CN101991998A - Tertiary filter - Google Patents
Tertiary filter Download PDFInfo
- Publication number
- CN101991998A CN101991998A CN2009101159669A CN200910115966A CN101991998A CN 101991998 A CN101991998 A CN 101991998A CN 2009101159669 A CN2009101159669 A CN 2009101159669A CN 200910115966 A CN200910115966 A CN 200910115966A CN 101991998 A CN101991998 A CN 101991998A
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- filter
- tank body
- gas
- annular seal
- filter core
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Abstract
The invention relates to a tertiary filter which comprises a tank body with a gas inlet and a gas outlet, and a baffle filtering device, a cooling filtering device and a filter element filtering device are arranged in the tank body from bottom to top in sequence. Compared with the prior art only using the filter element filtering device to filter, the invention is applicable to the filter element filtering device of a gas with high temperature and high moisture content and has wide application range. Moreover, because the gas is filtered by the first two levels of filtering devices, the load of the filter element in the filter element filtering device at the third level is much smaller than that of the traditional structure, and the service life of the filter element is longer.
Description
Technical field
The present invention relates to be used in a kind of gas generation to the dewater filter of oil removing of mist.
Background technology
Traditional filter generally includes the tank body with air inlet and gas outlet, is provided with the filter core that is used to filter moisture in the tank body, only relies on the interior filter core of filter to carry out oil removing and dewaters.The life-span of the filter core in the filter of this structure is shorter usually, and under the situation that particularly gas temperature in entering filter is higher, water content is bigger, water removal effect is undesirable, makes that the steam in the mist is very easily brought in the downstream component by gas.
Summary of the invention
In order to overcome the deficiencies in the prior art, the purpose of this invention is to provide a kind of tertiary filter, it can be applicable to that the gas higher to gas temperature, that water content is higher dewaters, service life applied widely and filter core is longer.
The present invention can be implemented by the following technical programs:
A kind of tertiary filter, it comprises the tank body with air inlet and gas outlet, be disposed with baffle plate filter, cold filtration device in the described tank body from the bottom to top, cross filter core filter three-stage filtration device, described baffle plate filter comprises the baffle plate that is horizontally set on described air inlet top; Described cold filtration device comprises the screen pipe that is used for logical mist and is used for the annular seal space of the logical described screen pipe of water quench that described screen pipe and described annular seal space are isolated mutually; The described filter core filter of crossing comprises a plurality of filter cores that are arranged on vertically in the described tank body.
The airintake direction of described air inlet is the tangential direction of the inwall of described tank body.
Also be provided with the cooling water inlet and the coolant outlet that are connected with described annular seal space on the described tank body.
The bottom of described tank body is provided with sewage draining exit, and described gas outlet is arranged on the top of described tank body.
Described filter core is the corundum filter core.
Described screen pipe is arranged in the described annular seal space vertically.
Compared with the prior art the present invention has following advantage:
Owing to be disposed with the baffle plate filter from the bottom to top in the described tank body, the cold filtration device, cross filter core filter three-stage filtration device, if water content is higher in the unstrpped gas, most of moisture can be amassed to the sewage draining exit place of bottom and remove behind the baffle plate of process baffle plate filter, enter into the cold filtration device then, logical cooling water in the annular seal space of cold filtration device, logical mist and cooling water and gas are isolated mutually in the screen pipe, when unstripped gas has uniform temperature, water condensation in the high-temperature gas can be got off flow to the ponding dish through the secondary type of cooling, water be discharged by sewage draining exit.Removed most of moisture through the unstrpped gas after the above-mentioned dual stage filter apparatus, the last corundum that passed through again in the filter core filter is crossed filter core and carried out the afterbody processed, and is better through the gas dewatering effect of three-stage filtration.
Compared with prior art, the present invention is applicable to that the gas higher to gas temperature, that water content is higher dewaters, and is applied widely.And because gas is little more a lot of than traditional structure at the filter core load of crossing in the filter core filter of the third level through after the filtration of preceding dual stage filter apparatus, so the service life of filter core is longer.
Description of drawings
Accompanying drawing 1 is a structural representation of the present invention;
Accompanying drawing 2 is the vertical view of accompanying drawing 1;
Accompanying drawing 3 is a filter structure schematic representation of the prior art;
Wherein:
1, air inlet 2, gas outlet 3, tank body 4, baffle plate filter 41, baffle plate 5, cold filtration device 51, annular seal space 52, screen pipe 6, mistake filter core filter 61, filter core 7, cooling water inlet 8 coolant outlets; 9, sewage draining exit.
The specific embodiment
Below in conjunction with accompanying drawing the preferred embodiments of the invention are elaborated:
As shown in Figures 1 and 2, a kind of tertiary filter, it comprises the tank body 3 with air inlet 1 and gas outlet 2, is disposed with baffle plate filter 4, cold filtration device 5 in the described tank body 3 from the bottom to top, crosses filter core filter 6 three-stage filtration devices.
Described baffle plate filter 4 comprises the baffle plate 41 that is horizontally set on described air inlet 1 top; Described cold filtration device 5 comprises screen pipe 52 that is used for logical mist and the annular seal space 51 that is used for the logical described screen pipe 52 of water quench, described screen pipe 52 is isolated mutually with described annular seal space 51, and described screen pipe 52 is arranged in the described annular seal space 51 vertically; The described filter core filter 6 of crossing comprises a plurality of corundum filter cores 61 that are arranged on vertically in the described tank body 3.
Also be provided with the cooling water inlet 7 and the coolant outlet 8 that are connected with described annular seal space 51 on the described tank body 3.
The bottom of described tank body 3 is provided with sewage draining exit 9, and described gas outlet 2 is arranged on the top of described tank body 3.
The airintake direction of described air inlet 1 is the tangential direction of the inwall of described tank body 3, therefore unstrpped gas forms the whirlwind shape entered the tank body of filter by air inlet 1 after, if the gas of whirlwind shape is higher through impingement baffles 41 back water content, the baffle plate 41 back most of moisture of process baffle plate filter 4 can be amassed to sewage draining exit 9 places of bottom and remove, enter into cold filtration device 5 then, logical cooling water in the annular seal space 51 of cold filtration device 5, logical mist and cooling water and gas are isolated mutually in the screen pipe 52, when unstripped gas has uniform temperature, water condensation in the high-temperature gas can be got off flow to the ponding dish through the secondary type of cooling, water be discharged by sewage draining exit 9.Removed most of moisture through the unstrpped gas after the above-mentioned dual stage filter apparatus, the corundum filter core 61 that passed through again in the filter core filter 6 at last carries out the afterbody processed, and is better through the gas dewatering effect of three-stage filtration.
Compared with prior art, the present invention dewaters applicable to the gas higher to gas temperature, that water content is higher, and the scope of application is wider. And because gas is little more a lot of than traditional structure at the filter core load of crossing in the filter core filter of the third level through after the filtration of front dual stage filter apparatus, so the service life of filter core is longer, and service life is longer more than 2 times than old structure usually.
Claims (6)
1. tertiary filter, it comprises the have air inlet tank body (3) of (1) and gas outlet (2), it is characterized in that: be disposed with baffle plate filter (4), cold filtration device (5) in the described tank body (3) from the bottom to top, cross filter core filter (6) three-stage filtration device, described baffle plate filter (4) comprises the baffle plate (41) that is horizontally set on described air inlet (1) top; Described cold filtration device (5) comprises the screen pipe (52) that is used for logical mist and is used for the annular seal space (51) of the logical described screen pipe of water quench (52) that described screen pipe (52) is isolated mutually with described annular seal space (51); The described filter core filter (6) of crossing comprises a plurality of filter cores (61) that are arranged on vertically in the described tank body (3).
2. a kind of tertiary filter according to claim 1 is characterized in that: the airintake direction of described air inlet (1) is the tangential direction of the inwall of described tank body (3).
3. a kind of tertiary filter according to claim 1 is characterized in that: also be provided with the cooling water inlet (7) and the coolant outlet (8) that are connected with described annular seal space (51) on the described tank body (3).
4. a kind of tertiary filter according to claim 1 is characterized in that: the bottom of described tank body (3) is provided with sewage draining exit (9), and described gas outlet (2) are arranged on the top of described tank body (3).
5. a kind of tertiary filter according to claim 1 is characterized in that: described filter core (61) is the corundum filter core.
6. a kind of tertiary filter according to claim 1 is characterized in that: described screen pipe (52) is arranged in the described annular seal space (51) vertically.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009101159669A CN101991998A (en) | 2009-08-11 | 2009-08-11 | Tertiary filter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009101159669A CN101991998A (en) | 2009-08-11 | 2009-08-11 | Tertiary filter |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN101991998A true CN101991998A (en) | 2011-03-30 |
Family
ID=43783052
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009101159669A Pending CN101991998A (en) | 2009-08-11 | 2009-08-11 | Tertiary filter |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN101991998A (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102225291A (en) * | 2011-05-27 | 2011-10-26 | 南通金坤机械设备有限公司 | Gas-liquid separator |
| CN102698538A (en) * | 2012-05-16 | 2012-10-03 | 李莉 | Precise filter |
| CN103264467A (en) * | 2013-05-31 | 2013-08-28 | 吉铨精密机械(苏州)有限公司 | Convenient and fast cooling system |
| CN104208988A (en) * | 2014-09-04 | 2014-12-17 | 王新建 | Device used for efficiently drying compressed air and provided with filtration device |
| CN107029512A (en) * | 2017-05-11 | 2017-08-11 | 洛阳千百度窑炉科技有限公司 | The smoke and dust eliminating method and equipment of white cigarette gas |
| CN108079732A (en) * | 2018-02-08 | 2018-05-29 | 江苏优耐特过滤装备有限公司 | Horizontal multi-stage separator |
| CN109893959A (en) * | 2019-04-23 | 2019-06-18 | 江苏博润通科技有限公司 | A kind of gas cooling water treatment plant |
| CN110193240A (en) * | 2018-02-26 | 2019-09-03 | 藟发有限公司 | Can dehumidify the pneumatics bucket of air filtering |
| CN110523189A (en) * | 2019-08-27 | 2019-12-03 | 安徽江淮汽车集团股份有限公司 | Gas cleaning plant |
-
2009
- 2009-08-11 CN CN2009101159669A patent/CN101991998A/en active Pending
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102225291A (en) * | 2011-05-27 | 2011-10-26 | 南通金坤机械设备有限公司 | Gas-liquid separator |
| CN102698538A (en) * | 2012-05-16 | 2012-10-03 | 李莉 | Precise filter |
| CN103264467A (en) * | 2013-05-31 | 2013-08-28 | 吉铨精密机械(苏州)有限公司 | Convenient and fast cooling system |
| CN104208988A (en) * | 2014-09-04 | 2014-12-17 | 王新建 | Device used for efficiently drying compressed air and provided with filtration device |
| CN104208988B (en) * | 2014-09-04 | 2016-04-20 | 王新建 | The compressed air drier that a kind of window filters |
| CN107029512A (en) * | 2017-05-11 | 2017-08-11 | 洛阳千百度窑炉科技有限公司 | The smoke and dust eliminating method and equipment of white cigarette gas |
| CN108079732A (en) * | 2018-02-08 | 2018-05-29 | 江苏优耐特过滤装备有限公司 | Horizontal multi-stage separator |
| CN110193240A (en) * | 2018-02-26 | 2019-09-03 | 藟发有限公司 | Can dehumidify the pneumatics bucket of air filtering |
| CN109893959A (en) * | 2019-04-23 | 2019-06-18 | 江苏博润通科技有限公司 | A kind of gas cooling water treatment plant |
| CN110523189A (en) * | 2019-08-27 | 2019-12-03 | 安徽江淮汽车集团股份有限公司 | Gas cleaning plant |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20110330 |