CN207478282U - A kind of centrifugal bispin hypergravity smoke eliminator - Google Patents
A kind of centrifugal bispin hypergravity smoke eliminator Download PDFInfo
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- CN207478282U CN207478282U CN201721469860.5U CN201721469860U CN207478282U CN 207478282 U CN207478282 U CN 207478282U CN 201721469860 U CN201721469860 U CN 201721469860U CN 207478282 U CN207478282 U CN 207478282U
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- centrifugal
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Abstract
The utility model discloses a kind of centrifugal bispin hypergravity smoke eliminator, the housing including being equipped with gas access and gas vent, revolving reaction area separates gas access and gas vent centered on housing central section, it is characterised in that：The filler of rotating disk and annular spread on the rotating pan is equipped in the center revolving reaction area, multidirectional rotary rocking arm and the multiple fluid jetting heads being opened on multidirectional rotary rocking arm are equipped among the inner ring of filler, rotating disk and multidirectional rotary rocking arm are respectively from different shaft connections and by the drive rotation of respective shaft.The utility model has certain linear velocity, being easier to creep reaches filler, and gas-liquid counter current contact washing absorption effect becomes apparent from, and desulfurization at normal-pressure liquid and flue gas mixing desulfuration efficiency higher can be widely applied to flue gas desulfurization due to centrifugal drying liquid when liquid phase is thrown away.
Description
Technical field
The utility model is related to flue gas desulfurization field, particularly a kind of reinforcing gas-liquid mass transfer reaction unit.
Background technology
Hypergravity swinging bed device drives filler high-speed rotation using high-speed rotating rotor, makes to be attached to anti-on filler
Liquid is answered to have centrifugal acceleration.Relative to the high chimney of the tens of rice of tradition, mass transfer intensity is greatly improved, and greatly reduce
The size of traditional mass transfer apparatus has traditional mass transfer apparatus breakthrough development.
The hypergravity swinging bed device in industry is applied at present, is largely sound structure, i.e. liquid phase liquid-jet device is static
Fixed, filler is rotated around liquid phase nozzle.In the case where rotating speed is constant, the hypergravity swinging bed device of sound structure is improved
Mass transfer effect, most efficient method be increase turntable diameter, thus and inevitably increase rotation filler thickness.Needle
The larger chimney smoke to flow, common centrifugal blower are aerated pressurization.But the flue gas static pressure of draft outlet and dynamic pressure are still relatively low,
It is caused to be difficult to through thicker filler, and hypergravity inner exhaust gas is caused to block.
Invention content
To solve the above problems, the utility model provides a kind of centrifugal bispin hypergravity smoke eliminator, normal pressure takes off
Sulphur liquid and flue gas mixing desulfuration efficiency higher.
The utility model is realized in this way：A kind of centrifugal bispin hypergravity smoke eliminator, including being equipped with gas
The housing of entrance and gas vent, revolving reaction area separates gas access and gas vent centered on housing central section, feature
It is：The filler of rotating disk and annular spread on the rotating pan is equipped in the center revolving reaction area, among the inner ring of filler
Equipped with multidirectional rotary rocking arm and the multiple fluid jetting heads being opened on multidirectional rotary rocking arm, rotating disk and multidirectional rotary rocking arm difference
From different shaft connections and by the drive rotation of respective shaft.
The multidirectional rotary rocking arm, which is connected with first rotating shaft and driven by first rotating shaft, to be rotated, inside first rotating shaft
Hollow composition rotating liquid channel.
The multidirectional rotary rocking arm is including two or more, and length is more than or equal to 200mm.
The filler is polytetrafluoroethylene (PTFE) ball.
The rotating disk side connect linkage with the second shaft, and opposite side is fixed with blocking solution rotary flange disk with one heart.
It is isolated between the center revolving reaction area and the second shaft by the first gas-liquid sealing part；Center revolving reaction
It is isolated between area and gas vent by the second gas-liquid sealing part；
The gas vent is isolated between first rotating shaft and the external world by third mechanical sealing member.
The first rotating shaft is driven by tape handler to be rotated, the first rotating shaft and the two of tape handler drive station
Side is supported respectively by the first nozzle shaft bearing and the second nozzle shaft bearing.
The first rotating shaft end has connected liquid inlet by the second nozzle shaft bearing, liquid inlet and the
It is isolated inside two nozzle shaft bearings and by the 4th mechanical sealing member between the external world.
Ozone generator is provided in the center revolving reaction area.
The utility model can be widely applied to flue gas desulfurization, have the beneficial effect that：
(1) with it is conventional it is high-gravity rotating bed compared with, the rotating disk and rotation filler of the utility model subtract center filler
After volume, filler is lighter, and rotation energy consumption is lower, and high speed rotation vibration is less, rotates disk diameter bigger, and rotating disk outer end liquid splashes
The linear velocity higher penetrated, gas-liquid counter current contact washing absorption effect become apparent from, and desulfurization at normal-pressure liquid and flue gas mixing desulfuration efficiency are more
It is high.
(2) with it is conventional it is high-gravity rotating bed compared with, jumped again after high speed rotation injection using liquid phase during the utility model
Rotating disk and filler are adjourned, in the process, liquid-liquid diphase filling out under Elevated Gravity of big hundreds times than earth gravitational field
Flowing contact is generated in material, huge shearing force makes liquid tear into nano level film, silk and drop.Due to centrifugal drying liquid, liquid phase
Has certain linear velocity when throwing away, being easier to creep reaches filler.
Description of the drawings
Fig. 1 is the structure diagram of the utility model embodiment 1；
Fig. 2 is filler and reaction solution water (flow) direction schematic diagram during the utility model embodiment 1 rotates；
Fig. 3 is the structure diagram in 2 center revolving reaction area of the utility model embodiment.
Specific embodiment
Embodiment 1
As shown in Figure 1, the utility model is a kind of centrifugal bispin hypergravity smoke eliminator, enter including being equipped with gas
Mouthfuls 5, the housing 1 of gas vent 13 and liquid outlet 6, centered on 1 middle part of housing revolving reaction area, by gas access 5 and gas
Outlet 13 separates.In the present embodiment, gas access 5 is set on the top in center revolving reaction area, and liquid outlet 6 is revolved set on center
Turn the bottom of reaction zone.Center revolving reaction area is connected by gas passage 16 with gas vent 13.
The filler 8 of rotating disk 7 and annular spread in rotating disk 7 is equipped in the revolving reaction area of center, in the inner ring of filler 8
Between be equipped with hollow multidirectional rotary rocking arm 9 and multiple fluid jetting heads 10 for being opened on multidirectional rotary rocking arm 9, rotating disk 7 and more
To rotating arm 9 respectively from different shaft connections and by the drive rotation of respective shaft.Rotating disk 7 and multidirectional rotary rocking arm 9
Direction of rotation it is opposite or identical, when direction of rotation is identical, rotating speed is preferably different.
In the present embodiment, rotating disk 7 and 9 respective shaft of multidirectional rotary rocking arm are respectively arranged on opposite direction.It is multidirectional
Rotating arm 9 connects with first rotating shaft 15 and drives rotation by first rotating shaft 15, and 15 inner hollow of first rotating shaft forms rotation
Turn fluid passage.Preferably, multidirectional rotary rocking arm 9 includes two or more, and length is more than or equal to 200mm.In the present embodiment
In, multidirectional rotary rocking arm 9 includes symmetrically arranged four, and in ┒ types, vertical part is connected with first rotating shaft 15, laterally
Part then offers multiple fluid jetting heads 10 towards filler 8.First rotating shaft 15 can clockwise or counterclockwise, multidirectional rotary
Rocking arm 9, nozzle 10 are rotated with first rotating shaft 15 so that reaction liquid is thrown away with higher linear velocity centrifugation.First rotating shaft 15 with
Gap between housing 1 is gas passage 16.
Preferably, filler 8 is adopted as polytetrafluoroethylene (PTFE) ball, has many advantages, such as high temperature resistant, acid-fast alkali-proof.It is and general stainless
Steel SUS304/316 wire packings, it is impossible to bear high temperature, and in flue gas band chlorion Cl-In the case of be easily corroded.Rotation
7 side of turntable connect linkage with the second shaft 3 (being driven by motor), and opposite side is fixed with blocking solution rotary flange disk 11 with one heart.The
Two shafts 3 are supported by filler shaft bearing 2.
It is isolated between center revolving reaction area and the second shaft 3 by the first gas-liquid sealing part 4；Center revolving reaction area with
It is isolated between gas passage 16, gas vent 13 by the second gas-liquid sealing part 12；The reaction of gas passage 16, gas vent 13
It is isolated between gas and first rotating shaft 15 and the external world by third mechanical sealing member 14 afterwards.
First rotating shaft 15 is driven by tape handler 20 to be rotated, the first rotating shaft 15 and 20 drive station of tape handler
Both sides pass through the first nozzle shaft bearing 17 and the second nozzle shaft bearing bearing 18 respectively.15 end of first rotating shaft passes through second
Nozzle shaft bearing 18 has connected liquid inlet 21, has press liquid and inside first rotating shaft 15, in liquid inlet 21
It is isolated between two nozzle shaft bearings, 18 inside and the external world by the 4th mechanical sealing member 19.
Preferably, ozone generator is additionally provided in the center revolving reaction area, effect is to generate ozone by cigarette
Nitric oxide NO in gas is converted to nitrogen dioxide NO2, absorbing liquid of being more convenient for absorb, further improve assimilation effect.
In use, pending flue gas enters the center revolving reaction area of housing from gas access 5, urea reaction liquid passes through
The centrifugation that liquid inlet 21, first rotating shaft 15, multidirectional rotary rocking arm 9, nozzle 10 rotate throws away (8 inner ring of filler as shown in Figure 2
Water (flow) direction), the rotating disk 7 and filler 8 in rotation are transitted to, is reacted with flue gas.After reaction, waste liquid passes through liquid outlet
6 outflow center revolving reaction areas, gas enters gas passage 16 by 11 intermediate throughholes of blocking solution rotary flange disk, finally in gas
13 discharge of outlet.
Embodiment 2
As shown in figure 3, in the present embodiment, rotating disk 7 and 9 respective shaft of multidirectional rotary rocking arm are respectively arranged on identical
Direction.First rotating shaft 15, the second shaft 3 are hollow at this time, and first rotating shaft 15 is concentric with the second shaft 3 and set on the second shaft
In 3.Gap between 15 and second shaft 3 of first rotating shaft forms gas passage 16.
Other are the same as embodiment 1.
Claims (10)
1. a kind of centrifugal bispin hypergravity smoke eliminator, the housing including being equipped with gas access and gas vent, housing
Revolving reaction area separates gas access and gas vent centered on middle part, it is characterised in that：In the center revolving reaction area
Filler equipped with rotating disk and annular spread on the rotating pan, the inner ring centre of filler are equipped with multidirectional rotary rocking arm and are opened in more
Multiple fluid jetting heads on rotating arm, rotating disk and multidirectional rotary rocking arm are respectively from different shaft connections and by respective
Shaft drives rotation.
2. centrifugal bispin hypergravity smoke eliminator according to claim 1, it is characterised in that：The multidirectional rotation
Turn rocking arm to connect with first rotating shaft and drive rotation by first rotating shaft, first rotating shaft inner hollow forms rotating liquid and leads to
Road.
3. centrifugal bispin hypergravity smoke eliminator according to claim 1, it is characterised in that：The multidirectional rotation
Turn rocking arm including two or more, and length is more than or equal to 200mm.
4. centrifugal bispin hypergravity smoke eliminator according to claim 1, it is characterised in that：The filler is
Polytetrafluoroethylene (PTFE) ball.
5. centrifugal bispin hypergravity smoke eliminator according to claim 1, it is characterised in that：The rotating disk
Side connect linkage with the second shaft, and opposite side is fixed with blocking solution rotary flange disk with one heart.
6. centrifugal bispin hypergravity smoke eliminator according to claim 5, it is characterised in that：The center rotation
Turn by the first gas-liquid sealing part to be isolated between reaction zone and the second shaft；Pass through between center revolving reaction area and gas vent
Second gas-liquid sealing part is isolated.
7. centrifugal bispin hypergravity smoke eliminator according to claim 2, it is characterised in that：The gas goes out
Mouth is isolated between first rotating shaft and the external world by third mechanical sealing member.
8. centrifugal bispin hypergravity smoke eliminator according to claim 2, it is characterised in that：Described first turn
Axis is driven by tape handler to be rotated, and the both sides of the first rotating shaft and tape handler drive station are turned respectively by the first nozzle
Axle bearing and the bearing of the second nozzle shaft bearing.
9. centrifugal bispin hypergravity smoke eliminator according to claim 8, it is characterised in that：Described first turn
Shaft end has connected liquid inlet by the second nozzle shaft bearing, liquid inlet with inside the second nozzle shaft bearing and
It is isolated between the external world by the 4th mechanical sealing member.
10. centrifugal bispin hypergravity smoke eliminator according to claim 1, it is characterised in that：The center
Revolving reaction is provided with ozone generator in area.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721469860.5U CN207478282U (en) | 2017-11-06 | 2017-11-06 | A kind of centrifugal bispin hypergravity smoke eliminator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721469860.5U CN207478282U (en) | 2017-11-06 | 2017-11-06 | A kind of centrifugal bispin hypergravity smoke eliminator |
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| Publication Number | Publication Date |
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| CN207478282U true CN207478282U (en) | 2018-06-12 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201721469860.5U Active CN207478282U (en) | 2017-11-06 | 2017-11-06 | A kind of centrifugal bispin hypergravity smoke eliminator |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107715669A (en) * | 2017-11-06 | 2018-02-23 | 惠州瑞浩环保科技有限公司 | A kind of centrifugal bispin hypergravity smoke eliminator |
| CN110280117A (en) * | 2019-05-27 | 2019-09-27 | 成都兴鑫悦环保技术开发有限公司 | It is centrifuged oxidizing process and cooperates with micro-nano steam bubble VOCs processing system |
-
2017
- 2017-11-06 CN CN201721469860.5U patent/CN207478282U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107715669A (en) * | 2017-11-06 | 2018-02-23 | 惠州瑞浩环保科技有限公司 | A kind of centrifugal bispin hypergravity smoke eliminator |
| CN107715669B (en) * | 2017-11-06 | 2023-10-03 | 广州市浩立生物科技有限公司 | Centrifugal double-rotation supergravity smoke purifying device |
| CN110280117A (en) * | 2019-05-27 | 2019-09-27 | 成都兴鑫悦环保技术开发有限公司 | It is centrifuged oxidizing process and cooperates with micro-nano steam bubble VOCs processing system |
| CN110280117B (en) * | 2019-05-27 | 2022-04-22 | 成都兴鑫悦环保技术开发有限公司 | Centrifugal oxidation method and micro-nano bubble VOCs (volatile organic chemicals) processing system |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20220317 Address after: 510399 self compiled 35 of Room 201, No. 550 Binjiang East Road, Haizhu District, Guangzhou, Guangdong Province (not for plant use) Patentee after: GUANGZHOU HAO LI TECHNOLOGY Co.,Ltd. Address before: 516000 south of tea team 4, Tonghu economic management zone, Zhongkai high tech Zone, Huizhou City, Guangdong Province (plant) Patentee before: HUIZHOU RUIHAO ENVIRONMENTAL PROTECTION TECHNOLOGY CO.,LTD. |
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| TR01 | Transfer of patent right |