CN204543610U - Vortex filament shape is from uniform regular packed tower - Google Patents
Vortex filament shape is from uniform regular packed tower Download PDFInfo
- Publication number
- CN204543610U CN204543610U CN201520103073.3U CN201520103073U CN204543610U CN 204543610 U CN204543610 U CN 204543610U CN 201520103073 U CN201520103073 U CN 201520103073U CN 204543610 U CN204543610 U CN 204543610U
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- China
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- dish
- vortex filament
- filament shape
- packing
- stacked corrugated
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Abstract
A kind of vortex filament shape is from uniform regular packed tower, it combines primarily of stacked corrugated regular filler dish and vortex filament shape structured packing dish, described multiple stacked corrugated regular filler dish forms the stacked corrugated regular filler bed of multistage, is inserted with the vortex filament shape structured packing bed that at least one deck is made up of vortex filament shape structured packing dish between every two sections or between one section of stacked corrugated regular filler bed; Described stacked corrugated regular filler dish adopts the packing sheet of different size chord length to be oppositely formed by stacking by ripple direction, and is formed with left and right two to runner; Described vortex filament shape structured packing dish is processed by vortex filament rotation mode by packing sheet, forms the rotary runner spread to the center of circle from packing box edge; It has rational in infrastructure, easy to process, effectively can realize the even of liquid in regular packed tower and distribute, reduce the use of distributor in tower, filler mass transfer area is effectively utilized, improve the features such as filler mass-transfer efficiency.
Description
Technical field
The utility model relates to and a kind ofly realize liquid in packed tower effectively from uniform thus reduce the vortex filament shape that relies on liquid distribution trough from uniform regular packed tower, belong to technical field of rectification.
Background technology
In rectifying industry, regular packed tower relies on its performance advantage and is used widely, but along with the maximization of tower equipment, common structured packing in large stuffing tower from uniform limited ability, wall stream effect equal distribution uneven phenomenon is obvious, liquid distribution trough must be relied on to improve this situation, thus ensure the separative efficiency of filler.In packed tower, the excessive use of distributor then can cause tower body too high, and cost of equipment and cost of labor all can increase.
Utility model content
The purpose of this utility model is the deficiency overcoming prior art existence, there is provided a kind of vortex filament shape of improvement from uniform regular packed tower, thus realize liquid being uniformly distributed in packing layer in packed tower, while it can improve filler mass-transfer efficiency, reduce the use of liquid distribution trough, thus tower height can be reduced, the holistic cost of control appliance.
The purpose of this utility model has been come by following technical solution, a kind of vortex filament shape is from uniform regular packed tower, it combines primarily of stacked corrugated regular filler dish and vortex filament shape structured packing dish, described multiple stacked corrugated regular filler dish forms the stacked corrugated regular filler bed of multistage, is inserted with the vortex filament shape structured packing bed that at least one deck is made up of vortex filament shape structured packing dish between every two sections or between one section of stacked corrugated regular filler bed.Described stacked corrugated regular filler dish, as the main body medium of gas-liquid mass transfer in tower, ensures the separating property of packed tower; Described vortex filament shape structured packing dish replaces the function of distributor in traditional regular packed tower, carries out evenly distributing to the liquid flowed down in the filler of upper strata again, to realize being uniformly distributed of liquid in whole tower.
Described stacked corrugated regular filler dish adopts the packing sheet of different size chord length to be oppositely formed by stacking by ripple direction, and is formed with left and right two to runner; Described vortex filament shape structured packing dish is processed by vortex filament rotation mode by packing sheet, forms the rotary runner spread to the center of circle from packing box edge;
In described vortex filament shape structured packing dish, packing sheet adopts vortex filament shape combination, packing sheet contrary for ripple direction is processed into packing box by vortex filament rotation mode, forms the rotary runner spread to the center of circle from packing box edge.The runner of this version makes the liquid in packing box realize annularly flow along each layer packing sheet, along the circumferential direction ecto-entad realizes the uniform of liquid in whole packing box, thus serves the effect distributed again to the liquid of the skewness flowed down in the packing layer of upper strata.Repeatedly evenly distributing again of liquid in whole packed tower can be realized by the use of polydisc vortex filament shape structured packing dish.
The utility model compared with prior art, has rational in infrastructure, easy to process, effectively can realize the even of liquid in regular packed tower and distribute, reduce the use of distributor in tower, filler mass transfer area is effectively utilized, improve the features such as filler mass-transfer efficiency.
Accompanying drawing explanation
Fig. 1 is sectional structure schematic diagram of the present utility model.
Fig. 2 is the schematic appearance of stacked corrugated regular filler dish described in the utility model.
Fig. 3 is the one-tenth dish top view of stacked corrugated regular filler dish described in the utility model.
Fig. 4 is the schematic appearance of vortex filament shape structured packing dish described in the utility model.
Fig. 5 is the one-tenth dish top view of vortex filament shape structured packing dish described in the utility model.
Detailed description of the invention
Below in conjunction with accompanying drawing, detailed introduction is done to the utility model: shown in Fig. 1, a kind of vortex filament shape described in the utility model is from uniform regular packed tower, it combines primarily of stacked corrugated regular filler dish 11,13 and vortex filament shape structured packing dish 12, described multiple stacked corrugated regular filler dish forms the stacked corrugated regular filler bed of multistage, is inserted with the vortex filament shape structured packing bed that at least one deck is made up of vortex filament shape structured packing dish between every two sections or between one section of stacked corrugated regular filler bed.
Shown in figure, described stacked corrugated regular filler dish adopts the packing sheet of different size chord length to be oppositely formed by stacking by ripple direction, and is formed with left and right two to runner; Described vortex filament shape structured packing dish is processed by vortex filament rotation mode by packing sheet, forms the rotary runner spread to the center of circle from packing box edge.
Embodiment: described in the utility modelly to be combined by stacked corrugated regular filler dish and vortex filament shape structured packing dish from uniform regular packed tower, a dish vortex filament shape structured packing dish is put into every one section of stacked corrugated regular filler bed during installation, as shown in Figure 1, described vortex filament shape structured packing dish 12 is between stacked corrugated regular filler layer 11 and 13.
As shown in Figure 2 and Figure 3, described stacked corrugated regular filler dish adopts the packing sheet of different size chord length to be oppositely formed by stacking by ripple direction, formed left and right two to runner, become the main body medium of gas-liquid distribution in tower.
As shown in Figure 4, Figure 5, described vortex filament shape structured packing dish is processed by vortex filament rotation mode by packing sheet 41 and 42, forms the rotary runner spread to the center of circle from packing box edge.The runner of this version makes the liquid in packing box realize annularly flow along each layer packing sheet, ecto-entad realizes the uniform of liquid in whole packing box, thus serves and carry out to the liquid of the skewness flowed down in the packing layer of upper strata the effect that evenly distributes again.Repeatedly evenly distributing again of liquid in whole packed tower can be realized by the use of polydisc vortex filament shape structured packing dish.
Claims (2)
1. a vortex filament shape is from uniform regular packed tower, it combines primarily of stacked corrugated regular filler dish and vortex filament shape structured packing dish, it is characterized in that described multiple stacked corrugated regular filler dish forms the stacked corrugated regular filler bed of multistage, between every two sections or between one section of stacked corrugated regular filler bed, be inserted with the vortex filament shape structured packing bed that at least one deck is made up of vortex filament shape structured packing dish.
2. vortex filament shape according to claim 1 is from uniform regular packed tower, it is characterized in that described stacked corrugated regular filler dish adopts the packing sheet of different size chord length to be oppositely formed by stacking by ripple direction, and is formed with left and right two to runner; Described vortex filament shape structured packing dish is processed by vortex filament rotation mode by packing sheet, forms the rotary runner spread to the center of circle from packing box edge.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520103073.3U CN204543610U (en) | 2015-02-13 | 2015-02-13 | Vortex filament shape is from uniform regular packed tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520103073.3U CN204543610U (en) | 2015-02-13 | 2015-02-13 | Vortex filament shape is from uniform regular packed tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204543610U true CN204543610U (en) | 2015-08-12 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520103073.3U Withdrawn - After Issue CN204543610U (en) | 2015-02-13 | 2015-02-13 | Vortex filament shape is from uniform regular packed tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204543610U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104689589A (en) * | 2015-02-13 | 2015-06-10 | 杭州杭氧填料有限公司 | Vortex-line self-homogenizing regulation packing tower |
| CN107224949A (en) * | 2017-05-19 | 2017-10-03 | 四川大学 | The method that a kind of super gravity field microreactor and liquid-phase precipitation method prepare nano material |
| CN107670470A (en) * | 2017-11-20 | 2018-02-09 | 宣城市楷昂化工有限公司 | A kind of new packing absorption tower |
| CN108147941A (en) * | 2017-12-22 | 2018-06-12 | 石家庄鼎盈化工股份有限公司 | Liquefied gas component separation of alkane and olefin system and separation method |
-
2015
- 2015-02-13 CN CN201520103073.3U patent/CN204543610U/en not_active Withdrawn - After Issue
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104689589A (en) * | 2015-02-13 | 2015-06-10 | 杭州杭氧填料有限公司 | Vortex-line self-homogenizing regulation packing tower |
| CN107224949A (en) * | 2017-05-19 | 2017-10-03 | 四川大学 | The method that a kind of super gravity field microreactor and liquid-phase precipitation method prepare nano material |
| CN107224949B (en) * | 2017-05-19 | 2023-02-14 | 四川大学 | Method for preparing nano material by using high-gravity field microreactor and liquid-phase precipitation method |
| CN107670470A (en) * | 2017-11-20 | 2018-02-09 | 宣城市楷昂化工有限公司 | A kind of new packing absorption tower |
| CN108147941A (en) * | 2017-12-22 | 2018-06-12 | 石家庄鼎盈化工股份有限公司 | Liquefied gas component separation of alkane and olefin system and separation method |
| CN108147941B (en) * | 2017-12-22 | 2020-09-08 | 石家庄鼎盈化工股份有限公司 | Liquefied gas component alkane and alkene separation system and separation method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20150812 Effective date of abandoning: 20160504 |
|
| C25 | Abandonment of patent right or utility model to avoid double patenting |