CN211025194U - Rectifying and separating tower - Google Patents
Rectifying and separating tower Download PDFInfo
- Publication number
- CN211025194U CN211025194U CN201921842458.6U CN201921842458U CN211025194U CN 211025194 U CN211025194 U CN 211025194U CN 201921842458 U CN201921842458 U CN 201921842458U CN 211025194 U CN211025194 U CN 211025194U
- Authority
- CN
- China
- Prior art keywords
- plate
- tower
- column plate
- subdivision
- fine
- 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.)
- Expired - Fee Related
Links
Images
Landscapes
- Separation By Low-Temperature Treatments (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a rectification separation tower is equipped with the subdivision board just directly over every column plate the subdivision board with but column plate edge split is connected, subdivision board middle zone with be equipped with the clearance between the column plate, be equipped with the subdivision hole on the subdivision board, subdivision hole aperture is less than through-flow hole aperture on the column plate. The utility model discloses utilize to add on the column plate and divide the board to make the bubble that overflows on the column plate break into littleer bubble, improved gas-liquid heat exchange efficiency, utilize the subplate that divides the board as the column plate to improve the veneer efficiency of column plate and the full column plate efficiency of whole rectification separation tower simultaneously.
Description
Technical Field
The utility model relates to a chemical production equipment technical field. In particular to a rectification separation tower.
Background
The plate-type rectifying-separating tower consists of cylindrical tower body and several horizontally arranged tower plates in the tower. The single tower plate efficiency is the first problem to be considered by people in designing a plate type rectifying and separating tower and the first problem to be solved by the plate type rectifying and separating tower, and therefore, a bubble cap tower, a sieve plate tower, a float valve tower, a tongue-shaped plate tower and the like are designed by people. However, the plate efficiency of the prior plate rectifying tower is obviously reduced when the liquid layer is thinner, and the heat exchange efficiency of the ascending air flow and the liquid layer on the plate is still lower.
SUMMERY OF THE UTILITY MODEL
Therefore, the technical problem to be solved by the utility model is to provide a rectification separating tower utilizes to add on the column plate and divides the board to make the bubble that overflows from the column plate break into littleer bubble, has improved gas-liquid heat exchange efficiency, utilizes the subplate that divides the board as the column plate to improve the veneer efficiency of column plate and the full column plate efficiency of whole rectification separating tower simultaneously.
In order to solve the technical problem, the utility model provides a following technical scheme:
The rectifying and separating tower is characterized in that a fine separation plate is arranged right above each tower plate and detachably connected with the edge of each tower plate, a gap is arranged between the middle area of each fine separation plate and each tower plate, fine separation holes are formed in each fine separation plate, and the aperture of each fine separation hole is smaller than that of a through hole in each tower plate.
In the rectification separation tower, the through-flow hole is a tapered hole with the aperture gradually decreasing from bottom to top in the thickness direction of the tower plate, and the aperture of the subdivided hole is smaller than that of the reducing end of the through-flow hole.
in the rectification separation tower, the included angle α between the wall of the through-flow hole and the central axis of the through-flow hole is 5-20 degrees.
In the above rectification separation column, the fine separation plate is a spherical plate.
In the rectification separation tower, one side of the fine separation plate adjacent to the downcomer is detachably connected with the side wall of the overflow weir.
In the rectification separation tower, the gas escape port is defined by one side of the fine separation plate adjacent to the liquid receiving disc and the tower plate.
The technical scheme of the utility model following profitable technological effect has been obtained:
1. The subdivision plate is additionally arranged above the tower plate, so that the air pressure of bubbles in liquid between the tower plate and the subdivision plate can be improved, the bubble escape speed is delayed, the gas-liquid mixing time is prolonged, and the efficiency of a single tower plate is improved.
2. The through-flow holes in the tower plate are designed into the tapered holes, so that the through-flow holes can be cleaned conveniently, and the probability of blockage of the through-flow holes can be reduced.
Drawings
Fig. 1 is a schematic structural view of an easy-to-clean buchner funnel of the present invention;
FIG. 2 is a schematic structural diagram of a column plate of the rectification separation column of the present invention;
FIG. 3 is a schematic structural diagram of a subdivision plate of the rectification separation tower of the present invention;
Fig. 4 is an oblique two-axis diagram of the subdivision plate (not shown) of the rectification separation tower of the present invention.
In the figure, 1-tower body; 2-a downcomer; 3-liquid receiving disc; 4-column plate; 5-fine dividing plate; 6-air outlet pipe; 7-a return pipe; 8-feeding pipe; 9-an air inlet pipe; 10-a discharge pipe; 11-a through-flow aperture; 12-subdivide the pores.
Detailed Description
as shown in fig. 1 and 2, the utility model discloses rectification knockout tower is equipped with subdivision board 5 just directly over every column plate 4 subdivision board 5 with but 4 edge of column plate detachable connections, subdivision board 5 middle zone with be equipped with the clearance between the column plate 4, be equipped with subdivision hole 12 on the subdivision board 5, subdivision hole 12 aperture is less than 11 apertures of discharge orifice on the column plate 4, wherein, discharge orifice 11 is the aperture and is in by the last bell mouth that diminishes gradually down in 4 thickness directions of column plate, 11 apertures of discharge orifice with contained angle α between 11 centraxonial in the discharge orifice is 15, subdivision hole 12 apertures is less than 11 throat end apertures in the discharge orifice.
In this embodiment, as shown in fig. 3 and 4, the fine dividing plate 5 is a spherical plate, and one side of the fine dividing plate 5 adjacent to the downcomer 2 is detachably connected to the sidewall of the overflow weir, and one side of the fine dividing plate 5 adjacent to the receiving tray 3 and the tray 4 form an air escape opening. The spherical panels are used as the subdivision plates 5, the tower plate 4 can be partitioned according to different bubble escape speeds, so that bubbles between the tower plate 4 and the subdivision plates 5 far away from the central area of the tower plate 4 can quickly escape to the upper part of the subdivision plates 5 through the subdivision holes 12, meanwhile, the speed of the bubbles between the tower plate 4 and the subdivision plates 5 in the central area of the tower plate 4 escaping upwards through the subdivision holes 12 is favorably delayed, the gas-liquid contact time is prolonged, the amount of mist is reduced, and the efficiency of a single tower plate is improved.
In actual production, a material to be rectified and separated is added into the tower body 1 through the feeding pipe 8, then high-temperature gas for heating is input into the tower body 1 through the air inlet pipe 9, after the material to be rectified and separated is heated by the high-temperature gas, substances with lower boiling points in the material to be rectified and separated are converted into gaseous states and ascend along the tower body 1, and when steam formed by the substances with lower boiling points meets the tower plate 4 with lower temperature, the steam is condensed into liquid drops. When the temperature in the whole tower body 1 rises to the normal working temperature (namely the temperature required by the materials to be separated in the materials to be rectified and separated can be obtained), the fraction enters the condenser through the air outlet pipe 6 and is condensed into a product, and a part of the product flows back into the tower body 1 through the return pipe 7. And the material with higher boiling point in the material to be rectified and separated is discharged out of the tower body 1 through the discharge pipe 10, wherein a part of the material with higher boiling point flows into the reboiler to be heated to form high-temperature gas, and then the high-temperature gas enters the tower body 1 through the gas inlet pipe 9 to be heated to the material to be rectified and separated.
In the rectification separation process, when the air flow through the through-flow hole 11 through the tray 4 is large, a part of the gas will be discharged out of the space enclosed by the fine-dividing plate 5 and the tray 4 through the air escape opening, while the rest of the gas will escape upwards through the fine-dividing hole 12, and when the air flow through the tray 4 through the through-flow hole 11 is small, the liquid overflowing from the liquid receiving tray 3 will block the bubbles in the space enclosed by the fine-dividing plate 5 and the tray 4. When the liquid amount on the tower plate 4 is less, the fine-dividing plate 5 can break bubbles in the mist, which is beneficial to gas-liquid heat exchange and gas heat transfer to the liquid on the upper layer of the tower plate 4.
Moreover, the through-flow holes 11 are tapered holes, so that the restriction of the ascending gas flow is facilitated, the pressurization is facilitated after the ascending gas flow passes through the tower plate 4 under the blocking of the fine-dividing plate 5, the dispersion of the gas flow is not large, the bubbles formed in the space enclosed by the fine-dividing plate 5 and the tower plate 4 are divided into bubbles with small volume through the fine-dividing holes 12, and the heat exchange between the high-temperature gas and the liquid is facilitated, so that the efficiency of the single tower plate is improved.
It should be understood that the above examples are only for clarity of illustration and are not intended to limit the embodiments. Other variations and modifications will be apparent to persons skilled in the art in light of the above description. And are neither required nor exhaustive of all embodiments. And obvious variations or modifications are possible which remain within the scope of the appended claims.
Claims (5)
1. The rectifying and separating tower is characterized in that a fine dividing plate (5) is arranged right above each tower plate (4), the fine dividing plate (5) is detachably connected with the edge of each tower plate (4), a gap is formed between the middle area of each fine dividing plate (5) and each tower plate (4), fine dividing holes (12) are formed in each fine dividing plate (5), and the aperture of each fine dividing hole (12) is smaller than that of a through flow hole (11) in each tower plate (4); the through-flow hole (11) is a tapered hole with the aperture gradually decreasing from bottom to top in the thickness direction of the tower plate (4), and the aperture of the subdivided hole (12) is smaller than that of the necking end of the through-flow hole (11).
2. the rectification separation column according to claim 1, characterized in that the angle α between the wall of the flow hole (11) and the central axis of the flow hole (11) is 5-20 °.
3. The rectifying-separating column according to claim 1 or 2, characterized in that the fine dividing plate (5) is a spherical plate.
4. The rectification separator column according to claim 3, characterized in that the side of the fine dividing plate (5) adjacent to the downcomer (2) is detachably connected to the side wall of the overflow weir.
5. The rectification column according to claim 4, characterized in that the side of the fine division plate (5) adjacent to the liquid pan (3) encloses an air escape with the tray (4).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921842458.6U CN211025194U (en) | 2019-10-28 | 2019-10-28 | Rectifying and separating tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921842458.6U CN211025194U (en) | 2019-10-28 | 2019-10-28 | Rectifying and separating tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN211025194U true CN211025194U (en) | 2020-07-17 |
Family
ID=71564636
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201921842458.6U Expired - Fee Related CN211025194U (en) | 2019-10-28 | 2019-10-28 | Rectifying and separating tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN211025194U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113730938A (en) * | 2021-09-19 | 2021-12-03 | 扬州扬海深能源科技有限公司 | Continuous rectification and purification system for liquefiable gas |
-
2019
- 2019-10-28 CN CN201921842458.6U patent/CN211025194U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113730938A (en) * | 2021-09-19 | 2021-12-03 | 扬州扬海深能源科技有限公司 | Continuous rectification and purification system for liquefiable gas |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN201299984Y (en) | High-speed three-dimensional mass-transfer tower plate with super-large air flow | |
| CN211025194U (en) | Rectifying and separating tower | |
| CN100469422C (en) | High-efficient gas-liquid mass transferring device | |
| CN215842077U (en) | Gas-liquid separating scrubber | |
| CN106310696A (en) | Gas phase distribution device of baffle plate tower | |
| CN209645880U (en) | A kind of new type of continuous mass-transfer valve tower | |
| CN203648122U (en) | Gas-liquid mass transfer improved structure of tower plate of float valve tower | |
| CN217593874U (en) | Strip tower for overflow weir | |
| CN205182229U (en) | Falling film jet tower tray | |
| CN101015748A (en) | Continuous stereo-spray knockout tower | |
| CN216170047U (en) | Suspension type downcomer | |
| CN212347770U (en) | Rectifying tower for high-speed high-recovery-rate purification | |
| CN212369604U (en) | Single overflow sieve plate tower | |
| CN203598642U (en) | Leaching device | |
| CN211999934U (en) | Partition plate type gas-liquid separator | |
| CN204352582U (en) | A kind of overflow-type sieve-plate tower with arc screening plate | |
| CN104436735B (en) | A kind of overflow-type sieve-plate tower with Novel arc sieve plate | |
| CN114602203B (en) | Pentane rectifying tower and application method thereof | |
| CN205627149U (en) | Column plate is all imitated to bilayer | |
| CN203170185U (en) | Novel plate tower | |
| CN206229152U (en) | Waste gas treatment equipment and its absorption tower | |
| CN203170206U (en) | Novel air absorption device | |
| CN210933868U (en) | Double-tower kettle rectifying tower | |
| CN209952260U (en) | High-efficient tower tray of methyl alcohol rectifying column | |
| CN216170044U (en) | Propylene stripping tower |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20200717 Termination date: 20211028 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |