CN205528647U - Separator - Google Patents
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- CN205528647U CN205528647U CN201620255304.7U CN201620255304U CN205528647U CN 205528647 U CN205528647 U CN 205528647U CN 201620255304 U CN201620255304 U CN 201620255304U CN 205528647 U CN205528647 U CN 205528647U
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- filter material
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- Separating Particles In Gases By Inertia (AREA)
- Filtering Of Dispersed Particles In Gases (AREA)
Abstract
The utility model discloses a separator belongs to machinery. Separator includes: the cylinder is provided with miscellaneous gas entry, net gas export and sundry outlet on, miscellaneous gas entry sets up the lateral wall at the cylinder, and the net gas export sets up respectively at the both ends of cylinder with sundry outlet, and the distance of net gas export and the face placed is greater than sundry outlet and a distance of placing, sundry outlet is last be provided with can shutoff sundry outlet the shutoff door, be provided with the first filter material layer of tube -shape in the cylinder, the export of first filter material layer shutoff net gas, first filter material layer by lurex, glass fiber, polytetrafluoroethylene fibre, mekralon and the at least a manufacturing in predetermineeing the fibre form, predetermine the fibre for hydrophilic oil transportation material or the hydrophobic material of oleophylic. The utility model provides a relatively poor problem of effect of debris separation, improved the effect of debris separation, the utility model is used for the debris separation of the natural gas.
Description
Technical field
This utility model relates to mechanical field, particularly to a kind of separator.
Background technology
By natural gas from underground mining out after, need with pipeline, mined natural gas to be carried,
During natural gas carries, in natural gas, meeting is doped with foreign material such as the grains of sand, welding slag, corrosion, oil and water,
Therefore, before using natural gas, need from natural gas, separate foreign material.
In correlation technique, separator is used the natural gas doped with foreign material to be processed, by foreign material from natural
Gas is separated.Concrete, separator is to be provided with entrance, natural gas on tubular, and separator
Outlet and miscellaneous object outlet, wherein, gas outlet and miscellaneous object outlet are separately positioned on the two ends of separator, enter
Mouth is arranged on the side of separator, and gas outlet is compared to miscellaneous object outlet, further from placed side.Using
During separator, the natural gas doped with foreign material can be inputted this separator from entrance so that natural gas is dividing
Carrying out eddy flow in device, and during eddy flow, the foreign material that the particle diameter that is entrained in natural gas is bigger are subject to
The effect of centrifugal force, can collide with the inwall of separator, and assemble on the inwall of separator, then at weight
Flow out from the miscellaneous object outlet of separator under the effect of power.And due to the lighter in weight of natural gas, so natural gas
Can flow out from gas outlet, it is achieved thereby that foreign material bigger for particle diameter are separated with natural gas.
Owing to the foreign material in natural gas comprise the bigger foreign material of particle diameter and the less foreign material of particle diameter, relevant skill simultaneously
Separator in art is merely capable of separating foreign material bigger for particle diameter from natural gas, and cannot be to natural
The foreign material that particle diameter in gas is less are separated from natural gas, therefore, from gas outlet flow out natural
Still doped with more foreign material in gas, the effect that foreign material separate is poor.
Utility model content
The problem poor in order to solve the effect of foreign material separation, this utility model provides a kind of separator.Institute
State technical scheme as follows:
Providing a kind of separator, described separator includes: cylinder, and described cylinder is provided with miscellaneous QI
The outlet of entrance, clean gas and miscellaneous object outlet,
Described miscellaneous QI entrance is arranged on the sidewall of described cylinder, and the outlet of described clean gas and described miscellaneous object outlet divide
It is not arranged on the two ends of described cylinder, and the outlet of described clean gas goes out more than described foreign material with the distance of placed side
Mouth and the distance of placed side, described miscellaneous object outlet is provided with block the closure gate of described miscellaneous object outlet；
Being provided with the first filter material layer of tubular in described cylinder, described first filter material layer blocks described clean gas and goes out
Mouthful, described first filter material layer by metallic fiber, glass fibre, polytetrafluoroethylene fibre, polypropylene fibre and
At least one preset in fiber is fabricated by, and described default fiber is hydrophilic oil transportation material or oleophilic drainage material
Matter.
Optionally, described miscellaneous QI entrance includes drain wall, and the wall of described drain wall is interior with described cylinder
Wall is tangent.
Optionally, in described cylinder, it is additionally provided with the adsorption layer of tubular,
Described adsorption layer blocks the outlet of described clean gas, and is arranged on described first filter material layer and the outlet of described clean gas
Between, described adsorption layer is fabricated by by least one in molecular sieve, activated carbon, silica gel and aluminium oxide.
Optionally, in described cylinder, it is additionally provided with the second filter material layer of tubular,
Described second filter material layer blocks the outlet of described clean gas, and is arranged on described adsorption layer and the outlet of described clean gas
Between, described second filter material layer is identical with the material of described first filter material layer.
Optionally, on described cylinder, the one end at described miscellaneous object outlet place is provided with liquid collecting room, described liquid collecting
Room is round platform cylinder, and the one end at the bottom surface place of described liquid collecting room is connected with described cylinder, described collection
The upper bottom surface of liquid chamber is provided with described miscellaneous object outlet, and described miscellaneous object outlet runs through the upper bottom surface of described liquid collecting room.
Optionally, described miscellaneous QI entrance is provided with inlet tube, the outlet of described clean gas is provided with the first outlet
Pipe, described inlet tube connects with described miscellaneous QI entrance, described first outlet and described clean gas outlet,
Described inlet tube is described drain wall away from the tube wall of the axis side of described cylinder, described drain wall
Wall be the described tube wall surface near the axis of described inlet tube.
Optionally, described miscellaneous object outlet is provided with the second outlet, one end of described second outlet and institute
State miscellaneous object outlet connection, and the other end of described second outlet is provided with described closure gate.
Optionally, it is provided with multiple swirl vane in described inlet tube, and each described swirl vane is with described
There is angle in the axis of inlet tube.
Optionally, the cross section of described inlet tube is annulus or Fang Huan.
Optionally, described inlet tube is scroll casing type inlet tube.
In sum, this utility model provides a kind of separator, owing to being provided with on the cylinder of separator
The first filter material layer of tubular it is provided with in the outlet of miscellaneous QI entrance, clean gas and miscellaneous object outlet, and cylinder, first
Filter material layer blocks the outlet of clean gas, be mixed with foreign material natural gas can after miscellaneous QI entrance enters in cylinder,
The foreign material that particle diameter in foreign material is bigger can be assembled at cylinder inwall, finally from miscellaneous during eddy flow
Thing outlet is flowed out, and the foreign material that particle diameter is less can be stopped by the first filter material layer flowing out from the outlet of clean gas when,
Thus assemble on the first filter material layer, and flow out from miscellaneous object outlet under gravity, so, decrease
From the natural gas that the outlet of clean gas is flowed out, the foreign material of doping, improve the effect that foreign material separate.
Accompanying drawing explanation
In order to be illustrated more clearly that the technical scheme in this utility model embodiment, embodiment will be described below
The accompanying drawing used required in is briefly described, it should be apparent that, the accompanying drawing in describing below is only this
Some embodiments of utility model, for those of ordinary skill in the art, are not paying creative work
On the premise of, it is also possible to other accompanying drawing is obtained according to these accompanying drawings.
The structural representation of the separator that Fig. 1 provides for this utility model embodiment；
The structural representation of the another kind of separator that Fig. 2 provides for this utility model embodiment；
The structural representation of a kind of liquid collecting room that Fig. 3 provides for this utility model embodiment；
The partial structurtes schematic diagram of a kind of inlet tube that Fig. 4 provides for this utility model embodiment；
The top view of a kind of separator that Fig. 5 provides for this utility model embodiment.
Detailed description of the invention
For making the purpose of this utility model, technical scheme and advantage clearer, below in conjunction with accompanying drawing to this
Utility model embodiment is described in further detail.
As it is shown in figure 1, this utility model embodiment provides a kind of separator 0, this separator 0 may include that
Cylinder 01, cylinder 01 is provided with miscellaneous QI entrance 02, clean gas outlet 03 and miscellaneous object outlet 04,
Miscellaneous QI entrance 02 is arranged on the sidewall of cylinder 01, and clean gas outlet 03 and miscellaneous object outlet 04 set respectively
Put the two ends at cylinder 01, and the distance of clean gas outlet 03 and placed side more than miscellaneous object outlet 04 and is placed
The distance in face, miscellaneous object outlet 04 is provided with closure gate 041, and closure gate 041 can block miscellaneous object outlet 04.
Being provided with the first filter material layer 05 of tubular in cylinder 01, the first filter material layer 05 blocks clean gas outlet 03,
First filter material layer 05 is by metallic fiber, glass fibre, polytetrafluoroethylene fibre, polypropylene fibre and presets fibre
At least one in dimension is fabricated by, and default fiber is hydrophilic oil transportation material or oleophilic drainage material.
In sum, this utility model embodiment provides a kind of separator, due on the cylinder of separator
The first filter material layer of tubular it is provided with in being provided with miscellaneous QI entrance, the outlet of clean gas and miscellaneous object outlet, and cylinder,
First filter material layer blocks the outlet of clean gas, and the natural gas being mixed with foreign material can enter in cylinder from miscellaneous QI entrance
After, the foreign material that particle diameter in foreign material is bigger can be assembled at cylinder inwall, finally during eddy flow
Flowing out from miscellaneous object outlet, the foreign material that particle diameter is less can be flowing out from the outlet of clean gas when, by the first filter material layer
Stop, thus assemble on the first filter material layer, and flow out from miscellaneous object outlet under gravity, so,
Decrease the foreign material of doping from the natural gas that the outlet of clean gas is flowed out, improve the effect that foreign material separate.
Optionally, miscellaneous QI entrance 02 can include drain wall (not shown in figure 1), and the wall of drain wall can
With tangent with the inwall of cylinder 01 so that at miscellaneous QI entrance 02, the flow direction of gas can with point
Tangent from the inwall of cylinder 01.Input in cylinder 01 from miscellaneous QI entrance 02 at the natural gas being blended with impurity
Time, it is mixed with the natural gas of the impurity flow direction at miscellaneous QI entrance 02 tangent with the inwall of cylinder 01,
And owing to when inputting natural gas, the flow velocity of natural gas is relatively big, so natural gas is after entering in cylinder 01
Can carry out eddy flow, and during eddy flow, the bigger foreign material of the particle diameter that is entrained in natural gas are by centrifugal
The effect of power, can collide with the inwall of cylinder, and assemble on the inwall of cylinder, then at gravity
Effect under from miscellaneous object outlet flow out.
The structural representation of the another kind of separator 0 that Fig. 2 provides for this utility model embodiment, refer to Fig. 2,
Being also provided with the adsorption layer 06 of tubular in cylinder 01, adsorption layer 06 can block clean gas outlet 03,
And adsorption layer 06 can be arranged between the first filter material layer 05 and clean gas outlet 03, adsorption layer 06 can be by
At least one in molecular sieve, activated carbon, silica gel and aluminium oxide is fabricated by, example, adsorption layer 06 energy
The water that enough absorption particle diameter is less.
Optionally, the second filter material layer 07 of tubular, the second filter material layer 07 it are also provided with in cylinder 01
Can also block clean gas outlet 03, and the second filter material layer can be arranged on adsorption layer 06 and clean gas outlet 03 it
Between, and the second filter material layer 07 is identical with the material of the first filter material layer 05.I.e. enter in cylinder 01 is natural
Gas needs to sequentially pass through the first filter material layer 05, adsorption layer 06 and the second filter material layer 07 could be from cylinder 01
Clean gas outlet 03 outflow.The foreign material that particle diameter is less cannot pass the first filter material layer 05 and the second filter material layer 07,
Adsorption layer can adsorb water so that water is assembled on adsorption layer 06, finally flows out from miscellaneous object outlet 04.
Optionally, on cylinder 01, the one end at miscellaneous object outlet 04 place can be provided with liquid collecting room 08.Specifically
, as it is shown on figure 3, liquid collecting room 08 can be frustum cone cylinder body, and bottom surface 081 place of liquid collecting room 08
One end can be connected with cylinder 01, the upper bottom surface 082 of liquid collecting room 08 can be provided with miscellaneous object outlet
04, and this miscellaneous object outlet 04 runs through the upper bottom surface 082 of liquid collecting room 08.During foreign material in separating natural gas,
Without miscellaneous object outlet 04 is opened, the foreign material (grains of sand, welding slag, corrosion, water and oil) being separated,
Under gravity, liquid collecting room 08 can be entered, when liquid collecting room 08 fills foreign material, foreign material can be gone out
Mouth 04 is opened, and is discharged by the foreign material in liquid collecting room 08.Owing to liquid collecting room 08 is round platform cylinder, so miscellaneous
When thing outlet 04 is opened, the foreign material in liquid collecting room 08 can be under gravity easier from liquid collecting room
Discharge in 08.
Seeing Fig. 2, miscellaneous QI entrance 02 can be provided with inlet tube (not shown in Fig. 2), clean gas exports
Can be provided with the first outlet 09 on 02, inlet tube connects with miscellaneous QI entrance 02, the first outlet 09 with
Clean gas outlet 03 connection, inlet tube can be drain wall away from the tube wall of the axis side of cylinder 01, and
Inlet tube is away from the surface of inlet pipe axial line close on the tube wall of the axis side of cylinder 01, with cylinder 01
Inwall tangent.The second outlet 10, one end of the second outlet 10 can be provided with on miscellaneous object outlet 04
Connect with miscellaneous object outlet 04, and the other end of the second outlet 10 is provided with closure gate 041.Example,
Need, when cylinder 01 input is mixed with the natural gas of foreign material, foreign material to be blended with by inlet tube
Natural gas input cylinder 01.When needing to discharge clean natural gas from cylinder 01, can be by first
Clean natural gas is discharged and is collected by outlet 09.Separate needing discharge from cylinder 01
During foreign material, miscellaneous object outlet 04 can be opened so that the foreign material separated can be arranged from the second outlet 10
Go out.Example, the cross section of inlet tube can be annulus or Fang Huan.
The partial structurtes schematic diagram of a kind of inlet tube M that Fig. 4 provides for this utility model embodiment, such as Fig. 4
Shown in, can be provided with multiple swirl vane M1 in inlet tube M, and each swirl vane M1 and inlet tube
Axis there is angle.Optionally, bowing of a kind of separator 0 that Fig. 5 provides for this utility model embodiment
View, as it is shown in figure 5, inlet tube M can be scroll casing type inlet tube.
When the separator using this utility model embodiment to provide, can first be blended with the natural of foreign material
Gas inputs in cylinder by inlet tube, example, if being provided with swirl vane in inlet tube, is then mixed with
The natural gas of foreign material is during entrance Bottomhole pressure, if the foreign material in natural gas touch with swirl vane
Hit, then foreign material can be assembled on swirl vane, and tentatively separates with natural gas.
Owing to the flow velocity of natural gas is relatively big, and the inwall of the flow direction of miscellaneous QI porch natural gas and cylinder
Tangent, so the natural gas being mixed with foreign material can carry out eddy flow after entering in cylinder in cylinder, mixed
The foreign material that some particle diameters of being combined in natural gas are bigger are subject to centrifugal forces during eddy flow, can hit
On the inwall of cylinder, and under gravity, the inwall along cylinder slides in liquid collecting room.With
This simultaneously, does not hit the foreign material (foreign material that particle diameter is less) on cylinder inwall, may be combined in natural gas
In, under the effect of cylinder internal gas pressure, it is intended to flow out from the outlet of clean gas.But, owing to depending in cylinder
Secondary it is provided with the first filter material layer, adsorption layer and the second filter material layer, so the particle diameter being blended in natural gas is less
Impurity directly stopped by the first filter material layer, it is impossible to through the first filter material layer, the particle diameter being blended in natural gas
Less granule (such as droplet) can pass the first filter material layer, certainly, owing to the particle diameter of gas is less,
So natural gas can pass the first filter material layer.The droplet being blended in natural gas is the least due to particle diameter,
So the first filter material layer also can be passed, and enter adsorption layer, due to adsorption layer be by molecular sieve, activated carbon,
At least one in silica gel and aluminium oxide is fabricated by, and therefore, adsorption layer can be to being blended in natural gas
Droplet adsorbs so that droplet is gathered into big drop on adsorption layer, the most under gravity
Fall into acquisition layer.
After adsorption layer, the most of foreign material being blended in natural gas are separated, now, natural
Being also possible in gas be mixed with a small amount of foreign material, the natural gas being mixed with a small amount of foreign material also needs to through the second filtrate
Layer, owing to foreign material cannot pass the second filter material layer, it is achieved that carry out the foreign material being blended in natural gas
Further separate so that the natural gas collected from the first outlet is clean natural gas.Need
Bright, during separating, can detect whether the foreign material in liquid collecting room are filled, if liquid collecting room
Interior foreign material are filled, then can be opened by miscellaneous object outlet, discharge the foreign material in liquid collecting room, then turn off miscellaneous
Thing exports.Although provide more separator in correlation technique, but the knot of the separator in correlation technique
Structure is more complicated, and cannot effectively remove the impurity that the particle diameter in natural gas is less.This utility model embodiment carries
The cyclone separator arrangement of confession is relatively simple, and takes full advantage of centrifugation, adsorbing separation, coarse separation, gravity
The methods such as sedimentation, it is possible to impurity that in efficient removal natural gas, particle diameter is bigger and the less impurity of particle diameter, prevent
Reentrainment, the low cost invested and operate, non-purified natural gas through centrifugation, coarse separation,
The multiple stage separation such as adsorbing separation, coarse separation, finally realizes the most de-liquid slagging-off of natural gas.
In sum, this utility model embodiment provides a kind of separator, due on the cylinder of separator
The first filter material layer of tubular it is provided with in being provided with miscellaneous QI entrance, the outlet of clean gas and miscellaneous object outlet, and cylinder,
First filter material layer blocks the outlet of clean gas, and the natural gas being mixed with foreign material can enter in cylinder from miscellaneous QI entrance
After, the foreign material that particle diameter in foreign material is bigger can be assembled at cylinder inwall, finally during eddy flow
Flowing out from miscellaneous object outlet, the foreign material that particle diameter is less can be flowing out from the outlet of clean gas when, by the first filter material layer
Stop, thus assemble on the first filter material layer, and flow out from miscellaneous object outlet under gravity, so,
Decrease the foreign material of doping from the natural gas that the outlet of clean gas is flowed out, improve the effect that foreign material separate.
The foregoing is only preferred embodiment of the present utility model, not in order to limit this utility model, all
Within spirit of the present utility model and principle, any modification, equivalent substitution and improvement etc. made, all should wrap
Within being contained in protection domain of the present utility model.
Claims (10)
1. a separator, it is characterised in that described separator includes: cylinder, described cylinder sets
It is equipped with miscellaneous QI entrance, the outlet of clean gas and miscellaneous object outlet,
Described miscellaneous QI entrance is arranged on the sidewall of described cylinder, and the outlet of described clean gas and described miscellaneous object outlet divide
It is not arranged on the two ends of described cylinder, and the outlet of described clean gas goes out more than described foreign material with the distance of placed side
Mouth and the distance of placed side, described miscellaneous object outlet is provided with block the closure gate of described miscellaneous object outlet；
Being provided with the first filter material layer of tubular in described cylinder, described first filter material layer blocks described clean gas and goes out
Mouthful, described first filter material layer by metallic fiber, glass fibre, polytetrafluoroethylene fibre, polypropylene fibre and
At least one preset in fiber is fabricated by, and described default fiber is hydrophilic oil transportation material or oleophilic drainage material
Matter.
Separator the most according to claim 1, it is characterised in that
Described miscellaneous QI entrance includes drain wall, and the wall of described drain wall is tangent with the inwall of described cylinder.
Separator the most according to claim 2, it is characterised in that
The adsorption layer of tubular it is additionally provided with in described cylinder,
Described adsorption layer blocks the outlet of described clean gas, and is arranged on described first filter material layer and the outlet of described clean gas
Between, described adsorption layer is fabricated by by least one in molecular sieve, activated carbon, silica gel and aluminium oxide.
Separator the most according to claim 3, it is characterised in that be additionally provided with cylinder in described cylinder
Second filter material layer of shape,
Described second filter material layer blocks the outlet of described clean gas, and is arranged on described adsorption layer and the outlet of described clean gas
Between, described second filter material layer is identical with the material of described first filter material layer.
Separator the most according to claim 4, it is characterised in that on described cylinder, described foreign material go out
The one end at mouth place is provided with liquid collecting room,
Described liquid collecting room is round platform cylinder, the one end at the bottom surface place of described liquid collecting room and described cylinder phase
Connection, the upper bottom surface of described liquid collecting room is provided with described miscellaneous object outlet, and described miscellaneous object outlet runs through described collection
The upper bottom surface of liquid chamber.
Separator the most according to claim 5, it is characterised in that
It is provided with inlet tube on described miscellaneous QI entrance, the outlet of described clean gas is provided with the first outlet, described
Inlet tube connects with described miscellaneous QI entrance, described first outlet and described clean gas outlet,
Described inlet tube is described drain wall away from the tube wall of the axis side of described cylinder, described drain wall
Wall be the described tube wall surface near the axis of described inlet tube.
Separator the most according to claim 5, it is characterised in that
Being provided with the second outlet on described miscellaneous object outlet, one end of described second outlet goes out with described foreign material
Mouth connects, and the other end of described second outlet is provided with described closure gate.
Separator the most according to claim 6, it is characterised in that be provided with multiple in described inlet tube
Swirl vane, and there is angle in the axis of each described swirl vane and described inlet tube.
Separator the most according to claim 6, it is characterised in that the cross section of described inlet tube is annulus
Or Fang Huan.
Separator the most according to claim 6, it is characterised in that described inlet tube is that scroll casing type enters
Mouth pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620255304.7U CN205528647U (en) | 2016-03-30 | 2016-03-30 | Separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620255304.7U CN205528647U (en) | 2016-03-30 | 2016-03-30 | Separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205528647U true CN205528647U (en) | 2016-08-31 |
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ID=56786660
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620255304.7U Active CN205528647U (en) | 2016-03-30 | 2016-03-30 | Separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205528647U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108404652A (en) * | 2018-03-26 | 2018-08-17 | 桐乡市致远环保科技有限公司 | A kind of glass fiber compound material pipe |
-
2016
- 2016-03-30 CN CN201620255304.7U patent/CN205528647U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108404652A (en) * | 2018-03-26 | 2018-08-17 | 桐乡市致远环保科技有限公司 | A kind of glass fiber compound material pipe |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 100007 No. 9 North Main Street, Dongcheng District, Beijing, Dongzhimen Patentee after: CHINA NATIONAL PETROLEUM Corp. Patentee after: CHINA PETROLEUM ENGINEERING & CONSTRUCTION Corp. Address before: 100007 No. 9 North Main Street, Dongcheng District, Beijing, Dongzhimen Patentee before: China National Petroleum Corp. Patentee before: CHINA PETROLEUM ENGINEERING & CONSTRUCTION Corp. |
|
| CP01 | Change in the name or title of a patent holder | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20210224 Address after: 100007 No. 9 North Main Street, Dongcheng District, Beijing, Dongzhimen Patentee after: CHINA NATIONAL PETROLEUM Corp. Patentee after: CHINA HUANQIU CONTRACTING & ENGINEERING Co.,Ltd. Patentee after: XINJIANG HUANQIU ENGINEERING Co. Address before: 100007 No. 9 North Main Street, Dongcheng District, Beijing, Dongzhimen Patentee before: CHINA NATIONAL PETROLEUM Corp. Patentee before: CHINA PETROLEUM ENGINEERING & CONSTRUCTION Corp. |
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| TR01 | Transfer of patent right |