CN206970257U - A kind of 2 naphthols negative pressure water separation devices - Google Patents
A kind of 2 naphthols negative pressure water separation devices Download PDFInfo
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- CN206970257U CN206970257U CN201720929815.7U CN201720929815U CN206970257U CN 206970257 U CN206970257 U CN 206970257U CN 201720929815 U CN201720929815 U CN 201720929815U CN 206970257 U CN206970257 U CN 206970257U
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- pipe
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- surge tank
- fluid reservoir
- pressure water
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Abstract
The utility model discloses a kind of 2 naphthols negative pressure water separation devices, belong to technical field of chemical production equipment, including vavuum pump, surge tank, fluid reservoir and the treatment fluid mouth of pipe, it is characterized in that the surge tank is arranged to capsule shape tank body, the vacuum mouth of pipe is connected by breather line with vavuum pump, and vacuum tube open height is not less than 10.336 meters, and gas-liquid separator is set in pipeline, the structure type that described fluid reservoir is arranged to close or opened wide, the beneficial effects of the utility model are：Vacuum tube open height is not less than 10.336 meters, using the principle of atmospheric pressure water column, can make to produce vacuum above surge tank, prevents that treatment fluid overflows pollution vavuum pump in surge tank；The gas-liquid separator adds the efficiency for the treatment of fluid gas separation；The structure type that described fluid reservoir is arranged to close or opened wide, add the applicability of device.
Description
Technical field
The utility model belongs to technical field of chemical, relates more specifically to a kind of beta naphthal negative pressure water separation device.
Background technology
Contain substantial amounts of waste gas in beta naphthal waste water, it is necessary to waste gas be discharged using vavuum pump, it is at present to use vavuum pump more
Add the structure of surge tank, but due to the finite capacity of surge tank, it is easy to occur to overflow after surge tank is full of and pollute vacuum
The problem of pump.
At present, it is more using periodically solving the method for the discharge of materials in surge tank in order to solve this problem, not only
Waste time and energy, and if once having delayed drain time, then be easy to pollute vavuum pump, or even cause the damage of vavuum pump.
The content of the invention
To solve the above problems, overcome the deficiencies in the prior art, the utility model provides one kind and effectively prevents from buffering
Tank is overfilled with polluting the beta naphthal negative pressure water separation device of vavuum pump, can effectively solve dirty because surge tank is overfilled with
The problem of contaminating vavuum pump.
The utility model solve above-mentioned technical problem concrete technical scheme be：Described beta naphthal negative pressure water separation dress
Put, including vavuum pump, surge tank, fluid reservoir and the treatment fluid mouth of pipe, it is characterised in that the surge tank is arranged to capsule shape tank body,
Surge tank upper end sets the vacuum mouth of pipe, and the lower end of surge tank sets the charging mouth of pipe, and the lower section of surge tank sets fluid reservoir, described true
Blank pipe mouth is connected by breather line with vavuum pump, and the treatment fluid mouth of pipe, the processing are set between the surge tank and fluid reservoir
Liquid pipe mouth is connected with the charging mouth of pipe and fluid reservoir respectively by pipeline, and the pipeline extends to fluid reservoir inner bottom, described true
Blank pipe open height is not less than 10.336 meters.
Further, the described treatment fluid mouth of pipe is provided with gas-liquid separator.
Further, the structure type that described fluid reservoir is arranged to close or opened wide.
The beneficial effects of the utility model are：The vacuum tube open height is not less than 10.336 meters, utilizes atmospheric pressure water column
Principle, can make to produce vacuum above surge tank, prevent that treatment fluid overflows pollution vavuum pump in surge tank；The gas-liquid separation
Device adds the efficiency for the treatment of fluid gas separation；The structure type that described fluid reservoir is arranged to close or opened wide, is added
The applicability of device.
Brief description of the drawings：
Accompanying drawing 1 is the utility model structure diagram；In accompanying drawing：
1. fluid reservoir, the 2. treatment fluid mouths of pipe, the 3. charging mouths of pipe, the 4. vacuum mouths of pipe, 5. surge tanks, 6. vavuum pumps.
Embodiment：
To make the purpose, technical scheme and advantage that the utility model is implemented clearer, referring now to accompanying drawing 1 more comprehensively
Ground describes.In to description of the present utility model, it is to be understood that term " " center ", " on ", " under ", "left", "right",
The orientation or position relationship of the instruction such as " rear ", " lower-left ", " upper right ", " outer " be based on orientation shown in the drawings or position relationship,
It is for only for ease of description the utility model and simplifies and describe, rather than indicates or imply that signified device or element must have
Specific orientation, with specific azimuth configuration and operation, therefore it is not intended that limitation to scope of protection of the utility model.This
Outside, term " first ", " second ", " the 3rd " are only used for describing purpose, and it is not intended that instruction or hint relative importance.
Specific embodiment of the present utility model：Described beta naphthal negative pressure water separation device, including vavuum pump 6, buffering
Tank 5, fluid reservoir 1 and the treatment fluid mouth of pipe 2, it is characterised in that the surge tank 5 is arranged to capsule shape tank body, and the upper end of surge tank 5 is set
The vacuum mouth of pipe 4 is put, the lower end of surge tank 5 sets the charging mouth of pipe 3, and the lower section of surge tank 5 sets fluid reservoir 1, the vacuum mouth of pipe 4
It is connected by breather line with vavuum pump 6, the treatment fluid mouth of pipe 2, the treatment fluid is set between the surge tank 5 and fluid reservoir 1
The mouth of pipe 2 is connected with the charging mouth of pipe 3 and fluid reservoir 1 respectively by pipeline, and the pipeline extends to the inner bottom of fluid reservoir 1, described
The height of the vacuum mouth of pipe 4 is not less than 10.336 meters.
Further, the described treatment fluid mouth of pipe 2 is provided with gas-liquid separator.
Further, the structure type that described fluid reservoir 1 is arranged to close or opened wide.
In use, concrete operations are as follows：
1. the pending liquid of gas-liquid mixed is transferred to surge tank 5 and fluid reservoir 1 by the treatment fluid mouth of pipe 2 through pipeline；
2. because containing substantial amounts of gas in treatment fluid, efficiently separated in gas-liquid separator, when the liquid level of surge tank 5 constantly rises
Height, because atmospheric pressure is approximately equal to 10.336 meter water columns, then after the liquid level of surge tank 5 is increased to 10.336 meters, no longer rise, above water column
Region of no pressure is produced, effectively prevents the water level of surge tank 5 from overflowing, pollutes vavuum pump 6.
Claims (3)
1. a kind of beta naphthal negative pressure water separation device, including vavuum pump（6）, surge tank（5）, fluid reservoir（1）With the treatment fluid mouth of pipe
（2）, it is characterised in that the surge tank（5）It is arranged to capsule shape tank body, surge tank（5）Upper end sets the vacuum mouth of pipe（4）, buffering
Tank（5）Lower end set charging the mouth of pipe（3）, surge tank（5）Lower section set fluid reservoir（1）, the vacuum mouth of pipe（4）By logical
Feed channel and vavuum pump（6）It is connected, the surge tank（5）And fluid reservoir（1）Between set the treatment fluid mouth of pipe（2）, the processing
Liquid pipe mouth（2）By pipeline respectively with feeding the mouth of pipe（3）And fluid reservoir（1）It is connected, the pipeline extends to fluid reservoir（1）It is internal
Bottom, the vacuum mouth of pipe（4）Highly it is not less than 10.336 meters.
2. beta naphthal negative pressure water separation device according to claim 1, it is characterised in that the described treatment fluid mouth of pipe（2）If
It is equipped with gas-liquid separator.
3. beta naphthal negative pressure water separation device according to claim 1, it is characterised in that described fluid reservoir（1）It is arranged to
Closing or unlimited structure type.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720929815.7U CN206970257U (en) | 2017-07-28 | 2017-07-28 | A kind of 2 naphthols negative pressure water separation devices |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720929815.7U CN206970257U (en) | 2017-07-28 | 2017-07-28 | A kind of 2 naphthols negative pressure water separation devices |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206970257U true CN206970257U (en) | 2018-02-06 |
Family
ID=61397844
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720929815.7U Active CN206970257U (en) | 2017-07-28 | 2017-07-28 | A kind of 2 naphthols negative pressure water separation devices |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206970257U (en) |
-
2017
- 2017-07-28 CN CN201720929815.7U patent/CN206970257U/en active Active
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