CN204051324U - A kind of continuous reformer gas-liquid coalescer - Google Patents
A kind of continuous reformer gas-liquid coalescer Download PDFInfo
- Publication number
- CN204051324U CN204051324U CN201420301900.5U CN201420301900U CN204051324U CN 204051324 U CN204051324 U CN 204051324U CN 201420301900 U CN201420301900 U CN 201420301900U CN 204051324 U CN204051324 U CN 204051324U
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- China
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- cylindrical shell
- cylinder
- filter
- liquid
- inlet plenum
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Abstract
The utility model discloses a kind of continuous reformer gas-liquid coalescer, comprise coalescent cylinder and be fixed on the filter assemblies in coalescent cylinder, cylindrical shell top is provided with fast opening blind, bottom has end socket, medium inlet is had on the downside of cylindrical shell, upside has media outlet, cylinder body bottom is provided with sewage draining exit, cylindrical shell is provided with liquid level gauge, described filter assemblies comprises that to be fixed on inside cylindrical shell upper, lower seal plate, on, cylinder intracorporeal space is divided into discharge chamber by lower seal plate from top to bottom, filter chamber and inlet plenum, discharge chamber, inlet plenum is communicated to together by the screen pipe of filter chamber.In the technical program, gas-liquid mixed shape contaminated-fluid enters filter chamber by inlet plenum, and its liquid particles and solid particle are removed and be deposited to device bottom by filter chamber, observe soiling solution situation at any time by liquid level gauge, to open sewage draining exit discharging soiling solution.
Description
Technical field
The utility model belongs to pollutant purification treatment technology apparatus field, especially relates to a kind of continuous reformer gas-liquid coalescer.
Background technology
The filter that current filtration art adopts generally adopts straight tube filter core to filter, this filter type, because gas-liquid just directly enters filter core without pretreatment, cause filter element life short, and gas-liquid does not have sufficient disengaging time to mix again in filtration agglomeration process, cause it more not easily by coalescent purification, reduce service efficiency.
Utility model content
Being not easy more renew cartridge, self-filtering weak effect to make up above-mentioned coalescer, cannot reaching the defect of filtering requirement, the utility model proposes one, can to carry out preliminary gas-liquid separation coalescent, has the continuous reformer gas-liquid coalescer of better filter effect.
The technical scheme realizing above-mentioned beneficial effect is, a kind of continuous reformer gas-liquid coalescer, comprise coalescent cylinder and be fixed on the filter assemblies in coalescent cylinder, cylindrical shell top is provided with fast opening blind, bottom is provided with end socket, medium inlet is had on the downside of cylindrical shell, upside has media outlet, cylinder body bottom is provided with sewage draining exit, cylindrical shell is provided with liquid level gauge, described filter assemblies comprises that to be fixed on inside cylindrical shell upper, lower seal plate, on, cylinder intracorporeal space is divided into discharge chamber by lower seal plate from top to bottom, filter chamber and inlet plenum, discharge chamber, inlet plenum is communicated to together by the screen pipe of filter chamber.In the technical program, gas-liquid mixed shape contaminated-fluid enters filter chamber by inlet plenum, and its liquid particles and solid particle are removed and be deposited to device bottom by filter chamber, observe soiling solution situation at any time by liquid level gauge, to open sewage draining exit discharging soiling solution.
Described screen pipe is also divided into the stay pipe of bottom and the filter tube at top, and stay pipe is Collapsible structure.In the technical program, stay pipe, filter tube are all hermetically-sealed constructions, filter core is the main thoroughfare that gas enters exhaust chamber, pollutant trickle in gas is responsible for filter, the coalescent purification of the spray film that gas is carried, the effect of part gas-liquid separation then born by stay pipe, by the gas-liquid separation in stay pipe of gas-liquid mixed contaminated-fluid, gas upwards enters filter tube, liquid and macromolecule contaminant are deposited to cylinder body bottom by stay pipe, adopt the structure of fast opening blind simultaneously, be convenient to the replacing of filter core and maintenance.Simultaneously stay pipe is Collapsible structure, is convenient to the replacing of filter core and stay pipe and maintenance.
In cylindrical shell, be also provided with differential pressure indicator, two induction end of differential pressure indicator are set together with inlet plenum and discharge chamber respectively.Whether, in the technical program, the pressure state of inlet plenum and discharge chamber monitored at any time by differential pressure indicator, judge whether filter core blocks and leak gas, occurring overhauling inside when pressure exceeds normal range (NR).
Accompanying drawing explanation
Fig. 1 is the structural representation of a kind of embodiment of the present utility model;
In figure, 1, coalescent cylinder; 2, filter assemblies; 21, upper sealing panel; 22, lower seal plate; 23, discharge chamber; 24, filter chamber; 25, inlet plenum; 26, screen pipe; 261, stay pipe; 262, filter tube; 3, end socket; 4, medium inlet; 5, media outlet; 6, sewage draining exit; 7, liquid level gauge; 8, differential pressure indicator; 9, fast opening blind.
Detailed description of the invention
Utility model content is further illustrated below in conjunction with specific embodiment.
Composition graphs 1, a kind of embodiment of the utility model.With reference to Fig. 1, a kind of continuous reformer gas-liquid coalescer, the filter assemblies 2 comprising coalescent cylinder 1 and be fixed in coalescent cylinder, cylindrical shell top is provided with fast opening blind 9, bottom is provided with end socket 3, medium inlet 4 is had on the downside of cylindrical shell, upside has media outlet 5, cylinder body bottom is provided with sewage draining exit 6, cylindrical shell is provided with liquid level gauge 7, described filter assemblies comprises the upper sealing panel 21 be fixed on inside cylindrical shell, lower seal plate 22, on, cylinder intracorporeal space is divided into discharge chamber 23 by lower seal plate from top to bottom, filter chamber 24 and inlet plenum 25, discharge chamber, inlet plenum is communicated to together by the screen pipe 26 of filter chamber.
In the present embodiment, described screen pipe is also divided into the stay pipe 261 of bottom and the filter tube 262 at top, and stay pipe is Collapsible structure.
In cylindrical shell, be also provided with differential pressure indicator 8, two induction end of differential pressure indicator are set together with inlet plenum and discharge chamber respectively.
In the utility model, bottom filter chamber, sidewall locations also has little sewage draining exit, and some leaked to the liquid of filter chamber of little sewage draining exit is got rid of, and prevents the filter tube of its contaminated filter indoor.
The utility model adopts vertical structure, by filter assemblies, equipment is divided into upper and lower two chambers.Medium leads to the change in access device space of access arrangement inside, and the flow regime of medium and speed are changed, and the drop having part free state or larger particles is separated, and the liquid be separated can be deposited to bottom.Hydrops situation can be monitored by liquid level gauge, after liquid level reaches certain scale, can discharge from sewage draining exit.The medium carrying dust and spray film enters filter tube, flow to outer surface flowing from the inner surface of filter core and carry out filtration and coalescent, through the discharge chamber of the medium access arrangement of cleaning process, hydrops situation can be monitored by liquid level gauge, after liquid level reaches certain scale, can discharge from sewage draining exit.The working condition of filter tube, can be monitored by differential pressure indicator.When difference gauge reaches certain numerical value, represent that needs are changed.
The foregoing is only the embodiment of the utility model the best, for a person skilled in the art, the utility model can have various modifications and variations.All within spirit of the present utility model and principle, any amendment done, equivalent replacement, improvement etc., all should be included within protection domain of the present utility model.
Claims (3)
1. a continuous reformer gas-liquid coalescer, comprise coalescent cylinder (1) and be fixed on the filter assemblies (2) in coalescent cylinder, cylindrical shell top is provided with fast opening blind (9), bottom is provided with end socket (3), medium inlet (4) is had on the downside of cylindrical shell, upside has media outlet (5), cylinder body bottom is provided with sewage draining exit (6), cylindrical shell is provided with liquid level gauge (7), it is characterized in that, described filter assemblies comprises that to be fixed on inside cylindrical shell upper, lower seal plate (21, 22), on, cylinder intracorporeal space is divided into discharge chamber (23) by lower seal plate from top to bottom, filter chamber (24) and inlet plenum (25), discharge chamber, inlet plenum is communicated to together by the screen pipe (26) of filter chamber.
2. continuous reformer gas-liquid coalescer according to claim 1, is characterized in that, described screen pipe is also divided into the stay pipe (261) of bottom and the filter tube (262) at top, and stay pipe is Collapsible structure.
3. continuous reformer gas-liquid coalescer according to claim 1, is characterized in that, is also provided with differential pressure indicator (8) in cylindrical shell, and two induction end of differential pressure indicator are set together with inlet plenum and discharge chamber respectively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420301900.5U CN204051324U (en) | 2014-06-09 | 2014-06-09 | A kind of continuous reformer gas-liquid coalescer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420301900.5U CN204051324U (en) | 2014-06-09 | 2014-06-09 | A kind of continuous reformer gas-liquid coalescer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204051324U true CN204051324U (en) | 2014-12-31 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420301900.5U Expired - Fee Related CN204051324U (en) | 2014-06-09 | 2014-06-09 | A kind of continuous reformer gas-liquid coalescer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204051324U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109260853A (en) * | 2018-11-21 | 2019-01-25 | 沈阳鑫联石化设备有限公司 | A kind of boat coal filter separator |
| CN109569165A (en) * | 2019-01-18 | 2019-04-05 | 安徽沃特普尔节能科技有限公司 | A kind of reciprocal device for filtering other ions in ammonia |
-
2014
- 2014-06-09 CN CN201420301900.5U patent/CN204051324U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109260853A (en) * | 2018-11-21 | 2019-01-25 | 沈阳鑫联石化设备有限公司 | A kind of boat coal filter separator |
| CN109569165A (en) * | 2019-01-18 | 2019-04-05 | 安徽沃特普尔节能科技有限公司 | A kind of reciprocal device for filtering other ions in ammonia |
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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: 20141231 Termination date: 20190609 |