CN219482689U - Parallel-flow jet tower plate and parallel-flow jet tower comprising same - Google Patents
Parallel-flow jet tower plate and parallel-flow jet tower comprising same Download PDFInfo
- Publication number
- CN219482689U CN219482689U CN202223374627.2U CN202223374627U CN219482689U CN 219482689 U CN219482689 U CN 219482689U CN 202223374627 U CN202223374627 U CN 202223374627U CN 219482689 U CN219482689 U CN 219482689U
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- China
- Prior art keywords
- tower
- tray
- jet
- flow jet
- parallel flow
- 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.)
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- 239000007788 liquid Substances 0.000 claims description 18
- 238000012856 packing Methods 0.000 claims description 14
- 235000017166 Bambusa arundinacea Nutrition 0.000 claims description 4
- 235000017491 Bambusa tulda Nutrition 0.000 claims description 4
- 241001330002 Bambuseae Species 0.000 claims description 4
- 235000015334 Phyllostachys viridis Nutrition 0.000 claims description 4
- 239000011425 bamboo Substances 0.000 claims description 4
- 229910000831 Steel Inorganic materials 0.000 claims description 3
- 239000010959 steel Substances 0.000 claims description 3
- 230000011218 segmentation Effects 0.000 claims description 2
- 235000008331 Pinus X rigitaeda Nutrition 0.000 claims 1
- 235000011613 Pinus brutia Nutrition 0.000 claims 1
- 241000018646 Pinus brutia Species 0.000 claims 1
- 239000000126 substance Substances 0.000 abstract description 2
- 238000005372 isotope separation Methods 0.000 abstract 1
- 238000005192 partition Methods 0.000 description 8
- 238000002347 injection Methods 0.000 description 4
- 239000007924 injection Substances 0.000 description 4
- RGCLLPNLLBQHPF-HJWRWDBZSA-N phosphamidon Chemical compound CCN(CC)C(=O)C(\Cl)=C(/C)OP(=O)(OC)OC RGCLLPNLLBQHPF-HJWRWDBZSA-N 0.000 description 3
- 239000007921 spray Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000000149 penetrating effect Effects 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000012530 fluid Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
The utility model discloses a parallel flow jet tower plate and a parallel flow jet tower comprising the same, and belongs to the field of chemical industry. The parallel flow jet tower plate has the advantages of high mass transfer efficiency and is suitable for isotope separation.
Description
Technical Field
The utility model belongs to the field of chemical industry, and relates to a parallel-flow jet tower plate and a parallel-flow jet tower comprising the same.
Background
The current parallel flow jet trays are often more complex in structure and are not suitable for isotope exchange.
Disclosure of Invention
The utility model aims to solve the technical problems pointed out in the background art, and provides a parallel flow jet tower plate with good separation effect.
The technical scheme of the utility model is as follows: the utility model provides a parallel flow jet tray, includes the tray body, the tray level sets up in the tower section of thick bamboo, just the tray will the tower section of thick bamboo cuts off, the tray upper end is vertical to be equipped with two baffles, two the baffle will the region segmentation of tray top is three cell, and a cell that is located the side is the receiver tank, the below of tray is equipped with a vertical setting's injection pipe, just the upper end and the another cell that is located the side of injection pipe are indoor intercommunication, are located the centre the packing layer has been filled in the cell, and liquid is experienced the cell overflow to be located the centre in to finally overflow to the flowing back inslot, and spout downwards through the injection pipe.
Preferably, the partition board near the spray pipe is uniformly provided with seepage holes penetrating through the partition board, and the seepage holes are communicated with the groove chambers at two sides of the partition board.
Preferably, the packing layer comprises a silk screen packing layer and a dixon packing layer which are sequentially arranged along the flowing direction of the liquid, and a cover net which is arranged at the notch of the groove chamber in the middle in a covering manner.
Preferably, the cover mesh is a 60-120 mesh steel wire mesh.
The utility model also provides a parallel flow spray tower with good separation effect.
The technical scheme of the utility model is as follows: the parallel flow jet tower comprises a tower barrel and the parallel flow jet tower plates, wherein the parallel flow jet tower plates are arranged in a plurality, the tower barrel is vertically arranged, the parallel flow jet tower plates are vertically arranged at intervals in the tower barrel, each tower plate body is horizontally arranged and connected with the inner wall of the tower barrel, and the lower end of each jet pipe extends into a liquid receiving groove of the parallel flow jet tower plate below the lower end of each jet pipe.
The parallel flow jet tower plate has the advantages that the mass transfer efficiency is high, the liquid can form tiny liquid drops after being ejected through the jet pipe, so that the liquid can be in full and rapid contact with gaseous fluid, the gas-liquid mass transfer efficiency is obviously improved, the ejected liquid is splashed or overflowed into the middle groove after entering the liquid receiving groove, flows in the middle groove towards the other groove chamber positioned at the side, is in full contact with the silk screen packing layer and the Dixon packing layer in sequence in the flowing process, is dispersed and overflowed into the other groove chamber positioned at the side through the liquid seepage hole, and then is ejected to the next stage through the jet pipe, and the parallel flow jet tower plate is suitable for separating isotopes.
Drawings
FIG. 1 is a cross-sectional view of a co-current jet tray as described in example 1;
fig. 2 is a cross-sectional view of the co-current spray tower of example 2.
Detailed Description
The following description of the embodiments of the present utility model will be made clearly and completely with reference to the accompanying drawings, in which it is apparent that the embodiments described are only some embodiments of the present utility model, but not all embodiments.
It should be noted that, in the case of no conflict, the embodiments and features in the embodiments may be combined with each other. The utility model will be described in detail below with reference to the drawings in connection with embodiments.
Referring to fig. 1 in detail, one embodiment of the present utility model is a parallel flow jet tray, which comprises a tray body 100, wherein the tray is horizontally arranged in a tower drum 20, the tray 1 partitions the tower drum 2, two partitions 101 are vertically arranged at the upper end of the tray 100, the two partitions 101 divide the area above the tray 100 into three chambers, one chamber at the side is a liquid receiving tank, a jet pipe 102 is arranged below the tray, the upper end of the jet pipe 102 is communicated with the other chamber at the side, a packing layer is filled in the chamber in the middle, and the liquid overflows into the chamber in the middle, finally overflows into a liquid draining tank, and is jetted downwards through the jet pipe 102.
Preferably, the partition plate 101 near the injection pipe 102 is uniformly provided with seepage holes penetrating through the partition plate, and the seepage holes communicate the chambers at two sides of the seepage holes.
Preferably, the packing layers comprise a silk screen packing layer 103 and a dixon packing layer 104 which are sequentially arranged along the flowing direction of the liquid, and a cover net 105 which is arranged at the notch of the groove chamber in the middle.
Preferably, the cover mesh 105 is a 60-120 mesh steel mesh.
Referring to fig. 2 for details, another embodiment of the present utility model is as follows: the parallel flow jet tower comprises a tower drum 20 and the parallel flow jet tower plates 10, wherein a plurality of parallel flow jet tower plates 10 are arranged, the tower drum 20 is vertically arranged, a plurality of parallel flow jet tower plates 10 are vertically arranged in the tower drum 20 at intervals, each tower plate body 100 is horizontally arranged and connected with the inner wall of the tower drum 20, and the lower end of each jet pipe 102 extends into a liquid receiving groove of the parallel flow jet tower plate 10 below.
The above description is only of the preferred embodiments of the present utility model and is not intended to limit the present utility model, but various modifications and variations can be made to the present utility model by those skilled in the art. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present utility model should be included in the protection scope of the present utility model.
Claims (5)
1. The utility model provides a parallel-flow jet tray, its characterized in that, includes the tray body, the tray level sets up in the tower section of thick bamboo, just the tray will the tower section of thick bamboo cuts off, the tray upper end is vertical to be equipped with two baffles, two the baffle will the region segmentation of tray top becomes three cell, is located a cell of side and is the receiver, the below of tray is equipped with the jet pipe of a vertical setting, just the upper end and the another cell intercommunication that is located the side of jet pipe, is located the centre the packing layer has been filled in the cell, and liquid is experienced the overflow of cistern to the cell that is located the centre to finally overflow to the flowing back inslot, and spout downwards through the jet pipe.
2. The co-current jet tray of claim 1, wherein the baffles adjacent to the jet tubes are evenly distributed with weeping holes therethrough, the weeping holes communicating the chambers on both sides thereof.
3. The co-current jet tray of claim 2, wherein the packing layers comprise a wire mesh packing layer and a dirk pine packing layer disposed sequentially in the direction of liquid flow, and a cover net covering the slot opening of the intermediate tank chamber.
4. A co-current jet tray according to claim 3, wherein the cover mesh is a 60-120 mesh steel mesh.
5. A parallel flow jet tower, comprising a tower barrel and the parallel flow jet tower plates as claimed in claim 1, 2, 3 or 4, wherein a plurality of parallel flow jet tower plates are arranged, the tower barrel is vertically arranged, a plurality of parallel flow jet tower plates are vertically arranged in the tower barrel at intervals, each tower plate body is horizontally arranged and connected with the inner wall of the tower barrel, and the lower end of each jet pipe extends into a liquid receiving groove of the parallel flow jet tower plate below the tower barrel.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202223374627.2U CN219482689U (en) | 2022-12-15 | 2022-12-15 | Parallel-flow jet tower plate and parallel-flow jet tower comprising same |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202223374627.2U CN219482689U (en) | 2022-12-15 | 2022-12-15 | Parallel-flow jet tower plate and parallel-flow jet tower comprising same |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN219482689U true CN219482689U (en) | 2023-08-08 |
Family
ID=87477319
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202223374627.2U Active CN219482689U (en) | 2022-12-15 | 2022-12-15 | Parallel-flow jet tower plate and parallel-flow jet tower comprising same |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN219482689U (en) |
-
2022
- 2022-12-15 CN CN202223374627.2U patent/CN219482689U/en active Active
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20240708 Address after: No. 130 Shipailing Road, Wuchang District, Wuhan City, Hubei Province 430061 New Residential, Commercial, and Business Project 11/Unit 09 Floor 8 Office Patentee after: Hubei Huake Petrochemical Engineering Co.,Ltd. Country or region after: China Address before: 433200 CaoShi Avenue, CaoShi Town, Honghu City, Jingzhou City, Hubei Province Patentee before: HUBEI XINGDA PETROCHEMICAL EQUIPMENT Co.,Ltd. Country or region before: China |