CN202087215U - Adsorption Dryer - Google Patents
Adsorption Dryer Download PDFInfo
- Publication number
- CN202087215U CN202087215U CN2011201160616U CN201120116061U CN202087215U CN 202087215 U CN202087215 U CN 202087215U CN 2011201160616 U CN2011201160616 U CN 2011201160616U CN 201120116061 U CN201120116061 U CN 201120116061U CN 202087215 U CN202087215 U CN 202087215U
- Authority
- CN
- China
- Prior art keywords
- adsorption towers
- adsorption
- air outlet
- towers
- pipe
- 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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- 238000001179 sorption measurement Methods 0.000 title claims abstract description 51
- 230000001105 regulatory effect Effects 0.000 claims 6
- 230000001276 controlling effect Effects 0.000 claims 1
- 238000010521 absorption reaction Methods 0.000 description 10
- 238000001035 drying Methods 0.000 description 3
- 230000008929 regeneration Effects 0.000 description 3
- 238000011069 regeneration method Methods 0.000 description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000007791 dehumidification Methods 0.000 description 1
- 239000002274 desiccant Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000002808 molecular sieve Substances 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 230000001007 puffing effect Effects 0.000 description 1
- 239000000741 silica gel Substances 0.000 description 1
- 229910002027 silica gel Inorganic materials 0.000 description 1
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 1
- 210000000952 spleen Anatomy 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 230000001052 transient effect Effects 0.000 description 1
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- Separation Of Gases By Adsorption (AREA)
Abstract
The utility model relates to a desiccator technical field refers in particular to adsorption dryer, and it is including the chassis, locate two adsorption towers on the chassis, control box, air inlet, air outlet, connects air inlet through admission line between the entry of two adsorption towers, connects air outlet through the pipeline of giving vent to anger between the export of two adsorption towers, is equipped with the first solenoid valve that control admission line leads to the break-make gas on the admission line between the entry of two adsorption towers and the air inlet respectively, the utility model discloses a circuit control is directly utilized to first solenoid valve, and control is convenient, as long as be in the phenomenon that unable normal work just can not appear in the on state, and the operation is reliable.
Description
Technical field:
The utility model relates to the drying machine technical field, refers in particular to absorption drier.
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.
Existing absorption drier includes underframe, is located at two adsorption towers, control cabinet, air intake, air outlet slit on the underframe, connect air intake by admission line between the inlet of two adsorption towers, connect air outlet slit by outlet pipe between the outlet of two adsorption towers.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 adsorption tower 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.Two tower periodic duties need not thermal source, provide dried compressed air to user's usefulness gas system continuously.
But existing absorption drier passes through the break-make by the operated pneumatic valve control admission line gas of compressed gas-driven in the porch of adsorption tower, because air compressor machine pressure transient, when air compressor machine pressure does not reach when requiring, the diaphragm of operated pneumatic valve can dash not open, cause the operated pneumatic valve can't operate as normal, make the gas of adsorption tower can't get out, influence the use of absorption drier, control is inconvenient, and it is unreliable to move.
The utility model content:
The purpose of this utility model be exactly the deficiency that exists at prior art and provide a kind of and control conveniently, reliable absorption drier.
To achieve these goals, the technical solution adopted in the utility model is: absorption drier, it includes underframe, is located at two adsorption towers, control cabinet, air intake, air outlet slit on the underframe, connect air intake by admission line between the inlet of two adsorption towers, connect air outlet slit by outlet pipe between the outlet of two adsorption towers, be respectively equipped with first magnetic valve of control admission line break-make gas on the inlet of two adsorption towers and the admission line between the air intake.
Be connected with muffler by connecting pipe between the inlet of described two adsorption towers.
Be respectively equipped with second magnetic valve on the inlet of described two adsorption towers and the connecting pipe between the muffler.
Be connected with pressure regulator valve by the pressure regulation pipeline between the outlet of described two adsorption towers.
Described pressure regulation pipeline is provided with heater.
Be respectively equipped with check valve on the outlet of described two adsorption towers and the pressure regulation pipeline between the pressure regulator valve, also be respectively equipped with check valve on the outlet of two adsorption towers and the outlet pipe between the air outlet slit.
Be combined to form the rectangle frame structure of horizontal distribution between described pressure regulation pipeline and the outlet pipe.
The utility model beneficial effect is: the utility model includes underframe, be located at two adsorption towers on the underframe, control cabinet, air intake, air outlet slit, connect air intake by admission line between the inlet of two adsorption towers, connect air outlet slit by outlet pipe between the outlet of two adsorption towers, be respectively equipped with first magnetic valve of control admission line break-make gas on the inlet of two adsorption towers and the admission line between the air intake, first magnetic valve of the present utility model directly utilizes circuit control, control is convenient, as long as be in "on" position just can not occur can't operate as normal phenomenon, reliable.
Description of drawings:
Fig. 1 is a structural representation of the present utility model.
Fig. 2 is a principle schematic of the present utility model.
The specific embodiment:
Below in conjunction with accompanying drawing the utility model is further described, see shown in Fig. 1～2, the utility model includes underframe 1, is located at two adsorption towers 2, control cabinet 3, air intake 4, air outlet slit 5 on the underframe 1, connect air intake 4 by admission line 6 between the inlet of two adsorption towers 2, be respectively equipped with first magnetic valve 8 of controlling admission line 6 break-make gas on the inlet that connects 5, two adsorption towers 2 of air outlet slits by outlet pipe 7 between the outlet of two adsorption towers 2 and the admission line 6 between the air intake 4.First magnetic valve 8 of the present utility model directly utilizes circuit control, and control is convenient, if be in "on" position just can not occur can't operate as normal phenomenon, reliable.
Be connected with muffler 10 by connecting pipe 9 between the inlet of two adsorption towers 2, weaken the noise synergistic effect, it is effective to eliminate the noise.Being respectively equipped with second magnetic valve, 11, the second magnetic valves 11 on the connecting pipe 9 between the inlet of two adsorption towers 2 and the muffler 10 also can be pneumatic operated valve, and control is convenient.
Be connected with heater 14 and pressure regulator valve 13 by pressure regulation pipeline 12 between the outlet of two adsorption towers 2.Be combined to form the rectangle frame structure of horizontal distribution between pressure regulation pipeline 12 and the outlet pipe 7.
Be respectively equipped with on the pressure regulation pipeline 12 between the outlet of two adsorption towers 2 and the pressure regulator valve 13 on the outlet of 15, two adsorption towers 2 of check valve and the outlet pipe 7 between the air outlet slit 5 and also be respectively equipped with check valve 15, guarantee the air current flow stable and consistent.
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)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201160616U CN202087215U (en) | 2011-04-18 | 2011-04-18 | Adsorption Dryer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201160616U CN202087215U (en) | 2011-04-18 | 2011-04-18 | Adsorption Dryer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202087215U true CN202087215U (en) | 2011-12-28 |
Family
ID=45362314
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011201160616U Expired - Fee Related CN202087215U (en) | 2011-04-18 | 2011-04-18 | Adsorption Dryer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202087215U (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105004143A (en) * | 2015-07-15 | 2015-10-28 | 苏州赛弗尔机械有限公司 | Horizontal low-pressure absorption dryer |
| CN105020991A (en) * | 2015-07-14 | 2015-11-04 | 苏州赛弗尔机械有限公司 | Low pressure adsorption dryer |
| CN105133271A (en) * | 2015-07-15 | 2015-12-09 | 苏州赛弗尔机械有限公司 | Horizontal clothes adsorption drying machine |
| CN105157357A (en) * | 2015-07-15 | 2015-12-16 | 苏州赛弗尔机械有限公司 | Garment adsorbing drying machine |
| CN106955560A (en) * | 2017-04-18 | 2017-07-18 | 湖南泰瑞医疗科技有限公司 | Air-treatment main frame and oxygen generation system |
| CN115784166A (en) * | 2022-12-13 | 2023-03-14 | 湖南卓誉科技有限公司 | Modularization system oxygen host |
-
2011
- 2011-04-18 CN CN2011201160616U patent/CN202087215U/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105020991A (en) * | 2015-07-14 | 2015-11-04 | 苏州赛弗尔机械有限公司 | Low pressure adsorption dryer |
| CN105004143A (en) * | 2015-07-15 | 2015-10-28 | 苏州赛弗尔机械有限公司 | Horizontal low-pressure absorption dryer |
| CN105133271A (en) * | 2015-07-15 | 2015-12-09 | 苏州赛弗尔机械有限公司 | Horizontal clothes adsorption drying machine |
| CN105157357A (en) * | 2015-07-15 | 2015-12-16 | 苏州赛弗尔机械有限公司 | Garment adsorbing drying machine |
| CN106955560A (en) * | 2017-04-18 | 2017-07-18 | 湖南泰瑞医疗科技有限公司 | Air-treatment main frame and oxygen generation system |
| CN115784166A (en) * | 2022-12-13 | 2023-03-14 | 湖南卓誉科技有限公司 | Modularization system oxygen host |
| CN115784166B (en) * | 2022-12-13 | 2024-04-12 | 湖南卓誉科技有限公司 | Modularized oxygen-making host |
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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 |