CN106914067A - Wind guiding device and cyclonic separation unit - Google Patents
Wind guiding device and cyclonic separation unit Download PDFInfo
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- CN106914067A CN106914067A CN201710244696.6A CN201710244696A CN106914067A CN 106914067 A CN106914067 A CN 106914067A CN 201710244696 A CN201710244696 A CN 201710244696A CN 106914067 A CN106914067 A CN 106914067A
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- guiding device
- wind guiding
- inner cylinder
- outer shroud
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/12—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces
- B01D45/16—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces generated by the winding course of the gas stream, the centrifugal forces being generated solely or partly by mechanical means, e.g. fixed swirl vanes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D47/00—Separating dispersed particles from gases, air or vapours by liquid as separating agent
- B01D47/02—Separating dispersed particles from gases, air or vapours by liquid as separating agent by passing the gas or air or vapour over or through a liquid bath
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/48—Sulfur compounds
- B01D53/50—Sulfur oxides
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/48—Sulfur compounds
- B01D53/50—Sulfur oxides
- B01D53/507—Sulfur oxides by treating the gases with other liquids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/77—Liquid phase processes
- B01D53/78—Liquid phase processes with gas-liquid contact
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/30—Sulfur compounds
- B01D2257/302—Sulfur oxides
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/02—Other waste gases
- B01D2258/0283—Flue gases
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- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Environmental & Geological Engineering (AREA)
- Health & Medical Sciences (AREA)
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- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Cyclones (AREA)
Abstract
The invention discloses a kind of Wind guiding device, including inner cylinder, outer shroud and some guide vanes being arranged between inner cylinder, outer shroud, some guide vanes are inclined at the annular region between the cylindrical section top of inner cylinder bottom and outer shroud, pilot flow is formed between guide vane, the top of the inner cylinder is enclosed construction.A kind of cyclonic separation unit formed based on the Wind guiding device, the outer shroud upper and lower end face of the Wind guiding device is extended to form cylinder, or by Wind guiding device combination assembling on the cylindrical tube suitable with outer shroud section.The central inner cylinder top seal of Wind guiding device of the invention is simultaneously designed as cone or spheroid, do not form central flow path, the flue gas in cyclonic separation unit is set to pass downwardly through distance cylinder more long, reach preferable cyclone effect, and can be fully contacted with the uniform water film of barrel, dusting solid particle is efficiently removed, desulfurization can be also realized after addition liquid.
Description
Technical field
The present invention relates to field of environment protection equipment, more particularly, to a kind of Wind guiding device of flue gas desulfurization and dedusting and eddy flow point
From unit.
Background technology
With expanding economy, the discharge of current boiler smoke and industrial tail gas increasingly increases, most of flue gas and tail gas
In contain volume of smoke and SO2Deng poisonous gas.Wet Flue Gas Desulfurization Technique, Wet Flue Gas Desulfurization Technique is used to be based on three-phase mostly at present
The strong mechanism of mass transfer of Turbulent Mixing, using gas dynamics, makes gas (with solid micronic dust and pernicious gas) and liquid
It is sufficiently mixed, increases the specific surface area of gas-liquid contact, so as to improve desulfurization dust-removing efficiency.Using sky more than current Wet Flue Gas Desulfurization Technique
Tower, the defect of this equipment is short gas-liquid contact time, and has some flue gases to have little time reaction directly off absorption tower,
Cause the small flue dust containing high level, gypsum slurries or other desulfurization products in the wet flue gas after desulfurization, flue gas hangover
It is very long, certain pollution is caused to environment.Therefore the country further reduces dirt frequently with " smoke re-heater+bag-type dust " technique
Contaminate thing discharge capacity, but the running resistance of this technique is huge, the construction cost of wherein smoke re-heater is very high, plant maintenance into
Originally especially the maintenance cost of cloth bag is very high, thus constrains the batch production of equipment, it is difficult to which reaching environmental protection equipment operation makes
It is required that.Other this technique contains large quantity of moisture and tar thing using being limited in scope in the flue dust after biological particles burning
Matter, easily causes cloth bag blocking when using this craft dust removal, and high-temperature flue gas also easily burn cloth bag when using this technique.Though
So also there is cyclone water-film cleaner at present, but it uses traditional whirlwind minor structure, and the center of cyclone blade is flue gas time
Circulation road, causes spray head to be difficult to arrange that spraying effect is not good, have impact on the dust removing effects of uniform water film.
The content of the invention
The applicant is directed to the shortcomings of equipment construction maintenance cost is high, running resistance is big present in above-mentioned existing production,
A kind of Wind guiding device rational in infrastructure and cyclonic separation unit are provided, efficient rotary remittance coupling is carried out using whirlwind module, make gas
The solid three-phase of liquid is fully contacted, and realizes that the harmful substance high-speed physical that liquid is carried to gas catches and dissolves, and fluid media (medium) is begun
Unsaturated state is in eventually, gas-liquid membrane mass transfer resistance is greatly reduced, and mass-transfer efficiency is improved, so as to realize small space, small liquid gas
Than, dedusting high, the target of desulfurization high.
The technical solution adopted in the present invention is as follows：
A kind of Wind guiding device, including inner cylinder, outer shroud and some guide vanes for being arranged between inner cylinder, outer shroud, it is described some
Guide vane is inclined at the annular region between the cylindrical section top of inner cylinder bottom and outer shroud, is formed between guide vane and led
To runner, the top of the inner cylinder is enclosed construction.
As the further improvement of above-mentioned technical proposal：
The top of the inner cylinder is the enclosed construction of the vertex of a cone, top dome, round platform or frustum.
The inner cylinder cylindrical section is highly 1~5 times of the height of guide vane.
The diameter of the outer shroud is 2~3 times of inner diameter of steel flue.
The guide vane is equally distributed 4~18.
The guide vane is plane or cambered surface.
The angle of inclination of the guide vane and the angle of horizontal plane are 15 degree~45 degree.
The Wind guiding device Cai Yong ceramic material molding fire, it would however also be possible to employ 316L stainless steels, alloy steel products,
The manufacture of PP materials, FRP glass-reinforced plastic materials or composite processing.
A kind of cyclonic separation unit formed based on the Wind guiding device, the outer shroud of the Wind guiding device is upper and lower
End face extends to form cylinder, or by Wind guiding device combination assembling on the cylindrical tube suitable with outer shroud section.
As the further improvement of above-mentioned technical proposal：
The height of the cylinder is 6~12 times of guide vane height.
Beneficial effects of the present invention are as follows：The guide vane of Wind guiding device of the invention can make by gas formed
Cyclone effect, the effect that solid and gas is separate is realized using centrifugal force；Uniform water film is formed on blade and barrel after spray head spray,
Rotation is sufficiently mixed dusting solid particle in flue gas at a high speed jointly with moisture film, forms emulsification shape liquid, and gas liquid interfacial area is big,
Further increase dust removing effects.The central inner cylinder top seal of Wind guiding device of the invention is simultaneously designed as cone or spheroid,
Central flow path is not formed, the flue gas in cyclonic separation unit is passed downwardly through distance cylinder more long, reached preferably
Cyclone effect, and can be fully contacted with the uniform water film of barrel, dusting solid particle is efficiently removed, also can be real after addition liquid
Existing desulfurization.Spray head of the invention can one by one correspond to the setting of cyclonic separation unit, rationally distributed, uniform spraying；Can play
The effect of temperature is reduced, cleaning can be also rinsed in periodic maintenance, it is ensured that system can be with continuous and steady operation, without fouling and clogging wind
Danger.
Pipe-type rotary-flow dust arrester of the invention is revolved by setting whirlwind module, flue gas below smoke inlet into each
Flow separation unit, forms independent high velocity air passage, compared to the whirlwind speed of existing single thick Whirlwind barrel
Higher, dust removing effects are more excellent, and the national newest environmental emission standard of flue gas ultra-clean quick drain can be reached during actual test
GB13271-2014 and place environmental protection minimum discharge standard, without using bag-type dust, maintenance cost is low, has a wide range of application.This
The tower tubular type cyclone dust catcher compact conformation of invention, rationally, floor space is small, is adapted to be used outside factory building for wind path.This hair
Bright horizontal pipe cyclone dust catcher carries out spray-absorption by setting whirlwind module in a side box body in another side box body
With demisting, rationally, casing can be designed as rectangular box body structure to wind path, and regular shape is easy to mass production and transport, whole
Body is highly low, is adapted to be used in the environment of limited space.
Brief description of the drawings
Fig. 1 is the structural representation of Wind guiding device of the invention.
Fig. 2 is the top view of Fig. 1.
Fig. 3 is the stereogram of the Wind guiding device of another structure.
Fig. 4 is the front view of cyclonic separation unit.
Fig. 5 is the structural representation of tower tubular type cyclone dust catcher.
Fig. 6 is the arrangement schematic diagram of whirlwind module in Fig. 5.
Fig. 7 is the structural representation of horizontal pipe cyclone dust catcher.
Fig. 8 is the arrangement schematic diagram of whirlwind module in Fig. 7.
Fig. 9 is the right view of Fig. 7.
In figure：1st, Wind guiding device；2nd, guide vane；3rd, pilot flow；4th, outer shroud；5th, inner cylinder；6th, the vertex of a cone；7th, top dome；
8th, cylinder；10th, cyclonic separation unit；11st, tower body；12nd, liquid outlet；13rd, smoke inlet；14th, guider；15th, central discharge air pipe；
16th, flue gases duct；17th, tank；18th, exhanst gas outlet；19th, slurry pool；20th, whirlwind module；21st, spray head；22nd, annular oriffice；
23rd, rectangle orifice plate；24th, left box body；25th, right case；26th, deflector；27th, demister；28th, support column.
Specific embodiment
Below in conjunction with the accompanying drawings, specific embodiment of the invention is illustrated.
As shown in figure 1, Wind guiding device of the invention 1 includes inner cylinder 5, guide vane 2 and the outer shroud 4 of top seal, it is interior
The top of cylinder 5 is the circular cone vertex of a cone 6, and bottom is cylindrical section, the annular region between the cylindrical section top of inner cylinder 5 and outer shroud 4, is inclined
Oblique certain angle is arranged with some guide vanes 2 in parallel, pilot flow 3 is formed between guide vane 2, under the cylindrical section of inner cylinder 5
Portion is steady flow segment.The height of outer shroud 4 is highly essentially identical with guide vane 2, and the cylindrical section of inner cylinder 5 is highly guide vane 2
1 ~ 5 times of height, the diameter of outer shroud 4 is 2 ~ 3 times of the diameter of inner cylinder 5, and guide vane 2 is 4 ~ 18 uniform, as shown in Figure 1 realities
It is 8 to apply example, and Fig. 3 is 6；Guide vane 2 can be plane or cambered surface, and its angle of inclination is 15 degree with the angle of horizontal plane
~ 45 degree, the present embodiment is 30 degree.The top of inner cylinder 5 can also be bulb top dome 7（As shown in Figure 3）, round platform or frustum etc.
Structure.Cai Yong the ceramic material molding of Wind guiding device 1 is fired, it would however also be possible to employ 316L stainless steels, alloy steel products, PP materials
Material, FRP glass-reinforced plastic materials or other can bear the composite processing manufacture that high-velocity flow washes away.The bottom of inner cylinder 5 can be sealed
Close or open.
As shown in figure 4, the upper and lower end face of outer shroud 4 is extended to form cylinder 8, or combination is equipped with and the section phase of outer shroud 4
When cylindrical tube 8, form cyclonic separation unit 10, the height of cylinder 8 is 6 ~ 12 times of the height of guide vane 2, cylinder 8
0 ~ 10 degree of taper can be carried.
Embodiment one：
Whirlwind module 20 of the present invention is formed by several horizontal arrangements of cyclonic separation unit 10, can be radial distribution or
Person's rectangular array is arranged.As shown in fig. 6, some cyclonic separation units 10 radially radiate arrangement be arranged on annular oriffice 22,
Some circular ports are offered on annular oriffice 22, the cylinder 8 of cyclonic separation unit 10 is set in circular port.Further, revolve
The top of wind module 20 is additionally provided with spray head 21 and corresponds to one by one, i.e., on the top pair of the vertex of a cone 6 of each cyclonic separation unit 10
A spray head 21 should be provided with, in the present embodiment, two spray heads 21 be provided with same radial direction, using same
Shower is connected feed liquor, when spray head 21 is blocked to need repairing, it is only necessary to which the shower removed on same radial direction is carried out
Maintenance is excluded, other spray heads 21 still can normally run while maintenance, not interfere with the continuity of production operation.When
So, in order to increase ventilation, it is also possible to increase in gap location and set cyclonic separation unit 10.
As shown in figure 5, the present embodiment is tower tubular type cyclone dust catcher, cigarette is disposed with from top to bottom in tower body 11
Gas outlet 18, flue gases duct 16, central discharge air pipe 15, smoke inlet 13, whirlwind module 20 and slurry pool 19.Annular oriffice 22 sets
Put in the top of slurry pool 19, the equal diameters of its outer circumference diameter and the bottom of tower body 11 are provided with the top of whirlwind module 20
Smoke inlet 13.The diameter on the top of tower body 11 is smaller than bottom, and central discharge air pipe 15 is arranged in the circular hole at the center of annular oriffice 22,
From in the flue gases duct 16 that the bottom of tower body 11 extends upwardly to the top of tower body 11, the closing of the internal upper part of central discharge air pipe 15.Center row
Less than the diameter on the top of tower body 11, the bottom for extending to the part of flue gases duct 16 in central discharge air pipe 15 is set the diameter of tracheae 15
There is guider 14.The lower section of the exhanst gas outlet 18 of tower body 11 is provided with tank 17.Certain gradient is arranged at the bottom of slurry pool 19, relatively low
One end tower body 11 on be provided with liquid outlet 12.
When the present embodiment works, dust-laden sulfurous gas enters whirlwind module 20 from the smoke inlet 13 of the side of tower body 11, by
In the top seal of inner cylinder 5 of Wind guiding device 1, flue gas is directly down into the pilot flow 3 of each cyclonic separation unit 10,
Produce whirlwind, flue gas to be oriented to acceleration by Wind guiding device 1 and reach 18 ~ 25m/s under the guide effect of guide vane 2, work as centrifugal rotary
Turn to be downwardly into after steady flow segment speed gradually steady decrease to 3.5 ~ 4.5m/s；Using principle of hydrodynamics, the powder in flue gas
Dirt solid particle rotates at a high speed with flue gas, forms the turbulent space that gas-liquid rotation is seethed, wherein tiny dust granules collision is solidifying
It is polymerized to larger particle to settle down, or is thrown to outer tube wall.Each top of cyclonic separation unit 10 sets a set of independent simultaneously
Spray head 21, the slurries of the spray of spray head 21 form the liquid film layer of certain stably amount of liquid on eddy flow barrel, are thrown to outer
Dusting solid particle on barrel is swept along after being fully contacted with liquid film layer, finally flows under the influence of gravity into the bottom of tower body 11
Slurry pool 19, the liquid in slurry pool 19 is discharged from liquid outlet 12, flow to circulating water pool reusable edible.Flue gas then turn into
Enter central discharge air pipe 15, due to the closed upper part of central discharge air pipe 15, flue gas enters flue gases duct through the guide effect of guider 14
16, the air-flow that rotation rises is formed when flue gas is by guider 14 simultaneously, the central discharge air pipe 15 on the top of guider 14 rises simultaneously
The water of spray tank 17 ejection set through the top of tower body 11 to the effect of current stabilization, flue gas is further cleaned, the flue gas after purification
Drained into outside tower body 11 from exhanst gas outlet 18.The present invention can rapidly react the pollutants such as efficient removal sulfur dioxide, dust, realize
The high-efficient purification of flue gas.Spray head 21 supports the use slurries and rinses Wind guiding device 1 during present invention work, can play stable temperature rise
Effect, spray head 21 supports the use water rinse-system and Wind guiding device 1 is rinsed during periodic maintenance, saves and manually takes apart
The trouble that tower body 11 is safeguarded, it is ensured that the effect of high-effective dust-removing in the continuous running of system.
Embodiment two：
The present embodiment is horizontal pipe cyclone dust catcher.As shown in fig. 7, the box house of horizontal pipe cyclone dust catcher point
It is two cavitys in left and right, is connected by the slurry pool 19 of the reverse taper of bottom half, whirlwind module is provided with left box body 24
20, as shown in figure 8, the arrangement of some rectangular arrays of cyclonic separation unit 10 is arranged on rectangle orifice plate 23, naturally it is also possible to staggeredly
Arrangement.Further, the top of cyclonic separation unit 10 in whirlwind module 20 is provided with spray head 21, can one by one correspond to and set
Put, it is also possible to some spray heads 21 are set and ensure to carry out spray covering to whole region.When the rectangular array of cyclonic separation unit 10
Arrangement is arranged on when on rectangle orifice plate 23, and the spray head 21 that will can laterally or longitudinally go up utilizes same shower feed liquor, just
Dismounting service work when spray head 21 is blocked.The top of whirlwind module 20 is provided with smoke inlet 13, bottom in right case 25
Portion is provided with several deflectors 26, and top is provided with demister 27, and exhanst gas outlet 18 is provided with top canister.Slurry pool 19
Bottom sets liquid outlet 12.Casing is arranged on support column 28.
When the present embodiment works, dust-laden sulfurous gas enters whirlwind module 20 from smoke inlet 13, by whirlwind module 20
Several cyclonic separation units 10 of interior parallel arrangement, the flue gas slurries that rotation sprays with spray head 21 at a high speed fully revolve remittance coupling
Close, the dusting solid particle in flue gas flows down into the slurry pool 19 of bottom half, in slurry pool 19 in gravity centrifugation
Liquid discharged from bottom liquid outlet 12, flow to circulating water pool and recycle；Flue gas is turned to upwards in slurry pool 19, is then passed through
Deflector 26 is directed into right case 25, is drained into outside casing from exhanst gas outlet 18 by after the dehydration of demister 27.
Above description is explanation of the invention, is not the restriction to inventing, without departing from the spirit of the invention,
The present invention can make any type of modification.For example tower body can increase spray equipment and sulfur dioxide etc. is further inhaled
Receive.
Claims (10)
1. a kind of Wind guiding device, including inner cylinder（5）, outer shroud（4）Be arranged on inner cylinder（5）, outer shroud（4）Between some guiding
Blade（2）, some guide vanes（2）It is inclined at inner cylinder（5）The cylindrical section top of bottom and outer shroud（4）Between ring
Shape region, guide vane（2）Between form pilot flow（3）, it is characterised in that：The inner cylinder（5）Top be enclosed construction.
2. according to the Wind guiding device described in claim 1, it is characterised in that：The inner cylinder（5）Top be the vertex of a cone（6）, ball
Top（7）, round platform or frustum enclosed construction.
3. according to the Wind guiding device described in claim 1, it is characterised in that：The inner cylinder（5）Cylindrical section is highly directing vane
Piece（2）1 ~ 5 times of height.
4. according to the Wind guiding device described in claim 1, it is characterised in that：The outer shroud（4）Diameter be inner cylinder（5）Diameter
2 ~ 3 times.
5. according to the Wind guiding device described in claim 1, it is characterised in that：The guide vane（2）For equally distributed 4 ~
18.
6. according to the Wind guiding device described in claim 1, it is characterised in that：The guide vane（2）It is plane or cambered surface.
7. according to the Wind guiding device described in claim 1, it is characterised in that：The guide vane（2）Angle of inclination and water
The angle of plane is 15 degree ~ 45 degree.
8. according to the Wind guiding device described in claim 1, it is characterised in that：The Wind guiding device（1）Cai Yong ceramics
Material molding is fired, it would however also be possible to employ 316L stainless steels, alloy steel products, PP materials, FRP glass-reinforced plastic materials or composite processing
Manufacture.
9. a kind of cyclonic separation unit formed based on Wind guiding device described in claim 1, it is characterised in that：By the rotation
Flow guiding apparatus（1）Outer shroud（4）Upper and lower end face extends to form cylinder（8）, or by the Wind guiding device（1）Combination is assemblied in
With outer shroud（4）The suitable cylindrical tube in section（8）On.
10. according to the cyclonic separation unit described in claim 9, it is characterised in that：The cylinder（8）Height be guide vane
（2）6 ~ 12 times of height.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710244696.6A CN106914067A (en) | 2017-04-14 | 2017-04-14 | Wind guiding device and cyclonic separation unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710244696.6A CN106914067A (en) | 2017-04-14 | 2017-04-14 | Wind guiding device and cyclonic separation unit |
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| Publication Number | Publication Date |
|---|---|
| CN106914067A true CN106914067A (en) | 2017-07-04 |
Family
ID=59567263
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710244696.6A Pending CN106914067A (en) | 2017-04-14 | 2017-04-14 | Wind guiding device and cyclonic separation unit |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108114538A (en) * | 2018-02-07 | 2018-06-05 | 无锡雪浪环境科技股份有限公司 | Centrifugal water conservancy diversion captation |
| CN108479201A (en) * | 2018-04-19 | 2018-09-04 | 成都瑞柯林工程技术有限公司 | Liquid phase and/or the equipment of solid formation are isolated from gas gas-phase objects |
| CN109794103A (en) * | 2019-01-24 | 2019-05-24 | 中国石油集团东北炼化工程有限公司 | Combined guide fluid for smoke dewatering device |
| CN110185420A (en) * | 2018-02-22 | 2019-08-30 | 中国石油化工股份有限公司 | A kind of ladder is continuously depressured supplementary potentiating oil pickup apparatus and method |
| CN113105925A (en) * | 2020-01-13 | 2021-07-13 | 中国石油天然气股份有限公司 | Natural gas desanding device and method |
| CN114177700A (en) * | 2021-12-07 | 2022-03-15 | 深圳市旋风流体科技有限公司 | Gas-solid gas-liquid separating device |
Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2393627Y (en) * | 1998-09-28 | 2000-08-30 | 冶金工业部武汉钢铁设计研究院 | Horizontal casing cyclone liquid remover |
| CN1419951A (en) * | 2001-11-15 | 2003-05-28 | 陈鸣楼 | Spiral swirl device |
| CN1528527A (en) * | 2003-09-30 | 2004-09-15 | 青岛科技大学化工学院 | Guide rectifier for circulating-current cycle dust-removing system |
| CN201127881Y (en) * | 2007-05-25 | 2008-10-08 | 天津东方环境工程有限责任公司 | Multiple-fluid column rotational flow scrubbing and desulfurizing tower |
| CN201154288Y (en) * | 2007-09-03 | 2008-11-26 | 北京华宇融通电力科技开发有限公司 | Self-distributing parallelflow pneumatic rotary packed tower |
| CN201676609U (en) * | 2010-05-21 | 2010-12-22 | 孙希杰 | Smoke elimination desulfurization dust remover |
| CN202460309U (en) * | 2012-03-09 | 2012-10-03 | 天津市嘉腾环保设备有限公司 | Exhaust gas dehydrator |
| CN103127779A (en) * | 2011-11-24 | 2013-06-05 | 启东市南洋冶金机械成套设备厂 | Horizontal dehydrator for rotational flow plate of sleeve |
| CN103409159A (en) * | 2013-09-05 | 2013-11-27 | 中国石油大学(华东) | Direct-current type short contact rotational flow reactor |
| CN206613274U (en) * | 2017-04-14 | 2017-11-07 | 宜兴市东方锅炉除尘设备厂有限公司 | Wind guiding device and cyclonic separation unit |
-
2017
- 2017-04-14 CN CN201710244696.6A patent/CN106914067A/en active Pending
Patent Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2393627Y (en) * | 1998-09-28 | 2000-08-30 | 冶金工业部武汉钢铁设计研究院 | Horizontal casing cyclone liquid remover |
| CN1419951A (en) * | 2001-11-15 | 2003-05-28 | 陈鸣楼 | Spiral swirl device |
| CN1528527A (en) * | 2003-09-30 | 2004-09-15 | 青岛科技大学化工学院 | Guide rectifier for circulating-current cycle dust-removing system |
| CN201127881Y (en) * | 2007-05-25 | 2008-10-08 | 天津东方环境工程有限责任公司 | Multiple-fluid column rotational flow scrubbing and desulfurizing tower |
| CN201154288Y (en) * | 2007-09-03 | 2008-11-26 | 北京华宇融通电力科技开发有限公司 | Self-distributing parallelflow pneumatic rotary packed tower |
| CN201676609U (en) * | 2010-05-21 | 2010-12-22 | 孙希杰 | Smoke elimination desulfurization dust remover |
| CN103127779A (en) * | 2011-11-24 | 2013-06-05 | 启东市南洋冶金机械成套设备厂 | Horizontal dehydrator for rotational flow plate of sleeve |
| CN202460309U (en) * | 2012-03-09 | 2012-10-03 | 天津市嘉腾环保设备有限公司 | Exhaust gas dehydrator |
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