CN104689589A - Vortex-line self-homogenizing regulation packing tower - Google Patents
Vortex-line self-homogenizing regulation packing tower Download PDFInfo
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- CN104689589A CN104689589A CN201510075850.2A CN201510075850A CN104689589A CN 104689589 A CN104689589 A CN 104689589A CN 201510075850 A CN201510075850 A CN 201510075850A CN 104689589 A CN104689589 A CN 104689589A
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- packing
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- vortex filament
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Abstract
The invention relates to a vortex-line self-homogenizing regulation packing tower. The vortex-line self-homogenizing regulation packing tower mainly consists of a plurality of laminate-type corrugated regulation packing trays and a vortex-line regulation packing tray, the plurality of laminate-type corrugated regulation packing trays form a plurality of sections of laminate-type corrugated regulation packing bed layers, and at least one vortex-line regulation packing bed layer formed by the vortex-line regulation packing tray is inserted between every two adjacent sections or every two separated sections of laminate-type corrugated regulation packing bed layers; each laminate-type corrugated regulation packing tray is formed by laminating packing sheets in different chord lengths in the direction opposite to the corrugated direction and is provided with a left passageway and a right passageway; the vortex-line regulation packing tray is formed in a rotation way of the vortex line and forms a rotating passageway which is scattered from the edge of the packing tray to the center. The vortex-line self-homogenizing regulation packing tower has characteristics that the structure is reasonable, the machining is convenient, the uniformity in redistribution of liquid in the regulation packing tower can be effectively realized, the use of distributors in the packing tower can be reduced, the packing transfer area can be effectively utilized, and the packing transfer efficiency can be improved.
Description
Technical field
What the present invention relates to is 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, belongs 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.
Summary of the invention
The object of the invention is to 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 object of the invention is to have 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 present invention 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 invention.
Fig. 2 is the schematic appearance of stacked corrugated regular filler dish of the present invention.
Fig. 3 is the one-tenth dish top view of stacked corrugated regular filler dish of the present invention.
Fig. 4 is the schematic appearance of vortex filament shape structured packing dish of the present invention.
Fig. 5 is the one-tenth dish top view of vortex filament shape structured packing dish of the present invention.
Detailed description of the invention
Below in conjunction with accompanying drawing, detailed introduction is done to the present invention: shown in Fig. 1, a kind of vortex filament shape of the present invention 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: of the present inventionly 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 |
|---|---|---|---|
| CN201510075850.2A CN104689589B (en) | 2015-02-13 | 2015-02-13 | A kind of vortex filament shape is from uniform regular packed tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510075850.2A CN104689589B (en) | 2015-02-13 | 2015-02-13 | A kind of vortex filament shape is from uniform regular packed tower |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN104689589A true CN104689589A (en) | 2015-06-10 |
| CN104689589B CN104689589B (en) | 2016-05-04 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201510075850.2A Active CN104689589B (en) | 2015-02-13 | 2015-02-13 | A kind of vortex filament shape is from uniform regular packed tower |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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 |
| CN108686614A (en) * | 2018-08-15 | 2018-10-23 | 重庆山巨化工机械股份有限公司 | High efficient gas and liquid reactor |
| CN111714915A (en) * | 2020-05-28 | 2020-09-29 | 杭州杭氧填料有限公司 | Mixed mass transfer interfacial type experimental-stage rectifying tower |
Citations (6)
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| CN2724823Y (en) * | 2004-06-21 | 2005-09-14 | 成建 | Grid type normalized packing used for tower and container |
| CN1772369A (en) * | 2005-04-01 | 2006-05-17 | 北京英诺威逊聚合技术有限公司 | Netted regular packing |
| CN101104140A (en) * | 2007-08-03 | 2008-01-16 | 褚雅安 | Tower bubbling stuffing with vortex-flow and defrosting function |
| CN201179446Y (en) * | 2007-10-23 | 2009-01-14 | 赵伟 | Ladder triangle regular packing |
| CN201257386Y (en) * | 2008-08-25 | 2009-06-17 | 吴佳栋 | Calendering hole ripple fillings |
| CN204543610U (en) * | 2015-02-13 | 2015-08-12 | 杭州杭氧填料有限公司 | Vortex filament shape is from uniform regular packed tower |
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2015
- 2015-02-13 CN CN201510075850.2A patent/CN104689589B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2724823Y (en) * | 2004-06-21 | 2005-09-14 | 成建 | Grid type normalized packing used for tower and container |
| CN1772369A (en) * | 2005-04-01 | 2006-05-17 | 北京英诺威逊聚合技术有限公司 | Netted regular packing |
| CN101104140A (en) * | 2007-08-03 | 2008-01-16 | 褚雅安 | Tower bubbling stuffing with vortex-flow and defrosting function |
| CN201179446Y (en) * | 2007-10-23 | 2009-01-14 | 赵伟 | Ladder triangle regular packing |
| CN201257386Y (en) * | 2008-08-25 | 2009-06-17 | 吴佳栋 | Calendering hole ripple fillings |
| CN204543610U (en) * | 2015-02-13 | 2015-08-12 | 杭州杭氧填料有限公司 | Vortex filament shape is from uniform regular packed tower |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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 |
| CN108686614A (en) * | 2018-08-15 | 2018-10-23 | 重庆山巨化工机械股份有限公司 | High efficient gas and liquid reactor |
| CN111714915A (en) * | 2020-05-28 | 2020-09-29 | 杭州杭氧填料有限公司 | Mixed mass transfer interfacial type experimental-stage rectifying tower |
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| Publication number | Publication date |
|---|---|
| CN104689589B (en) | 2016-05-04 |
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Address after: 799 Xiangfu Road, Qingshanhu street, Lin'an District, Hangzhou City, Zhejiang Province Patentee after: HANGZHOU HANGYANG PACKINGS Co.,Ltd. Address before: 311305 No.99, East Ring Road, Qingshanhu street, Lin'an City, Hangzhou City, Zhejiang Province Patentee before: HANGZHOU HANGYANG PACKINGS Co.,Ltd. |