CN206439627U - A kind of liquid dirt separates air accumulator - Google Patents
A kind of liquid dirt separates air accumulator Download PDFInfo
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- CN206439627U CN206439627U CN201720085855.8U CN201720085855U CN206439627U CN 206439627 U CN206439627 U CN 206439627U CN 201720085855 U CN201720085855 U CN 201720085855U CN 206439627 U CN206439627 U CN 206439627U
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- spiral plate
- liquid
- dust
- plate
- filtration
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Abstract
The utility model provides a kind of liquid dirt and separates air accumulator, including tank body, liquid dust separating device and depositing dust adsorption plate, liquid dust separating device and depositing dust adsorption plate are setting up and down in tank body, liquid dust separating device includes the liquid guide flow spiral plate and the first dust removal and filtration spiral plate being staggered, conduit is provided with the lower edge of liquid guide flow spiral plate, conduit lower end is passed through in tank base, air inlet and gas outlet through depositing dust adsorption plate and is respectively provided with the second dust removal and filtration spiral plate.Advantage is：, can effective dust removal and filtration in gas inlet and outlet air accumulator；After gas enters tank inner chamber by air inlet, the first dust removal and filtration spiral plate can carry out secondary filter dedusting to gas；Condensation vapor in tank body in gas into drop, under liquid guide flow spiral plate spiral flow, dust removal and filtration plate will not be touched, prevent from being mixed with dust and impurity in hydrops, it is to avoid dirt is formed；Effectively the dust and impurity in the gas of standing can be again collected by filtration.
Description
Technical field
The utility model is related to air accumulator technical field, more particularly to a kind of liquid dirt separation air accumulator.
Background technology
Air accumulator refers to the equipment for being specifically used to store gas, while playing systems stabilisation pressure, according to air accumulator
Bear pressure difference and can be divided into high pressure tank, low pressure gasholder, normal pressure air accumulator.Air accumulator difference point：Carbon steel is stored up
Gas tank, low-alloy steel air accumulator, stainless steel air accumulator.Air accumulator（Pressure vessel）It is general by cylinder, it is end socket, flange, adapter, close
Seal the part and assembly such as element and bearing composition.In addition, being also equipped with safety device, meter and completing various processes effect
Internals.
Existing air accumulator, due to being inherently mingled with this dust and steam in gas, is entering gas storage when storing gas
During tank, air accumulator is difficult to carry out dedusting dehumidifying to the gas of inflow in time in itself, meanwhile, when in tank body to gas pressure testing or tank
During temperature reduction, the steam in tank body in gas can condense into drop in inner tank wall, and be flowed down along inner tank wall, though
During some right built in gas tank have a screen pack, but drop is flowed down can inclusion of dirt, and dirt is formed, when hydrops in tank body
During discharge, dirt can easily cause discharge outlet control valve it is stuck, it is necessary to the long period carry out unpick and wash replacing, take time and effort.
The content of the invention
To solve the above problems, separating air accumulator the utility model discloses a kind of liquid dirt.
In order to reach object above, the utility model provides following technical scheme：
A kind of liquid dirt separates air accumulator, it is characterised in that：It is described including tank body, liquid dust separating device and depositing dust adsorption plate
Tank body is provided with air inlet, gas outlet and sewage draining exit, and the liquid dust separating device and depositing dust adsorption plate are setting up and down in tank body,
The liquid dust separating device includes the liquid guide flow spiral plate and the first dust removal and filtration spiral plate set along tank body axial direction, institute
Liquid guide flow spiral plate is stated to be staggered with the first dust removal and filtration spiral plate, and the upper and lower ends of liquid guide flow spiral plate are longer than
The outer ledge of the upper and lower ends of first dust removal and filtration spiral plate, the liquid guide flow spiral plate and the first dust removal and filtration spiral plate
It is close to inner tank wall setting, the lower end of the first dust removal and filtration spiral plate is higher than the top of air inlet, the liquid guide flow
Conduit is provided with the lower edge of spiral plate, the conduit upper end is located at the lower end of liquid guide flow spiral plate, and conduit lower end is passed through
Depositing dust adsorption plate, which is passed through in tank base, the air inlet and gas outlet, is respectively provided with the second dust removal and filtration spiral plate.
Further, the depositing dust adsorption plate is adapted with inner tank wall, and depositing dust adsorption plate is provided with and mutually fitted with conduit
The through hole matched somebody with somebody.
Further, the second dust removal and filtration spiral plate in the air inlet and gas outlet is respectively along air inlet and outlet
The axial direction of mouth is set.
Further, the liquid guide flow spiral plate and inner tank wall angle are 60~85 °.
Further, the tank base is provided with support.
Further, filter bores are equipped with the first dust removal and filtration spiral plate and the second dust removal and filtration spiral plate.
Further, the depositing dust adsorption plate is provided with adsorption layer.
Compared with prior art, the beneficial effects of the utility model are：Gas is entering air accumulator from air inlet and gone out
When gas port discharges air accumulator, dust removal and filtration is carried out by the second dust removal and filtration spiral plate, so as to not only enter gas storage in gas
During tank, effective dust removal and filtration is carried out, moreover it is possible to when gas discharges air accumulator, dust removal and filtration is carried out again, the matter of gas is improved
Amount；After gas enters tank inner chamber by air inlet, along the first dust removal and filtration spiral plate spiral, and in uphill process
In, the first dust removal and filtration spiral plate effectively can carry out secondary filter dedusting to the gas entered in tank body, further reduce gas
In the impurity content such as dust；When to gas pressure testing or pot temperature reduction, steam in tank body in gas can be in tank body
Condense into drop in inner tank wall, and along inner tank wall flow down when, drop can be first flowed on liquid guide flow spiral plate, and
Due to being inclined upwardly on the inside of liquid guide flow plate and tank body, the edge that drop can be contacted along liquid guide flow spiral plate with tank body
Under spiral flow, in the conduit for being then imported into liquid guide flow spiral plate lower end, and tank base is flowed to eventually through conduit；Pass through
The depositing dust adsorption plate below liquid dust separating device is arranged in tank body, after gas stands a period of time in tank body, is floated in gas
Floating dust and impurity gradually fall under gravity, after falling on depositing dust adsorption plate, and dust and impurity are adsorbed by adsorption layer,
So as to which effectively the dust and impurity in the gas of standing be collected by filtration again；By by the upper and lower ends of liquid guide flow spiral plate
The upper and lower ends for being longer than the first dust removal and filtration spiral plate are respectively provided with, and the conduit for conducting fluid is arranged through depositing dust and are inhaled
Attached plate, can effectively play liquid and collect and the first dust removal and filtration spiral plate and depositing dust adsorption plate will not be touched in flow process
On dust, so as to effectively prevent from being mixed with dust and impurity in hydrops, it is to avoid dirt is formed, play protection draining control valve work
With.
Brief description of the drawings
Fig. 1 is the structural representation that a kind of liquid dirt of the utility model separates air accumulator.
Fig. 2 is the structural representation of liquid guide flow spiral plate and tank body angle in a kind of liquid dirt separation air accumulator of the utility model
Figure.
Fig. 3 is the structural representation of depositing dust adsorption plate in a kind of liquid dirt separation air accumulator of the utility model.
Reference numerals list：
1- tank bodies, 11- air inlets, 12- gas outlets, 13- sewage draining exits, 2- liquid dust separating devices, 21- liquid guide flow spirals
Plate, 22- the first dust removal and filtration spiral plates, 3- depositing dust adsorption plates, 31- adsorption layers, 32- through holes, 4- conduits, the dust removal and filtrations of 5- second
Spiral plate, 6- supports, 7- filter bores.
Embodiment
With reference to the accompanying drawings and detailed description, the utility model is further elucidated, it should be understood that following specific embodiment parties
Formula is merely to illustrate the utility model rather than limits scope of the present utility model.
As illustrated, a kind of liquid dirt separation air accumulator, including tank body 1, liquid dust separating device 2 and depositing dust adsorption plate 3, tank body
1 is provided with air inlet 11, gas outlet 12 and sewage draining exit 13, and liquid dust separating device 2 and depositing dust adsorption plate 3 are setting up and down in tank body 1
Interior, liquid dust separating device 2 includes the dust removal and filtration spiral plate of liquid guide flow spiral plate 21 and first set along the axial direction of tank body 1
22, liquid guide flow spiral plate 21 is staggered with the first dust removal and filtration spiral plate 22, and up and down the two of liquid guide flow spiral plate 21
End is longer than the upper and lower ends of the first dust removal and filtration spiral plate 22, the dust removal and filtration spiral plate 22 of liquid guide flow spiral plate 21 and first
Outer ledge be close to the setting of the inwall of tank body 1, the lower end of the first dust removal and filtration spiral plate 22 is higher than the top of air inlet 11, liquid
Conduit 4 is provided with the lower edge of body water conservancy diversion spiral plate 21, the upper end of conduit 4 is located at the lower end of liquid guide flow spiral plate 21, conduit 4
Lower end is passed through in the bottom of tank body 1, air inlet 11 and gas outlet 12 through depositing dust adsorption plate 3 and is respectively provided with the second dust removal and filtration spiral shell
Rotating plate 5.Wherein, depositing dust adsorption plate 3 is adapted with the inwall of tank body 1, and depositing dust adsorption plate 3 is provided with what is be adapted with conduit 4
The second dust removal and filtration spiral plate 5 in through hole 32, air inlet 11 and gas outlet 12 is respectively along air inlet 11 and gas outlet 12
Axial direction is set.
Gas passes through the second dust removal and filtration spiral shell when entering air accumulator and the discharge air accumulator of gas outlet 12 from air inlet 11
Rotating plate 5 carries out dust removal and filtration, so as to not only carry out effective dust removal and filtration when gas enters air accumulator, moreover it is possible in gas row
When going out air accumulator, dust removal and filtration is carried out again, improves the quality of gas；After gas enters the inner chamber of tank body 1 by air inlet 11,
Along the spiral of the first dust removal and filtration spiral plate 22, and in uphill process, the first dust removal and filtration spiral plate 22 can be effectively right
Secondary filter dedusting is carried out into the gas in tank body, further the impurity content such as dust in reduction gas.In the present embodiment
In, filter bores 7 are equipped with the first dust removal and filtration spiral plate 22 and the second dust removal and filtration spiral plate 5, effectively can be filtered in gas
Dust and impurity.
Meanwhile, it is longer than the first dust removal and filtration spiral plate 22 by the way that the upper and lower ends of liquid guide flow spiral plate 21 are respectively provided with
Upper and lower ends, and the conduit 4 for conducting fluid is arranged through depositing dust adsorption plate 3, can effectively play liquid collecting and
The first dust removal and filtration spiral plate 22 and dust and impurity on depositing dust adsorption plate 3 will not be touched in flow process, so that effectively
Prevent from being mixed with dust and impurity in hydrops, it is to avoid dirt is formed, play a part of protecting draining control valve.
When being reduced in tank body 1 to gas pressure testing or pot temperature, the steam in tank body 1 in gas can be in the inwall of tank body 1
On condense into drop, and along the inwall of tank body 1 flow down when, drop can be first flowed on liquid guide flow spiral plate 21, and due to
The inner side of liquid guide flow plate 21 is inclined upwardly, and the upper surface of liquid guide flow plate 21 and the inwall angle of tank body 1 are at an acute angle, and drop can be suitable
Under the edge spiral flow that liquid guide flow spiral plate 21 is contacted with tank body 1, be then imported into the lower end of liquid guide flow spiral plate 21
Conduit 4 in, and flow to the bottom of tank body 1 eventually through conduit 4.In the present embodiment, in liquid guide flow spiral plate 21 and tank body 1
Wall angle is 60~85 °, and angle preferably is 80 °, but those skilled in the art also can select other angles.
A kind of depositing dust adsorption plate 3 of liquid dirt separation air accumulator of the utility model is provided with adsorption layer 31, when gas in tank body
Stand after a period of time, the dust and impurity floated in gas gradually falls under gravity, falls and is being arranged on liquid in tank body 1
The depositing dust adsorption plate 3 of the lower section of dust separating device 2, and adsorption layer 31 on depositing dust adsorption plate 3 adsorbs dust and impurity, so as to have
Dust and impurity in the gas of standing is collected by filtration effect again.
The bottom of tank body 1 of the present utility model is provided with support 6.
Technological means disclosed in the utility model scheme is not limited only to the technological means disclosed in above-mentioned embodiment, also
Including being combined constituted technical scheme by above technical characteristic.It should be pointed out that for the ordinary skill of the art
For personnel, on the premise of the utility model principle is not departed from, some improvements and modifications can also be made, these improve and moistened
Decorations are also considered as protection domain of the present utility model.
Claims (7)
1. a kind of liquid dirt separates air accumulator, it is characterised in that：Including tank body（1）, liquid dust separating device（2）With depositing dust adsorption plate
（3）, the tank body（1）It is provided with air inlet（11）, gas outlet（12）And sewage draining exit（13）, the liquid dust separating device（2）With
Depositing dust adsorption plate（3）It is setting up and down in tank body（1）It is interior, the liquid dust separating device（2）Including along tank body（1）Axial direction is set
Liquid guide flow spiral plate（21）With the first dust removal and filtration spiral plate（22）, the liquid guide flow spiral plate（21）With the first dedusting
Filtering screw plate（22）It is staggered, and liquid guide flow spiral plate（21）Upper and lower ends be longer than the first dust removal and filtration spiral plate
（22）Upper and lower ends, the liquid guide flow spiral plate（21）With the first dust removal and filtration spiral plate（22）Outer ledge be close to
Tank body（1）Inwall is set, the first dust removal and filtration spiral plate（22）Lower end be higher than air inlet（11）Top, the liquid
Water conservancy diversion spiral plate（21）Lower edge at be provided with conduit（4）, the conduit（4）Upper end is located at liquid guide flow spiral plate（21）'s
Lower end, conduit（4）Lower end passes through depositing dust adsorption plate（3）It is passed through tank body（1）Bottom, the air inlet（11）And gas outlet（12）It is interior
Respectively it is provided with the second dust removal and filtration spiral plate（5）.
2. a kind of liquid dirt separation air accumulator according to claim 1, it is characterised in that：The depositing dust adsorption plate（3）With tank
Body（1）Inwall is adapted, and depositing dust adsorption plate（3）It is provided with and conduit（4）The through hole being adapted（32）.
3. a kind of liquid dirt separation air accumulator according to claim 1, it is characterised in that：The air inlet（11）And gas outlet
（12）The second interior dust removal and filtration spiral plate（5）Respectively along air inlet（11）And gas outlet（12）Axial direction set.
4. a kind of liquid dirt separation air accumulator according to claim 1, it is characterised in that：The liquid guide flow spiral plate（21）
Inner side phase on tilt, and and tank body（1）Inwall angle is 60~85 °.
5. a kind of liquid dirt separation air accumulator according to claim 1, it is characterised in that：The tank body（1）Bottom is provided with branch
Frame（6）.
6. a kind of liquid dirt separation air accumulator according to claim 1, it is characterised in that：The first dust removal and filtration spiral plate
（22）With the second dust removal and filtration spiral plate（5）On be equipped with filter bores（7）.
7. a kind of liquid dirt separation air accumulator according to claim 1, it is characterised in that：The depositing dust adsorption plate（3）On set
There is adsorption layer（31）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720085855.8U CN206439627U (en) | 2017-01-23 | 2017-01-23 | A kind of liquid dirt separates air accumulator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720085855.8U CN206439627U (en) | 2017-01-23 | 2017-01-23 | A kind of liquid dirt separates air accumulator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206439627U true CN206439627U (en) | 2017-08-25 |
Family
ID=59635388
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720085855.8U Expired - Fee Related CN206439627U (en) | 2017-01-23 | 2017-01-23 | A kind of liquid dirt separates air accumulator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206439627U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107588319A (en) * | 2017-10-17 | 2018-01-16 | 上海市奉贤设备容器厂 | A kind of energy-conserving and environment-protective vibration damping air accumulator |
-
2017
- 2017-01-23 CN CN201720085855.8U patent/CN206439627U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107588319A (en) * | 2017-10-17 | 2018-01-16 | 上海市奉贤设备容器厂 | A kind of energy-conserving and environment-protective vibration damping air accumulator |
| CN107588319B (en) * | 2017-10-17 | 2023-11-03 | 上海市奉贤设备容器厂有限公司 | Energy-saving environment-friendly vibration reduction air storage tank |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170825 Termination date: 20180123 |
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| CF01 | Termination of patent right due to non-payment of annual fee |