CN202087219U - Pressure tank of absorption drier - Google Patents
Pressure tank of absorption drier Download PDFInfo
- Publication number
- CN202087219U CN202087219U CN2011201160885U CN201120116088U CN202087219U CN 202087219 U CN202087219 U CN 202087219U CN 2011201160885 U CN2011201160885 U CN 2011201160885U CN 201120116088 U CN201120116088 U CN 201120116088U CN 202087219 U CN202087219 U CN 202087219U
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- tank body
- air
- absorption drier
- diffuser
- diffusers
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- Separation Of Gases By Adsorption (AREA)
Abstract
The utility model relates to the technical field of driers, in particular to a pressure tank of an absorption drier, which comprises a tank body. An air outlet is arranged at the top of the tank body, an air inlet is arranged at the bottom of the tank body, and diffusers are respectively arranged at the positions of the air inlet and the air outlet in a cavity of the tank body. The diffusers are cylindrical net structures, wherein a plurality of meshes are evenly distributed on the surfaces of the cylindrical net structures. Air stream can be rapidly diffused out towards all directions through the meshes arranged on the surfaces all around the diffusers after entering the cavity of the tank body from the air inlet, thereby enabling the air stream to pass through an adsorbent layer evenly, and having high absorption efficiency and good absorption and drying effect. Furthermore, the diffusers can effectively filer absorbent powder and small impurity particles.
Description
Technical field:
The utility model relates to the drying machine technical field, refers in particular to the absorption drier pressure volume pot.
Background technology:
Absorption drier is to utilize adsorbent (activated alumina, silica gel, the molecular sieve) characteristic of adsorption moisture to reduce the content of moisture in the compressed air, and the dew point of working off one's feeling vent one's spleen is reached more than-40 degree.Absorption drier is to reach drying effect by the transformation absorption principle.Because holding the ability and the pressure of steam, air is inversely proportional to, its dried portion of air (being called regeneration gas) puffing is to atmospheric pressure, this pressure changes makes expanded air become drier, allow it flow through the desiccant layer (promptly having absorbed the pressure volume pot of enough steam) of the need regeneration of access failure air-flow then, moisture in the dry regeneration gas sucking-off drier is taken it out of purpose that drying machine reaches dehumidification.
But the pressure volume pot of existing absorption drier is bad to the diffusion effect of air-flow, and air-flow can not evenly pass through adsorbent layer, influences the adsorption dry effect of drying machine.
The utility model content:
The purpose of this utility model is exactly to provide a kind of absorption drier pressure volume pot that can make air-flow evenly pass through adsorbent layer, raising adsorption dry effect at the deficiency of prior art existence.
To achieve these goals, the technical solution adopted in the utility model is: the absorption drier pressure volume pot, it includes tank body, the top of tank body is provided with air outlet slit, the bottom of tank body is provided with air intake, the position that is positioned at air intake and air outlet slit in the tank inner chamber is respectively equipped with diffuser, and diffuser is the cylindrical shape network structure that is evenly distributed with a plurality of mesh on the surface.
Described diffuser vertically is provided with.
The diameter of described diffuser is 90~100mm.
The diameter of described mesh is 3~5mm.
As preferred version, the diameter of described mesh is 4mm.
The top of described tank body and bottom are respectively hemisphere shape structure.
Described tank body is provided with Pressure gauge.
The utility model beneficial effect is: the utility model includes tank body, the top of tank body is provided with air outlet slit, the bottom of tank body is provided with air intake, the position that is positioned at air intake and air outlet slit in the tank inner chamber is respectively equipped with diffuser, diffuser is the cylindrical shape network structure that is evenly distributed with a plurality of mesh on the surface, after air-flow enters tank inner chamber from air intake, can to all the winds evenly spread out rapidly by the mesh of diffuser surrounded surface, make air-flow evenly pass through adsorbent layer, the adsorption efficiency height, adsorption dry is effective, and diffuser can effectively filter absorbent powder, the fine impurities particle.
Description of drawings:
Fig. 1 is an internal structure schematic diagram of the present utility model.
The specific embodiment:
Below in conjunction with accompanying drawing the utility model is further described, see shown in Figure 1, the utility model includes tank body 1, the top of tank body 1 is provided with air outlet slit 2, the bottom of tank body 1 is provided with air intake 3, the position that is positioned at air intake 3 and air outlet slit 2 in tank body 1 inner chamber is respectively equipped with diffuser 4, and diffuser 4 is for being evenly distributed with the cylindrical shape network structure of a plurality of mesh 5 on the surface.After air-flow enters tank body 1 inner chamber from air intake 3, can to all the winds evenly spread out rapidly by the mesh 5 of diffuser 4 surrounded surfaces, make air-flow evenly pass through adsorbent layer, the adsorption efficiency height, adsorption dry is effective, and diffuser 4 can effectively filter absorbent powder, fine impurities particle.
Diffuser 4 vertically is provided with.The diameter of diffuser 4 is 90~100mm, can spread air-flow better.The diameter of mesh 5 is 3~5mm, can be 3mm, 4mm, 5mm as the diameter of mesh 5, is 4mm at the diameter of embodiment mesh 5, can pass through air-flow better, and play better filtration.
The top of tank body 1 and bottom are respectively hemisphere shape structure.Tank body 1 is provided with Pressure gauge 6, can show the pressure condition of gas in the tank body 1 in real time.
Certainly, the above only is a better embodiment of the present utility model, so all equivalences of doing according to the described structure of the utility model patent claim, feature and principle change or modify, is included in the utility model patent claim.
Claims (7)
1. absorption drier pressure volume pot, it includes tank body (1), it is characterized in that: the top of described tank body (1) is provided with air outlet slit (2), the bottom of tank body (1) is provided with air intake (3), the position that is positioned at air intake (3) and air outlet slit (2) in tank body (1) inner chamber is respectively equipped with diffuser (4), and diffuser (4) is for being evenly distributed with the cylindrical shape network structure of a plurality of mesh (5) on the surface.
2. absorption drier pressure volume pot according to claim 1 is characterized in that: described diffuser (4) vertically is provided with.
3. absorption drier pressure volume pot according to claim 1 is characterized in that: the diameter of described diffuser (4) is 90~100mm.
4. absorption drier pressure volume pot according to claim 1 is characterized in that: the diameter of described mesh (5) is 3~5mm.
5. absorption drier pressure volume pot according to claim 4 is characterized in that: the diameter of described mesh (5) is 4mm.
6. absorption drier pressure volume pot according to claim 1 is characterized in that: the top of described tank body (1) and bottom are respectively hemisphere shape structure.
7. according to any described absorption drier pressure volume pot of claim 1~6, it is characterized in that: described tank body (1) is provided with Pressure gauge (6).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2011201160885U CN202087219U (en) | 2011-04-18 | 2011-04-18 | Pressure tank of absorption drier |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2011201160885U CN202087219U (en) | 2011-04-18 | 2011-04-18 | Pressure tank of absorption drier |
Publications (1)
Publication Number | Publication Date |
---|---|
CN202087219U true CN202087219U (en) | 2011-12-28 |
Family
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN2011201160885U Expired - Fee Related CN202087219U (en) | 2011-04-18 | 2011-04-18 | Pressure tank of absorption drier |
Country Status (1)
Country | Link |
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CN (1) | CN202087219U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107511032A (en) * | 2017-09-06 | 2017-12-26 | 武汉钢铁集团气体有限责任公司 | A kind of gas cleaning plant |
CN114225654A (en) * | 2021-11-18 | 2022-03-25 | 宁夏东部热电股份有限公司 | Layered modular adsorption type dryer |
-
2011
- 2011-04-18 CN CN2011201160885U patent/CN202087219U/en not_active Expired - Fee Related
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107511032A (en) * | 2017-09-06 | 2017-12-26 | 武汉钢铁集团气体有限责任公司 | A kind of gas cleaning plant |
CN107511032B (en) * | 2017-09-06 | 2020-01-07 | 武汉钢铁集团气体有限责任公司 | Gas purification device |
CN114225654A (en) * | 2021-11-18 | 2022-03-25 | 宁夏东部热电股份有限公司 | Layered modular adsorption type dryer |
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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: 20111228 Termination date: 20120418 |