CN220939160U - High-efficient rectifying column distributor - Google Patents
High-efficient rectifying column distributor Download PDFInfo
- Publication number
- CN220939160U CN220939160U CN202322477049.3U CN202322477049U CN220939160U CN 220939160 U CN220939160 U CN 220939160U CN 202322477049 U CN202322477049 U CN 202322477049U CN 220939160 U CN220939160 U CN 220939160U
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- Prior art keywords
- discharging pipe
- pipe
- shell
- funnel
- discharging
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- 238000007599 discharging Methods 0.000 claims abstract description 51
- 239000007788 liquid Substances 0.000 claims abstract description 43
- 238000009835 boiling Methods 0.000 claims abstract description 28
- 239000000126 substance Substances 0.000 claims abstract description 28
- 238000000926 separation method Methods 0.000 claims abstract description 12
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 16
- 230000003014 reinforcing effect Effects 0.000 claims description 8
- 229910052742 iron Inorganic materials 0.000 claims description 6
- 238000004821 distillation Methods 0.000 claims 1
- 238000000746 purification Methods 0.000 abstract description 10
- 239000000463 material Substances 0.000 abstract description 7
- 238000000034 method Methods 0.000 abstract description 5
- 238000005192 partition Methods 0.000 description 12
- 238000010586 diagram Methods 0.000 description 3
- 239000007791 liquid phase Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000012071 phase Substances 0.000 description 2
- 230000001174 ascending effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000005194 fractionation Methods 0.000 description 1
- 239000003205 fragrance Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
Landscapes
- Extraction Or Liquid Replacement (AREA)
Abstract
The utility model discloses a distributor of a high-efficiency rectifying tower, which comprises a distributing funnel, wherein the distributing funnel is arranged in a shell; and a liquid inlet pipe is arranged above the distribution funnel and connected to the shell. The high-efficiency rectifying tower distributor drives the distributing hopper to swing left and right through the driving component, so that feed liquid with different component boiling points is distributed to the first discharging pipe or the second discharging pipe, when the distributing hopper swings to the position of the first discharging pipe, the feed liquid in the distributing hopper flows into the first discharging pipe to be collected as low-boiling point substances, when the distributing hopper swings to the position of the second discharging pipe, the feed liquid of the distributing hopper flows into the second discharging pipe to achieve the aim of separating the low-boiling point substances from the high-boiling point substances, and the process is continuously carried out along with continuous swing of the distributing hopper, so that the low-boiling point substances are continuously separated from the tower kettle, the rectifying separation and purification of complex component materials are conveniently carried out, the continuity of separation and purification is enhanced, and the rectifying efficiency is accelerated.
Description
Technical Field
The utility model belongs to the technical field of rectifying towers, and particularly relates to a distributor of a high-efficiency rectifying tower.
Background
In order to increase the purity of the product in the production of fragrances, we often use a rectifying column vessel, and during the rectifying process, the traditional rectifying column or separation method is to control the heating rate, so as to control the evaporation rate of the materials to a certain range, and the purpose is to make the gas phase form an arrangement of low boilers, medium boilers and high boilers from top to bottom in the column.
However, only some simple fractionation can be performed, when the low boiling point substances and other boiling point substances cooled by the condenser tube are collected, the low boiling point substances and other boiling point substances are generally recovered through a discharging tube, the collection tank is required to be continuously replaced, the cooled low boiling point substances and other boiling point substances are recovered, the rectification separation and purification of complex component materials are inconvenient to perform, and the continuity of separation and purification is poor.
Disclosure of utility model
The utility model aims to solve the defects in the prior art, and comprises a distribution funnel, wherein the distribution funnel is arranged inside a shell;
The distribution funnel is rotationally connected with a liquid inlet pipe through a rotating shaft, and the liquid inlet pipe is connected to the shell;
A first discharging pipe and a second discharging pipe are arranged below the distribution funnel, the first discharging pipe is used for discharging low boiling point substances, the second discharging pipe is used for discharging high boiling point substances, the first discharging pipe and the second discharging pipe are connected below the shell, and a partition plate is connected between the first discharging pipe and the second discharging pipe;
The distribution funnel is connected with the driving assembly, and the driving assembly is used for driving the distribution funnel to swing left and right.
Preferably, the liquid inlet pipe is connected with a condenser through a first liquid guide pipe, and the condenser is connected with the rectifying tower through a second liquid guide pipe.
Preferably, the second discharging pipe is connected with the rectifying tower through a flow guiding pipe.
Preferably, the two sides of the shell are connected with reinforcing plates.
Preferably, the driving assembly comprises a suction iron sleeve, the suction iron sleeve is connected with the shell through a sleeve seat, a suction iron core is arranged in the suction iron sleeve, and the lower part of the suction iron core is connected with the distribution funnel.
Preferably, the liquid inlet pipe is detachably connected with the shell through a flange, and the liquid inlet pipe is positioned in the middle of the shell.
Preferably, a control box is arranged on one side of the reinforcing plate.
Preferably, the flow guide pipe is connected to the upper part of the rectifying tower.
Preferably, the first discharging pipe and the second discharging pipe are detachably connected with the shell.
The technical scheme has the following advantages or beneficial effects:
According to the utility model, the distribution funnel is driven to swing left and right by the driving component, so that the distribution funnel is used for leading feed liquid into the left side or the right side of the partition plate, feed liquid with different component boiling points is distributed to the first discharge pipe or the second discharge pipe, when the distribution funnel swings to the left side of the partition plate, feed liquid in the distribution funnel flows into the first discharge pipe to be collected as low-boiling-point substances, and when the distribution funnel swings to the right side of the partition plate, the feed liquid flows into the second discharge pipe, so that the aim of separating the low-boiling-point substances from the high-boiling-point substances is achieved, and the process is continuously carried out along with continuous swing of the distribution funnel, so that the low-boiling-point substances are continuously separated out of the tower kettle, rectification separation and purification of complex component materials are conveniently carried out, the continuity of separation and purification is enhanced, and the rectification efficiency is accelerated.
Drawings
FIG. 1 is a schematic diagram of a distributor of a high efficiency rectifying tower according to an embodiment of the present utility model;
FIG. 2 is a schematic diagram showing the operation of a distributor of a high efficiency rectifying tower according to one embodiment of the present utility model;
Fig. 3 is a second schematic diagram illustrating the operation of the distributor of the high efficiency rectifying tower according to an embodiment of the present utility model.
Legend description:
1. A dispensing funnel; 2. a housing; 3. a liquid inlet pipe; 4. a first discharge pipe; 5. a second discharge pipe; 6. a drive assembly; 7. a first catheter; 8. a condenser; 9. a second catheter; 10. a rectifying tower; 11. a flow guiding pipe; 12. a reinforcing plate; 13. a flange; 14. a control box; 15. a rotating shaft; 16. a partition plate; 61. a suction sleeve; 62. a sleeve seat; 63. and the iron-absorbing core.
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. All other embodiments, which can be made by those skilled in the art based on the embodiments of the utility model without making any inventive effort, are intended to be within the scope of the utility model.
As shown in fig. 1-3, the high-efficiency rectifying tower distributor comprises a distributing funnel 1, wherein the distributing funnel 1 is arranged inside a shell 2; the distribution funnel 1 is rotationally connected with the liquid inlet pipe 3 through a rotating shaft 15, and the liquid inlet pipe 3 is connected to the shell 2; a first discharging pipe 4 and a second discharging pipe 5 are arranged below the distribution funnel 1, the first discharging pipe 4 is used for discharging low boiling point substances, the second discharging pipe 5 is used for discharging high boiling point substances, the first discharging pipe 4 and the second discharging pipe 5 are connected below the shell 2, and a partition plate 16 is connected between the first discharging pipe 4 and the second discharging pipe 5; the distribution funnel 1 is connected with a driving component 6, and the driving component 6 is used for driving the distribution funnel 1 to swing left and right; the distribution funnel 1 is driven to swing left and right by the driving component 6, so that the distribution funnel 1 is used for leading feed liquid into the left side or the right side of the partition plate 16, feed liquid with different component boiling points is distributed to the first discharge pipe 4 or the second discharge pipe 5, when the distribution funnel 1 swings to the left side position of the partition plate 16, feed liquid in the distribution funnel 1 flows into the first discharge pipe 4 to be collected as low boiling point substances, and when the distribution funnel swings to the right side position of the partition plate 16, feed liquid flows into the second discharge pipe 5, so that the aim of separating the low boiling point substances from high boiling point substances is achieved, and the process is continuously carried out along with continuous swing of the distribution funnel 1, so that the low boiling point substances are continuously separated out of a tower kettle, rectification separation and purification of complex component materials are conveniently carried out, the continuity of separation and purification is enhanced, and the rectification efficiency is accelerated.
As shown in fig. 1 and 3, further, the liquid inlet pipe 3 is connected with the condenser 8 through the first liquid guide pipe 7, the condenser 8 is connected with the rectifying tower 10 through the second liquid guide pipe 9, and the second liquid outlet pipe 5 is connected with the rectifying tower 10 through the liquid guide pipe 11; the second discharging pipe 5 is connected with the rectifying tower 10 by the guide pipe 11, and the condensed material (liquid phase) can return to the rectifying tower 10 along the second discharging pipe 5 to exchange heat with the ascending gas phase part in the tower kettle, so that the liquid phase required for heat exchange can be continuously provided to the rectifying tower kettle, and the cost is reduced.
As shown in fig. 1 and 2, further, two sides of the casing 2 are connected with a reinforcing plate 12, and one side of the reinforcing plate 12 is provided with a control box 14; the strength of the shell 2 can be enhanced through the reinforcing plates 12 on the two sides of the shell 2, the working state of the driving assembly 6 can be controlled through the control box 14, the working frequency can be conveniently adjusted, and the practicability of the distributor is enhanced.
As shown in fig. 1 and 2, further, the driving assembly 6 includes a suction sleeve 61, the suction sleeve 61 is connected with the housing 2 through a sleeve seat 62, a suction core 63 is arranged inside the suction sleeve 61, and a lower part of the suction core 63 is connected with the dispensing funnel 1; through the circular telegram of magnet sleeve pipe 61, can adsorb inside magnet core 63, when the outage, magnet core 63 can descend owing to the effect of gravity, when magnet sleeve pipe 61 outage, magnet core 63 descends and can drive distribution funnel 1 and rotate left through pivot 15 for when distribution funnel 1 swings to the left side position of division board 16, the feed liquid in the distribution funnel 1 just flows into first discharging pipe 4, when magnet sleeve pipe 61 circular telegram, magnet core 63 rises and can drive distribution funnel 1 and rotate right through pivot 15, so that when distribution funnel 1 swings to the right side position of division board 16, the feed liquid in the distribution funnel 1 just flows into second discharging pipe 5.
As shown in fig. 1 and 2, further, the liquid inlet pipe 3 is detachably connected with the shell 2 through a flange 13, the liquid inlet pipe 3 is located in the middle of the shell 2, the flow guide pipe 11 is connected to the upper part of the rectifying tower 10, and the first discharging pipe 4 and the second discharging pipe 5 are detachably connected with the shell 2; the liquid inlet pipe 3 is convenient to install and detach through the flange 13, and the first discharging pipe 4 and the second discharging pipe 5 are detachably connected with the shell 2, so that the later maintenance is convenient.
Working principle: the distribution funnel 1 is driven to swing left and right by the driving component 6, so that the distribution funnel 1 is used for leading feed liquid into the left side or the right side of the partition plate 16, feed liquid with different component boiling points is distributed to the first discharge pipe 4 or the second discharge pipe 5, when the distribution funnel 1 swings to the left side position of the partition plate 16, feed liquid in the distribution funnel 1 flows into the first discharge pipe 4 to be collected as low boiling point substances, and when the distribution funnel swings to the right side position of the partition plate 16, feed liquid flows into the second discharge pipe 5, so that the aim of separating the low boiling point substances from high boiling point substances is achieved, and the process is continuously carried out along with continuous swing of the distribution funnel 1, so that the low boiling point substances are continuously separated out of a tower kettle, rectification separation and purification of complex component materials are conveniently carried out, the continuity of separation and purification is enhanced, and the rectification efficiency is accelerated.
Finally, it should be noted that: the foregoing description is only illustrative of the preferred embodiments of the present utility model, and although the present utility model has been described in detail with reference to the foregoing embodiments, it will be apparent to those skilled in the art that modifications may be made to the embodiments described, or equivalents may be substituted for elements thereof, and any modifications, equivalents, improvements or changes may be made without departing from the spirit and principles of the present utility model.
Claims (9)
1. The efficient rectifying tower distributor is characterized by comprising a distributing funnel (1), wherein the distributing funnel (1) is arranged inside a shell (2);
the distribution funnel (1) is rotationally connected with the liquid inlet pipe (3) through a rotating shaft (15), and the liquid inlet pipe (3) is connected to the shell (2);
A first discharging pipe (4) and a second discharging pipe (5) are arranged below the distribution funnel (1), the first discharging pipe (4) is used for discharging low boiling point substances, the second discharging pipe (5) is used for discharging high boiling point substances, the first discharging pipe (4) and the second discharging pipe (5) are connected below the shell (2), and a separation plate (16) is connected between the first discharging pipe (4) and the second discharging pipe (5);
The distribution funnel (1) is connected with the driving assembly (6), and the driving assembly (6) is used for driving the distribution funnel (1) to swing left and right.
2. The high efficiency rectifying column distributor according to claim 1, wherein: the liquid inlet pipe (3) is connected with the condenser (8) through the first liquid guide pipe (7), and the condenser (8) is connected with the rectifying tower (10) through the second liquid guide pipe (9).
3. The high efficiency rectifying column distributor according to claim 1, wherein: the second discharging pipe (5) is connected with the rectifying tower (10) through a flow guiding pipe (11).
4. The high efficiency rectifying column distributor according to claim 1, wherein: reinforcing plates (12) are connected to two sides of the shell (2).
5. The high efficiency rectifying column distributor according to claim 1, wherein: the driving assembly (6) comprises a suction iron sleeve (61), the suction iron sleeve (61) is connected with the shell (2) through a sleeve seat (62), a suction iron core (63) is arranged inside the suction iron sleeve (61), and the lower part of the suction iron core (63) is connected with the distribution funnel (1).
6. The high efficiency rectifying column distributor according to claim 1, wherein: the liquid inlet pipe (3) is detachably connected with the shell (2) through a flange (13), and the liquid inlet pipe (3) is positioned in the middle of the shell (2).
7. The high efficiency distillation column distributor according to claim 4 wherein: one side of the reinforcing plate (12) is provided with a control box (14).
8. A high efficiency rectifying column distributor according to claim 3, characterized in that: the flow guide pipe (11) is connected to the upper part of the rectifying tower (10).
9. The high efficiency rectifying column distributor according to claim 1, wherein: the first discharging pipe (4) and the second discharging pipe (5) are detachably connected with the shell (2).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322477049.3U CN220939160U (en) | 2023-09-12 | 2023-09-12 | High-efficient rectifying column distributor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322477049.3U CN220939160U (en) | 2023-09-12 | 2023-09-12 | High-efficient rectifying column distributor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220939160U true CN220939160U (en) | 2024-05-14 |
Family
ID=91010802
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202322477049.3U Active CN220939160U (en) | 2023-09-12 | 2023-09-12 | High-efficient rectifying column distributor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220939160U (en) |
-
2023
- 2023-09-12 CN CN202322477049.3U patent/CN220939160U/en active Active
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| GR01 | Patent grant |