CN206229073U - A kind of gas-liquid separator for exhaust-gas treatment - Google Patents
A kind of gas-liquid separator for exhaust-gas treatment Download PDFInfo
- Publication number
- CN206229073U CN206229073U CN201621318466.7U CN201621318466U CN206229073U CN 206229073 U CN206229073 U CN 206229073U CN 201621318466 U CN201621318466 U CN 201621318466U CN 206229073 U CN206229073 U CN 206229073U
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- CN
- China
- Prior art keywords
- inner cylinder
- outer barrel
- gas
- exhaust
- diameter
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Abstract
The utility model discloses a kind of gas-liquid separator for exhaust-gas treatment, including tower body, including nested outer barrel and inner cylinder, the top of inner cylinder is the air inlet of open type, it is provided between the top of outer barrel and inner cylinder and is tightly connected plate, the bottom of outer barrel is provided with gas outlet, bottom of the bottom of inner cylinder higher than outer barrel, the bottom of inner cylinder is provided with centre bore, the aperture of centre bore is the 1/4 of inner cylinder bottom diameter, the bottom of outer barrel is closed, the bottom sides of outer barrel are provided with tap hole, the reflecting plate of circular conical surface is provided with the space formed between the bottom of inner cylinder and the bottom of outer barrel, connected using link between reflecting plate and inner cylinder;It is covered with the exhaust hole for having aperture not wait on the side wall of inner cylinder, all exhaust holes are to be gradually reduced to set from top to bottom according to aperture, a diameter of 5~10mm of exhaust hole., using vertical-flow and orifice-plate type structure, equipment resistance is small, and power consumption is small for the utility model gas-liquid separator, saves space, material-saving in tower.
Description
Technical field
The utility model is related to a kind of gas-liquid separator, more particularly to a kind of exhaust-gas treatment gas-liquid separator.
Background technology
In waste gas treatment process, it is often necessary to which gas is carried out into spray washing and absorption process, in the process, have
A part of water is pulled away, and this allows for spray liquid and constantly reduces, it is necessary to constantly be supplemented, another aspect is sprayed by pre-treatment
The technique drenched after absorbing generally is required to the moisture content of gas, in order that the reduction of gas moisture content is, it is necessary to carry out gas-liquid separation,
To reach water content requirement.
The gas-liquid separator of current commercial Application mainly has mesh mist eliminator, vortex-flow and defrosting device, folded plate gas-liquid separator, silk
Net demister is easily blocked when dusty gas is processed, and equipment resistance is larger, and power consumption is larger.Vortex-flow and defrosting device, folding
Plate gas-liquid separator is typically mounted on tower top, increased the height of tower, increased cost of investment.
Utility model content
For problems of the prior art, the utility model proposes a kind of gas-liquid separator for exhaust-gas treatment,
Using vertical-flow and orifice-plate type structure, equipment resistance is small, and power consumption is small, saves space, material-saving in tower.
In order to solve the above-mentioned technical problem, the utility model proposes a kind of gas-liquid separator for exhaust-gas treatment, bag
Tower body is included, described including nested outer barrel and inner cylinder, the top of the inner cylinder is the air inlet of open type, the top of the outer barrel
It is provided between the inner cylinder and is tightly connected plate, the bottom of the outer barrel is provided with gas outlet, and the bottom of the inner cylinder is higher than outer barrel
Bottom, the bottom of the inner cylinder is provided with centre bore, and the aperture of the centre bore is the 1/4 of inner cylinder bottom diameter, the outer barrel
For closed, the bottom sides of the outer barrel are provided with tap hole for bottom, the bottom of the bottom of the inner cylinder and the outer barrel it
Between be provided with the reflecting plate of circular conical surface in the space that is formed, connected using link between the reflecting plate and the inner cylinder;It is described
It is covered with the exhaust hole for having aperture not wait on the side wall of inner cylinder, all exhaust holes are to be gradually reduced to set from top to bottom according to aperture
Put, a diameter of 5~10mm of the exhaust hole.
The utility model is used for the gas-liquid separator of exhaust-gas treatment, wherein, between being waited from top to bottom on the inwall of the outer barrel
Away from be provided with four layers of water leg, each water leg is set along the circle of outer tube inner wall one, is led with one between adjacent two layers water leg
Liquid pipe UNICOM.
Water leg width dimensions diametrically are 50mm, are highly 50mm.
Its opening area of the exhaust hole of setting is the top 300mm apart from inner cylinder to apart from the bottom of inner cylinder on the inner tube wall
The scope of portion 100mm;In opening area, positioned at a diameter of 10mm of exhaust hole in the region of top 1/3, the row in the region of middle part 1/3
The a diameter of 8mm of steam vent, a diameter of 5mm of exhaust hole in the region of bottom 1/3;The central row of all exhaust holes away from row away from being
80mm。
The water cone drift angle of the reflecting plate is 120 degree, and the cone bottom diameter of the reflecting plate is inner diameter of steel flue and outer barrel diameter
Average value.
The link is made up of 4 pieces of uniform in the circumferential connecting ribs, one end of the connecting rib and reflecting plate
It is connected, the other end of the connecting rib is connected with inner cylinder.
Compared with prior art, the beneficial effects of the utility model are:
Because the utility model uses vertical-flow double-barrel structure, can double as from the downward pipeline of tower top, and in outer tower
Wall is provided with multi-level water leg, and catheter is connected between water leg, and collection liquid automatically is guided into bottom of towe, saves tower
Internal occupied space, reduces overall dimensions, material-saving, reduces cost.
Because the utility model tower body is inside and outside nested double-barrel structure, exhaust hole is disposed with inner tube wall, using hole
Hardened structure is not easily blocked, and clashes into form liquid with outer barrel from after exhaust hole ejection into the gas in tower, and liquid is along outer tube inner wall
Flow in water leg, then tower bottom is flow to through catheter, equipment resistance is small, and power consumption is small;By practice test, this practicality is new
The de-water ratio of type gas-liquid separator can reach follow-up charcoal absorption handling process requirement.
Brief description of the drawings
Fig. 1 is the axial schematic cross-sectional view of the gas-liquid separator that the utility model is used for exhaust-gas treatment.
In figure:1- outer barrels, 2- inner cylinders, 3- air inlets, 4- connecting plates, 5- gas outlets, 6- tap holes, 7- reflecting plates, 8- rows
Steam vent, 9- water legs, 10- catheters, 11- links.
Specific embodiment
Technical solutions of the utility model are described in further detail with specific embodiment below in conjunction with the accompanying drawings, it is described
Specific embodiment is only explained to the utility model, is not used to limit the utility model.
As shown in figure 1, the utility model proposes a kind of gas-liquid separator for exhaust-gas treatment, including tower body, tower body
Base altitude be 4 to 5 meters, its external diameter is about 1 meter, and the tower body includes nested outer barrel 1 and inner cylinder 2, the top of the inner cylinder 2
Portion is the air inlet 3 of open type, is provided between the top of the outer barrel 1 and the inner cylinder 2 and is tightly connected plate 4, in order to improve this
The de-water ratio of utility model gas-liquid separator, is provided with four layers of water leg 9 at equal intervals from top to bottom on the inwall of the outer barrel 1,
Each water leg 9 is set along the circle of 1 inwall of outer barrel one, with the UNICOM of a catheter 10 between adjacent two layers water leg 9.Water leg
9 width dimensions diametrically are 50mm, are highly 50mm.The bottom of the outer barrel 1 is provided with gas outlet 5, the inner of gas outlet 5
The inside 50mm of outer barrel 1 is stretched to, and the flange of 30mm is provided with the inner of gas outlet 5, to prevent the water of the inwall of outer barrel 1 from outlet
Mouth 5 flows out.The bottom of the inner cylinder 2 is higher than the bottom of outer barrel 1, and the bottom of the inner cylinder 2 is provided with centre bore, the centre bore
Aperture is the 1/4 of inner cylinder bottom diameter, and the bottom of the outer barrel 1 is closed, and the bottom sides of the outer barrel 1 are provided with tap hole 6,
The reflecting plate 7 of circular conical surface is provided with the space formed between the bottom of the bottom of the inner cylinder 2 and the outer barrel 1, it is described anti-
It is 120 degree to penetrate the water cone drift angle of plate 7, and the cone bottom diameter of the reflecting plate 7 is the average value of inner diameter of steel flue and outer barrel diameter, described
Connected using link 11 between reflecting plate 7 and the inner cylinder 4;The link 11 is by 4 pieces of uniform in the circumferential dowels
Plate is constituted, and one end of the connecting rib is connected with reflecting plate 7, and the other end of the connecting rib is connected with inner cylinder 2.In described
It is covered with the exhaust hole 8 for having aperture not wait on the side wall of cylinder 2, all exhaust holes 8 are to be gradually reduced to set from top to bottom according to aperture
Put, a diameter of 5~10mm of the exhaust hole 8, its opening area of the exhaust hole 8 of setting is apart from inner cylinder 4 on the wall of the inner cylinder 2
Top 300mm to apart from inner cylinder 4 bottom 100mm scope;In opening area, positioned at the exhaust hole in the region of top 1/3
A diameter of 10mm, a diameter of 8mm of exhaust hole in the region of middle part 1/3, a diameter of 5mm of exhaust hole in the region of bottom 1/3;All steam discharges
The central row in hole away from row away from being 80mm.
Using the utility model proposes gas-liquid separator, gas-liquid mixture from air inlet 3 enter inner cylinder 2, a part of gas
Body is sprayed by the exhaust hole 8 on the wall of inner cylinder 2, and is clashed into the inwall of outer barrel 1, and the liquid that gas is formed after clashing into is along outer barrel 1
Inwall is flowed downwardly into water leg 9, then the bottom of tower is flow to through catheter 10, then is discharged by tap hole 6, another part gas
Sprayed by the centre bore of the bottom of inner cylinder 2, and clashed into reflecting plate 7, the liquid of formation flow to the bottom of tower along reflecting plate 7,
Discharged by tap hole 6 again, gas flows out from gas outlet 5.
Although being described to the utility model above in conjunction with accompanying drawing, the utility model is not limited to above-mentioned
Specific embodiment, above-mentioned specific embodiment is only schematical, rather than restricted, the ordinary skill of this area
Personnel, in the case where the utility model objective is not departed from, can also make many variations under enlightenment of the present utility model, this
Belong within protection of the present utility model.
Claims (6)
1. a kind of gas-liquid separator for exhaust-gas treatment, including tower body, it is described including nested outer barrel (1) and inner cylinder (2), institute
The top for stating inner cylinder (2) is the air inlet (3) of open type, and sealing is provided between the top of the outer barrel (1) and the inner cylinder (2)
Connecting plate (4), the bottom of the outer barrel (1) is provided with gas outlet (5), and the bottom of the inner cylinder (2) is higher than the bottom of outer barrel (1),
The bottom of the inner cylinder (2) is provided with centre bore, and the aperture of the centre bore is the 1/4 of inner cylinder bottom diameter, the bottom of the outer barrel (1)
Portion is closed, and the bottom sides of the outer barrel (1) are provided with tap hole (6), in the bottom of the inner cylinder (2) and the outer barrel
(1) reflecting plate (7) of circular conical surface is provided with the space formed between bottom, between the reflecting plate (7) and the inner cylinder (2)
Connected using link (11);It is covered with the exhaust hole (8) for having aperture not wait, all exhaust holes (8) on the side wall of the inner cylinder (2)
It is to be gradually reduced to set from top to bottom according to aperture, a diameter of 5~10mm of the exhaust hole (8).
2. the gas-liquid separator of exhaust-gas treatment is used for according to claim 1, it is characterised in that the inwall of the outer barrel (1)
On be provided with four layers of water leg (9) at equal intervals from top to bottom, each water leg (9) is set along the circle of outer barrel (1) inwall one, phase
With a catheter (10) UNICOM between adjacent two-layer water leg (9).
3. the gas-liquid separator of exhaust-gas treatment is used for according to claim 2, it is characterised in that water leg (9) is diametrically
Width dimensions be 50mm, be highly 50mm.
4. the gas-liquid separator of exhaust-gas treatment is used for according to claim 1, it is characterised in that set on inner cylinder (2) wall
Exhaust hole (8) its opening area put is the model of the top 300mm to the bottom 100mm apart from inner cylinder (2) apart from inner cylinder (2)
Enclose;In opening area, positioned at a diameter of 10mm of exhaust hole in the region of top 1/3, the exhaust hole in the region of middle part 1/3 is a diameter of
8mm, a diameter of 5mm of exhaust hole in the region of bottom 1/3;The central row of all exhaust holes away from row away from being 80mm.
5. the gas-liquid separator of exhaust-gas treatment is used for according to claim 1, it is characterised in that the water of the reflecting plate (7)
Cone-apex angle is 120 degree, and the cone bottom diameter of the reflecting plate (7) is inner diameter of steel flue and the average value of outer barrel diameter.
6. according to claim 1 be used for exhaust-gas treatment gas-liquid separator, it is characterised in that the link (11) by
4 pieces of connecting ribs uniform in circumference are constituted, and one end of the connecting rib is connected with reflecting plate (7), the connecting rib
The other end is connected with inner cylinder (2).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621318466.7U CN206229073U (en) | 2016-12-01 | 2016-12-01 | A kind of gas-liquid separator for exhaust-gas treatment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621318466.7U CN206229073U (en) | 2016-12-01 | 2016-12-01 | A kind of gas-liquid separator for exhaust-gas treatment |
Publications (1)
Publication Number | Publication Date |
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CN206229073U true CN206229073U (en) | 2017-06-09 |
Family
ID=58977832
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201621318466.7U Expired - Fee Related CN206229073U (en) | 2016-12-01 | 2016-12-01 | A kind of gas-liquid separator for exhaust-gas treatment |
Country Status (1)
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CN (1) | CN206229073U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108506912A (en) * | 2018-07-03 | 2018-09-07 | 河北建筑工程学院 | Steam generation facility |
CN111298523A (en) * | 2018-12-12 | 2020-06-19 | 中国石油化工股份有限公司 | Cyclone demister |
-
2016
- 2016-12-01 CN CN201621318466.7U patent/CN206229073U/en not_active Expired - Fee Related
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108506912A (en) * | 2018-07-03 | 2018-09-07 | 河北建筑工程学院 | Steam generation facility |
CN111298523A (en) * | 2018-12-12 | 2020-06-19 | 中国石油化工股份有限公司 | Cyclone demister |
CN111298523B (en) * | 2018-12-12 | 2022-02-08 | 中国石油化工股份有限公司 | Cyclone demister |
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Legal Events
Date | Code | Title | Description |
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GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170609 Termination date: 20181201 |
|
CF01 | Termination of patent right due to non-payment of annual fee |