CN207270740U - A kind of lotion VOC release units - Google Patents
A kind of lotion VOC release units Download PDFInfo
- Publication number
- CN207270740U CN207270740U CN201721570490.4U CN201721570490U CN207270740U CN 207270740 U CN207270740 U CN 207270740U CN 201721570490 U CN201721570490 U CN 201721570490U CN 207270740 U CN207270740 U CN 207270740U
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- CN
- China
- Prior art keywords
- tower
- lotion
- destilling tower
- release units
- destilling
- 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.)
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- 239000006210 lotion Substances 0.000 title claims abstract description 62
- 239000007789 gas Substances 0.000 claims abstract description 37
- 239000000463 material Substances 0.000 claims abstract description 36
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 26
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 14
- 239000003546 flue gas Substances 0.000 claims abstract description 14
- 239000011261 inert gas Substances 0.000 claims abstract description 5
- 238000001816 cooling Methods 0.000 claims description 9
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 claims description 7
- 239000012528 membrane Substances 0.000 claims 1
- 239000007787 solid Substances 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 7
- 238000000034 method Methods 0.000 abstract description 6
- 239000000498 cooling water Substances 0.000 description 10
- 239000000839 emulsion Substances 0.000 description 6
- 238000004821 distillation Methods 0.000 description 5
- 238000010586 diagram Methods 0.000 description 3
- 239000005416 organic matter Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000012752 auxiliary agent Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 210000000481 breast Anatomy 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010892 electric spark Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Treating Waste Gases (AREA)
Abstract
The utility model discloses a kind of lotion VOC release units, including destilling tower, collect tower and exhaust gas tower, the bottom of the destilling tower is connected with collecting the top of tower by first material circulation pipe, the top of destilling tower is connected with the bottom for collecting tower by second material circulation pipe, the upper end for collecting tower is connected with inert gas conveyance conduit, the bottom of destilling tower is also associated with feed pipe, discharge nozzle and hot-water line, connected between destilling tower and the exhaust gas tower by flue gas leading, vacuum pump is connected with exhaust gas tower；When described device is run, lotion circulates in destilling tower and collection tower, coordinates the internal environment of the gas being passed through in a plurality of pipeline and vacuum, the disengaging effect of VOC has been significantly increased, and the technique of described device operation is simple, operating cost is low, the quality not product influence on lotion.
Description
Technical field
Polymer separating and treating apparatus field is the utility model is related to, more particularly to a kind of lotion VOC release units.
Background technology
At present, more and more with the species of product emulsion, its application is also increasingly extensive, but in existing product emulsion
Generally all contain more VOC（Volatile organic matter）, the requirement of environmental protection is not met, is unfavorable for the health of human body yet.
Perfect not enough to the treatment technology of volatile organic matter in product emulsion, traditional VOC departs from technique not only
It is of high cost, time-consuming, and depart from effect it is undesirable, greatly limit the exploitation of high-quality product emulsion.
As it can be seen that the prior art could be improved and improve.
Utility model content
In view of in place of above-mentioned the deficiencies in the prior art, depart from the purpose of this utility model is to provide a kind of lotion VOC and fill
Put, realize the volatile organic matter efficiently separated in product emulsion, product emulsion is reached the standard of environmental protection, not to using
The health of person produces harm.
In order to achieve the above object, the utility model takes following technical scheme：
A kind of lotion VOC release units, including destilling tower, collection tower and exhaust gas tower, the bottom of the destilling tower and collection
The top of tower is connected by first material circulation pipe, and the top of destilling tower and the bottom of collection tower are connected by second material circulation pipe
Connect, the upper end for collecting tower is connected with inert gas conveyance conduit, the bottom of destilling tower be also associated with feed pipe, discharge nozzle and
Hot-water line, is connected between destilling tower and the exhaust gas tower by flue gas leading, vacuum pump is connected with exhaust gas tower.
In the lotion VOC release units, the destilling tower includes superposed distributary division and is stirred positioned at lower part
Portion is mixed, connecting tube is provided with mixing part, the upper end of the connecting tube and the lower end of distributary division are seamlessly connected, and lower end is less than exhaust gas
The connector of pipe and destilling tower.
In the lotion VOC release units, the connecting tube in annular shape, the distributary division of its internal diameter and destilling tower
Internal diameter is in the same size.
In the lotion VOC release units, the destilling tower be also associated with steam pipeline, circulating water inlet,
Circulating water outlet pipe and working water water inlet pipe, the steam pipeline are connected to the top of destilling tower, circulating water inlet connection
In the lower part of destilling tower distributary division, circulating water outlet pipe is connected to the top of destilling tower distributary division, and working water water inlet pipe is connected to
The mixing part of destilling tower.
In the lotion VOC release units, the inside of the distributary division of the destilling tower is vertically arranged with some points
Flow tube, equidistantly, its both ends is separately fixed in fixed plate the isocon, and the fixed plate is fixed on point of destilling tower
The both ends in stream portion.
In the lotion VOC release units, the lower end of the mixing part of the destilling tower is provided with agitating device, is used for
Material is uniformly mixed.
In the lotion VOC release units, the feed pipe along feedstock direction be disposed with first filter and
First diaphragm pump, is disposed with the second filter and the second diaphragm pump on first material circulation pipe along the flow direction of material.
In the lotion VOC release units, it is empty that compression is also associated with first diaphragm pump and the second diaphragm pump
Letter shoot.
In the lotion VOC release units, the first material circulation pipe is connected by return duct with feed pipe, institute
The one end for stating return duct is connected on the feed pipe between the first diaphragm pump and destilling tower, the other end be connected to the second diaphragm pump with
Collect on the first material circulation pipe between tower.
In the lotion VOC release units, the top of the exhaust gas tower is vertically arranged with the cooling of some " u "-shapeds
Pipe, the both ends of the cooling tube are connected with circulating water inlet and circulating water outlet pipe respectively.
Beneficial effect：
The utility model provides a kind of lotion VOC release units, and the content of VOC in lotion can be greatly reduced, carry
The quality of high lotion；Described device is by making lotion circulate in a distillation column and setting isocon to make to be mixed with mixing in a distillation column
The material of gas is flowed down from isocon, increases the contact area of material and environment, improves the separative efficiency of VOC, and
Vacuum pump is connected with exhaust gas tower, the VOC for enabling to separate in destilling tower is rapidly discharged from flue gas leading, avoids VOC
Mixed again with lotion；Destilling tower is stirred using agitating device and lotion is preheated using hot water, both contributes to VOC in lotion
Separation；The top of the connector of flue gas leading sets recirculated cooling water pipeline in exhaust gas tower, can make to enter from flue gas leading useless
The VOC of gas tower is quickly cooled down, and is back in exhaust gas tower and is absorbed or collected；Described device running is simple and convenient, and cost is low, right
The disengaging of VOC is efficient, and does not influence the quality of lotion.
Brief description of the drawings
Fig. 1 is the connection relationship diagram of the lotion VOC release units provided by the utility model,
Wherein, the signified direction of arrow is the flow direction with the fluid in immediate pipeline in figure.
Fig. 2 is the structure diagram of the destilling tower.
Fig. 3 is sectional view of the destilling tower along A-A ' described in Fig. 2.
Fig. 4 is the structure diagram of the exhaust gas tower.
Fig. 5 is sectional view of the exhaust gas tower along B-B ' described in Fig. 4.
Embodiment
The utility model provides a kind of lotion VOC release units, to make the purpose of this utility model, technical solution and effect
Clearer, clear and definite, the utility model is further described in the embodiment that develops simultaneously referring to the drawings.It should be appreciated that herein
Described specific embodiment only to explain the utility model, is not used to limit the utility model.
Referring to Fig. 1, the utility model provides a kind of lotion VOC release units, including destilling tower 1, collection tower 2 and exhaust gas
Tower 3, the bottom of the destilling tower 1 are connected with collecting the top of tower 2 by first material circulation pipe 4, the top of destilling tower 1 and receipts
The bottom of collection tower 2 is connected by second material circulation pipe 5, and the upper end for collecting tower 2 is connected with inert gas conveyance conduit 21,
The bottom of destilling tower 1 is also associated with feed pipe 6, discharge nozzle 7 and hot-water line 8, by useless between the destilling tower 1 and exhaust gas tower 3
Tracheae 9 connects, and vacuum pump 10 is connected with exhaust gas tower 3.
Valve is both provided with pipeline in described device, in the process of running, lotion is from being connected to 1 bottom of destilling tower
Feed, preheated into the lotion in destilling tower 1 by the hot water flowed into hot-water line 8 in destilling tower 1, in lotion in feed pipe 6
VOC is gradually separated, and lotion through initial gross separation VOC flows into first material circulation pipe 4, be delivered to collect in tower 2 with from inertia
Gas transmission pipeline 21 enters inert gas, preferred nitrogen in present embodiment, mixing, from the second material for collecting 2 bottom of tower
Flowed into circulation pipe 5 in destilling tower 1, be again separate out VOC, the VOC separated is delivered in exhaust gas tower 3 through flue gas leading 9, even
The vacuum pump 10 for connecing exhaust gas tower 3 is opened, and makes the state that negative pressure is in exhaust gas tower 3, so that separated in destilling tower 1
VOC, which can be rapidly delivered in exhaust gas tower 3, to be absorbed or is collected；Lotion circulates in destilling tower 1, and the disengaging of VOC is efficient,
Technique is simple, and the quality of lotion has been significantly increased.
Referring to Fig. 2, specifically, the destilling tower 1 includes superposed distributary division 1A and positioned at lower part mixing part
It is provided with the upper end of connecting tube 1B1, the connecting tube 1B1 in 1B, mixing part 1B to be seamlessly connected with the lower end of distributary division 1A, lower end
Less than flue gas leading 9 and the connector of destilling tower 1.
When described device is run, lotion is flowed down from the distributary division 1A of destilling tower 1, and the distillation is fallen on through connecting tube 1B1
1 bottom of tower, it is useless that the connecting tube 1B1 can prevent that lotion from being brought into when passing through 9 connector of flue gas leading during falling by air-flow
In tracheae 9, unnecessary waste is caused.
Preferably, the connecting tube 1B1 is in annular shape, the internal diameter size one of its internal diameter and the distributary division 1A of destilling tower 1
Cause, ensure that the material that distributary division 1A is flowed down in destilling tower 1 is all flowed down from connecting tube 1B1, from airflow influence.
Please refer to Fig.1, it is preferable that the destilling tower 1 is also associated with steam pipeline 11, circulating water inlet 12, follows
Ring water outlet pipe 13 and working water water inlet pipe 14, the steam pipeline 11 are connected to the top of destilling tower 1, circulating water inlet
12 are connected to the lower part of the distributary division 1A of destilling tower 1, and 13 pipe of recirculated water water outlet is connected to the top of the distributary division 1A of destilling tower 1,
Working water water inlet pipe 14 is connected to the mixing part 1B of destilling tower 1.
When described device is run, steam pipeline 11 conveys steam into the distributary division 1A of destilling tower 1, is mixed with lotion,
When the temperature of charge in destilling tower 1 is excessive, recirculated cooling water is passed through from circulating water inlet 12 to the distributary division of destilling tower 1
1A, the cooling water are flowed into from the lower part of distributary division 1A, and top outflow, fully contacts, maximum limit with the conveyance conduit of material
Degree can utilize the cooling effect of recirculated cooling water.
Refer to Fig. 2 and 3, it is preferable that the inside of the distributary division 1A of the destilling tower 1 is vertically arranged with some shuntings
Equidistantly, its both ends is separately fixed on fixed plate 1A2 by pipe 1A1, the isocon 1A1, and the fixed plate 1A2 is fixed on
The both ends of the distributary division 1A of destilling tower 1.
The material entered from second material circulation pipe 5 in destilling tower 1 is flowed down from isocon 1A1, is had between isocon 1A1
Certain gap, recirculated cooling water are flowed from the gap between isocon 1A1, and some horizontal strokes are additionally provided with the distributary division 1A1
To baffle plate, increase the flow of recirculated cooling water and make its flow velocity increase, reduce dead band, make cooling water and isocon
1A1 comes into full contact with, and improves the effect of heat exchange, and play the role of certain support and positioning to isocon 1A1.Material from point
Flowed out in flow tube 1A1, the form maintained like in dropping process is fallen, and surface area ratio is not provided with isocon 1A1 and flows directly into institute
It is much bigger to state 1 bottom of destilling tower, effectively enhances the separating effect of VOC in lotion.
Preferably, the lower end of the mixing part 1B of the destilling tower 1 is provided with agitating device 1B2, for material to be mixed
Uniformly；Logistics is stirred and is conducive to material and is heated evenly, improves the separative efficiency of VOC.
Please refer to Fig.1, it is preferable that the feed pipe 6 is disposed with first filter 15 and first along feedstock direction
Diaphragm pump 17, is disposed with the second filter 16 and the second diaphragm pump on first material circulation pipe 4 along the flow direction of material
18。
Lotion due to raw material or generating means, may produce some impurity particle things in process of production,
15 and second filter 16 of first filter is set to filter out lotion respectively in feed pipe 6 and first material circulation pipe 4
In particulate matter, avoid increase the first diaphragm pump 17 and the second diaphragm pump 18 operating pressure and block destilling tower 1 in shunting
Pipe 1A1, also improves the quality of lotion finished product to a certain extent.
Preferably, it is also associated with blowpipe 19 on first diaphragm pump 17 and the second diaphragm pump 18；Make
Lotion is mixed into compressed air during by the first diaphragm pump 17 and the second diaphragm pump 18, drives breast in the VOC in lotion
Depart from liquid, can also make the first diaphragm pump 17 and the second diaphragm pump 18 can be with cold situation in addition, being passed through compressed air
Run by air pressure down, the auxiliary agent in lotion belongs to combustibles, and electric spark or mistake may be produced during the work time using electric pump
Thermal phenomenon, there is some potential safety problems, and the generation of this problem can be avoided using the diaphragm pump of compressed air-driven.
Preferably, the first material circulation pipe 4 is connected by return duct 20 with feed pipe 6, the return duct 20
One end is connected on the feed pipe 6 between the first diaphragm pump 17 and destilling tower 1, and the other end is connected to the second diaphragm pump 18 with collecting
On first material circulation pipe 4 between tower 2.
Please refer to Fig.1,4 and 5 preferably, the top of the exhaust gas tower 3 is vertically arranged with the cooling tube of some " u "-shapeds
3A, the both ends of the cooling tube 3A are connected with circulating water inlet 12 and circulating water outlet pipe 13 respectively.Enter from flue gas leading 9 useless
The bottom that exhaust gas tower 3 is flow to after the circulating cooling water cooling that VOC in gas tower 3 is cooled in pipe 3A is absorbed or is collected, " u "-shaped
Cooling tube 3A increase length of flow of the cooling water in exhaust gas tower 3, fully utilize its heat transfer effect.
In conclusion the lotion VOC release units, can be greatly reduced the content of VOC in lotion, improve lotion
Quality；Described device is by making lotion circulate in a distillation column and setting isocon to make to be mixed with mixed gas in a distillation column
Material is flowed down from isocon, increases the contact area of material and environment, improves the separative efficiency of VOC, and exhaust gas tower
In be connected with vacuum pump, the VOC for enabling to separate in destilling tower is rapidly discharged from flue gas leading, avoid VOC again with
Lotion mixes；Destilling tower is stirred using agitating device and lotion is preheated using hot water, both contributes to point of VOC in lotion
From；The top of the connector of flue gas leading sets recirculated cooling water pipeline in exhaust gas tower, can make to enter exhaust gas tower from flue gas leading
VOC quickly cool down, be back in exhaust gas tower and absorbed or collected；Described device running is simple and convenient, and cost is low, to VOC's
Depart from quality that is efficient, and not influencing 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 lotion VOC release units, it is characterised in that including destilling tower, collect tower and exhaust gas tower, the bottom of the destilling tower
Portion is connected with collecting the top of tower by first material circulation pipe, and the top of destilling tower and the bottom of collection tower pass through second material
Circulation pipe connects, and the upper end for collecting tower is connected with inert gas conveyance conduit, the bottom of destilling tower be also associated with feed pipe,
Discharge nozzle and hot-water line, are connected between destilling tower and the exhaust gas tower by flue gas leading, vacuum pump are connected with exhaust gas tower.
2. lotion VOC release units according to claim 1, it is characterised in that the destilling tower includes being located at top
Distributary division and connecting tube, the upper end of the connecting tube and the lower end of distributary division are provided with lower part mixing part, mixing part
It is seamlessly connected, lower end is less than flue gas leading and the connector of destilling tower.
3. lotion VOC release units according to claim 2, it is characterised in that the connecting tube is in annular shape, in it
The internal diameter of the distributary division of footpath and destilling tower is in the same size.
4. lotion VOC release units according to claim 2, it is characterised in that the destilling tower is also associated with steam
Delivery pipe, circulating water inlet, circulating water outlet pipe and working water water inlet pipe, the steam pipeline are connected to the top of destilling tower
Portion, circulating water inlet are connected to the lower part of destilling tower distributary division, and circulating water outlet pipe is connected to the top of destilling tower distributary division,
Working water water inlet pipe is connected to the mixing part of destilling tower.
5. lotion VOC release units according to claim 2, it is characterised in that the distributary division of the destilling tower it is interior
Portion is vertically arranged with some isocons, and equidistantly, its both ends is separately fixed in fixed plate the isocon, described solid
Fixed board is fixed on the both ends of the distributary division of destilling tower.
6. lotion VOC release units according to claim 2, it is characterised in that under the mixing part of the destilling tower
End is provided with agitating device, for material to be uniformly mixed.
7. lotion VOC release units according to claim 1, it is characterised in that the feed pipe along feedstock direction according to
It is secondary to be provided with first filter and the first diaphragm pump, on first material circulation pipe second is disposed with along the flow direction of material
Filter and the second diaphragm pump.
8. lotion VOC release units according to claim 7, it is characterised in that first diaphragm pump and second every
Blowpipe is also associated with membrane pump.
9. lotion VOC release units according to claim 7, it is characterised in that the first material circulation pipe passes through
Return duct is connected with feed pipe, and one end of the return duct is connected on the feed pipe between the first diaphragm pump and destilling tower, separately
One end is connected on the first material circulation pipe between the second diaphragm pump and collection tower.
10. lotion VOC release units according to claim 1, it is characterised in that the top of the exhaust gas tower is longitudinally set
The cooling tube of some " u "-shapeds is equipped with, the both ends of the cooling tube are connected with circulating water inlet and circulating water outlet pipe respectively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721570490.4U CN207270740U (en) | 2017-11-22 | 2017-11-22 | A kind of lotion VOC release units |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721570490.4U CN207270740U (en) | 2017-11-22 | 2017-11-22 | A kind of lotion VOC release units |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207270740U true CN207270740U (en) | 2018-04-27 |
Family
ID=61978670
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721570490.4U Active CN207270740U (en) | 2017-11-22 | 2017-11-22 | A kind of lotion VOC release units |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207270740U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107715486A (en) * | 2017-11-22 | 2018-02-23 | 广东银洋环保新材料有限公司 | A kind of emulsion VOC release units |
-
2017
- 2017-11-22 CN CN201721570490.4U patent/CN207270740U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107715486A (en) * | 2017-11-22 | 2018-02-23 | 广东银洋环保新材料有限公司 | A kind of emulsion VOC release units |
| CN107715486B (en) * | 2017-11-22 | 2023-09-12 | 广东银洋环保新材料有限公司 | Emulsion VOC breaks away from device |
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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 |
Assignee: Guangdong Yaoda Financial Leasing Co.,Ltd. Assignor: GUANGDONG YINYANG ENVIRONMENT-FRIENDLY NEW MATERIALS Co.,Ltd. Contract record no.: X2021980003247 Denomination of utility model: An emulsion VOC detaching device Granted publication date: 20180427 License type: Exclusive License Record date: 20210506 |
|
| EE01 | Entry into force of recordation of patent licensing contract | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: An emulsion VOC detaching device Effective date of registration: 20210508 Granted publication date: 20180427 Pledgee: Guangdong Yaoda Financial Leasing Co.,Ltd. Pledgor: GUANGDONG YINYANG ENVIRONMENT-FRIENDLY NEW MATERIALS Co.,Ltd. Registration number: Y2021980003370 |
|
| PE01 | Entry into force 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: 20180427 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 |
Assignee: Guangdong Yaoda Financial Leasing Co.,Ltd. Assignor: GUANGDONG YINYANG ENVIRONMENT-FRIENDLY NEW MATERIALS Co.,Ltd. Contract record no.: X2021980003247 Date of cancellation: 20240613 |