CN203170122U - Gas-liquid separation device suitable for spray system - Google Patents
Gas-liquid separation device suitable for spray system Download PDFInfo
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- CN203170122U CN203170122U CN 201320170787 CN201320170787U CN203170122U CN 203170122 U CN203170122 U CN 203170122U CN 201320170787 CN201320170787 CN 201320170787 CN 201320170787 U CN201320170787 U CN 201320170787U CN 203170122 U CN203170122 U CN 203170122U
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Abstract
The utility model discloses a gas-liquid separation device suitable for a spray system. The gas-liquid separation device comprises a spray tower, wherein a spray device, a filler layer and a gas inlet are sequentially arranged at the middle part of the spray tower from top to bottom; and a gas-liquid separation layer is arranged at the top of the spray tower. According to the gas-liquid separation device disclosed by the utility model, the gas-liquid separation layer is added to the top of the spray tower, gas flow is guided via a fixed impeller to generate a centrifugal vortex, the passing section area of the gas flow is reduced to increase the flowing speed of the gas flow and improve the centrifugal effect, so that liquid effectively contacts a gas-liquid separation surface to be separated, and arrives at a waste liquid drainage point via a flow guide device; the separation effect is not influenced by a wind speed and a wind pressure; and the adjustment is easy.
Description
Technical field
The utility model relates to carbon disulfide vent gas treatment field, particularly relates to a kind of gas-liquid separation device that is applicable to spray system.
Background technology
At present, the tradition spray column adopts demister to carry out gas-liquid separation, and demister is corrugated deflection plate, is positioned over behind the coiling in the tower, its operation principle is: gas is carried out water conservancy diversion, and drop and corrugated plating crest are collided back deceleration, stop, deposition to reach the gas-liquid separation effect in the air-flow.Its separating effect and wind speed, blast are inversely proportional to, and are directly proportional with the thickness of self arranging, density, and gas-liquid separation effectiveness affects factor interweaves, and regulate difficulty; Separative efficiency is lower, drop is easily discharged outside the tower with air-flow, and environment is damaged.
For example application number is CN200920067065.2, and publication number is the Chinese utility model patent " a kind of desulfurization regeneration tail gas demister " of CN201361495, discloses a kind of desulfurization regeneration tail gas demister, has: the demister body; The gas that is located at the regeneration tail gas introduced of this demister body one side enters pipe; Be located at the intrinsic deflection plate of described demister; Be located at the discharging tube on the described demister body bottom; And gas outlet tube, it is characterized in that, described gas outlet tube is located on the top of described demister body, be provided with the demist layer at the intrinsic close top end of described demister, be provided with the flushing branch pipe more than at least two that links to each other with the flushing house steward respectively on the top of described demister body.Adopt the utility model, can improve the effect of trap sulfur mist, and can improve rinse capability and the developing result of demister, improve long-pending sulphur situation, the life cycle that prolongs demister.The weak point of this patent is, the circuit complexity, and the cost height, and do not possess emergent arbitration functions, be not suitable in the automation control system.
The utility model content
The purpose of this utility model is to overcome the problems referred to above that prior art exists, and proposes a kind of gas-liquid separation device that is applicable to spray system.The utility model adopts the newly-increased gas-liquid separation layer at the spray column top, and by fixed impeller air-flow is led, produce centrifugal eddy current, and compressed air-flow and increased air-flow velocity by sectional area, strengthen centrifugal effect, make liquid effectively divide the inside contact to reach with gas-liquid and separate purpose, by drainage system to the discharging of waste liquid point; Its separating effect is not subjected to wind speed, influenced by wind pressure; Regulate easily.
The utility model is realized by the following technical solutions:
A kind of gas-liquid separation device that is applicable to spray system comprises spray column, and the middle part of described spray column is provided with spray equipment, packing layer and air inlet from top to bottom successively, it is characterized in that: the top of described spray column is provided with the gas-liquid separation layer.
Be provided with counterflow unit in the described gas-liquid separation layer.
Described counterflow unit comprises fixed impeller.
Described counterflow unit also comprises blade angle adjusting dress device.
Described gas-liquid separation layer is one or more layers, is equipped with counterflow unit in every layer of gas-liquid separation layer.
The utility model compared with prior art, its advantage is:
1, the utility model adopts the newly-increased gas-liquid separation layer at the spray column top, and by fixed impeller air-flow is led, produce centrifugal eddy current, and compressed air-flow and increased air-flow velocity by sectional area, strengthen centrifugal effect, make liquid effectively divide the inside contact to reach with gas-liquid and separate purpose, by drainage system to the discharging of waste liquid point; Its separating effect is not subjected to wind speed, influenced by wind pressure; Regulate easily.
2, the utility model adopts counterflow unit, and the liquid that guiding in time separates leaves the gas-liquid separation zone, avoids being blown away by air-flow again.
3, the utility model adopts blade angle to regulate the dress device, can regulate separative efficiency by changing the refluence blade angle; In time realize adjustment and control to separative efficiency; Liquid is told the outer probability of tower with air-flow and is reduced greatly, and separative efficiency is far above traditional isolation technics.
4, the utility model employing gas-liquid separation layer is one or more layers, is equipped with counterflow unit in every layer of gas-liquid separation layer, can increase or reduce the quantity of gas-liquid separation layer according to the actual recovered needs, and is easy to use, simple to operate.
5, the utility model compared with prior art, changed original gas-liquid separation mode, its separating effect is more remarkable, separative efficiency strengthens greatly, improves with volume device processes ability, and system controllability and measurability is stronger, reduced the maintenance and inspection rate, the drop tower body rear perimeter edge environment that no longer flies out is improved, and has also prolonged the service life of peripheral equipment virtually, no longer operating personnel is damaged simultaneously.
Description of drawings
Fig. 1 is the utility model structural representation
Be labeled as among the figure: 1, spray column, 2, spray equipment, 3, packing layer, 4, air inlet, 5, the gas-liquid separation layer, 6, fixed impeller.
The specific embodiment
Embodiment 1:
A kind of gas-liquid separation device that is applicable to spray system comprises spray column 1, and the middle part of described spray column 1 is provided with spray equipment 2, packing layer 3 and air inlet 4 from top to bottom successively, and the top of described spray column 1 is provided with gas-liquid separation layer 5.
In the utility model, be provided with counterflow unit in the described gas-liquid separation layer 5.
In the utility model, described counterflow unit comprises fixed impeller 6.
In the utility model, described counterflow unit also comprises blade angle adjusting dress device.
In the utility model, described gas-liquid separation layer 5 is multilayer, is equipped with counterflow unit in every layer of gas-liquid separation layer 5.
The utility model in use, the newly-increased gas-liquid separation layer 5 at spray column 1 top, adopt 6 pairs of air-flows of the fixed impeller of multilayer to lead, produce centrifugal eddy current, and compressed air-flow and increased air-flow velocity by sectional area, strengthen centrifugal effect, make liquid effectively divide the inside contact to reach with gas-liquid and separate purpose, again by drainage system to the discharging of waste liquid point; Separating effect of the present utility model is not subjected to wind speed, influenced by wind pressure; Regulate easily, can regulate separative efficiency by changing the refluence blade angle; Liquid is told the outer probability of tower with air-flow and is reduced greatly, and separative efficiency is far above traditional isolation technics.
Embodiment 2:
A kind of gas-liquid separation device that is applicable to spray system comprises spray column 1, and the middle part of described spray column 1 is provided with spray equipment 2, packing layer 3 and air inlet 4 from top to bottom successively, and the top of described spray column 1 is provided with gas-liquid separation layer 5.
In the utility model, be provided with counterflow unit in the described gas-liquid separation layer 5.
In the utility model, described counterflow unit comprises fixed impeller 6.
In the utility model, described counterflow unit also comprises blade angle adjusting dress device.
In the utility model, described gas-liquid separation layer 5 is multilayer, is equipped with counterflow unit in every layer of gas-liquid separation layer 5.
Embodiment 3:
A kind of gas-liquid separation device that is applicable to spray system comprises spray column 1, and the middle part of described spray column 1 is provided with spray equipment 2, packing layer 3 and air inlet 4 from top to bottom successively, and the top of described spray column 1 is provided with gas-liquid separation layer 5.
In the utility model, be provided with counterflow unit in the described gas-liquid separation layer 5.
In the utility model, described counterflow unit comprises fixed impeller 6.
In the utility model, described counterflow unit also comprises blade angle adjusting dress device.
In the utility model, described gas-liquid separation layer 5 is one deck.
Claims (5)
1. gas-liquid separation device that is applicable to spray system, comprise spray column (1), the middle part of described spray column (1) is provided with spray equipment (2), packing layer (3) and air inlet (4) from top to bottom successively, it is characterized in that: the top of described spray column (1) is provided with gas-liquid separation layer (5).
2. a kind of gas-liquid separation device that is applicable to spray system according to claim 1 is characterized in that: be provided with counterflow unit in the described gas-liquid separation layer (5).
3. a kind of gas-liquid separation device that is applicable to spray system according to claim 2, it is characterized in that: described counterflow unit comprises fixed impeller (6).
4. a kind of gas-liquid separation device that is applicable to spray system according to claim 3 is characterized in that: described counterflow unit comprises that also blade angle regulates the dress device.
5. a kind of gas-liquid separation device that is applicable to spray system according to claim 1 is characterized in that: described gas-liquid separation layer (5) is one or more layers, is equipped with counterflow unit in every layer of gas-liquid separation layer (5).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320170787 CN203170122U (en) | 2013-04-08 | 2013-04-08 | Gas-liquid separation device suitable for spray system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320170787 CN203170122U (en) | 2013-04-08 | 2013-04-08 | Gas-liquid separation device suitable for spray system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203170122U true CN203170122U (en) | 2013-09-04 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201320170787 Expired - Fee Related CN203170122U (en) | 2013-04-08 | 2013-04-08 | Gas-liquid separation device suitable for spray system |
Country Status (1)
| Country | Link |
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| CN (1) | CN203170122U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104941323A (en) * | 2015-06-10 | 2015-09-30 | 青岛京润石化工程有限公司 | Multi-stage agglomeration and rotational flow combined method for removing liquid from gas |
-
2013
- 2013-04-08 CN CN 201320170787 patent/CN203170122U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104941323A (en) * | 2015-06-10 | 2015-09-30 | 青岛京润石化工程有限公司 | Multi-stage agglomeration and rotational flow combined method for removing liquid from gas |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130904 Termination date: 20150408 |
|
| EXPY | Termination of patent right or utility model |