CN218742013U - Corrugated structured packing and packing area for gas-liquid exchange container - Google Patents
Corrugated structured packing and packing area for gas-liquid exchange container Download PDFInfo
- Publication number
- CN218742013U CN218742013U CN202223320252.1U CN202223320252U CN218742013U CN 218742013 U CN218742013 U CN 218742013U CN 202223320252 U CN202223320252 U CN 202223320252U CN 218742013 U CN218742013 U CN 218742013U
- Authority
- CN
- China
- Prior art keywords
- corrugated
- packing
- liquid
- guide groove
- liquid guide
- 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.)
- Active
Links
Images
Landscapes
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
The utility model relates to a ripple is regular to be packed, the ripple is regular to be packed includes: a corrugated plate of which an extending direction of a corrugated body is obliquely oriented at a corrugation inclination angle with respect to a height direction of the corrugated plate; the liquid guide groove, the liquid guide groove is designed to be suitable for guide liquid, the liquid guide groove is full the surface of buckled plate, every liquid guide groove on the buckled plate has the same extension trend, wherein, the extending direction of the main part of liquid guide groove for the extending direction of ripple main part becomes an contained angle, the width of liquid guide groove is less than the ripple width of buckled plate for can have the starting point of many liquid guide grooves in a ripple. The utility model discloses still relate to a filler district for gas-liquid exchange container, the filler district is superpose from top to bottom with crisscross orientation by the packing layer that the coincide of above-mentioned ripple regular packing formed.
Description
Technical Field
The utility model relates to a regular filler of ripple, especially a regular filler of ripple that is used for the gas-liquid of oil refining, petrochemical industry, chemical industry, light industry and environmental protection field, liquid-liquid contact mass transfer splitter. The utility model discloses still relate to a filler district for gas-liquid exchange container.
Background
The corrugated structured packing has the advantages of large flux, small resistance, high efficiency, convenient installation and the like, and is widely applied to the fields of oil refining, petrifaction, chemical industry, light industry and environmental protection. The angle of inclination of the corrugations of a typical corrugated structured packing to the horizontal is typically in the range of 45 to 60 degrees. The corrugated structured packing is vertically arranged, the wave crest directions of two adjacent sheets are arranged in opposite directions to leave a gap for liquid to flow downwards, and the corrugated structured packing of each layer stacked up and down are stacked at 90 degrees in a staggered manner.
Because the corrugation trend of the corrugated structured packing is not completely consistent with the flow direction of the fluid in the tower, when the fluid at the boundary of the packing enters the next layer of the stacked packing from one layer of the packing, the flow direction of the fluid is changed rapidly, the flow resistance of the gas is increased, and the processing capacity of the packing is reduced.
In addition, it is also desirable to increase the mass transfer efficiency of the filler, that is, to increase the specific surface area of the filler, to improve the wettability of the liquid on the surface of the filler, and to form an effective mass transfer liquid film.
To this end, the present applicant, in the invention patent application with application No. 201210367704.3, entitled "a composite corrugated structured packing with guide corrugations", filed on 28.9/2012, discloses a composite corrugated structured packing whose surface is machined with transverse and longitudinal small corrugations (the transverse small corrugations are not shown in the abstract drawing of the invention patent application or in fig. 1, but the longitudinal small corrugations are shown in a partial detail view circled by a dotted line, and the transverse and longitudinal small corrugations existing on the structured packing surface at the same time are shown in fig. 2 of the invention patent application), and is configured as a corrugated plate with oblique corrugations and edge guide corrugations. Wherein, the inclination angle between the oblique ripple and the horizontal direction is 45 degrees to 60 degrees, and the flow guide ripple is processed at the two sides of the ripple-shaped plate, the included angle between the flow guide ripple and the oblique ripple is 135 degrees to 175 degrees, and the section of the flow guide ripple is in a sine wave shape.
The technical scheme disclosed in the above patent application increases the specific surface area of the packing through the transverse and longitudinal small corrugations, and simultaneously reduces the flow resistance of the fluid between the packings by establishing continuous flow lines at the positions where one layer of the packing is transited to the other layer of the packing through the guide corrugations. However, the presence of the small transverse corrugations hinders the downward flow of liquid in the corrugations. Also, the guide corrugations of both sides of the corrugated plate and the corrugated body of the corrugated plate have different cross sections, which brings about processing complexity.
It is therefore desirable to provide a corrugated structured packing that not only achieves sufficient infiltration of the mass transfer fluid by increasing the specific surface area of the packing and improves the mass transfer efficiency, but also achieves convenient flow of the fluid between each layer of the installed corrugated structured packing in a structural form that facilitates simple processing.
Disclosure of Invention
In order to solve the technical problem, the utility model provides a regular packing of ripple, include: a corrugated plate of which an extending direction of a corrugated body is obliquely oriented at a corrugation inclination angle with respect to a height direction of the corrugated plate; the liquid guide groove, the liquid guide groove is designed to be suitable for guide liquid, the liquid guide groove is full the surface of buckled plate, every liquid guide groove on the buckled plate has the same extension trend, wherein, the extending direction of the main part of liquid guide groove for the extending direction of ripple main part becomes an contained angle, the width of liquid guide groove is less than the ripple width of buckled plate for can have the starting point of many liquid guide grooves in a ripple.
The arrangement of the liquid guide groove increases the specific surface area of the filler and increases the wetting degree of the surface of the filler. Since each liquid guiding groove on the corrugated plate has the same extension direction, the liquid is not blocked transversely but guided by the liquid guiding grooves to flow downwards along a specific direction, and the packing efficiency is improved. For packings, which are usually made of metal, the presence of the liquid-conducting channels further increases the strength of the corrugated plate of the packing.
Preferably, the corrugations smoothly transition from the extending direction of the corrugated body to the height direction of the corrugated plate from both ends of the height of the corrugated plate.
The present invention is directed to a corrugated plate in which a corrugated inclination angle formed by the extending direction of a corrugated main body of the corrugated plate with respect to the height direction of the corrugated plate smoothly transitions to zero in the vicinity of both high ends of the corrugated plate. Such a design helps to reduce the flow resistance at the edges of the packing in the case of a plurality of packings, allowing liquid to flow unimpeded from one packing to another. The liquid moves along the height direction of the corrugated plate when leaving the corrugation of the upper layer corrugated structured packing and entering the corrugation of the lower layer corrugated structured packing, and the corrugation can be processed to be smoothly transited to the vertical height direction from a certain corrugation inclination angle due to the absence of transverse small corrugations, and the smooth transition also reduces the flow resistance received by the fluid flowing in the corrugation.
According to an alternative embodiment of the corrugated structured packing according to the invention, the corrugations do not run smoothly into the vertical height direction, but remain extended at the corrugation angle at the high ends of the corrugated plate. In this case, the plurality of liquid guiding grooves provided in each corrugation play a main role in guiding the liquid when the liquid flows downwards.
According to an embodiment of the corrugated structured packing of the present invention, the liquid guiding groove is continuous in the length direction of the liquid guiding groove. Alternatively or additionally, the fluid channels may be discontinuous along their length. It is understood that it is possible to design one portion of the fluid sink to be continuous and another portion of the fluid sink to be intermittent without departing from the spirit of the invention. The continuous liquid guide groove structure is beneficial to guiding the fluid and improving the flow speed. The discontinuous liquid guide groove structure is more beneficial to the distribution of the liquid than the continuous liquid guide groove structure and can further increase the specific surface area of the filler.
According to the utility model discloses an implementation form of corrugated structured packing, the degree of depth of liquid guide groove does 0.1 to 30 times of corrugated plate thickness. Preferably, the depth of the liquid guide groove is 5 to 15 times of the thickness of the corrugated plate.
The liquid guide groove can be formed on the front surface and the back surface of the corrugated structured packing simultaneously by bending a corrugated blank of the corrugated structured packing as a metal piece in a stamping mode and the like. The liquid guide grooves can also be formed on only one surface of the corrugated structured packing in the modes of die casting, 3D printing and the like, or two liquid guide grooves with different arrangement, depth and direction can be formed on the front surface and the back surface of the corrugated structured packing.
According to the utility model discloses an implementation form of ripple regular packing, the extending direction of the ripple main part of buckled plate for the ripple inclination that the direction of height of buckled plate becomes is in the scope of 15 degrees to 75 degrees.
To according to the utility model discloses a regular packing of ripple, the extending direction of the main part of liquid guide groove for the contained angle that the extending direction of buckled plate main part becomes can be at 0 to 180 degrees within ranges optional. For example, it is entirely possible to select the direction of extension of the body of the liquid guide channel to be within the range of the angle between the height direction of the corrugated plate and the direction of extension of the body of the corrugated plate.
According to the utility model discloses an implementation form of corrugated structured packing, every the liquid guide groove is in one extend in the ripple. The liquid guide grooves have a narrower width than the corrugations, so that even if the liquid guide grooves and the corrugations are not completely consistent in trend and slightly inclined, each liquid guide groove does not extend out of the range of one corrugation.
According to the utility model discloses a corrugated structured packing's another embodiment, every the liquid guide groove is respectively in a plurality of extend in the ripple. This facilitates uniform distribution of the liquid across the entire cross-section of the corrugated structured packing as it moves downward, making full use of the individual corrugations of each corrugated structured packing.
According to the utility model discloses a regular packing's of ripple preferred embodiment form, regular packing of ripple still has a plurality of apertures that run through just, reverse surface to make the enrichment can flow the opposite side of the regular packing of ripple through the aperture in the liquid of the regular packing one side of ripple, thereby be favorable to the evenly distributed of liquid and the homogeneous mixing of gas-liquid.
According to the utility model discloses a further aspect still provides a filler district for gas-liquid exchange container, the filler district is formed by the superpose from top to bottom of a plurality of packing layers, the packing layer is formed by the face-to-face coincide of the above-mentioned corrugated regular packing of a plurality of mutual parallels erects, wherein, every adjacent corrugated regular packing has opposite direction's ripple inclination alpha in the packing layer, therefore separates out the space that allows the liquid to flow through between adjacent corrugated regular packing, and corrugated regular packing in the upper and lower adjacent packing layer then has crisscross orientation, and this is favorable to the stability of structure and keeps the unblocked of liquid way.
Drawings
The present invention will be explained in detail with reference to the accompanying drawings. In the drawings:
FIG. 1 schematically illustrates a front view of one embodiment of a corrugated structured packing in accordance with the present invention;
FIG. 2 schematically illustrates a front view of another embodiment of a corrugated structured packing in accordance with the present invention;
FIG. 3 schematically illustratesbase:Sub>A cross-sectional view along A-A of the corrugated structured packing shown in FIGS. 1 and 2;
FIG. 4 schematically illustrates a partial perspective view of one embodiment of a corrugated structured packing in accordance with the present invention;
FIG. 5 schematically illustrates a partial perspective view of another embodiment of a corrugated structured packing in accordance with the present invention;
FIG. 6 schematically illustrates a partial perspective view of yet another embodiment of a corrugated structured packing in accordance with the present invention;
FIG. 7 schematically illustrates a blank having a liquid directing groove machined but not yet corrugated, according to an embodiment of the present invention;
FIG. 8 schematically illustrates a blank according to another embodiment of the present invention in which the fluid directing channels have a different orientation than the fluid directing channels shown in FIG. 7.
Detailed Description
The following further describes the embodiments of the present invention with reference to the drawings. In the drawings, identical reference numbers indicate identical or functionally similar features.
FIG. 1 schematically shows a front view of a corrugated structured packing according to an embodiment of the present invention. The corrugated regular packing comprises corrugated plates and liquid guide grooves distributed on the surfaces of the corrugated plates. The extending direction of the corrugated plate's corrugated bodies is oriented obliquely with respect to the height direction of the corrugated plate. The corrugated body has a corrugation pitch angle alpha and smoothly transitions to the corrugation height direction, i.e. the vertical direction in the figure, towards both height ends of the corrugated plate. The liquid guiding grooves are distributed over the surface of the corrugated plate, and only a part of the liquid guiding grooves is exemplarily shown in fig. 1 to illustrate the position relationship between the liquid guiding grooves and the corrugations. It will be appreciated that each channel of the corrugated plate has the same extent and that once the liquid enters the channels it is directed in a uniform direction. As shown in FIG. 1, the width of the liquid guiding groove is significantly smaller than the corrugation width of the corrugated plate, so that there can be a plurality of starting points of the liquid guiding groove in one corrugation.
FIG. 2 schematically shows a front view of another embodiment of a corrugated structured packing according to the present invention. The difference with the embodiment of fig. 1 is that the corrugations in fig. 2 do not smoothly transition into the corrugation height direction of the corrugated sheet at both ends of the height, but extend at the same corrugation angle as the corrugated body. Furthermore, the channels in fig. 2 are also angled differently with respect to the corrugations. It will be understood, however, that the angle between the channels and the corrugations is not strictly dependent on whether the corrugations smoothly transition into the direction of the height of the corrugations at both ends of the height, and it is obvious that they may be designed and combined differently in other embodiments not shown.
FIG. 3 schematically showsbase:Sub>A cross-sectional view along the line A-A of the corrugated structured packing of FIGS. 1 and 2, in which the corrugations are seen inbase:Sub>A zigzag pattern and the channels are seen inbase:Sub>A concave-convex pattern distributed over the surfaces of the corrugations. Of course, in a cross-sectional view in this direction, the angular relationship between the corrugations and the channels and the orientation of the corrugations and the channels in the direction of extension are not shown.
Fig. 4 to 6 show schematically in partial perspective views different embodiments of the corrugated structured packing according to the invention. The channels may extend in unison with the corrugation orientation (fig. 4) or may extend within the corrugation but at an alternating angle to the corrugation (fig. 5). When the channels have a larger angle to the corrugations, the channels extend across a plurality of corrugations (fig. 6). In fig. 6, the angle β between the direction of extension of the flow channels and the direction of extension of the corrugated body is particularly clearly shown.
Fig. 7 and 8 schematically show processing blanks of different embodiments of corrugated structured packings according to the invention, wherein the liquid guide channel has been processed but no corrugations have yet been processed. The fluid sink in FIG. 8 has a different orientation than the fluid sink shown in FIG. 7.
In use, a plurality of corrugated structured packings standing parallel to each other are stacked face to form a packing tray (or block), wherein the corrugated inclination angles α of adjacent corrugated structured packings are opposite (i.e., symmetrical with respect to the height direction of the corrugated plates). Multiple layers of packing trays formed in this way are stacked up and down, and two adjacent layers of packing trays (or packing blocks) are stacked up and down in a staggered manner (namely corrugated structured packing is crossed due to different orientations). It is also possible to punch a plurality of small holes through the front and back surfaces of the corrugated structured packing to increase the fluid passage and mixing capacity.
The foregoing describes preferred embodiments of the present invention, but the spirit and scope of the present invention is not limited to the specific disclosure herein. Those skilled in the art can freely combine and expand the above embodiments in accordance with the teachings of the present invention to make further embodiments and applications within the spirit and scope of the present invention. The spirit and scope of the present invention are not to be limited by the specific embodiments but by the appended claims.
List of reference numerals
10. Corrugated plate
Angle of inclination of alpha corrugation
20. Liquid guide groove
Angle of beta
Claims (10)
1. A corrugated structured packing, comprising:
a corrugated plate of which an extending direction of a corrugated body is obliquely oriented at a corrugation inclination angle with respect to a height direction of the corrugated plate;
the liquid guide groove, the liquid guide groove is designed to be suitable for guide liquid, the liquid guide groove is full the surface of buckled plate, every liquid guide groove on the buckled plate has the same extension trend, wherein, the extending direction of the main part of liquid guide groove for the extending direction of ripple main part becomes an contained angle, the width of liquid guide groove is less than the ripple width of buckled plate for can have the starting point of many liquid guide grooves in a ripple.
2. The corrugated structured packing of claim 1, wherein the corrugations smoothly transition from the direction of elongation of the corrugated body to the direction of the height of the corrugations of the corrugated sheets at both ends of the height of the corrugated sheets.
3. The corrugated structured packing of claim 1 or 2, wherein the fluid directing channel is discontinuous along its length.
4. The corrugated structured packing of claim 1 or 2, wherein the depth of the liquid directing groove is 0.1 to 30 times the thickness of the corrugated sheet.
5. The corrugated structured packing of claim 1 or 2, wherein the inclination angle of the corrugations of the extending direction of the corrugated plate's corrugated bodies with respect to the height direction of the corrugated plate is in the range of 15 degrees to 75 degrees.
6. The corrugated structured packing of claim 1 or 2, wherein the extending direction of the body of the liquid guiding groove forms an included angle in the range of 0 to 180 degrees with respect to the extending direction of the corrugated body.
7. The corrugated structured packing of claim 1 or 2, wherein each of the channels extends within one of the corrugations.
8. The corrugated structured packing of claim 1 or 2, wherein each of the channels extends within a respective plurality of the corrugations.
9. The corrugated structured packing of claim 1 or 2, wherein the corrugated structured packing further has a plurality of small holes through the front and back surfaces.
10. A packing region for a gas-liquid exchange container, wherein the packing region is formed by stacking a plurality of packing layers one on top of the other, the packing layers being formed by stacking a plurality of corrugated structured packings as defined in any one of claims 1 to 9 standing in parallel with each other in a face-to-face relationship, wherein adjacent corrugated structured packings in each of the packing layers have corrugated inclination angles α in opposite directions, and the corrugated structured packings in the adjacent packing layers have staggered orientations.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202223320252.1U CN218742013U (en) | 2022-12-09 | 2022-12-09 | Corrugated structured packing and packing area for gas-liquid exchange container |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202223320252.1U CN218742013U (en) | 2022-12-09 | 2022-12-09 | Corrugated structured packing and packing area for gas-liquid exchange container |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN218742013U true CN218742013U (en) | 2023-03-28 |
Family
ID=85681314
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202223320252.1U Active CN218742013U (en) | 2022-12-09 | 2022-12-09 | Corrugated structured packing and packing area for gas-liquid exchange container |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN218742013U (en) |
-
2022
- 2022-12-09 CN CN202223320252.1U patent/CN218742013U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4604247A (en) | Tower packing material and method | |
| US4597916A (en) | Method of and apparatus for intermediate lamella vapor liquid contact | |
| EP0130745B1 (en) | Expanded metal packing and method of manufacture | |
| CN101162132B (en) | Plate heat exchanger | |
| JP5940285B2 (en) | Heat exchanger | |
| RU2153933C2 (en) | Metal member with cellular structural | |
| CN1284958C (en) | Heat exchanger with brazed plates | |
| EP2728292A1 (en) | Heat transfer plate and plate heat exchanger comprising such a heat transfer plate | |
| EP0807462A1 (en) | Structured packing element with bi-directional surface texture and a mass and heat transfer process using such packing element | |
| US11118848B2 (en) | Heat-exchanging plate, and plate heat exchanger using same | |
| GB2362456A (en) | Heat exchange fin | |
| JP2012112645A (en) | Heat exchanger | |
| EP3115731A1 (en) | Heat exchange plate used for plate-type heat exchanger and plate-type heat exchanger provided with the heat exchange plate | |
| US11175097B2 (en) | Packing for heat and/or mass transfer | |
| US4593756A (en) | Fin-and-tube type heat exchanger | |
| CN104110996A (en) | Mixed type fin for plate-fin heat exchanger | |
| US6942024B2 (en) | Corrugated heat exchange element | |
| CN218742013U (en) | Corrugated structured packing and packing area for gas-liquid exchange container | |
| JP2004125388A (en) | Fin for plate heat exchanger, manufacturing method for fin, and plate heat exchanger with fin | |
| JP4462653B2 (en) | Plate heat exchanger | |
| CN115945159A (en) | Corrugated structured packing and packing area for gas-liquid exchange container | |
| CN211451981U (en) | Plate heat exchanger | |
| WO2019234756A1 (en) | A plate of plate heat exchangers | |
| JP2670512B2 (en) | Heat transfer element plate stack | |
| EP4141372A2 (en) | A plate of plate heat exchangers |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |