CN211328723U - Stripper export liquid return mechanism - Google Patents
Stripper export liquid return mechanism Download PDFInfo
- Publication number
- CN211328723U CN211328723U CN201921761757.7U CN201921761757U CN211328723U CN 211328723 U CN211328723 U CN 211328723U CN 201921761757 U CN201921761757 U CN 201921761757U CN 211328723 U CN211328723 U CN 211328723U
- Authority
- CN
- China
- Prior art keywords
- liquid
- baffle
- outlet duct
- outlet
- folded plate
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- 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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- 239000007788 liquid Substances 0.000 title claims abstract description 52
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 2
- 229910052782 aluminium Inorganic materials 0.000 claims description 2
- 239000003595 mist Substances 0.000 description 3
- 239000000725 suspension Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 230000002745 absorbent Effects 0.000 description 1
- 239000002250 absorbent Substances 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 238000010977 unit operation Methods 0.000 description 1
Images
Landscapes
- Separating Particles In Gases By Inertia (AREA)
Abstract
The utility model relates to strip tower equipment field, concretely relates to strip tower export liquid return mechanism. Including the strip tower, strip tower exit end is fixed with the outlet duct rather than the intercommunication, is provided with throttling arrangement in the outlet duct, and the outlet duct internal fixation on throttling arrangement right side has the folded plate, two sides are buckled to strip tower exit end direction about the folded plate, and trompil and folded plate on the baffle of rightmost side correspond, are fixed with the fender liquid board on the outlet duct bottom plate on folded plate right side, have all seted up the liquid hole on the outlet duct bottom plate between two adjacent baffles and on the bottom plate between rightmost side baffle and the fender liquid board, and the outlet duct lower extreme is fixed with the collecting hopper with liquid hole intercommunication, and the collecting hopper lower extreme is fixed with the hose rather than inside intercommunication, hose and the. The utility model discloses, can effectually intercept the great liquid fog that floats in gas, the liquid fog condenses after being intercepted, and the liquid after condensing enters into the collecting hopper through the liquid hole, then returns to in the strip tower through the hose.
Description
Technical Field
The utility model relates to strip tower equipment field, concretely relates to strip tower export liquid return mechanism.
Background
Stripping is a unit operation used to recover absorbed solutes and to separate the absorbent from the solutes for regeneration. Meanwhile, in some cases, the stripping is also used for removing light components in liquid, such as the oil refining industry which uses steam as a stripping agent to remove the light components of oil varieties. Stripping can be used in conjunction with absorption or alone. The liquid fog of the great granule of the clamp matter often can be in the gas that current strip tower came out when atomizing, influences the subsequent order and uses, and the anti-liquid mechanism of current strip tower export influences its exhaust owing to set up too much filter equipment and makes the resistance of venthole great, influences its exhaust, uses inconveniently.
SUMMERY OF THE UTILITY MODEL
The utility model aims to solve the technical problem that effectively reduce the suspension in the gas, make the more even strip tower export of air humidity of output return liquid mechanism.
In order to realize the purpose, the utility model provides a technical scheme is:
stripper export liquid return mechanism, including the stripper, stripper exit end is fixed with the outlet duct rather than the intercommunication, is provided with throttling arrangement in the outlet duct, throttling arrangement includes and extends its fixed a plurality of baffles of length direction in the outlet duct, staggers on two adjacent baffles and is equipped with a plurality of trompils, and the trompil internal fixation has the filter screen, and the outlet duct on throttling arrangement right side is fixed with the folded plate, about the folded plate two sides buckle to stripper exit end direction, the trompil on the baffle of rightmost side corresponds with the folded plate, is fixed with the fender liquid board on the outlet duct bottom plate on folded plate right side, all seted up the liquid hole on the outlet duct bottom plate between two adjacent baffles and the outlet duct bottom plate between rightmost baffle and the fender liquid board, the outlet duct lower extreme is fixed with the collection hopper rather than the inside hose that communicates, hose and the inside intercommunication of stripper are fixed.
Specifically, a gap is arranged between the upper end and the lower end of the folded plate and the rightmost baffle.
Specifically, the upper end of the baffle penetrates through the top plate of the air outlet pipe.
Specifically, the front end and the rear end of the folded plate penetrate through the front side plate and the rear side plate of the air outlet pipe.
Specifically, the baffle plate and the folded plate are both aluminum plates.
Specifically, the included angle between the upper side and the lower side of the folded plate is 145 degrees.
Compared with the prior art, the beneficial effects of the utility model are that:
the utility model discloses, simple structure, convenient to use can effectually intercept the great liquid fog that floats in gas, condenses after the liquid fog is intercepted, and the liquid after condensing enters into the collecting hopper through the liquid hole, then returns to the strip tower in through the hose, can effectively reduce the suspension in the gas, makes the air humidity of output more even.
Drawings
Fig. 1 is a schematic structural diagram of the present invention.
Fig. 2 is a side view of the outlet duct.
Detailed Description
As shown in fig. 1-2, the liquid returning mechanism at the outlet of the stripping tower comprises a stripping tower 1, an outlet pipe 2 communicated with the stripping tower 1 is fixed at the outlet end of the stripping tower 1, a throttling device is arranged in the outlet pipe 2, the throttling device comprises a plurality of baffle plates 3 fixed in the length direction of the outlet pipe 2, the upper ends of the baffle plates 3 penetrate through a top plate of the outlet pipe 2, a plurality of openings 4 are alternately arranged on two adjacent baffle plates 3, a filter screen 5 is fixed in each opening 4, folded plates 6 are fixed in the outlet pipe 2 on the right side of the throttling device, the front ends and the rear ends of the folded plates 6 penetrate through front and rear side plates of the outlet pipe 2, the upper ends and the lower ends of the folded plates 6 are bent towards the outlet end of the stripping tower 1, an included angle between the upper side and the lower sides of the folded. Trompil 4 on the rightmost baffle 3 corresponds with folded plate 6, be fixed with on 2 bottom plates of outlet duct on folded plate 6 right side and keep off liquid board 7, all seted up liquid hole 8 on 2 bottom plates of outlet duct between two adjacent baffles 3 and 2 bottom plates of outlet duct between rightmost baffle 3 and the fender liquid board 7, 2 lower extremes of outlet duct are fixed with the collecting hopper 9 with liquid hole 8 intercommunication, collecting hopper 9 lower extreme is fixed with the hose 10 rather than inside intercommunication, hose 10 and strip 1 inside intercommunication of tower.
When the utility model is used, the gas containing a large amount of liquid fog enters the outlet pipe 2, because the outlet pipe 2 is internally fixed with a plurality of baffles 3, the openings 4 are alternately arranged on two adjacent baffles 3, the filter screen 5 is arranged in the opening 4, after the gas containing a large amount of liquid fog passes through the opening 4 on the front side baffle 3, part of the liquid fog is condensed on the filter screen 5 and the front side baffle 3 under the action of the filter screen 5 and the front side baffle 3, after the gas passing through the opening 4 collides on the baffle 3 at the rear side, the liquid fog in the gas can be condensed on the baffle 3 at the rear side, therefore, the contact area between the gas and the baffles 3 can be increased through the opening 4 alternately arranged on two adjacent baffles 3, the condensation efficiency of the liquid fog is increased, the discharge resistance of the gas is reduced, after the gas passes through the throttling device, the gas is blocked by the folded plate 6, the part of the liquid fog in the gas is condensed on the folded plate 6 again, the throttling effect of liquid mist in the gas is improved, the condensed liquid on the baffle 3 and the folded plate 6 enters the water collecting hopper 9 through the liquid hole 8, and the liquid entering the water collecting hopper 9 enters the stripping tower 1 again through the hose 10.
The upper end of the baffle 3 runs through the upper end of the air outlet pipe 2, the front side plate and the rear side plate of the air outlet pipe 2 run through the front end and the rear end of the folded plate 6, heat dissipation of the baffle 3 and the folded plate 6 can be accelerated, more liquid mist can be condensed on the baffle 3 and the folded plate 6, and further condensing efficiency of the liquid mist in the gas is improved.
The above description is only exemplary of the present invention and should not be taken as limiting the scope of the present invention, as any modifications, equivalents, improvements and the like made within the spirit and principles of the present invention are intended to be included within the scope of the present invention.
Claims (6)
1. Stripper export liquid return mechanism, including stripper (1), its characterized in that, stripper (1) exit end is fixed with outlet duct (2) rather than the intercommunication, is provided with throttling arrangement in outlet duct (2), throttling arrangement includes that outlet duct (2) are internal to extend its length direction fixed a plurality of baffle (3), staggers on two adjacent baffle (3) and is equipped with a plurality of trompils (4), and trompil (4) internal fixation have filter screen (5), and outlet duct (2) internal fixation on throttling arrangement right side has folded plate (6), both sides are buckled to stripper (1) outlet end direction about folded plate (6), and trompil (4) on the baffle (3) of rightmost side correspond with folded plate (6), are fixed with on outlet duct (2) bottom plate on folded plate (6) right side and are fixed with on baffle (7), and outlet duct (2) bottom plate between two adjacent baffle (3) and outlet duct (2) bottom plate between rightmost baffle (3) and baffle (7) have all seted up liquid hole (7) on the bottom plate (8) The lower end of the air outlet pipe (2) is fixedly provided with a liquid collecting hopper (9) communicated with the liquid hole (8), the lower end of the liquid collecting hopper (9) is fixedly provided with a hose (10) communicated with the inside of the liquid collecting hopper, and the hose (10) is communicated with the inside of the stripping tower (1).
2. The outlet liquid returning mechanism of the stripping tower according to claim 1, characterized in that a gap is arranged between the upper end and the lower end of the folded plate (6) and the rightmost baffle (3).
3. The outlet liquid returning mechanism of the stripping tower according to claim 1, characterized in that the upper end of the baffle (3) penetrates through the top plate of the gas outlet pipe (2).
4. The outlet liquid returning mechanism of the stripping tower according to claim 1, characterized in that the front end and the rear end of the folded plate (6) penetrate through the front side plate and the rear side plate of the outlet pipe (2).
5. The stripper column outlet liquid return mechanism according to claim 1, wherein the baffle (3) and the flap (6) are both made of aluminum plate.
6. The stripper column outlet liquid return mechanism of claim 1, wherein the included angle between the upper side and the lower side of the folded plate (6) is 145 degrees.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921761757.7U CN211328723U (en) | 2019-10-21 | 2019-10-21 | Stripper export liquid return mechanism |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921761757.7U CN211328723U (en) | 2019-10-21 | 2019-10-21 | Stripper export liquid return mechanism |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN211328723U true CN211328723U (en) | 2020-08-25 |
Family
ID=72093427
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201921761757.7U Active CN211328723U (en) | 2019-10-21 | 2019-10-21 | Stripper export liquid return mechanism |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN211328723U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115738342A (en) * | 2022-12-28 | 2023-03-07 | 扬州晨化新材料股份有限公司 | Catalytic distillation tower reactor for catalyst production |
-
2019
- 2019-10-21 CN CN201921761757.7U patent/CN211328723U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115738342A (en) * | 2022-12-28 | 2023-03-07 | 扬州晨化新材料股份有限公司 | Catalytic distillation tower reactor for catalyst production |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address | ||
| CP03 | Change of name, title or address |
Address after: 457000 the west section of Shengli Road, Puyang, Henan Province Patentee after: New Maiqi Materials Co.,Ltd. Country or region after: China Address before: 457000 the west section of Shengli Road, Puyang, Henan Province Patentee before: MYJ CHEMICAL CO.,LTD. Country or region before: China |