CN204637792U - A kind of heat exchange type deflector-type separator - Google Patents
A kind of heat exchange type deflector-type separator Download PDFInfo
- Publication number
- CN204637792U CN204637792U CN201420690074.8U CN201420690074U CN204637792U CN 204637792 U CN204637792 U CN 204637792U CN 201420690074 U CN201420690074 U CN 201420690074U CN 204637792 U CN204637792 U CN 204637792U
- Authority
- CN
- China
- Prior art keywords
- endothermic tube
- flap
- support ring
- wireway
- heat exchange
- 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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Abstract
The utility model relates to a kind of heat exchange type deflector-type separator, comprise support ring, endothermic tube, flap, wireway, convex axle, catheter, liquid level gauge, flexible pipe, heat release pipe, cooling bath, gag lever post, its feature endothermic tube freely can rotate within the scope of certain angle, endothermic tube both sides are welded with flap respectively, and support ring and endothermic tube are all hollow structure inside and inner hollow space is interconnected, and support ring and endothermic tube are built with refrigerating fluid.When the solvent air foam of high temperature impacts flap, liquid solvent is tackled by flap due to effect of inertia, and gaseous solvent then meets condensation knot on flap.The utility model is mainly used in the occasion that the industries such as petrochemical industry, thermoelectricity, iron and steel need to remove solvent air foam from high-temperature gas.
Description
Technical field
The utility model relates to a kind of demister for removing solvent air foam from high-temperature gas that the industries such as petrochemical industry, thermoelectricity, iron and steel use.
Background technology
The drop that demister is carried secretly for separating of gas in tower, to ensure mass-transfer efficiency, reduces valuable material and damages
Become estranged and improve the operation of compressor after tower, reduce water content, extend the life-span of compressor, generally many demister is set at tower top,
Effectively can remove the droplet of 3 one 5um, if arrange demister between tower tray, not only can ensure the mass-transfer efficiency of tower tray, can also subtract
Little distance between plates.Folded plate type demister is one of principal mode of demister, is divided by the drop carried secretly in gas by gas baffling
From out; Traditional folded plate type demister cannot according to gas flow rate size adjustment flap angle, in some cases, during liquid flux absorption gaseous solute, fuel factor is very large, thus causes liquid flux to be vaporized, and vaporized liquid flux cannot be effectively separated by traditional demister.
Summary of the invention
For above-mentioned prior art Problems existing, the utility model provides a kind of heat exchange type deflector-type separator, can according to gas flow rate size adjustment flap angle and can the liquid flux of effective separation of vaporization.
To achieve these goals, the technical solution adopted in the utility model is: a kind of heat exchange type deflector-type separator, comprise support ring, endothermic tube, flap, wireway, convex axle, catheter, liquid level gauge, flexible pipe, heat release pipe, cooling bath, gag lever post, it is characterized in that support ring is connected with endothermic tube, endothermic tube welds with flap, and endothermic tube welds with wireway, wireway is welded with convex axle, gag lever post has aperture to be used for being connected with convex axle, wireway and flexible pipe, heat release pipe, catheter are linked in sequence.
Wherein, endothermic tube freely can rotate within the scope of certain angle, and support ring and endothermic tube are all hollow structure inside and inner hollow space is interconnected, and support ring and endothermic tube are built with refrigerating fluid.
The utility model compared with prior art has the following advantages: because endothermic tube freely can rotate within the scope of certain angle, can according to gas flow rate size adjustment flap angle; Support ring and endothermic tube are all hollow structure inside and inner hollow space is interconnected, support ring and the endothermic tube liquid flux built with the effective separation of vaporization of refrigerating fluid.
Accompanying drawing explanation
Accompanying drawing 1 is the plan structure schematic diagram of this heat exchange type deflector-type separator.
Accompanying drawing 2 is the example structure schematic diagram of this heat exchange type deflector-type separator.
In figure: 1, support ring, 2, endothermic tube, 3, flap, 4, wireway, 5, convex axle, 6, catheter, 7, liquid level gauge, 8, flexible pipe, 9, heat release pipe, 10, cooling bath, 11, gag lever post.
Detailed description of the invention
As follows with reference to accompanying drawing 1: a kind of heat exchange type deflector-type separator, comprises support ring 1, endothermic tube 2, flap 3, wireway 4, convex axle 5, catheter 6, liquid level gauge 7, flexible pipe 8, heat release pipe 9, cooling bath 10, gag lever post 11.It is characterized in that support ring 1 is connected with endothermic tube 2, endothermic tube 2 welds with flap 3, and endothermic tube 2 welds with wireway 4, wireway 4 is welded with convex axle 5, gag lever post 11 has aperture to be used for being connected with convex axle 5, wireway 4 and flexible pipe 8, heat release pipe 9, Liquid pouring pipe 6 are linked in sequence.It is characterized in that endothermic tube 2 freely can rotate within the scope of certain angle, endothermic tube 2 flip angle can be controlled by pulling gag lever post 11, described gag lever post 11 is connected with convex axle 5, wherein, the corresponding wireway 4 of each convex axle 5, the corresponding endothermic tube 2 of each wireway 4, support ring 1 and endothermic tube 2 are all hollow structure inside and inner hollow space is interconnected, and support ring 1 and endothermic tube 2 are built with refrigerating fluid.
During knockout tower work, rise in knockout tower containing liquid foam air-flow, and change at flap place air flow direction, large drop impinges upon on flap 3 due to effect of inertia, falls back in knockout tower.When gas flow rate changes in knockout tower, gag lever post 11 can be pulled thus the deflection angle of adjustment flap 3, play air foam and be separated maximized object.Because fuel factor during liquid flux absorption gaseous solute is very large, liquid flux can be caused to vaporize, therefore a large amount of high-temperature gas solvent is contained in ascending air, when high-temperature gas solvent fully contacts with low temperature flap 3, the rapid heat release of high-temperature gas solvent is also liquefied as droplet and adheres on flap 3, and droplet constantly merges final drippage.Cold-producing medium in endothermic tube 2 then absorbs heat vaporization, rises to heat release pipe 9, cool through cooling bath 10 along wireway 4, and refrigerant liquefaction also flows back to the inner chamber of bracing ring 1 again along catheter 6.
Claims (3)
1. heat exchange type deflector-type separator, comprise support ring (1), endothermic tube (2), flap (3), wireway (4), convex axle (5), catheter (6), liquid level gauge (7), flexible pipe (8), heat release pipe (9), cooling bath (10), gag lever post (11), it is characterized in that support ring (1) is connected with endothermic tube (2), endothermic tube (2) welds with flap (3), endothermic tube (2) welds with wireway (4), wireway (4) is welded with convex axle (5), gag lever post (11) has aperture to be used for being connected with convex axle (5), wireway (4) and flexible pipe (8), heat release pipe (9), catheter (6) is linked in sequence.
2. heat exchange type deflector-type separator according to claim 1, is characterized in that described endothermic tube (2) freely can rotate within the scope of certain angle.
3. heat exchange type deflector-type separator according to claim 1, it is characterized in that described support ring (1) and endothermic tube (2) are all hollow structure inside and inner hollow space is interconnected, support ring (1) and endothermic tube (2) are built with refrigerating fluid.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420690074.8U CN204637792U (en) | 2014-11-18 | 2014-11-18 | A kind of heat exchange type deflector-type separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420690074.8U CN204637792U (en) | 2014-11-18 | 2014-11-18 | A kind of heat exchange type deflector-type separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204637792U true CN204637792U (en) | 2015-09-16 |
Family
ID=54090569
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420690074.8U Expired - Fee Related CN204637792U (en) | 2014-11-18 | 2014-11-18 | A kind of heat exchange type deflector-type separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204637792U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105214331A (en) * | 2015-10-28 | 2016-01-06 | 航天环境工程有限公司 | A kind of high-efficiency condensation tube bank demister and application |
-
2014
- 2014-11-18 CN CN201420690074.8U patent/CN204637792U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105214331A (en) * | 2015-10-28 | 2016-01-06 | 航天环境工程有限公司 | A kind of high-efficiency condensation tube bank demister and application |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150916 Termination date: 20161118 |