CN201101904Y - Sidetrack discharge collector - Google Patents
Sidetrack discharge collector Download PDFInfo
- Publication number
- CN201101904Y CN201101904Y CNU2007200434256U CN200720043425U CN201101904Y CN 201101904 Y CN201101904 Y CN 201101904Y CN U2007200434256 U CNU2007200434256 U CN U2007200434256U CN 200720043425 U CN200720043425 U CN 200720043425U CN 201101904 Y CN201101904 Y CN 201101904Y
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- CN
- China
- Prior art keywords
- gatherer
- tower
- steam guiding
- evenly distributed
- steam
- 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
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
A draw-off gathering device is provided with a gathering tank, the bottom of which is connected with an extracting tube, a flange plate is connected with a tower body on the upper and the lower parts of the gathering device. The utility model is characterized in that a plurality of steam guiding tubes and a plurality of return tubes are evenly distributed in the gathering tank. The steam guiding tubes have the structure that the steam guiding tubes are evenly distributed at the bottom of the gathering device and are arranged in parallel to the tower body; the return tubes have the structure that the return tubes are evenly distributed at the bottom of the gathering device and is arranged in parallel to the tower body, the length of the steam guiding tubes is a litter longer than that of the return tubes. The draw-off gathering device has simple structure and convenient sampling; the utility model not only can gather liquid, but also can ensure the flow of the steam, thereby not damaging the steam-liquid equilibrium in the tower. The draw-off gathering device has the advantages that: (1) sampling does not influence the steam-liquid equilibrium in the tower; (2) the gathering device is connected with the flange plate, thereby facilitating disassembly and maintenance.
Description
Technical field
The utility model relates to a kind of chemical industry equipment, is specifically related to a kind of side line discharging gatherer, is a kind ofly to be applied in the separation process of vapour-liquid mixture middle discharging gathering-device.
Background technology
Employed various gatherers structurally divide direct collection type and batch (-type) collection type at present.Intermittently collection type is generally in tower certain position gas is drawn outside the tower, adopts condenser condenses again, partial reflux, and another part takes out as product, and this method is feasible, but the process complexity; The direct-type gatherer directly takes out material for design feeder in tower, and method is simple, flows but feeder influences vapour-liquid, destroys in the tower and balances each other.
Summary of the invention
At the above-mentioned deficiency of prior art, the purpose of the utility model device provides a kind of simple in structure, easy to operate, novel side line discharging gatherer of not influencing VLE in the tower.
The side line discharging gatherer that the utility model provides is a kind ofly to be adapted in the separation process of vapour-liquid mixture middle discharging gathering-device.The structure of this side line discharging gatherer is: be provided with feeder, the feeder bottom connects gets the material pipe, and gatherer adopts flange plate to be connected with tower body up and down, it is characterized in that, is evenly distributed with some steam guiding tubes and some overflow pipes in the described feeder.
The concrete structure of above-described " steam guiding tube " is: be evenly distributed on the bottom of gatherer, be arranged in parallel with tower body; Gas below the gatherer can flow into the gatherer top smoothly by steam guiding tube.
The concrete structure of described overflow pipe is: be evenly distributed on the bottom of gatherer, be arranged in parallel with tower body.The a little higher than overflow pipe of steam guiding tube length.When liquid level was higher than overflow pipe, tower joint below liquid flows into by overflow pipe was guaranteed the highly stable of liquid level in the gatherer.
The length of described steam guiding tube is 31～35mm, and diameter is 6mm, can amplify in proportion with tower diameter as required; The length of described overflow pipe is 25～30mm, is slightly smaller than the diameter of steam guiding tube, and diameter is 4mm, or amplifies in proportion with tower diameter.
Beneficial effect: the utility model side line discharging gatherer has advantages such as simple in structure, that sampling is convenient, because " gatherer " of the present utility model not only can collect liquid, has guaranteed flowing of gas simultaneously, so can not destroy the VLE in the tower.
Be embodied in: 1. sampling does not influence VLE in the tower.2. gathering-device is connected with the tower flange plate, is convenient to dismounting and maintenance.
Description of drawings
Fig. 1 is the utility model side line discharging collector structure schematic diagram;
Fig. 2 is the vertical view of Fig. 1.
The specific embodiment
The utility model side line discharging gatherer is a kind of device that vapour-liquid mixture mid-boiling point is formed discharging that is adapted to.Be φ 300mm at tower diameter, highly for 150mm, steam guiding tube diameter phi 6mm, highly be 31～35mm, evenly distribute 37, overfall tube diameter φ 4mm, highly be 25～30mm, evenly distribute 32.When treating capacity is big, can also amplify in proportion.
Claims (5)
1, a kind of side line discharging gatherer is provided with feeder, and the feeder bottom connects gets the material pipe, and gatherer adopts flange plate to be connected with tower body up and down, it is characterized in that, is evenly distributed with some steam guiding tubes and some overflow pipes in the described feeder.
2, side line discharging gatherer according to claim 1 is characterized in that the concrete structure of described steam guiding tube is: be evenly distributed on the bottom of gatherer, be arranged in parallel with tower body;
The concrete structure of described overflow pipe is: be evenly distributed on the bottom of gatherer, be arranged in parallel with tower body, a little higher than overflow pipe of steam guiding tube length.
3, side line discharging gatherer according to claim 2 is characterized in that, the length of described steam guiding tube is 31～35mm, diameter 6mm, or amplify in proportion with tower diameter; The length of described overflow pipe is 25～30mm, diameter 4mm, or amplify in proportion with tower diameter.
4, according to claim 1 or 2 or 3 described side line discharging gatherers, it is characterized in that, when tower diameter be φ 300mm, highly when the 150mm, steam guiding tube evenly distributes 37; Overflow pipe evenly distributes 32.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007200434256U CN201101904Y (en) | 2007-10-19 | 2007-10-19 | Sidetrack discharge collector |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007200434256U CN201101904Y (en) | 2007-10-19 | 2007-10-19 | Sidetrack discharge collector |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201101904Y true CN201101904Y (en) | 2008-08-20 |
Family
ID=39948922
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2007200434256U Expired - Fee Related CN201101904Y (en) | 2007-10-19 | 2007-10-19 | Sidetrack discharge collector |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201101904Y (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102327699A (en) * | 2011-10-18 | 2012-01-25 | 天津大学 | Dual-layer collective liquid distributor with lateral line withdrawal function |
| CN103768820A (en) * | 2014-02-17 | 2014-05-07 | 无锡市杨市化工有限公司 | Graphite distribution collector |
| CN114405038A (en) * | 2022-01-26 | 2022-04-29 | 福建钰融科技有限公司 | Condensation flow guide assembly and waste liquid recovery device |
-
2007
- 2007-10-19 CN CNU2007200434256U patent/CN201101904Y/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102327699A (en) * | 2011-10-18 | 2012-01-25 | 天津大学 | Dual-layer collective liquid distributor with lateral line withdrawal function |
| CN103768820A (en) * | 2014-02-17 | 2014-05-07 | 无锡市杨市化工有限公司 | Graphite distribution collector |
| CN103768820B (en) * | 2014-02-17 | 2015-08-19 | 无锡市杨市化工有限公司 | graphite distribution collector |
| CN114405038A (en) * | 2022-01-26 | 2022-04-29 | 福建钰融科技有限公司 | Condensation flow guide assembly and waste liquid recovery device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20080820 Termination date: 20121019 |