distributary division 1, the baffle plate 17 is equidistantly wrong
Position arrangement, is distributed between two fixed plates 12.The baffle plate 17 increases the flow of cooling water, and increases its flow velocity,
Reduce dead zone, cooling water is made to be come into full contact with isocon 11, improve the effect of heat exchange, and have to isocon 11 certain
Support and the effect of positioning.
Further, the lower end of the mixing part 2 is additionally provided with feed inlet 24 and discharge port 25.
Preferably, agitating device 26 is provided in the mixing part 2, the agitating device 26 is located under mixing part 2
End, for material to be uniformly mixed；Be conducive to material thermally equivalent, improve the separative efficiency of VOC.
It is highly preferred that the agitating device 26 includes upper agitating paddle 261 and lower stirring paddle 262, upper agitating paddle 261 is under
Agitating paddle 262 is connected by rotating bar 263 and motor 264, and the motor 264 is located at the lower section of lower stirring paddle 262.The motor
By packing seal between 264 and the inner cavity of mixing part 2, prevent the material in mixing part 2 from flowing in motor 264 and cause motor
264 damage；Motor 264 is arranged on the lower section of agitating paddle, facilitates being isolated for motor 264 and material, is also convenient for tearing open for motor 264
It unloads and installation, maintenance.
In conclusion the destilling tower, by setting the interface of a variety of carrier gas and Matter Transfer pipe, isocon 11, makes breast
Liquid is mixed into mixed gas, shunts from isocon 11 and is recycled in destilling tower and pipeline, increases contact of the lotion with environment
Area, improves the separative efficiency of VOC, and the VOC isolated is discharged from outlet port 22 immediately, reduces destilling tower
In air pressure, so as to which VOC be promoted to be detached from lotion, and avoid VOC and mixed again with lotion；Distillation tower bottom, which uses, to be stirred
It mixes device 26 and stirs and added in chuck 3 hot water to lotion preheating, all accelerate the separation of VOC in lotion；The distillation
Tower structure is simple, and operating cost is low, can efficiently detach the VOC in lotion, the content of VOC in lotion is greatly reduced, carries
The high quality of lotion.
It is understood that for those of ordinary skills, can with technical solution according to the present utility model and
Its inventive concept is subject to equivalent substitution or change, and all these changes or replacement should all belong to the right appended by the utility model
It is required that protection domain.
Claims (10)
1. a kind of destilling tower, which is characterized in that including superposed distributary division and positioned at the mixing part of lower part, the distributary division
Inside vertically it is provided with several isocons；Connecting tube is provided in the mixing part, under the upper end and distributary division of connecting tube
End connection, lower end are less than the outlet port being arranged on the side wall of mixing part.
2. destilling tower according to claim 1, which is characterized in that the destilling tower further includes chuck, the chuck packet
The lower part of mixing part is rolled in, the first thermometer connector is respectively arranged in the bottom and side wall of chuck and is connected with second temperature meter
Mouthful, the first thermometer connector runs through chuck, extends in mixing part, and the second temperature meter connector is through chuck
Side wall is extended to inside chuck.
3. destilling tower according to claim 1, which is characterized in that the connecting tube is in annular shape, internal diameter and destilling tower
Distributary division internal diameter it is in the same size.
4. destilling tower according to claim 1, which is characterized in that the top and lower end of the distributary division are respectively fixed with
One piece of fixed plate, the diameter of fixed plate is consistent with the internal diameter of distributary division, and the both ends of isocon are separately fixed in fixed plate.
5. destilling tower according to claim 1, which is characterized in that the lower end of the mixing part is provided with and first material
The first material cycle tube connection ports of circulation pipe connection, the upper end of distributary division is provided with connect with second material circulation pipe second
Matter Transfer tube connection ports.
6. destilling tower according to claim 1, which is characterized in that the upper end of the distributary division is additionally provided with steam pipe company
Interface and recirculated water water outlet, the lower end of distributary division are provided with recirculated water water inlet.
7. destilling tower according to claim 1, which is characterized in that several bafflings have been longitudinally disposed in the distributary division
Plate, the baffle plate equidistantly Heterogeneous Permutation, is distributed between two fixed plates.
8. destilling tower according to claim 1, which is characterized in that the lower end of the mixing part be additionally provided with feed inlet and
Discharge port.
9. destilling tower according to claim 1, which is characterized in that agitating device is provided in the mixing part, it is described
Agitating device is located at the lower end of mixing part, for material to be uniformly mixed.
10. destilling tower according to claim 9, which is characterized in that the agitating device includes upper agitating paddle and stirred under
Paddle is mixed, upper agitating paddle is connected with lower stirring paddle by rotating bar with motor, and the motor is located at the lower section of agitating paddle.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721570489.1U CN207575817U (en) | 2017-11-22 | 2017-11-22 | A kind of destilling tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721570489.1U CN207575817U (en) | 2017-11-22 | 2017-11-22 | A kind of destilling tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207575817U true CN207575817U (en) | 2018-07-06 |
Family
ID=62732989
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721570489.1U Active CN207575817U (en) | 2017-11-22 | 2017-11-22 | A kind of destilling tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207575817U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107715489A (en) * | 2017-11-22 | 2018-02-23 | 广东银洋环保新材料有限公司 | A kind of destilling tower |
-
2017
- 2017-11-22 CN CN201721570489.1U patent/CN207575817U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107715489A (en) * | 2017-11-22 | 2018-02-23 | 广东银洋环保新材料有限公司 | A kind of destilling tower |
| CN107715489B (en) * | 2017-11-22 | 2024-01-16 | 广东银洋环保新材料有限公司 | Distillation tower |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| EE01 | Entry into force of recordation of patent licensing contract | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Guangdong Yaoda Financial Leasing Co.,Ltd. Assignor: GUANGDONG YINYANG ENVIRONMENT-FRIENDLY NEW MATERIALS Co.,Ltd. Contract record no.: X2021980003247 Denomination of utility model: A kind of distillation tower Granted publication date: 20180706 License type: Exclusive License Record date: 20210506 |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: A kind of distillation tower Effective date of registration: 20210508 Granted publication date: 20180706 Pledgee: Guangdong Yaoda Financial Leasing Co.,Ltd. Pledgor: GUANGDONG YINYANG ENVIRONMENT-FRIENDLY NEW MATERIALS Co.,Ltd. Registration number: Y2021980003370 |
|
| PC01 | Cancellation of the registration of the contract for pledge of patent right | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Granted publication date: 20180706 Pledgee: Guangdong Yaoda Financial Leasing Co.,Ltd. Pledgor: GUANGDONG YINYANG ENVIRONMENT-FRIENDLY NEW MATERIALS Co.,Ltd. Registration number: Y2021980003370 |
|
| EC01 | Cancellation of recordation of patent licensing contract | ||
| EC01 | Cancellation of recordation of patent licensing contract |
Assignee: Guangdong Yaoda Financial Leasing Co.,Ltd. Assignor: GUANGDONG YINYANG ENVIRONMENT-FRIENDLY NEW MATERIALS Co.,Ltd. Contract record no.: X2021980003247 Date of cancellation: 20240613 |