CN106731934A - Cyclone mixer and the desulfurizer using the blender - Google Patents
Cyclone mixer and the desulfurizer using the blender Download PDFInfo
- Publication number
- CN106731934A CN106731934A CN201710063200.5A CN201710063200A CN106731934A CN 106731934 A CN106731934 A CN 106731934A CN 201710063200 A CN201710063200 A CN 201710063200A CN 106731934 A CN106731934 A CN 106731934A
- Authority
- CN
- China
- Prior art keywords
- cylinder
- annular slab
- deflector
- housing
- cyclone mixer
- 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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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/10—Mixing by creating a vortex flow, e.g. by tangential introduction of flow components
-
- 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
- B01D53/501—Sulfur oxides by treating the gases with a solution or a suspension of an alkali or earth-alkali or ammonium compound
- B01D53/502—Sulfur oxides by treating the gases with a solution or a suspension of an alkali or earth-alkali or ammonium compound characterised by a specific solution or suspension
-
- 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
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/21—Mixing gases with liquids by introducing liquids into gaseous media
Abstract
The present invention relates to emission-control equipment technical field, more particularly, to a kind of cyclone mixer and the desulfurizer using the blender.Cyclone mixer, including cylinder, annular slab and base plate, one end of the cylinder is used to be fixedly connected with the inwall of the housing of desulfurizer, the other end of the cylinder is fixedly connected with the annular slab, multiple deflectors are provided between the base plate and the annular slab, multiple deflector being provided at circumferentially spaced along the annular slab, the passage passed through for flue gas is formed between the two neighboring deflector;The outer shroud of annular slab and the edge of the deflector have an intersection point, and the diameter of the mistake of the outer shroud intersection point is set with the plate face of deflector in inclination angle.Present invention also offers a kind of desulfurizer.The present invention can increase the contact area of flue gas and alkali lye so that the sulfur dioxide in flue gas is more abundant with the reaction of alkali lye, so as to enhance desulfurized effect by setting deflector.
Description
Technical field
The present invention relates to emission-control equipment technical field, more particularly, to a kind of cyclone mixer and the blender is used
Desulfurizer.
Background technology
China is developing country, and industrialization development is inexorable trend.However as expanding economy and the progress of society,
Flue gas SO2Discharge capacity with dust also gradually increases, and has been developed as endangering the healthy key factor of people.Due to row
The amount of letting off and the acid rain that is formed has spread on both sides of the Changjiang River, not only heavy corrosion building and industrial plants, and large area is broken
Bad forest, soil, jeopardize the growth of crops, and serious harm is caused to the living environment of the mankind, and constrain China can
Sustainable development.
All there is viscosity due to most of flue dust, can adsorb on desulfurating dust-removing equipment inner facility, cause hot resistance
Increase so that flue gas cannot be fully contacted with absorbing liquid, so as to cause desulfurized effect undesirable.
The content of the invention
It is an object of the invention to provide a kind of cyclone mixer, cannot be with absorbing liquid to solve the flue gas in sweetening process
The technical problem being fully contacted.
The present invention also aims to provide a kind of desulfurizer, with solve that existing desulfurizer is present because flue gas without
Method and absorbing liquid be fully contacted caused by the undesirable technical problem of desulfurized effect.
Based on above-mentioned first purpose, the invention provides a kind of cyclone mixer, including cylinder, annular slab and base plate, institute
Stating one end of cylinder is used to be fixedly connected with the inwall of the housing of desulfurizer, and the other end of the cylinder is solid with the annular slab
Fixed connection, is provided with multiple deflectors between the base plate and the annular slab, multiple deflectors are along the annular slab
It is provided at circumferentially spaced, the passage passed through for flue gas is formed between the two neighboring deflector;The outer shroud of the annular slab and institute
Stating the edge of deflector has an intersection point, and the diameter of the mistake of the outer shroud intersection point is set with the plate face of the deflector in inclination angle.
Further, the plate face of the deflector is vertical with the plate face of the base plate.
Further, the cross-sectional area of the cylinder is gradually subtracted from one end of the cylinder to the other end of the cylinder
It is small.
Further, gap is set between the inwall of the edge of the outer shroud of the annular slab and the housing.
Further, the inclination angle is 30~60 °.
Further, the inclination angle is 40 °.
Further, also including trunnion, one end of the trunnion is fixedly connected with the other end of the cylinder, the trunnion
The other end be fixedly connected with the annular slab.
Based on above-mentioned second purpose, present invention also offers a kind of desulfurizer, including housing, the inside of the housing by
Spray thrower and described cyclone mixer are up to disposed with down, and the feed tube of the spray thrower is used to be connected with alkali liquid tank;
Air inlet, gas outlet and leakage fluid dram are provided with the housing, the air inlet is located at the lower section of the cyclone mixer, is used for
Connected with the air outlet of air-introduced machine, to introduce flue gas;The gas outlet is located at the top of the housing, after discharging desulfurization
Gas;The leakage fluid dram is located at the bottom of the housing, for discharging and the alkali lye after the smoke reaction.
Further, the spray thrower includes multiple fog-spray nozzles, multiple fog-spray nozzle interval settings.
Further, also including liquid withdrawal system, the inlet of the liquid withdrawal system is connected with the leakage fluid dram
It is logical.
The cyclone mixer that the present invention is provided, including cylinder, annular slab and base plate, one end of the cylinder are used for and desulfurization
The inwall of the housing of device is fixedly connected, and the other end of the cylinder is fixedly connected with the annular slab, the base plate with it is described
Multiple deflectors are provided between annular slab, the multiple deflector being provided at circumferentially spaced along the annular slab are two neighboring
The passage passed through for flue gas is formed between the deflector;The outer shroud of the annular slab has with the edge of the deflector to be handed over
Point, the diameter of the mistake of the outer shroud intersection point is set with the plate face of the deflector in inclination angle.The present invention by setting deflector,
The contact area of flue gas and alkali lye can be increased so that the sulfur dioxide in flue gas is more abundant with the reaction of alkali lye, so as to increase
Strong desulfurized effect.When in use, the cyclone mixer that the present invention is provided is placed on the lower section of the spray thrower of desulfurizer, and
One end of cylinder is fixedly connected with the inwall of the housing of desulfurizer, after flue gas enters desulfurizer, flue gas can enter phase
The passage formed between adjacent two deflectors, produces swirling eddy, swirling eddy to enter cylinder;Meanwhile, spray thrower will be used to inhale
The alkali lye atomisation of sulfur dioxide is received, vaporific alkali lye enters the inside of cylinder, with the sulfur dioxide reaction in flue gas, reaction
Gas afterwards is continued up, and is discharged from the gas outlet of housing tip;And reacted liquid is in the effect of swirling eddy
Under be thrown on the inwall of housing, then flow to the bottom of housing along the inwall of housing, and from leakage fluid dram discharge.
The desulfurizer that the present invention is provided, by using the cyclone mixer that the present invention is provided, can increase flue gas and alkali
The contact area of liquid so that the sulfur dioxide in flue gas is more abundant with the reaction of alkali lye, so as to enhance desulfurized effect.Make
Used time, flue gas is introduced by air-introduced machine, flue gas can enter the passage formed between two neighboring deflector, produce swirling eddy,
Swirling eddy enters cylinder;Meanwhile, by for the alkali lye atomisation of sulfur dioxide absorption, vaporific alkali lye enters cylinder to spray thrower
Sulfur dioxide reaction in the inside of body, with flue gas, reacted gas continues up, and from the gas outlet of housing tip
Discharge;And reacted liquid is thrown on the inwall of housing in the presence of swirling eddy, then flowed to along the inwall of housing
The bottom of housing, and discharged from leakage fluid dram.
Brief description of the drawings
In order to illustrate more clearly of the specific embodiment of the invention or technical scheme of the prior art, below will be to specific
The accompanying drawing to be used needed for implementation method or description of the prior art is briefly described, it should be apparent that, in describing below
Accompanying drawing is some embodiments of the present invention, for those of ordinary skill in the art, before creative work is not paid
Put, other accompanying drawings can also be obtained according to these accompanying drawings.
Fig. 1 is the main structure diagram of the cyclone mixer that the embodiment of the present invention one is provided;
(cylinder and annular slab are the overlooking the structure diagram of the cyclone mixer that Fig. 2 is provided for the embodiment of the present invention one
Show);
Fig. 3 is the overlooking the structure diagram of the cylinder that the embodiment of the present invention one is provided;
Fig. 4 is the structural representation of the desulfurizer that the embodiment of the present invention two is provided.
Icon:101- cylinders;102- annular slabs;103- base plates;104- deflectors;105- housings;106- fog-spray nozzles;107-
Liquid withdrawal system;108- leakage fluid drams;109- air inlets;110- gas outlets;111- trunnions.
Specific embodiment
Technical scheme is clearly and completely described below in conjunction with accompanying drawing, it is clear that described implementation
Example is a part of embodiment of the invention, rather than whole embodiments.Based on the embodiment in the present invention, ordinary skill
The every other embodiment that personnel are obtained under the premise of creative work is not made, belongs to the scope of protection of the invention.
In the description of the invention, it is necessary to explanation, term " " center ", " on ", D score, "left", "right", " vertical ",
The orientation or position relationship of the instruction such as " level ", " interior ", " outward " be based on orientation shown in the drawings or position relationship, merely to
Be easy to the description present invention and simplify describe, rather than indicate imply signified device or element must have specific orientation,
With specific azimuth configuration and operation, therefore it is not considered as limiting the invention.Additionally, term " first ", " second ",
" the 3rd " is only used for describing purpose, and it is not intended that indicating or implying relative importance.
In the description of the invention, it is necessary to illustrate, unless otherwise clearly defined and limited, term " installation ", " phase
Company ", " connection " should be interpreted broadly, for example, it may be being fixedly connected, or being detachably connected, or be integrally connected;Can
Being to mechanically connect, or electrically connect;Can be joined directly together, it is also possible to be indirectly connected to by intermediary, Ke Yishi
Two connections of element internal.For the ordinary skill in the art, with concrete condition above-mentioned term can be understood at this
Concrete meaning in invention.
Embodiment one
Fig. 1 is the main structure diagram of the cyclone mixer that the embodiment of the present invention one is provided;Fig. 2 is the embodiment of the present invention
The overlooking the structure diagram (cylinder and annular slab are and show) of one cyclone mixer for providing;Fig. 3 is the embodiment of the present invention one
The overlooking the structure diagram of the cylinder of offer.Wherein, the dotted line in Fig. 3 represents the edge of the outer shroud of annular slab 102.Referring to Fig. 1
Shown in Fig. 3, arrow A represents the flow direction of flue gas, and arrow B represents the flow direction of alkali lye, present embodiments provides a kind of eddy flow mixing
Device, including cylinder 101, annular slab 102 and base plate 103, one end of cylinder 101 are used for the inwall with the housing 105 of desulfurizer
It is fixedly connected, the other end of cylinder 101 is fixedly connected with annular slab 102, and multiple is provided between base plate 103 and annular slab 102
Deflector 104, multiple deflectors 104 are provided at circumferentially spaced along annular slab 102, are formed between two neighboring deflector 104 and supplied
The passage that flue gas passes through;The outer shroud of annular slab 102 and the edge of deflector 104 have an intersection point, the diameter of the mistake of the outer shroud intersection point
Plate face with deflector 104 is set in inclination angle, preferably, the plate face of the base plate 103 of the present embodiment offer and annular slab 102
Plate face is parallel, and deflector 104 is in tabular, and deflector 104 has the first long side and the second long side being oppositely arranged, the
One long side is fixedly connected with base plate 103, and the second long side is fixedly connected with annular slab 102, plate face and the annular of deflector 104
The length direction of intersecting the formed intersection of the plate face of plate 102 overlaps with the length direction of the second long side, wherein, the intersection and
The edge of the outer shroud of annular slab 102 has an intersection point, and the diameter of the mistake of the outer shroud intersection point is set with the intersection in inclination angle, referring to Fig. 2
Shown, the inclination angle is α.The cyclone mixer that the present embodiment is provided, by setting deflector 104, can increase flue gas and alkali lye
Contact area so that the sulfur dioxide in flue gas is more abundant with the reaction of alkali lye, so as to enhance desulfurized effect.Using
When, by the present embodiment provide cyclone mixer be placed on desulfurizer spray thrower lower section, and by one end of cylinder 101 with
The inwall of the housing 105 of desulfurizer is fixedly connected, and after flue gas enters desulfurizer, flue gas can enter phase along arrow A directions
The passage that space between adjacent two deflectors 104 is formed, produces swirling eddy, swirling eddy to enter cylinder 101;Meanwhile,
By for the alkali lye atomisation of sulfur dioxide absorption, vaporific alkali lye enters in cylinder 101 spray thrower along arrow B directions
Sulfur dioxide reaction in portion, with flue gas, reacted gas continues to be moved upwards along arrow A directions, and from the top of housing 105
Gas outlet 110 discharge;And reacted liquid is thrown on the inwall of housing 105 in the presence of swirling eddy, Ran Houyan
The inwall of housing 105 flows to the bottom of housing 105, and is discharged from leakage fluid dram 108.
In the alternative of the present embodiment, the plate face of deflector 104 is vertical with the plate face of base plate 103.
The plate face of deflector 104 is set to vertical with the plate face of base plate 103, such mode enables to flue gas to enter
Produced swirling eddy is continued up after passage, and is fully contacted with vaporific alkali lye, so that the titanium dioxide in flue gas
Reaction between sulphur and vaporific alkali lye more fully thoroughly, enhances desulfurized effect.
In the alternative of the present embodiment, the cross-sectional area of cylinder 101 is from one end of cylinder 101 to the another of cylinder 101
End is gradually reduced.
The cross-sectional area of cylinder 101 is set to be gradually reduced from one end of cylinder 101 to the other end of cylinder 101, this
One end that the mode of sample not only contributes to cylinder 101 is fixedly connected with the inwall of housing 105 so that vaporific alkali lye can enter
Simultaneously fully reacted with the sulfur dioxide in flue gas, and be conducive to the other end and annular slab of cylinder 101 inside of cylinder 101
102 are fixedly connected, so that the diameter of required annular slab 102 is smaller, not only save raw material, reduce cost, and
Gap is set between meeting the inwall of annular slab 102 and housing 105.
In the alternative of the present embodiment, gap sets between the edge of the outer shroud of annular slab 102 and the inwall of housing 105
Put.
Gap between the inwall of the edge of the outer shroud of annular slab 102 and housing 105 is set, such mode is enabled to
Reacted liquid is flowed in housing 105 from cylinder 101 along arrow B directions under the drive of swirling eddy by passage
Wall.
In the alternative of the present embodiment, inclination angle is 30~60 °.
If inclination alpha is excessive, the distribution of deflector 104 is more intensive, is unfavorable for that flue gas enters cyclone mixer, so that
The reaction of the sulfur dioxide in vaporific alkali lye and flue gas is hindered, causes desulfurized effect poor.
If inclination alpha is too small, flue gas enters after passage, will not produce swirling eddy, and flue gas is not only resulted in vaporific alkali
The contact area of liquid is smaller, and reacted liquid will not be thrown on the inwall of housing 105, but directly accumulates in base plate
On 103, being smoothed out for sweetening process is have impact on.
Preferably, inclination alpha is 40 °.
In the alternative of the present embodiment, also including trunnion 111, one end and the other end of cylinder 101 of trunnion 111 are fixed
Connection, the other end of trunnion 111 is fixedly connected with annular slab 102.
Preferably, the section of the trunnion 111 of the present embodiment offer is circle, by one end of trunnion 111 and cylinder 101
The other end is fixedly connected, and the other end of trunnion 111 is fixedly connected with annular slab 102, and such mode enables to the He of cylinder 101
Connection between annular slab 102 is more firm, so as to improve the physical life of cyclone mixer.
In the alternative of the present embodiment, the plate face of two neighboring deflector 104 is set in inclination angle, the angular range at inclination angle
It it is 18~30 °, preferably, inclination angle is 22.5 °
Preferably, cylinder 101, annular slab 102, base plate 103 and deflector 104 that the present embodiment is provided are by propylene
Nitrile-BS (ABS) is made.ABS not only has good impact resistance, heat resistance, lower temperature resistance and resistance to
Chemicals, but also with easy processing, product size stabilization, lustrous surface is good the features such as, it is easy to application and coloring, also
The secondary operation such as surface metallization, plating, welding, hot pressing and bonding can be carried out, is a kind of extremely wide thermoplasticity work of purposes
Engineering plastics.ABS outward appearances for opaque in ivory white pellet, its product can into colourful, and with high gloss.
The alkali lye that the present embodiment is provided uses existing alkali lye.
Embodiment two
Fig. 4 is the structural representation of the desulfurizer that the embodiment of the present invention two is provided.Shown in Figure 4, arrow A represents cigarette
The flow direction of gas, arrow B represents the flow direction of alkali lye, present embodiments provides a kind of desulfurizer, including housing 105, housing 105
Inside is from top to bottom disposed with the cyclone mixer that spray thrower and the embodiment of the present invention one are provided, and the feed tube of spray thrower is used
Connected in alkali liquid tank;Air inlet 109, gas outlet 110 and leakage fluid dram 108 are provided with housing 105, air inlet 109 is located at rotation
The lower section of blender is flowed, is connected for the air outlet with air-introduced machine, to introduce flue gas;Gas outlet 110 is located at the top of housing 105
End, for discharging the gas after desulfurization;Leakage fluid dram 108 is located at the bottom of housing 105, for discharging and the alkali after smoke reaction
Liquid.The desulfurizer that the present embodiment is provided, by using the cyclone mixer that the embodiment of the present invention one is provided, can increase flue gas
With the contact area of alkali lye so that the sulfur dioxide in flue gas is more abundant with the reaction of alkali lye, so as to enhance desulfurized effect.
When in use, flue gas is introduced by air-introduced machine, flue gas can be formed along arrow A directions between two neighboring deflector 104
Passage, produces swirling eddy, swirling eddy to enter cylinder 101;Meanwhile, spray thrower will be sprayed into for the alkali lye of sulfur dioxide absorption
Vaporific, vaporific alkali lye enters the inside of cylinder 101 along arrow B directions, with the sulfur dioxide reaction in flue gas, reacted gas
Body continues to be moved upwards along arrow A directions, and is discharged from the gas outlet 110 on the top of housing 105;And reacted liquid is in rotation
It is thrown in the presence of air-flow on the inwall of housing 105, then flows to the bottom of housing 105 along the inwall of housing 105, and from row
Liquid mouthful 108 is discharged.
In the alternative of the present embodiment, spray thrower includes multiple fog-spray nozzles 106, the interval setting of multiple fog-spray nozzles 106.
The set-up mode of fog-spray nozzle 106 has various, for example:Multiple fog-spray nozzles 106 can along housing 105 it is circumferential uniform between
Every setting, can be with circumferentially arranged one circle, it is also possible to along the multi-turn that is radially arranged of housing 105, the fog-spray nozzle 106 in two adjacent rings
It is staggered, such mode can make that the vaporific alkali lye of ejection is more uniform, and area coverage is bigger, so as to the contact with flue gas
Area is bigger, reacts more abundant.
And for example:Multiple fog-spray nozzles 106 can be set along the spaced radial of housing 105.
Shown in Figure 4, the quantity of the fog-spray nozzle 106 that the present embodiment is provided is four, and four fog-spray nozzles 106 are along housing
105 spaced radial is set.
In the alternative of the present embodiment, also including liquid withdrawal system 107, the inlet of liquid withdrawal system 107 with
Leakage fluid dram 108 is connected.
By setting liquid withdrawal system 107, pair can be recycled with the alkali lye after smoke reaction, prevent its dirty
Dye environment.Preferably, the liquid withdrawal system 107 that the present embodiment is provided uses existing liquid withdrawal system.
It should be noted that in the alternative of the present embodiment, the quantity of fog-spray nozzle 106 is not only limited to above-mentioned one kind,
The fog-spray nozzle 106 of other quantity can also be chosen according to actual treatment quantity, is used to realize the function of alkali lye atomisation;
The present embodiment of fog-spray nozzle 106 for other quantity is no longer specifically repeated one by one.
Finally it should be noted that:Various embodiments above is merely illustrative of the technical solution of the present invention, rather than its limitations;To the greatest extent
Pipe has been described in detail with reference to foregoing embodiments to the present invention, it will be understood by those within the art that:Its according to
The technical scheme described in foregoing embodiments can so be modified, or which part or all technical characteristic are entered
Row equivalent;And these modifications or replacement, the essence of appropriate technical solution is departed from various embodiments of the present invention technology
The scope of scheme.
Claims (10)
1. a kind of cyclone mixer, it is characterised in that:Including cylinder, annular slab and base plate, one end of the cylinder is used for and takes off
The inwall of the housing of sulphur device is fixedly connected, and the other end of the cylinder is fixedly connected with the annular slab, the base plate and institute
State and be provided with multiple deflectors, the multiple deflector being provided at circumferentially spaced along the annular slab, adjacent two between annular slab
The passage passed through for flue gas is formed between the individual deflector;The outer shroud of the annular slab has with the edge of the deflector to be handed over
Point, the diameter of the mistake of the outer shroud intersection point is set with the plate face of the deflector in inclination angle.
2. cyclone mixer according to claim 1, it is characterised in that:The plate of the plate face of the deflector and the base plate
Face is vertical.
3. cyclone mixer according to claim 1, it is characterised in that:The cross-sectional area of the cylinder is by the cylinder
One end is gradually reduced to the other end of the cylinder.
4. cyclone mixer according to claim 1, it is characterised in that:The edge of the outer shroud of the annular slab and the shell
Gap is set between the inwall of body.
5. cyclone mixer according to claim 1, it is characterised in that:The inclination angle is 30~60 °.
6. cyclone mixer according to claim 5, it is characterised in that:The inclination angle is 40 °.
7. cyclone mixer according to any one of claim 1 to 6, it is characterised in that:Also include trunnion, the trunnion
One end be fixedly connected with the other end of the cylinder, the other end of the trunnion is fixedly connected with the annular slab.
8. a kind of desulfurizer, it is characterised in that:Including housing, the inside of the housing is from top to bottom disposed with spray thrower
With the cyclone mixer as any one of claim 1 to 7, the feed tube of the spray thrower with alkali liquid tank for connecting;
Air inlet, gas outlet and leakage fluid dram are provided with the housing, the air inlet is located at the lower section of the cyclone mixer, is used for
Connected with the air outlet of air-introduced machine, to introduce flue gas;The gas outlet is located at the top of the housing, after discharging desulfurization
Gas;The leakage fluid dram is located at the bottom of the housing, for discharging and the alkali lye after the smoke reaction.
9. desulfurizer according to claim 8, it is characterised in that:The spray thrower includes multiple fog-spray nozzles, Duo Gesuo
State fog-spray nozzle interval setting.
10. desulfurizer according to claim 8, it is characterised in that:Also include liquid withdrawal system, the liquids recovery
The inlet of device is connected with the leakage fluid dram.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201710063200.5A CN106731934A (en) | 2017-01-25 | 2017-01-25 | Cyclone mixer and the desulfurizer using the blender |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201710063200.5A CN106731934A (en) | 2017-01-25 | 2017-01-25 | Cyclone mixer and the desulfurizer using the blender |
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Publication Number | Publication Date |
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CN106731934A true CN106731934A (en) | 2017-05-31 |
Family
ID=58956497
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Application Number | Title | Priority Date | Filing Date |
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CN201710063200.5A Withdrawn CN106731934A (en) | 2017-01-25 | 2017-01-25 | Cyclone mixer and the desulfurizer using the blender |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN114504922A (en) * | 2022-01-29 | 2022-05-17 | 联丰环保科技有限公司 | Ozone treatment equipment and treatment method thereof |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4273750A (en) * | 1979-04-24 | 1981-06-16 | Energy And Pollution Controls, Inc. | Flue gas desulfurization apparatus and method |
CN2797900Y (en) * | 2004-12-29 | 2006-07-19 | 国家环境保护总局华南环境科学研究所 | Wet type flue-gas purification equipment |
CN1820836A (en) * | 2006-01-25 | 2006-08-23 | 山东大学 | Circulation fluidized bed swirl-direct flow composite fluidizing device |
CN206483348U (en) * | 2017-01-25 | 2017-09-12 | 大连铭晟环保设备有限公司 | Cyclone mixer and the desulfurizer using the blender |
-
2017
- 2017-01-25 CN CN201710063200.5A patent/CN106731934A/en not_active Withdrawn
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4273750A (en) * | 1979-04-24 | 1981-06-16 | Energy And Pollution Controls, Inc. | Flue gas desulfurization apparatus and method |
CN2797900Y (en) * | 2004-12-29 | 2006-07-19 | 国家环境保护总局华南环境科学研究所 | Wet type flue-gas purification equipment |
CN1820836A (en) * | 2006-01-25 | 2006-08-23 | 山东大学 | Circulation fluidized bed swirl-direct flow composite fluidizing device |
CN206483348U (en) * | 2017-01-25 | 2017-09-12 | 大连铭晟环保设备有限公司 | Cyclone mixer and the desulfurizer using the blender |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN114504922A (en) * | 2022-01-29 | 2022-05-17 | 联丰环保科技有限公司 | Ozone treatment equipment and treatment method thereof |
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Application publication date: 20170531 |
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