CN104667708B - Gas cyclone packing - Google Patents
Gas cyclone packing Download PDFInfo
- Publication number
- CN104667708B CN104667708B CN201510133791.XA CN201510133791A CN104667708B CN 104667708 B CN104667708 B CN 104667708B CN 201510133791 A CN201510133791 A CN 201510133791A CN 104667708 B CN104667708 B CN 104667708B
- Authority
- CN
- China
- Prior art keywords
- plate
- spinning disk
- filler
- gas
- cyclone
- 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.)
- Expired - Fee Related
Links
Landscapes
- Cyclones (AREA)
Abstract
The invention relates to packing and in particular relates to gas cyclone packing, belonging to the technical field of environmental resource protection and flue gas desulphurization. The gas cyclone packing consists of multiple cyclone packing units connected with one another, wherein each cyclone packing unit consists of a hexagonal ring plate, cyclone plates and a fixing ring; the fixing ring is arranged in the center of each hexagonal ring plate; the cyclone plates are uniformly distributed between the circumference of each fixing rings and the corresponding hexagonal ring plates; one end of each cyclone plate is fixedly connected with the corresponding fixing ring; and the other end of each cyclone plate is fixedly connected with the corresponding hexagonal ring plate. The packing is stable in structure, high in strength, high in ventilation capacity, high in gas-liquid mass transfer efficiency and good in demisting effect, has the corrosion-resistant effect, and can be detached, washed and repeatedly used, and the problems that conventional packing is low in overall strength and once the packing is blocked and is detached to be washed, the packing falls apart and deforms and cannot be repeatedly used are solved. The gas cyclone packing disclosed by the invention is particularly applied to flue gas desulphurization and demisting.
Description
Technical field
The present invention relates to a kind of filler, and in particular to a kind of gas cyclone filler, belongs to environmental resource protection flue gas desulfurization
Technical field.
Background technology
At present during the industry flue gas desulfurization such as Coal Chemical Industry, steel-making, thermoelectricity, dedusting, demisting, because of flue gas corrosivity
Relatively strong, generally use shower nozzle spray, dual-flow tray, folding ripple filler, the device such as plastics mellapak packing, filler carry out desulfurization, remove
Dirt, demisting, these devices, filler respectively have excellent, shortcoming because of structure difference.Shower nozzle spraying and dedusting effect is good, pressure drop is little, but desulfurization effect
Rate is low, and can produce a large amount of mist flowers, easily by discharge of poisonous waste such as sulphur foams in air；And dual-flow tray, folding ripple filler
It is that mass transfer is carried out by gas baffling and liquid, atomization yield is less, but desulfurization, dust removing effects are poor, as Despumation device
Effect is also not ideal；Plastics mellapak packing desulfuration efficiency is higher, but anti-blockage capability is poor, and this filler screw rod is even
Connect, filler bulk strength is not high, once disassembly, cleaning will fall apart, deform it is impossible to reuse after blocking.In addition, spiral board
Column plate foam removal effect preferably, but is closed in the middle of spiral board column plate, around has seal pot, gas passage area is little, pressure drop is big,
Mass transfer component can not be done use, and because material is metal and makes, be not suitable with and use under the corrosive environment of flue gas.
Content of the invention
It is an object of the invention to: provide that a kind of structure is simple, practicality is good, and corrosion-resistant, intensity is big, both can guarantee that and fills out
The ventilation capacity of material, and air-liquid mass transfer effect and efficient demisting efficiency, disassembling cleaning can reuse after blocking again
Gas cyclone filler.
The technical scheme is that
A kind of gas cyclone filler, it is made up of multiple interconnective eddy flow filler units；It is characterized in that: described
Eddy flow filler unit is made up of hexagon ring flat-plate, spinning disk and retainer ring, hexagon ring flat-plate be provided centrally with retainer ring；Fixing
Be evenly equipped with spinning disk between the circumference of ring and hexagon ring flat-plate, one end of spinning disk is fixedly connected with retainer ring, spinning disk another
One end is fixedly connected with hexagon ring flat-plate.
Described spinning disk is triangle, and described spinning disk quantity is 6.
Described spinning disk oblique spiral between retainer ring and hexagon ring flat-plate is installed.
Between described spinning disk and hexagon ring flat-plate inwall it is in 35 40 ° to tilt fixation is installed.
Described spinning disk is provided with gas passage each other.
Described hexagonal rings plate hight degree is 8-10cm；Equilateral a diameter of 6.5-8cm of hexagon ring flat-plate, described fixation
Ring height is 1-2cm；Equilateral a diameter of 1.5-2.5cm of retainer ring
The thickness of described hexagon ring flat-plate and spinning disk is respectively 1.5-2.5mm.
It is respectively arranged with gas cyclone cavity in hexagon ring flat-plate above and below described spinning disk.
Described retainer ring is hexagonal rings.
The beneficial effects of the present invention is:
This gas cyclone filler is made up using the disposable injection of injection machine of plastic material, is effectively improved the whole of filler
Body intensity.When this gas cyclone filler works as mass transfer component, gas is guided by spinning disk by lower section, through gas passage
Enter the gas cyclone cavity above spinning disk, and the liquid mixing eddy flow mass transfer falling above filler, the gas after mass transfer enters
Enter above filler, a part of liquid falls into below filler below hexagonal ring flat-plate and spinning disk, another part liquid is through solid
Determine ring to fall into below filler.This filling-material structure is stable, corrosion-resistant, and intensity is big, and ventilation capacity is strong, and air-liquid mass-transfer efficiency is high, demisting
Effect is good, and detachably rinses, reuses, and it is not high to solve existing filler bulk strength, once after blocking disassembly, cleaning are just
Can fall apart, deform it is impossible to reusable problem.It is particularly suitable for flue gas desulfurization, demisting uses.
Brief description
Fig. 1 is the structural representation of the present invention；
Fig. 2 is the perspective view of the eddy flow filler unit of the present invention；
Fig. 3 is the overlooking the structure diagram of the eddy flow filler unit of the present invention；
Fig. 4 is the expanded schematic diagram of the present invention.
In figure: 1, eddy flow filler unit, 2, hexagon ring flat-plate, 3, spinning disk, 4, retainer ring.
Specific embodiment
This gas cyclone filler is made up of multiple interconnective eddy flow filler units 1.Eddy flow filler unit 1 is by hexagon
Ring flat-plate 2, spinning disk 3 and retainer ring 4 are constituted.Hexagon ring flat-plate 2 height is 8-10cm；Hexagon ring flat-plate 2 equilateral a diameter of
6.5-8cm.
Hexagon ring flat-plate 2 be provided centrally with retainer ring 4；Retainer ring 4 is hexagonal rings, and retainer ring 4 height is 1-2cm；
Equilateral a diameter of 1.5-2.5cm of retainer ring 4；It is evenly equipped with spinning disk 3 between the circumference of retainer ring 4 and hexagon ring flat-plate 2 inwall.
Spinning disk 3 is shaped as triangle, and the quantity of spinning disk 3 is 6.Between one side of spinning disk 3 and hexagon ring flat-plate 2 inwall it is in
35 40 ° tilt to install fixation.
The drift angle that the other end of spinning disk 3 is formed by another both sides is fixedly connected with retainer ring 4.Hexagon ring flat-plate 2 and rotation
The sheet of flow 3 is respectively 1.5-2.5cm.Spinning disk 3 and hexagon ring flat-plate 2 center are in 150The radial angle of left and right, eddy flow
Piece 3 is in 22 by the outside eaves of hexagon aperture0The left and right elevation angle.
The spinning disk 3 of this gas cyclone filler oblique spiral between retainer ring 4 and hexagon ring flat-plate 2 is installed；Rotation
Flow 3 is provided with gas passage each other.It is respectively arranged with hexagon in hexagon ring flat-plate 2 above and below spinning disk 3
Ring flat-plate 2 and the gas cyclone cavity of retainer ring 4 high low head formation.
This gas cyclone filler is made up using the disposable injection of injection machine of plastic material, can effectively improve the whole of filler
Body intensity；It is arranged in tower (holding above-below direction is consistent) in layered laminate during use.This gas cyclone filler is as mass transfer unit
Part work when, gas by below filler enter, due to spinning disk 3 between retainer ring 4 and hexagon ring flat-plate 2 oblique spiral
Install；And the angle of inclination of spinning disk 3 be 35 40 °, therefore to enter gas formed guiding, then through spinning disk 3 mutual it
Between be spaced formed gas passage, enter the gas cyclone cavity of spinning disk 3 top, with filler above (last layer filler) fall
Under liquid mixing eddy flow mass transfer, gas after mass transfer enters last layer filler.During this, a part of liquid is along hexagonal
Fall into below ring flat-plate 2 and spinning disk 3 below this layer of filler, another part liquid falls into below this layer of filler through retainer ring 4, thus
Complete the mass transfer of air-liquid.
When this filler works as demister, gas is entered by lower section, by the guiding of spinning disk 3, leads to through gas
Road enters the gas cyclone cavity eddy flow of spinning disk 3 top, thus gas and hexagon ring flat-plate 2 collision will under the action of the centrifugal force
Mist is separated with gas, thus completes demisting work.When this filler is as desorption element manipulation, by filler reverse side (i.e. reverse side court
On) upward, after needing the solution of desorption heated, solution flows down above filler, is guided by spinning disk 3, and through eddy flow
, in spinning disk eddy flow outward below, solution and hexagon ring flat-plate 2 collision rift, the gas in solution is from molten for gas passage between piece 3
Flow up after separating in liquid, through spinning disk guiding, by spinning disk 3 between gas passage to inward eddy, Ran Houqi
Body departs from filler and enters above filler, thus reaches desorption purpose.This filling-material structure is stable, corrosion-resistant, and intensity is big, ventilation capacity
By force, air-liquid mass-transfer efficiency is high, except fog effect is good, and detachably rinses, reuses, solves existing filler bulk strength not
Height, once disassembly, cleaning will fall apart, deform it is impossible to reusable problem after blocking.It is particularly suitable for flue qi exhaustion
Sulphur, demisting use.
Claims (4)
1. a kind of gas cyclone filler, it is made up of multiple interconnective eddy flow filler units (1)；It is characterized in that: described
Eddy flow filler unit (1) be made up of hexagon ring flat-plate (2), spinning disk (3) and retainer ring (4), the center of hexagon ring flat-plate (2)
It is provided with retainer ring (4)；It is evenly equipped with spinning disk (3) between the circumference of retainer ring (4) and hexagon ring flat-plate (2), spinning disk (3)
One end is connected with retainer ring (4), and the other end of spinning disk (3) is connected with hexagon ring flat-plate (2)；
Described spinning disk (3) oblique spiral between retainer ring (4) and hexagon ring flat-plate (2) is installed；
Described spinning disk (3) is provided with gas passage each other；
Described hexagon ring flat-plate (2) is highly 8-10cm；Equilateral a diameter of 6.5-8cm of hexagon ring flat-plate (2), described consolidates
Determining ring (4) is highly 1-2cm；Equilateral a diameter of 1.5-2.5cm of retainer ring；
It is respectively arranged with gas cyclone cavity in hexagon ring flat-plate above and below described spinning disk (3)；
Between described spinning disk (3) and hexagon ring flat-plate (2) inwall it is in 35 40 ° to tilt fixation is installed；With to the gas entering
Body forms guiding, then is spaced formed gas passage each other through spinning disk (3), enters the gas above spinning disk (3)
Eddy flow cavity, with the liquid mixing eddy flow mass transfer falling above filler, the gas entrance last layer filler after mass transfer；This process
In, a part of liquid falls into below this layer of filler along below hexagonal ring flat-plate (2) and spinning disk (3), and another part liquid is through solid
Determine ring (4) and fall into the mass transfer thus completing air-liquid below this layer of filler.
2. a kind of gas cyclone filler according to claim 1 it is characterised in that: described spinning disk (3) be triangle,
The quantity of spinning disk (3) is 6.
3. a kind of gas cyclone filler according to claim 1 it is characterised in that: described hexagon ring flat-plate (2) and rotation
The thickness of flow (3) is respectively 1.5-2.5cm.
4. a kind of gas cyclone filler according to claim 1 it is characterised in that: described retainer ring (4) be hexagon
Ring.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510133791.XA CN104667708B (en) | 2015-03-26 | 2015-03-26 | Gas cyclone packing |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510133791.XA CN104667708B (en) | 2015-03-26 | 2015-03-26 | Gas cyclone packing |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN104667708A CN104667708A (en) | 2015-06-03 |
| CN104667708B true CN104667708B (en) | 2017-01-25 |
Family
ID=53303613
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510133791.XA Expired - Fee Related CN104667708B (en) | 2015-03-26 | 2015-03-26 | Gas cyclone packing |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN104667708B (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114713014A (en) * | 2022-03-23 | 2022-07-08 | 成都兴鑫悦环保技术开发有限公司 | Rotary packed bed of honeycomb type hypergravity machine |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2488595Y (en) * | 2001-06-22 | 2002-05-01 | 中美合资北京威肯环境工程有限公司 | Demister with whirl board of improved model |
| CN202179970U (en) * | 2011-08-01 | 2012-04-04 | 荆州市金威石化配件有限公司 | Integrally structured packing |
| CN204543930U (en) * | 2015-03-26 | 2015-08-12 | 荆州市金威石化配件有限公司 | A kind of gas cyclone filler |
-
2015
- 2015-03-26 CN CN201510133791.XA patent/CN104667708B/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| CN104667708A (en) | 2015-06-03 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| WO2018103340A1 (en) | Water scrubber for high-efficiency removal of aerosol | |
| CN205287962U (en) | Desulfurization absorption tower is with rapid ball self -purification combination formula defogging device | |
| CN201543367U (en) | Wet flue gas desulfuration dedusting device | |
| CN205730730U (en) | A kind of multitube Venturi | |
| CN202191835U (en) | Granite spraying desulphurization equipment | |
| CN104667708B (en) | Gas cyclone packing | |
| CN204582907U (en) | A kind of multistage pair of cyclone demist deduster and the desulfuration absorbing tower containing multistage pair of cyclone demist deduster | |
| CN102580504A (en) | Novel ammonia desulphurization absorption device | |
| CN204193780U (en) | A kind of high-efficiency desulfurization absorption tower | |
| CN202161916U (en) | Flue gas desulfurization spraying equipment | |
| CN202590581U (en) | Defogger adapted to changes in gas flow | |
| CN202506306U (en) | Novel ammonia process desulfurization absorption device | |
| CN204543930U (en) | A kind of gas cyclone filler | |
| CN209406036U (en) | Organic waste-gas purification spray column | |
| CN204768247U (en) | Defogging wet -type desulfurizing tower system | |
| CN206631430U (en) | Lime stone gypsum wet flue gas desulfurizing device | |
| CN203220848U (en) | Plastic exhaust gas scrubbing tower | |
| CN203139879U (en) | Spray scrubbing tower for treating organic waste gas in industries with stink pollution | |
| CN202277775U (en) | Multifunctional square desulfurization tower | |
| CN104492167A (en) | Desulfurizing tower | |
| CN203899366U (en) | Horizontal urea dust-extraction unit | |
| CN102228780B (en) | Pneumatic flow dividing, spraying and desulfurizing equipment | |
| CN102225255A (en) | Inclined plate settling separating device | |
| CN203699961U (en) | Efficient ammonia stripping tower | |
| CN206240272U (en) | A kind of exhaust gas washing tower |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address |
Address after: 434020, Jingzhou Road, Jingzhou District, Hubei Province, Jin Jiang Road Patentee after: Hubei Liang Kai environmental protection Polytron Technologies Inc. Address before: 434020 No. 11 Jin Jiang Road, Jingzhou school, Jingzhou District, Hubei, China Patentee before: JINGZHOU JINWEI PETROCHEMICAL FITTINGS CO.,LTD. |
|
| CP03 | Change of name, title or address | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170125 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |