CN105833710A - Centrifugal reaction tower - Google Patents
Centrifugal reaction tower Download PDFInfo
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- CN105833710A CN105833710A CN201610322461.XA CN201610322461A CN105833710A CN 105833710 A CN105833710 A CN 105833710A CN 201610322461 A CN201610322461 A CN 201610322461A CN 105833710 A CN105833710 A CN 105833710A
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- absorbent
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- 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
- B01D53/80—Semi-solid phase processes, i.e. by using slurries
-
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
-
- 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
-
- 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
- B01D53/501—Sulfur oxides by treating the gases with a solution or a suspension of an alkali or earth-alkali or ammonium compound
-
- 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
- B01D53/46—Removing components of defined structure
- B01D53/60—Simultaneously removing sulfur oxides and nitrogen 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
- B01D53/74—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
- B01D2251/00—Reactants
- B01D2251/40—Alkaline earth metal or magnesium compounds
- B01D2251/404—Alkaline earth metal or magnesium compounds of calcium
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Environmental & Geological Engineering (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Treating Waste Gases (AREA)
- Gas Separation By Absorption (AREA)
Abstract
The invention discloses a centrifugal reaction tower which comprises a shell for providing space for smoke flowing and chemical reacting, and a spraying liquid generating device for providing absorbent in an atomizing state or spraying state or washing state. The spraying liquid generating device is located in an inner cavity of the shell. A smoke inlet for smoke to enter the shell, a smoke discharge opening for discharging reacting smoke, and a discharge opening for discharging reaction products are formed in the shell. A rotating mechanism which is used for making reacting smoke move at high speed under centrifugal force along a spiral or swirl-shaped flowing track in the inner cavity of the whole shell and increasing the number of contact times and the contact strength of smoke and the absorbent without leaving contact dead corners is arranged in the inner cavity of the shell. The requirements for environment protection or industrial indexes can be met in the same way by decreasing the size of a centrifugal reaction tower, investment and running cost and running power can be reduced, and the effects of rapid desulfuration, dust removal and removal of other heavy metal can be achieved, and the desulfuration efficiency is remarkably improved.
Description
Technical field
The present invention relates to mass transfer, heat transfer and chemical reaction tower technology field, especially, relate to one and be applied to thermoelectricity, chemical industry etc.
The reaction towers such as the semidry method tower of industry, packed tower, liquid column tower.
Background technology
The chemical reaction towers such as semidry method tower, packed tower, liquid column tower are widely used in thermal power plant, chemical plant etc., such as in thermal power plant
In, these reaction towers are applied in flue gas desulfurization and the denitration of thermal power plant, by nebulizer or the first spray in its desulfurization reaction tower
The flue gas of sulfur-bearing is mixed or washs by mouth or fluid column etc., and its desulfurizing agent produces chemical reaction with the sulfur in flue gas, produces Gypsum Fibrosum
Or lime-ash etc., thus remove the sulfurous gas in flue gas.
But existing chemical reaction tower has the disadvantage in that
1, the chemical reaction equipment during reaction tower is thermal power plant or other industry, in its whole technique, cost is maximum, and energy consumption is the highest；
And in the course of reaction that flue gas or fluid are in tower, flow velocity must be low because the highest meeting of flow velocity cause reaction frequency of exposure few or
It is not in contact with, thus causes reaction effect difference or the problem such as efficiency is low, and make to discharge gas and do not reach environmental protection or industrial index
Requirement；Flow velocity is the lowest the most also can have problems, and can make to require that the diameter of reaction tower and height increase, also require that spray or spray
The absorbent gone out or the flow of reacting fluid and flow velocity increase, and the requirement that can meet environmental protection or industrial index with this so can
Investment is increased, and power consumption increases.
2, the efficiency of the chemical reaction such as the mass transfer in tower or heat transfer is low, if needing to improve efficiency, cost of investment can be multiplied.
3, in the industries such as thermal power plant, chemical plant, steel mill, dedusting in flue gas desulfurization and except fog effect is poor, water consumption greatly, Yi Jie
Dirt or blocking etc..
Summary of the invention
The invention provides a kind of centrifugal reaction tower, to solve existing mass transfer, heat transfer and chemical reaction tower, exist bulky,
The technical problems such as power consumption is big, cost of investment is high.
The present invention provides a kind of centrifugal reaction tower, including for for flow of flue gas and carry out chemical reaction provide space housing and
For providing the hydrojet generating means of the absorbent of spray pattern or spray state or washing state, hydrojet generating means is in housing
In inner chamber, housing be provided with for flue gas enter housing cavity air inlet, for discharge reacted flue gas air vent and
For discharging the floss hole of reaction product, housing cavity is provided with the flue gas reacted for making whole housing cavity carry out and is centrifuged
Power effect spirally or the flow trace high-speed motion of eddy flow shape and increase the frequency of exposure of flue gas and absorbent and contact strength and
Do not stay the rotating mechanism at contact dead angle.
Further, rotating mechanism includes the main shaft being vertically laid in housing cavity, is installed on main shaft and with main axis
The flue gas reacted for making whole housing cavity carry out by centrifugal action spirally or eddy flow shape flow trace high-speed motion also
Increase flue gas and the frequency of exposure of absorbent and the impeller of contact strength and be located at housing driving that is outer and that rotate for drive shaft
Device.
Further, centrifugal reaction tower is centrifugal semidry method tower, centrifugal packed tower or centrifugal liquid column tower.
Further, being provided with least one set impeller in the housing cavity of centrifugal semidry method tower, hydrojet generating means is located at impeller extremely
Few side, hydrojet generating means uses the absorbent slurry pipeline with the atomizing wheel for producing atomization absorption agent, and atomizing wheel fills
In the outfan of absorbent slurry pipeline, absorbent slurry pipeline is communicated to outside housing；Air inlet is located at the top of housing, aerofluxus
Mouth and floss hole are respectively arranged on the bottom of housing.
Further, being provided with least one set impeller in the housing cavity of centrifugal semidry method tower, hydrojet generating means is located at case top,
The outfan of hydrojet generating means is towards housing cavity, and hydrojet generating means uses with the atomizing wheel for producing atomization absorption agent
Absorbent slurry pipeline, atomizing wheel is loaded on the outfan of absorbent slurry pipeline, and absorbent slurry pipeline is communicated to outside housing；
Air inlet is located at the top of housing, air vent and floss hole and is respectively arranged on the bottom of housing.
Further, being provided with least one set impeller in the housing cavity of centrifugal semidry method tower, hydrojet generating means is located at impeller extremely
Few side, hydrojet generating means uses with for the absorbent slurry pipe to the first jet of housing cavity jet atomization absorbent
Road, first jet is loaded on the delivery outlet of absorbent slurry pipeline, and absorbent slurry pipeline is communicated to outside housing；Air inlet is located at
The top of housing, air vent and floss hole are respectively arranged on the bottom of housing.
Further, being provided with demister in the housing cavity of centrifugal packed tower, hydrojet generating means uses with in housing
The absorbent slurry pipeline of the first jet of chamber jet atomization absorbent, first jet is loaded on the delivery outlet of absorbent slurry pipeline,
Absorbent slurry pipeline is communicated to outside housing, is provided with impeller described in least one set in housing cavity；Air inlet and floss hole set respectively
In the bottom of housing, the top of housing is located at by air vent；Sieve plate with holes it is additionally provided with between air inlet and absorbent slurry pipeline,
The upper surface of sieve plate is covered with packing layer.
Further, being provided with demister in the housing cavity of centrifugal liquid column tower, hydrojet generating means uses band for upwards spraying liquid
Post and with smoke contacts with the absorbent slurry pipeline of second nozzle of washing flue gas, second nozzle is loaded on absorbent slurry pipeline
On delivery outlet, absorbent slurry pipeline is communicated to outside housing, is provided with impeller described in least one set in housing cavity；Air inlet and row
Putting mouth and be respectively arranged on the bottom of housing, the top of housing is located at by air vent, and lower housing portion is additionally provided with air intake.
Further, the laying mode of the blade of impeller uses along the radially extending of main shaft, uses the inlet end direction to housing to incline
Tiltedly, at least one in the direction, outlet side of housing tilts is used.
Further, the blade of impeller uses plate blade or arc shaped blade.
The method have the advantages that
The present invention is centrifuged reaction tower, changes the flow of flue gas track in housing cavity by rotating mechanism, makes whole housing cavity enter
By centrifugal action spirally or the flow trace high-speed motion of eddy flow shape, thus it is raw with hydrojet to increase flue gas for the flue gas of row reaction
Become frequency of exposure and the contact strength of the absorbent of the spray pattern that generated of device or spray state or washing state, to reach fast
Speed and the purpose of fully reaction, make contacting between flue gas with absorbent not stay contact dead angle.Flue gas is through contacting with absorbent soon
Speed reacts, thus generates the little granule of lime-ash, Gypsum Fibrosum or ammonium sulfate, and these granules are gone forward side by side along with absorbent discharges housing cavity
Row is collected, is dried or filtering means dehydration collection, can become lime-ash, Gypsum Fibrosum or chemical fertilizer and be utilized.Flue gas quickly rotates so that powder
Reunite between dirt especially fine dust and combine with adhesive Gypsum Fibrosum or ammonium sulfate, thus strengthen in reactor
The removing of dust.The size of centrifugal reaction tower can be reduced to reach the requirement of environmental protection or industrial index equally, it is possible to reduction investment,
Reduce usable floor area, reduce operating cost and reduce operation power, desulfurization rapidly, dedusting can be obtained simultaneously, dehumidify and de-
Except the effect of other heavy metal, the efficiency of desulfurization also significantly improves.The consumable goodss such as absorbent can sufficiently be reacted and be used,
Utilization rate is high, thus reduces the usage amount of the consumable goods such as absorbent and water consumption.
In addition to objects, features and advantages described above, the present invention also has other objects, features and advantages.Below
With reference to the accompanying drawings, the present invention is further detailed explanation.
Accompanying drawing explanation
The accompanying drawing of the part constituting the application is used for providing a further understanding of the present invention, the illustrative examples of the present invention and
Its explanation is used for explaining the present invention, is not intended that inappropriate limitation of the present invention.In the accompanying drawings:
Fig. 1 is one of structural representation of centrifugal semi-dry desulphurization tower of the preferred embodiment of the present invention；
Fig. 2 is the two of the structural representation of the centrifugal semi-dry desulphurization tower of the preferred embodiment of the present invention；
Fig. 3 is the three of the structural representation of the centrifugal semi-dry desulphurization tower of the preferred embodiment of the present invention；
Fig. 4 is the structural representation of the centrifugal packed tower of the preferred embodiment of the present invention；
Fig. 5 is the structural representation of the centrifugal liquid column tower of the preferred embodiment of the present invention.
Marginal data:
1, housing；101, air inlet；102, air vent；103, floss hole；104, air intake；2, hydrojet generates dress
Put；201, atomizing wheel；202, absorbent slurry pipeline；203, first jet；204, fluid column；205, second nozzle；3、
Rotating mechanism；301, main shaft；302, impeller；303, driving means；4, demister；5, sieve plate；6, packing layer.
Detailed description of the invention
Below in conjunction with accompanying drawing, embodiments of the invention are described in detail, but the present invention can by following be limited and covered
Multitude of different ways is implemented.
Fig. 1 is one of structural representation of centrifugal semi-dry desulphurization tower of the preferred embodiment of the present invention；Fig. 2 is that the present invention is the most real
Execute the centrifugal semi-dry desulphurization tower of example structural representation two；Fig. 3 is the centrifugal semi-dry desulphurization tower of the preferred embodiment of the present invention
Structural representation three；Fig. 4 is the structural representation of the centrifugal packed tower of the preferred embodiment of the present invention；Fig. 5 is that the present invention is excellent
Select the structural representation of the centrifugal liquid column tower of embodiment.
As it is shown in figure 1, the centrifugal reaction tower that the band CENTRIFUGAL ACCELERATING of the present embodiment rotates, including for for flow of flue gas and changing
Learn reaction and provide the housing 1 in space and for providing the hydrojet of the absorbent of spray pattern or spray state or washing state to generate
Device 2, hydrojet generating means 2 is in housing 1 inner chamber, and housing 1 is provided with the air inlet entering housing 1 inner chamber for flue gas
101, for discharging the air vent 102 of reacted flue gas and for discharging the floss hole 103 of reaction product, in housing 1
Chamber is provided with for the flue gas making whole housing 1 inner chamber carry out reacting by centrifugal action spirally or eddy flow shape flowing at a high speed
Orbiting motion also increases the frequency of exposure of flue gas and absorbent and contact strength and does not stay the rotating mechanism 3 contacting dead angle.The present invention from
Heart reaction tower, changes the flow of flue gas track in housing cavity by rotating mechanism, makes the flue gas of whole housing 1 inner chamber be centrifuged
Power effect spirally or the flow trace high-speed motion of eddy flow shape, thus increases the atomization that flue gas is generated with hydrojet generating means
The frequency of exposure of the absorbent of state or spray state or washing state and contact strength, to reach the purpose of quick and abundant reaction,
Contacting between flue gas with absorbent is made not stay contact dead angle.Flue gas quickly reacts through contacting with absorbent, thus generates
The little granule of lime-ash, Gypsum Fibrosum or ammonium sulfate, these granules are along with absorbent discharges housing cavity and is collected, is dried or filters de-
Water is collected, and can become lime-ash, Gypsum Fibrosum or chemical fertilizer and be utilized.Flue gas quickly rotates so that between dust especially fine dust
Reunite and combine with adhesive Gypsum Fibrosum or ammonium sulfate, thus strengthen the removing of the dust in reactor.Can reduce
The size of centrifugal reaction tower is to reach the requirement of environmental protection or industrial index equally, it is possible to reduces investment, reduce operating cost and reduction
Running power, can obtain desulfurization rapidly, dedusting simultaneously and remove the effect of other heavy metal, the efficiency of desulfurization significantly carries
High.The consumable goodss such as absorbent can sufficiently be reacted and be used, and utilization rate is high, thus reduces making of the consumable goodss such as absorbent
Consumption.
As shown in Figure 1, Figure 2, shown in Fig. 3, Fig. 4 and Fig. 5, in the present embodiment, rotating mechanism 3 includes vertically being laid in housing
Main shaft 301 in 1 inner chamber, it is installed on main shaft 301 and rotates with main shaft 301 and react for making whole housing 1 inner chamber carry out
Flue gas by centrifugal action spirally or the flow trace high-speed motion of eddy flow shape and increase flue gas and absorbent frequency of exposure and
Contact strength and do not stay the impeller 302 at contact dead angle and be located at housing 1 driving means that is outer and that rotate for drive shaft 301
303.Rotating mechanism 3 includes: main shaft 301, and gas flow direction along housing 1 inner chamber is rotating to be assemblied in housing 1
Chamber.Impeller 302, is installed on main shaft 301 and rotates the gas flowing for extending and change in housing 1 inner chamber with main shaft 301
Track, spray pattern that the flue gas of whole housing 1 inner chamber generates in hydrojet generating means or spray state or the absorption of washing state
Helical form at a high speed or the high-speed motion of eddy flow shape is made, so that flue gas is more with the frequency of exposure of absorbent and contacts strong around agent
Degree more greatly and does not stay dead angle.Driving means 303, is located at outside housing 1 and rotates for drive shaft 301.Driving means 303
Output shaft coaxially arranged with main shaft 301, or the output shaft of driving means 303 be perpendicular to main shaft 301 arrange and pass through switching
Part connects and drive shaft 301 rotates.Driving means 303 is utilized to drive main shaft 301 to rotate, main shaft 301 impeller 302
Rotating, the flue gas in agitation housing 1 inner chamber mix with absorbent, thus in multiple times, react rapidly, reduces and react extremely
Angle.Driving means 303 is placed in outside housing 1, thus without sealing and reducing the mixed gas corrosion to driving means 303,
Thus improve the service life of driving means 303, and facilitate control and the maintenance of driving means 303.Driving means 303
Output shaft is coaxially arranged with main shaft 301, or the output shaft of driving means 303 is perpendicular to main shaft 301 and arranges and pass through adaptor
Connect and drive shaft 301 rotates.Different set-up modes can be selected according to using environment and installation environment, thus reduce
Space occupancy rate.
In the present embodiment, as shown in Figure 1, Figure 2 and Figure 3, centrifugal reaction tower is centrifugal semidry method tower.As shown in Figure 4, centrifugal
Reaction tower is centrifugal packed tower.As it is shown in figure 5, centrifugal reaction tower is centrifugal liquid column tower.Make the scope of application wider.
As it is shown in figure 1, in the present embodiment, housing 1 inner chamber of centrifugal semidry method tower is provided with least one set impeller 302.Hydrojet is raw
Device 2 is become to be located at least side of impeller 302.Alternatively, housing 1 inner chamber of centrifugal semidry method tower is provided with at least two group leaves
Wheel 302.Hydrojet generating means 2 is located between adjacent two impellers 302.Hydrojet generating means 2 uses with for producing atomization suction
Receive the absorbent slurry pipeline 202 of the atomizing wheel 201 of agent.Atomizing wheel 201 is loaded on the outfan of absorbent slurry pipeline 202.Inhale
Receive agent slurry pipeline 202 to be communicated to outside housing 1.The top of housing 1 is located at by air inlet 101.Air vent 102 and floss hole 103
It is respectively arranged on the bottom of housing 1.Changed the flow of flue gas track in housing cavity by two groups of impellers 302 respectively, make whole shell
The flue gas of body 1 inner chamber by centrifugal action spirally or the flow trace high-speed motion of eddy flow shape, thus increases flue gas and atomization
Take turns frequency of exposure and the contact strength of the absorbent of 201 spray patterns generated or spray state or washing state, to reach fast
Speed and the purpose of fully reaction, make contacting between flue gas with absorbent not stay contact dead angle.Flue gas is through contacting with absorbent soon
Speed reacts, thus generates the little granule of lime-ash, and these granules are along with absorbent discharges housing cavity and is collected, Ji Kecheng
It is utilized for lime-ash.Flue gas quickly rotates so that between dust especially fine dust, reunion and adhesive lime-ash are combined in one
Rise, thus strengthen the removing of dust.The air-flow of high speed rotating makes to reduce or exempt fouling and blocking simultaneously.Can reduce from
The size of heart semidry method tower is to reach the requirement of environmental protection or industrial index equally, it is possible to reduces investment, reduce operating cost and reduction
Running power, can obtain desulfurization rapidly, dedusting simultaneously, dehumidify and remove the effect of other heavy metal, the efficiency of desulfurization is also
Significantly improve.The consumable goodss such as absorbent can sufficiently be reacted and be used, and utilization rate is high, thus reduce electricity or water etc. and consume
The usage amount of product.Alternatively, floss hole 103 use opening towards taper bucket.
As in figure 2 it is shown, in the present embodiment, housing 1 inner chamber of centrifugal semidry method tower is provided with least one set impeller 302.Alternatively,
Housing 1 inner chamber of centrifugal semidry method tower is provided with one group of impeller 302.Hydrojet generating means 2 is located at housing 1 top.Hydrojet generates
The outfan of device 2 is towards housing 1 inner chamber.Hydrojet generating means 2 uses with the atomizing wheel 201 for producing atomization absorption agent
Absorbent slurry pipeline 202.Atomizing wheel 201 is loaded on the outfan of absorbent slurry pipeline 202.Absorbent slurry pipeline 202
It is communicated to outside housing 1.The top of housing 1 is located at by air inlet 101.Air vent 102 and floss hole 103 are respectively arranged on housing 1
Bottom.Air inlet 101 is made to be mutually perpendicular to and make flue gas and atomization absorption agent direct collision with the outfan of atomizing wheel 201, logical
Crossing the flow of flue gas track that impeller 302 changes in housing cavity, the flue gas making whole housing 1 inner chamber carry out reacting is centrifuged masterpiece
With spirally or the flow trace high-speed motion of eddy flow shape, thus increase spray pattern that flue gas generated with atomizing wheel 201 or
The frequency of exposure of the absorbent of spray state or washing state and contact strength, to reach the purpose of quick and abundant reaction, make cigarette
Contacting between gas with absorbent does not stays contact dead angle.Flue gas quickly reacts through contacting with absorbent, thus generates lime-ash
Little granule, these granules are discharged housing cavity along with absorbent and are dried or filtering means dehydration is collected, can become lime-ash and quilt
Utilize.Flue gas quickly rotates and combines with adhesive lime-ash so that reuniting between dust especially fine dust, thus adds
The strong removing of dust.The air-flow of high speed rotating makes to reduce or exempt fouling and blocking simultaneously.Centrifugal semidry method tower can be reduced
Size to reach the requirement of environmental protection or industrial index equally, it is possible to reduce investment, reduce operating cost and reduce run power,
Can obtain desulfurization rapidly, dedusting simultaneously and remove the effect of other heavy metal, the efficiency of desulfurization also significantly improves.Absorbent
Can sufficiently be reacted Deng consumable goods and use, utilization rate is high, thus reduces the usage amount of the consumable goodss such as electricity and water.Optional
Ground, floss hole 103 use opening towards taper bucket.
As it is shown on figure 3, in the present embodiment, housing 1 inner chamber of centrifugal semidry method tower is provided with in inner chamber and is provided with least one set impeller
302.Hydrojet generating means 2 is located at least side of impeller 302.Alternatively, housing 1 inner chamber of centrifugal semidry method tower is provided with
At least two group impellers 302.Hydrojet generating means 2 is located between adjacent two impellers 302 and/or in the bottom cavity of impeller 302.
Hydrojet generating means 2 uses with the absorbent slurry pipeline 202 for the first jet 203 to housing 1 inner chamber injection absorbent.
First jet 203 is loaded on the delivery outlet of absorbent slurry pipeline 202.Absorbent slurry pipeline 202 is communicated to outside housing 1.
The top of housing 1 is located at by air inlet 101.Air vent 102 and floss hole 103 are respectively arranged on the bottom of housing 1.Pass through impeller
302 with the interphase distribution of absorbent slurry pipeline 202, utilize impeller 302 to change the flow of flue gas track in housing cavity, make whole
Individual housing 1 inner chamber carries out the flue gas that reacts by centrifugal action spirally or the flow trace high-speed motion of eddy flow shape, thus increases
Add the absorbent of spray pattern that flue gas and first jet 203 ejected or spray state or washing state frequency of exposure and
Contact strength, to reach the purpose of quick and abundant reaction, makes contacting between flue gas with absorbent not stay contact dead angle.Flue gas
Quickly reacting through contacting with absorbent, thus generate the little granule of lime-ash, these granules discharge housing cavity along with absorbent
And be dried or filtering means dehydration collection.Flue gas quickly rotates reunites between the especially fine dust of the dust so that lime-ash, thus
Strengthen the removing of dust.The air-flow of high speed rotating makes to reduce or exempt fouling and blocking simultaneously.Centrifugal semidry method can be reduced
The size of tower is to reach the requirement of environmental protection or industrial index equally, it is possible to reduces investment, reduces operating cost and reduce operation power,
Can obtain desulfurization rapidly, dedusting simultaneously and remove the effect of other heavy metal, the efficiency of desulfurization also significantly improves.Absorbent
Can sufficiently be reacted Deng consumable goods and use, utilization rate is high, thus reduces the usage amount of the consumable goodss such as electricity and water.Optional
Ground, floss hole 103 use opening towards taper bucket.
As shown in Figure 4, in the present embodiment, housing 1 inner chamber of centrifugal packed tower is provided with demister 4.Hydrojet generating means 2 is adopted
With with for the absorbent slurry pipeline 202 to the first jet 203 of housing 1 inner chamber jet atomization absorbent.First jet
On 203 delivery outlets being loaded on absorbent slurry pipeline 202.Absorbent slurry pipeline 202 is communicated to outside housing 1.Housing 1 inner chamber
In be provided with impeller 302 described in least one set.Impeller 302 is located between demister 4 and absorbent slurry pipeline 202.Air inlet
101 and floss hole 103 be respectively arranged on the bottom of housing 1.The top of housing 1 is located at by air vent 102.Air inlet 101 and absorption
Sieve plate 5 with holes it is additionally provided with between agent slurry pipeline 202.The upper surface of sieve plate 5 is covered with packing layer 6.Impeller 302 is located at
Between demister 4 and absorbent slurry pipeline 202, utilize impeller 302 to change the flow of flue gas track in housing cavity, make whole
Individual housing 1 inner chamber and absorbent carry out the flue gas that reacts by centrifugal action spirally or the flow trace high-speed motion of eddy flow shape,
Thus increase spray pattern or spray state or the absorbent of washing state that flue gas ejected with first jet 203 and remove
The frequency of exposure of day with fog 4 and contact strength, to reach the purpose of quick and abundant reaction, make flue gas and absorbent and demister 4
Between contact do not stay contact dead angle.Flue gas quickly reacts through contacting with absorbent, thus generates Gypsum Fibrosum or ammonium sulfate is little
Granule, these granules are discharged housing cavity along with absorbent and are dried or filtering means dehydration collection, can become Gypsum Fibrosum or chemical fertilizer
And be utilized.Flue gas quickly rotates and is combined in adhesive Gypsum Fibrosum or ammonium sulfate so that reuniting between dust especially fine dust
Together, thus strengthen the removing of dust.The size of centrifugal packed tower can be reduced to reach wanting of environmental protection or industrial index equally
Ask, it is possible to reduce investment, reduce operating cost and reduce run power, can obtain simultaneously desulfurization rapidly, dedusting, dehumidifying with
And removing the effect of other heavy metal, the efficiency of desulfurization also significantly improves.The consumable goodss such as absorbent can sufficiently be reacted and
Using, utilization rate is high, thus reduces the usage amount of the consumable goodss such as absorbent.
As it is shown in figure 5, in the present embodiment, housing 1 inner chamber of centrifugal liquid column tower is provided with demister 4.Hydrojet generating means 2 is adopted
With band for upwards spraying fluid column 204 and with smoke contacts to wash the absorbent slurry pipeline 202 of the second nozzle 205 of flue gas.
Second nozzle 205 is loaded on the delivery outlet of absorbent slurry pipeline 202.Absorbent slurry pipeline 202 is communicated to outside housing 1.
Housing 1 inner chamber is provided with impeller 302 described in least one set.Impeller 302 is between demister 4 and second nozzle 205.Air inlet
Mouth 101 and floss hole 103 are respectively arranged on the bottom of housing 1.The top of housing 1 is located at by air vent 102.Housing 1 bottom is also
It is provided with air intake 104.Impeller 302 is located between demister 4 and second nozzle 205, utilizes impeller 302 to change in housing
Flow of flue gas track in chamber, make flue gas that whole housing 1 inner chamber and absorbent carry out reacting by centrifugal action spirally or
The flow trace high-speed motion of eddy flow shape, thus increase spray pattern or the shape spray that flue gas is ejected with first jet 203
State or the washing absorbent of state and the frequency of exposure of demister 4 and contact strength, to reach the purpose of quick and abundant reaction,
Contacting between flue gas with absorbent and demister 4 is made not stay contact dead angle.Flue gas quickly reacts through contacting with absorbent,
Thus generating Gypsum Fibrosum or the little granule of ammonium sulfate, these granules are discharged housing cavity along with absorbent and are dried or filtering means dehydration receipts
Collection, can become Gypsum Fibrosum or chemical fertilizer and be utilized.Flue gas quickly rotates so that reuniting between dust especially fine dust viscous with band
Gypsum Fibrosum or the ammonium sulfate of property combine, thus strengthen the removing of dust.The size of centrifugal liquid column tower can be reduced with equally
Reach the requirement of environmental protection or industrial index, it is possible to reduce investment, reduce operating cost and reduce operation power, can obtain simultaneously
Desulfurization rapidly, dedusting, dehumidifying and remove the effect of other heavy metal, the efficiency of desulfurization also significantly improves.Absorbent etc. consume
Product can sufficiently be reacted and be used, and utilization rate is high, thus reduce the usage amount of the consumable goodss such as electricity and water.
In the present embodiment, the laying mode of the blade of impeller 302 uses along the radially extending of main shaft 301, uses to housing 1
Inlet end direction tilts, uses at least one in the direction, outlet side of housing 1 tilts.Can be according to space chi in housing 1
Very little size, flue gas flow and flue gas compounds content select the laying angle that blade is different so that flue gas can fully and
Absorbent contact and fast reaction.
In the present embodiment, the blade of impeller 302 uses plate blade or arc shaped blade.The blade of impeller 302 uses tabular knot
Structure the central axis with main shaft 301, at this moment flue gas is made to approximate pure contorted moving forward.The blade of impeller 302 is with anti-
Answer the centrage of device housing 1 at an angle, or blade shape in curved surface structure, at this moment flue gas not only moves forward with contorted,
The most also force flue gas rolling or in turbulence-like or in the axially-movable accelerated.In housing 1 inner chamber, impeller 302 quickly rotates
Flue gas and absorbent and dehumidifier intense contact more times, and contactless dead angle can be made so that the reaction with absorbent faster,
More thorough, exhaustive, is remarkably improved the efficiency of desulfurization so that being dried of reacted flue gas is more thorough；Flue gas can also be made
By the speed of housing 1 inner chamber faster, thus be substantially reduced the size of housing 1 and the power of generator, it is possible to reduce equipment throw
Money, minimizing equipment operating cost and power consumption, meet high-level environmental requirement simultaneously.
During enforcement, it is provided that the towers such as a kind of centrifugal semidry method tower, centrifugal semi-dry desulphurization tower, centrifugal packed tower, centrifugal liquid column tower.
Rotary blade mechanism is set up in tower, can at a slow speed or atwirl impeller 302 is to the fluid in tower, such as centrifugal desulfurizing tower
The flue gas of whole inner chamber is produced by centrifugal action to rotate or produce and had not only rotated but also the effect of turbulent flow, at impeller in centrifugal desulfurizing tower
Under the effect of 302, when rotation and rapid flue gas meet with absorbent, not only produce strong effect of impact, and at same section
Have in the shortest time on face and clash in multiple times.And in the reaction tower not having impeller that compares, flue gas and the chance of meeting of absorbent
It is perhaps only and contacts the most light and slowly.
When impeller 302 rotating speed is the highest, the shock number of times of flue gas and absorbent the most the more, clashes into the most violent.So mass transfer,
Also the most faster, in certain scope, the rotating speed of impeller 302 is more for heat transfer and the effect of chemical reaction or efficiency and speed
Height, its effect is the strongest, the most not only significantly improves desulfuration efficiency, it is also possible to significantly reduce diameter and the tower of centrifugal reaction tower
Height, after the size of centrifugal reaction tower is substantially reduced, the corresponding and blower fan of centrifugal reaction tower adapted, pump its system
Other parts can reduce or reduce, thus can significantly reduce investment and reduce the expense such as power consumption, water consumption, spillage of material
With, and place area occupied.The form of impeller 302 also can be varied from, the such as blade shape of impeller 302 be tabular and with
The central axis of tower, at this moment the flue gas in desulfurizing tower is in approximation pure rotational motion.The blade of impeller 302 can also be with
The centrage of tower is at an angle, or shape in curved surface, and at this moment flue gas not only rotates, and the most also forces flue gas to roll in turbulent flow
Shape and quickening move axially.
As it is shown in figure 1, Fig. 1 is a kind of centrifugal semi-dry desulphurization tower, the top of housing 1 is equipped with driving means 303, driving means
The bottom of 303 connects to be had main shaft 301 and it can be driven to rotate.The top of main shaft 301 is equipped with an impeller 302, impeller 302 times
Portion is equipped with can the atomizing wheel 201 of high speed rotating.The serosity of absorbent enters atomizing wheel 201 from absorbent slurry pipeline 202.Atomization
The bottom of wheel 201 is also equipped with an impeller 302.During work, sulfur-containing smoke gas enters from the top of housing 1, and impeller 302 is rotated
Main shaft 301 drives, and impeller 302 makes the flue gas in housing 1 quickly stir and rotate, or at varied angle or curved impeller
302 drive the rolling of lower rotation limit, flue gas limit or limit to move to bottom, after the droplet of the absorbent that flue gas sprays with atomizing wheel 201 meets
Producing chemical reaction and produce lime-ash i.e. desulfurization product, water smoke is by the flue gas drying of higher temperature, and the flue gas after desulfurization is from housing 1
Bottom is discharged, and lime-ash is discharged from the foot of housing 1.Atomizing wheel 201 in Fig. 1 can be one or more.Impeller 302
Can be one or more.
As in figure 2 it is shown, Fig. 2 is a kind of centrifugal semi-dry desulphurization tower, the difference with Fig. 1 is, atomizing wheel 201 is disposed upon
The top of housing 1.
As it is shown on figure 3, Fig. 3 is a kind of centrifugal semi-dry desulphurization tower, the difference with Fig. 1 is, is replaced to by atomizing wheel 201
The spraying piping that the absorbent slurry pipeline 202 of two groups of band first jet 203 is formed.The moisture of spraying can be by the higher cigarette of temperature
Gas is dried, and becomes lime-ash from bottom discharge after absorbent and the reaction of Salmon-Saxl in flue gas.Impeller 302 in housing 1 can be one
Or it is multiple.
As shown in Figure 4, Fig. 4 is a kind of centrifugal packed tower, and sulfurous gas enters from the bottom of housing 1, by porose sieve plate 5
Enter the region of packing layer 6, there is on the top of packing layer 6 the absorbent slurry pipeline 202 of one group of band first jet 203,
One group of impeller 302 is arranged at the top of absorbent slurry pipeline 202, and impeller 302 is fixed on main shaft 301, and main shaft 301 is by driving
Device 303 drives and rotates, and impeller 302 drives flue gas rotate together or roll simultaneously in rotary course.Impeller 302 top has
Demister 4, impeller 302 also enhance simultaneously demister except mist and the ability of collecting powder, under the influence of centrifugal force, dust
And the collision opportunity between demister 4 and housing 1 inwall and dust increases, so that droplet and dust are easier to by collecting.
Impeller 302 in housing 1 can be one or more.
As it is shown in figure 5, Fig. 5 is a kind of centrifugal liquid column tower, not having filler in housing 1 unlike Fig. 4, absorbent relies on
The sulfur-containing smoke gas that housing 1 inner chamber bottom is entered by the fluid column 204 of multiple second nozzles 205 ejection contacts and washs, other
Structure is similar with Fig. 4.
Above-described embodiment can vertical structure as shown, it is also possible to be horizontal type structure.These towers can be centrifugal desulfurizing tower,
Can also be centrifugal denitrating tower or other carry out the multiple centrifugal chemistry reaction tower such as mass transfer, heat transfer.When for desulfurization, absorbent
Can be limestone, Calx, sea water, ammonia etc..Flue gas can enter from the bottom of housing 1, it is also possible to enters from top.
In existing reaction tower, typically just fluid makees the contact of pure upper or pure lower movement, and the number of times of contact is little, in tower arbitrary section
Face flue gas in a certain short time may for once contact with absorbent and the limited strength of contact-impact.The present invention is by increasing
If the atwirl impeller 302 producing centrifugal force field makes the frequency of exposure between the fluid in whole tower to control, and significantly
Increasing, the rotating speed of adjustable impeller 302 is several turns per minute, Ji Shizhuan, Ji Baizhuan, Ji Qianzhuan so that flue gas and absorbent
The number of times of chemical reaction of contact once can be increased to several times, Ji Shici, Ji Baici by original, or more, additionally its
The intensity of making contact is fiercer.The most not only can make chemical reaction effect the most faster, it is also possible to substantially reduce reaction unit
Size or volume, reduce power and the expense run, thus notable investment reduction and operating cost.
Reaction efficiency improves the increase of centrifugal force along with the rotating speed of impeller 302 and improves rapidly within the specific limits.Such as mesh
The minimum discharge of the desulphurization denitration of front thermal power plant or nearly zero requirement, need to use double tower Two-way Cycle can reach discharge index, and
After using the technology of the present invention, small size single column single cycle is only needed i.e. to can reach the standard of discharge standard or requirements at the higher level.
Owing to reaction effect is good, centrifugal reaction tower is made to less, so can save great amount of investment.Such as in thermal power plant
In, existing reaction tower or reactor size are very big, and this not only makes investment big, and floor space is big, and the pumping of absorbent
Amount is very big, and after using the present invention, the diameter of desulfurizing tower can be designed to the least, and the height of tower can also significantly reduce, in tower
The flow of the absorbent of ejection can also reduce, and pressure can also reduce, and therefore operating cost can also significantly reduce.
In spraying layer and demister, due to the effect of powerful centrifugal force of the impeller 302 of high speed rotating so that grit is especially
Minute dust and fine droplet collide with each other adhesion and and get rid of and catch to the inwall of tower more, old dirt effect on moisture extraction is more preferable, can
To save follow-up dust arrester installation and the employing of special dehydrating unit.
Due to the effect of high-speed rotating impeller, fluid mass transfer, heat transfer and chemical reaction etc. in centrifugal reactor are more fierce,
The most less scaling or blocking, can shut down cleaning or reduce flushing water use, this is for being prone to the half-dried of fouling and clogging
The effect of method reaction tower becomes apparent from.
When the main shaft 301 of above-mentioned various centrifugal reaction tower is oversize, supporting arrangement can be set up in the bottom of the inner shell of its housing 1 to protect
The smooth running of card main shaft 301.
Present invention may apply among the reactor of multiple fluid, various mass transfer such as such as desulfurizing tower, Benitration reactor etc., heat transfer
And among the reactor of chemical reaction etc..
The foregoing is only the preferred embodiments of the present invention, be not limited to the present invention, for those skilled in the art
For, the present invention can have various modifications and variations.All within the spirit and principles in the present invention, any amendment of being made, etc.
With replacement, improvement etc., should be included within the scope of the present invention.
Claims (10)
1. a centrifugal reaction tower, including for providing the housing (1) in space for flow of flue gas with carrying out chemical reaction and be used for carrying
For spray pattern or the hydrojet generating means (2) of the absorbent of spray state or washing state,
Described hydrojet generating means (2) is in described housing (1) inner chamber,
Described housing (1) is provided with and enters the air inlet (101) of described housing (1) inner chamber for flue gas, be used for discharging
The air vent (102) of reacted flue gas and for discharging the floss hole (103) of reaction product,
It is characterized in that,
Described housing (1) inner chamber is provided with for the flue gas making whole described housing (1) inner chamber carry out reacting by centrifugal force
Effect is spirally or the flow trace high-speed motion of eddy flow shape increase frequency of exposure and the contact strength of flue gas and absorbent
And do not stay the rotating mechanism (3) at contact dead angle.
Centrifugal reaction tower the most according to claim 1, it is characterised in that
Described rotating mechanism (3) includes the main shaft (301) being vertically laid in described housing (1) inner chamber, is installed in
Described main shaft (301) is upper and rotates with described main shaft (301) and is used for making whole described housing (1) inner chamber to carry out reacting
Flue gas is by centrifugal action spirally or the flow trace high-speed motion of eddy flow shape increase contacting time of flue gas and absorbent
Number and contact strength and not staying contact the impeller (302) at dead angle and are located at described housing (1) outward and described in being used for driving
The driving means (303) that main shaft (301) rotates.
Centrifugal reaction tower the most according to claim 2, it is characterised in that
Described centrifugal reaction tower is centrifugal semidry method tower, centrifugal packed tower or centrifugal liquid column tower.
Centrifugal reaction tower the most according to claim 3, it is characterised in that
Housing (1) inner chamber of described centrifugal semidry method tower is provided with impeller described in least one set (302),
Described hydrojet generating means (2) is located at least side of described impeller (302),
Described hydrojet generating means (2) uses the absorbent slurry with the atomizing wheel (201) for producing atomization absorption agent
Body pipeline (202),
Described atomizing wheel (201) is loaded on the outfan of described absorbent slurry pipeline (202),
Described absorbent slurry pipeline (202) is communicated to described housing (1) outward；
The top of described housing (1) is located at by described air inlet (101),
Described air vent (102) and described floss hole (103) are respectively arranged on the bottom of described housing (1).
Centrifugal reaction tower the most according to claim 3, it is characterised in that
Housing (1) inner chamber of described centrifugal semidry method tower is provided with impeller described in least one set (302),
Described hydrojet generating means (2) is located at described housing (1) top,
The outfan of described hydrojet generating means (2) towards described housing (1) inner chamber,
Described hydrojet generating means (2) uses the absorbent slurry with the atomizing wheel (201) for producing atomization absorption agent
Body pipeline (202),
Described atomizing wheel (201) is loaded on the outfan of described absorbent slurry pipeline (202),
Described absorbent slurry pipeline (202) is communicated to described housing (1) outward；
The top of described housing (1) is located at by described air inlet (101),
Described air vent (102) and described floss hole (103) are respectively arranged on the bottom of described housing (1).
Centrifugal reaction tower the most according to claim 3, it is characterised in that
Housing (1) inner chamber of described centrifugal semidry method tower is provided with impeller described in least one set (302),
Described hydrojet generating means (2) is located at least side of described impeller (302),
Described hydrojet generating means (2) uses with for the first of described housing (1) inner chamber jet atomization absorbent
The absorbent slurry pipeline (202) of nozzle (203),
Described first jet (203) is loaded on the delivery outlet of described absorbent slurry pipeline (202),
Described absorbent slurry pipeline (202) is communicated to described housing (1) outward；
The top of described housing (1) is located at by described air inlet (101),
Described air vent (102) and described floss hole (103) are respectively arranged on the bottom of described housing (1).
Centrifugal reaction tower the most according to claim 3, it is characterised in that
Housing (1) inner chamber of described centrifugal packed tower is provided with demister (4),
Described hydrojet generating means (2) uses with for the first of described housing (1) inner chamber jet atomization absorbent
The absorbent slurry pipeline (202) of nozzle (203),
Described first jet (203) is loaded on the delivery outlet of described absorbent slurry pipeline (202),
Described absorbent slurry pipeline (202) is communicated to described housing (1) outward,
Described housing (1) inner chamber is provided with impeller described in least one set (302)；
Described air inlet (101) and described floss hole (103) are respectively arranged on the bottom of described housing (1),
The top of described housing (1) is located at by described air vent (102)；
Sieve plate (5) with holes it is additionally provided with between described air inlet (101) and described absorbent slurry pipeline (202),
The upper surface of described sieve plate (5) is covered with packing layer (6).
Centrifugal reaction tower the most according to claim 3, it is characterised in that
Housing (1) inner chamber of described centrifugal liquid column tower is provided with demister (4),
Described hydrojet generating means (2) uses band for upwards spraying fluid column (204) and with smoke contacts to wash flue gas
The absorbent slurry pipeline (202) of second nozzle (205),
Described second nozzle (205) is loaded on the delivery outlet of described absorbent slurry pipeline (202),
Described absorbent slurry pipeline (202) is communicated to described housing (1) outward,
Described housing (1) inner chamber is provided with impeller described in least one set (302)；
Described air inlet (101) and described floss hole (103) are respectively arranged on the bottom of described housing (1),
The top of described housing (1) is located at by described air vent (102),
Described housing (1) bottom is additionally provided with air intake (104).
9. according to the centrifugal reaction tower according to any one of claim 2 to 8, it is characterised in that
The laying mode of the blade of described impeller (302) uses along the radially extending of described main shaft (301), uses to institute
The inlet end direction stating housing (1) tilts, uses at least one in the direction, outlet side of described housing (1) tilts.
10. according to the centrifugal reaction tower according to any one of claim 2 to 8, it is characterised in that
The blade of described impeller (302) uses plate blade or arc shaped blade.
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| CN201610322461.XA CN105833710A (en) | 2016-05-16 | 2016-05-16 | Centrifugal reaction tower |
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| CN201610322461.XA CN105833710A (en) | 2016-05-16 | 2016-05-16 | Centrifugal reaction tower |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109078469A (en) * | 2018-09-27 | 2018-12-25 | 高根树 | Two-stage coupling machinery mixes gas-gas reactor |
| CN109173613A (en) * | 2018-09-30 | 2019-01-11 | 国网黑龙江省电力有限公司电力科学研究院 | Sulfur hexafluoride waste gas recovering device |
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| CN204294109U (en) * | 2014-12-04 | 2015-04-29 | 成都创客之家科技有限公司 | A kind of desulfurizer of spiral spiral board |
| CN204672123U (en) * | 2015-05-03 | 2015-09-30 | 陈斌 | A kind of waste gas purification tower with swirling flow plate |
| CN105289188A (en) * | 2015-12-01 | 2016-02-03 | 天紫环保产业开发有限责任公司 | Waste gas treatment system for treating waste gas in granulation process of waste plastic |
| CN205760584U (en) * | 2016-05-16 | 2016-12-07 | 长沙深湘通用机器有限公司 | Centrifugal reaction tower |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5154084A (en) * | 1974-11-06 | 1976-05-12 | Kobayashi Kk | DATSUSHUSHORIHOHO |
| CN204294109U (en) * | 2014-12-04 | 2015-04-29 | 成都创客之家科技有限公司 | A kind of desulfurizer of spiral spiral board |
| CN204672123U (en) * | 2015-05-03 | 2015-09-30 | 陈斌 | A kind of waste gas purification tower with swirling flow plate |
| CN105289188A (en) * | 2015-12-01 | 2016-02-03 | 天紫环保产业开发有限责任公司 | Waste gas treatment system for treating waste gas in granulation process of waste plastic |
| CN205760584U (en) * | 2016-05-16 | 2016-12-07 | 长沙深湘通用机器有限公司 | Centrifugal reaction tower |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN109078469A (en) * | 2018-09-27 | 2018-12-25 | 高根树 | Two-stage coupling machinery mixes gas-gas reactor |
| CN109173613A (en) * | 2018-09-30 | 2019-01-11 | 国网黑龙江省电力有限公司电力科学研究院 | Sulfur hexafluoride waste gas recovering device |
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