CN208389734U - Desulphurization denitration gas wash tower nethike embrane splinter device and desulphurization denitration gas wash tower - Google Patents
Desulphurization denitration gas wash tower nethike embrane splinter device and desulphurization denitration gas wash tower Download PDFInfo
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- CN208389734U CN208389734U CN201820738699.5U CN201820738699U CN208389734U CN 208389734 U CN208389734 U CN 208389734U CN 201820738699 U CN201820738699 U CN 201820738699U CN 208389734 U CN208389734 U CN 208389734U
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- nethike embrane
- desulphurization denitration
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Abstract
The utility model provides a kind of desulphurization denitration gas wash tower nethike embrane splinter device and desulphurization denitration gas wash tower, including absorption tower, nethike embrane splashing component and spray assemblies, absorption tower is provided with flow channel, air inlet and gas outlet, and air inlet and air outlet are connected to flow channel.Nethike embrane splashing component includes at least one splashing web plate, and splashing web plate is mounted in flow channel, and splashing web plate is provided at least one mesh through splashing web plate between air inlet and gas outlet on splashing web plate.Spray assemblies are mounted on absorption tower, and spray assemblies are used for nethike embrane splashing component liquid-spraying purified liquid.In purification there are also when the flue gas of harmful substance, the mixing of flue gas and scavenging solution is more uniform, and flue gas contacts sufficiently with mixed liquor, and clean-up effect is more preferable, and purification efficiency is high, saves cost, more environmentally-friendly.
Description
Technical field
The utility model relates to field of environment protection equipment, splash and fill in particular to a kind of desulphurization denitration gas wash tower nethike embrane
It sets and desulphurization denitration gas wash tower.
Background technique
Atmosphere is the most basic important environment of human survival, it not only carries out heat, momentum and water by displacement and provides
The profile adjustment process in source, and create a suitable living environment to the mankind is effectively protected the mankind and tellurian
Biology.But with the increase of human being's production and social activities, the burning of especially a large amount of fuel, the discharge of industrial waste gas makes
Atmospheric environment deteriorates increasingly.In the pollutant of all kinds of atmosphere, main is pollution caused by stove is coal-fired, and fire coal is big compression ring
The main source of the pollutants such as sulfur dioxide, nitrogen oxides, flue dust in border.From the point of view of the consumption of coal: coal is in China's energy
Ratio in consumption is maintained at 70% or so, and is difficult to change in a short time；From the usage mode of coal: consumption of coal
80% is directly used in burning, and wherein coal-burning utilities Coal-fired capacity accounts for 50% or more of coal consumption amount.
With the continuous development of industrial economy, world environments increasingly deteriorates.Especially with the industrialization of developing country
The pollutant absolute magnitude rapid growth to atmosphere is arranged in the continuous propulsion of process.The mankind's increasingly disastrous effect caused by due to oneself
And feels to be too tired to deal with, is even frightened.Dust sulfur dioxide and nitrogen oxides in the discharged flue gas of coal-fired furnace kiln are to cause greatly
Gas pollutes one of main factor, it can not only cause acid rain to endanger the mankind, and according to nearest world environments expert pronounced, still
Destroy a key factor of atmospheric ozone layer.Therefore, the improvement of dust and sulfur dioxide is extremely urgent.
The pollution of atmospheric environment can bring on a disaster to the existence of the mankind, life, work, sustainable development, therefore control
The practical technique equipment of air environmental pollution just seems comparable important.Current scientific and technical innovation, social progress and human lives
The raising of quality, environmental protection quality are got more and more attention, and environmental protection discharge standard is also higher and higher and protects to international environment
Shield discharge standard integrates with, and the technological innovation level of environmental protection equipment industry is also just higher and higher thus.Air environmental pollution is (especially
Acid rain) it is borderless, so more stringent requirements are proposed to air environmental pollution control technology equipment.With China and state
Border society integrates with, and environmental protection increasingly draws attention, and becomes the emphasis invested from now on, if do not administered in these flue gases
Flue dust and sulfur dioxide will will cause to be caused seriously to pollute to atmosphere and city.
Inventor has found that traditional smoke dust-removing equipment at least has the following disadvantages: in use under study for action
Desulphurization and denitration, cleaner have that device structure is single, and absorption efficiency is low substantially at present, desulphurization and denitration, dedusting
Low efficiency, energy consumption is high, and atmospheric environment is vulnerable to pollution.
Utility model content
The purpose of this utility model is to provide a kind of desulphurization denitration gas wash tower nethike embrane splinter devices, to improve traditional take off
The problem of sulphur denitration dust collecting tower structure is single, purification efficiency is low, environment easy to pollute.
The purpose of this utility model is to provide a kind of desulphurization denitration gas wash towers, to improve traditional desulphurization denitration gas wash tower
The problem of structure is single, purification efficiency is low, environment easy to pollute.
The embodiments of the present invention are achieved in that
Based on above-mentioned first purpose, the utility model provides a kind of desulphurization denitration gas wash tower nethike embrane splinter device, packet
It has included:
Absorption tower, the absorption tower are provided with flow channel, air inlet and gas outlet, the air inlet and the outlet
Mouth is connected to the flow channel,
Nethike embrane splashing component, the nethike embrane splashing component include at least one splashing web plate, the splashing web plate installation
In the flow channel, the splashing web plate is set on the splashing web plate between the air inlet and the gas outlet
It is equipped at least one mesh through the splashing web plate,
And spray assemblies, the spray assemblies are mounted on the absorption tower, the spray assemblies are used for the net
Film splashing component liquid-spraying purified liquid.
In the utility model preferred embodiment, at least one lug boss, institute are provided on each splashing web plate
It states and is provided with the mesh at least one lug boss.
In the utility model preferred embodiment, the lug boss is Conical Shells With.
In the utility model preferred embodiment, the splashing web plate be bending plate, the splashing web plate along vertical
Section in its bending line direction extends in nonlinear type.
In the utility model preferred embodiment, the edge of the splashing web plate is in perpendicular to the section in its bending line direction
Fold-line-shaped extends.
In the utility model preferred embodiment, the splashing web plate includes the first web plate and the second net being arranged alternately
Plate, adjacent first web plate and the second web plate are arranged in angle, and the angle of adjacent first web plate and the second web plate is 60
Degree is to 90 degree.
In the utility model preferred embodiment, the edge of the splashing web plate is in perpendicular to the section in its bending line direction
Wave extends.
In the utility model preferred embodiment, the splashing web plate is provided at least two, and at least two is described winged
Web plate is splashed to be intervally arranged along the central axes direction of the flow channel.
In the utility model preferred embodiment, the spray assemblies include spray tube and at least one spray head, institute
It states spray tube to protrude into the flow channel, at least one described spray head is mounted on the spray tube, at least one described spray
Head is located in the flow channel, and the splashing web plate is between the spray head and the air inlet.
Based on above-mentioned second purpose, the utility model provides a kind of desulphurization denitration gas wash tower, including air-introduced machine and institute
The desulphurization denitration gas wash tower nethike embrane splinter device stated, the air-introduced machine are used to flue gas introducing the flowing from the air inlet logical
In road.
The beneficial effect of the utility model embodiment is:
In conclusion the utility model embodiment provides a kind of desulphurization denitration gas wash tower nethike embrane splinter device, structure
Advantages of simple, convenient for manufacture processing, installation with it is easy to use, meanwhile, purification there are also harmful substance flue gas when, flue gas with only
The mixing for changing liquid is more uniform, and flue gas contacts sufficiently with mixed liquor, and clean-up effect is more preferable, and purification efficiency is high, saves cost, more
Environmental protection.It is specific as follows:
Desulphurization denitration gas wash tower nethike embrane splinter device provided in this embodiment comprising have absorption tower, nethike embrane splashing component
And spray assemblies, absorption tower are the mixing place of flue gas and scavenging solution, flue gas introduces absorption tower from air inlet by air-introduced machine
In, scavenging solution is sprayed by spray assemblies, and flue gas and scavenging solution touch splashing web plate, when flue gas passes through splashing web plate, process
Impact interception, online liquid film intercept, the broken processes such as interception of splashing of droplet, improve the purification efficiency to harmful material in smoke,
Reduction uses power, has arrived the purpose of energy-saving and emission-reduction.Practical work process is that kiln gas is under the action of air-introduced machine with every
The speed of 17 meters -19 meters or so of second enters desulphurization and denitration, dedusting absorption tower, and bulk velocity of the flue gas in absorption tower is about
3 meters of each second, when flue gas passes through the splashing web plate being arranged in tower, under the action of splashing web plate, the flow direction of flue gas
Change, increases the time that flue gas rests in absorption tower, also increase the diffusion area of flue gas, meanwhile, when from bottom to top
Flue gas can collide with absorption cleaning liquid from top to bottom when passing through nethike embrane splashing component, flow back, absorption drop from top to bottom
When being dropped on splashing web plate, it is broken that absorbing liquid droplet will form liquid film and droplet on nethike embrane splashing web plate, when having in flue gas
It when harmful object passes through nethike embrane splinter device, intercepts, the broken processes such as interception of splashing of droplet, improves by impact interception, online liquid film
To the purification efficiency of harmful material in smoke, reduction uses power, has arrived the purpose of energy-saving and emission-reduction, more environmentally-friendly.
Desulphurization denitration gas wash tower provided in this embodiment includes above-mentioned desulphurization denitration gas wash tower nethike embrane splinter device, is had
All advantages of desulphurization denitration gas wash tower nethike embrane splinter device.
Detailed description of the invention
It, below will be to use required in embodiment in order to illustrate more clearly of the technical solution of the utility model embodiment
Attached drawing be briefly described, it should be understood that the following drawings illustrates only some embodiments of the utility model, therefore should not be by
Regard the restriction to range as, for those of ordinary skill in the art, without creative efforts, may be used also
To obtain other relevant attached drawings according to these attached drawings.
Fig. 1 is the schematic diagram of the desulphurization denitration gas wash tower nethike embrane splinter device of the utility model embodiment；
Fig. 2 is the operation schematic diagram of the desulphurization denitration gas wash tower nethike embrane splinter device of the utility model embodiment；
Fig. 3 is the vertical view signal of the splashing web plate of the desulphurization denitration gas wash tower nethike embrane splinter device of the utility model embodiment
Figure；
Fig. 4 is the distressed structure of the splashing web plate of the desulphurization denitration gas wash tower nethike embrane splinter device of the utility model embodiment
Schematic cross-sectional view；
Fig. 5 is the distressed structure schematic diagram of the desulphurization denitration gas wash tower nethike embrane splinter device of the utility model embodiment.
Icon: the absorption tower 100-；110- flow channel；120- air inlet；The gas outlet 130-；200- net mould splashes
Component；210- splashing web plate；211- mesh；The first web plate of 212-；The second web plate of 213-；214- protrusion；300- spray
Drench component；310- spray tube；320- spray head.
Specific embodiment
Desulphurization and denitration, cleaner have that device structure is single, and absorption efficiency is low substantially at present, desulphurization and denitration, dedusting
Low efficiency, energy consumption is high, and atmospheric environment is vulnerable to pollution.
In consideration of it, inventor devises a kind of desulphurization denitration gas wash tower nethike embrane splinter device and desulphurization denitration gas wash tower,
In purification there are also when the flue gas of harmful substance, the mixing of flue gas and scavenging solution is more uniform, and flue gas contacts sufficiently, only with mixed liquor
It is more preferable to change effect, purification efficiency is high, saves cost, more environmentally-friendly.
It is practical new below in conjunction with this to keep the objectives, technical solutions, and advantages of the embodiments of the present invention clearer
Attached drawing in type embodiment, the technical scheme in the utility model embodiment is clearly and completely described, it is clear that is retouched
The embodiment stated is the utility model a part of the embodiment, instead of all the embodiments.Usually here in attached drawing description and
The component of the utility model embodiment shown can be arranged and be designed with a variety of different configurations.
Therefore, requirement is not intended to limit to the detailed description of the embodiments of the present invention provided in the accompanying drawings below
The scope of the utility model of protection, but it is merely representative of the selected embodiment of the utility model.Based in the utility model
Embodiment, every other embodiment obtained by those of ordinary skill in the art without making creative efforts, all
Belong to the range of the utility model protection.
It should also be noted that similar label and letter indicate similar terms in following attached drawing, therefore, once a certain Xiang Yi
It is defined in a attached drawing, does not then need that it is further defined and explained in subsequent attached drawing.
In the description of the present invention, it should be noted that the orientation of the instructions such as term "horizontal", "inner", "outside" or
Positional relationship be based on the orientation or positional relationship shown in the drawings or the utility model product using when the side usually put
Position or positional relationship, are merely for convenience of describing the present invention and simplifying the description, rather than the device of indication or suggestion meaning
Or element must have a particular orientation, be constructed and operated in a specific orientation, therefore should not be understood as to the utility model
Limitation.
In the description of the present invention, it should also be noted that, unless otherwise clearly defined and limited, term " is set
Set ", " installation ", " connection " shall be understood in a broad sense, for example, it may be being fixedly connected, may be a detachable connection, or integrally
Connection；It can be mechanical connection, be also possible to be electrically connected；Can be directly connected, can also indirectly connected through an intermediary,
It can be the connection inside two elements.For the ordinary skill in the art, above-mentioned art can be understood with concrete condition
The concrete meaning of language in the present invention.
It should be noted that in the absence of conflict, the feature in the embodiments of the present invention and embodiment can
To be combined with each other.
Embodiment
Fig. 1-Fig. 5 is please referred to, a kind of desulphurization denitration gas wash tower nethike embrane splinter device is present embodiments provided, is used for desulfurization
The contact area for increasing flue gas and scavenging solution when denitration dust collecting tower purifying smoke, increases the time of contact of flue gas and scavenging solution, mentions
High purification efficiency, purified flue gas are more environmentally-friendly.
In the present embodiment, desulphurization denitration gas wash tower nethike embrane splinter device include absorption tower 100, nethike embrane splashing component and
Spray assemblies 300.Absorption tower 100 is main reacting environment, and flue gas is introduced into absorption tower 100 by air-introduced machine, spray group
Absorbing liquid is injected in absorption tower 100 by part 300, and flue gas flows in absorption tower 100, touches nethike embrane splashing component, meanwhile,
Absorbing liquid flows in absorption tower 100 touches nethike embrane splashing component, and during being somebody's turn to do, the time of contact of flue gas and absorbing liquid increases
Add, flue gas is more fully mixed with absorbing liquid, improves purification efficiency.
In the present embodiment, absorption tower 100 has flow channel 110, air inlet 120 and gas outlet 130, air inlet 120
Flow channel 110 is connected to gas outlet 130.Absorption tower 100 can be cylindrical tube, square column type cylinder etc., be arranged on demand.It inhales
Receiving tower 100 can be made of steel plate, and structural strength is high, long service life.The top on absorption tower 100 has end cap, in end cap
On be provided with gas outlet 130, outlet pipe is installed at gas outlet 130, convenient for purified gas is emitted into atmosphere, or
Purified gas is delivered to next purification place again and is purified again by person, improves clean-up effect.On absorption tower 100
Position on barrel close to bottom is provided with air inlet 120, and air inlet 120 can be circular port, easy to process, is also convenient for close
Envelope, is not easy gas leakage.Air inlet 120 is arranged on the side wall on absorption tower 100, is placed in ground by its bottom convenient for absorption tower 100
On face, the placement on absorption tower 100 is safer, is not easy to topple over.
Optionally, collecting tank is installed in the bottom on absorption tower 100, collecting tank absorbs the net of harmful substance for collecting
Change liquid, is provided with water pump in collecting tank, is extracted out after the liquid in collecting tank reaches a certain amount of by water pump.Optionally, it is absorbing
Observation window is installed on the barrel of tower 100, convenient for the liquid storage amount in observation collecting tank.
In the present embodiment, nethike embrane splashing component includes at least one splashing web plate 210, at least one splashing web plate 210
It is provided at least one mesh 211, mesh 211 is used to pass through splashing web plate 210 for flue gas and absorbing liquid, makes flue gas and absorbing liquid
It comes into full contact with.When actual processing, mesh 211 can be round hole, and the aperture of mesh 211 is between 4mm-6mm, for example, mesh
211 aperture can be, but not limited to be 4mm, 5mm or 6mm.At least one splashing web plate 210 is mounted on flow channel 110
In, play the role of obstructing flue gas and absorbing liquid.
Optionally, splashing web plate 210 is provided at least two, axis of at least two splashing web plates 210 along absorption tower 100
Line direction is intervally arranged, i.e. short transverse of the splashing web plate 210 on absorption tower 100 is layered setting, can be improved barrier effect in this way
Fruit further extends the time that flue gas flows in absorption tower 100, improves clean-up effect.
In the present embodiment, at least one lug boss is provided on splashing web plate 210, at least one boss is in splashing net
In one plate face of plate 210, at least one lug boss by 210 bending of splashing web plate or stretch is formed, reduce material, saving at
This.Mesh 211 is provided on each lug boss.Further, lug boss is that circular cone is shelly-shaped.
In other embodiments, splashing web plate 210 is bending plate, and splashing web plate 210 can be parallel to it by rectangular slab edge
The bending line of width direction or length direction is bent to form, and splashing web plate 210 has at least two bending parts, i.e. splashing web plate
210 have at least two parallel bending lines.The side view that the edge of splashing web plate 210 is parallel to its bending line direction is non-straight
Linear, in other words, the edge of splashing web plate 210 extends perpendicular to the section configuration in its bending line direction in non-linear.For example,
The edge of splashing web plate 210 extends perpendicular to the section in its bending line direction in fold-line-shaped.Alternatively, splashing web plate 210 along vertical
Section in its bending line direction extends in wave.
It should be noted that the bending angle of splashing web plate 210 is arranged on demand when splashing 210 bending of web plate.The present embodiment
In, it is illustrated so that the transverse shape of splashing web plate 210 is fold-line-shaped as an example.
Splashing web plate 210 includes the first web plate 212 and the second web plate 213 being arranged alternately, adjacent first web plate 212
It is arranged with the second web plate 213 in angle, the angle of adjacent first web plate 212 and the second web plate 213 is 60 degree to 90 degree.Fly
It splashes web plate 210 to be mounted in absorption tower 100, the generally horizontal setting of splashing web plate 210, i.e. the central axes on absorption tower 100 are vertical
Across splashing web plate 210, the angle of the first web plate 212 and vertical direction is between 30 degree of -45 degree.
In the present embodiment, the setting of splashing web plate 210 is played and is blocked to the nethike embrane of sulfur dioxide, nitrogen oxides, dust
It cutting, fluid spills are broken, increase the incorporation time of liquid surface area, reinforce the absorption to harmful material in smoke, operating cost is reduced,
Improve nuisance absorption efficiency.
In the present embodiment, spray assemblies 300 are installed in flow channel 110, and spray assemblies 300 are used to be oriented to towards umbrella shape
Cap liquid-spraying purified liquid.Spray assemblies 300 include spray tube 310 and at least one spray head 320, and it is logical that spray tube 310 protrudes into flowing
In road 110, at least one spray head 320 is mounted on spray tube 310, at least one spray head 320 is located in flow channel 110.It can
Choosing, spray head 320 is provided at least two, and at least two spray heads 320 are intervally arranged along the length direction of spray tube 310.Into one
Step, spray tube 310 includes spraying supervisor and at least two spray branch pipes, and at least two spray branch pipe connection sprays are responsible for, until
Few two spray branch pipes are arranged side by side, and are equipped with spray head 320 on every spray branch pipe.Spray head 320 is distributed more reasonable, scavenging solution
Area coverage it is big, the contact with flue gas is more abundant, conducive to the absorption of harmful substances from flue gases.
At work, kiln gas is under the action of air-introduced machine with per second 17 for desulphurization denitration gas wash tower provided in this embodiment
The speed of -19 meters or so of rice enters desulphurization and denitration, dedusting absorption tower 100, and bulk velocity of the flue gas in absorption tower 100 is big
3 meters of each second is caused, is in bending plate structure since nethike embrane splashes when flue gas passes through the multilayer splashing web plate 210 being arranged in tower,
The area of splashing nethike embrane is bigger than the area of the cross section on absorption tower 100 at this time, thus flue gas pass through splashing web plate 210 when
Speed at 2 meters or so, meanwhile, when flue gas from bottom to top can touch when through splashing web plate 210 with absorbing liquid from top to bottom
It hits, flow back, when absorption drop from top to bottom is dropped in splashing web plate 210, absorbing liquid droplet will form on splashing web plate 210
Liquid film and droplet are broken, when harmful material in smoke passes through splashing web plate 210, intercept by impact interception, online liquid film, droplet
The broken processes such as interception of splashing, improve the purification efficiency to harmful material in smoke, and reduction uses power, arrived energy-saving and emission-reduction
Purpose.
Embodiment
Present embodiments provide a kind of desulphurization denitration gas wash tower, including air-introduced machine and desulphurization denitration provided by the above embodiment
Gas wash tower nethike embrane splinter device, air-introduced machine is for flue gas to be introduced into flow channel 110 from air inlet 120.
The above descriptions are merely preferred embodiments of the present invention, is not intended to limit the utility model, for this
For the technical staff in field, various modifications and changes may be made to the present invention.It is all in the spirit and principles of the utility model
Within, any modification, equivalent replacement, improvement and so on should be included within the scope of protection of this utility model.
Claims (10)
1. a kind of desulphurization denitration gas wash tower nethike embrane splinter device, which is characterized in that it includes:
Absorption tower, the absorption tower are provided with flow channel, air inlet and gas outlet, and the air inlet and the gas outlet connect
Lead to the flow channel,
Nethike embrane splashing component, the nethike embrane splashing component include at least one splashing web plate, and the splashing web plate is mounted on institute
It states in flow channel, the splashing web plate is provided on the splashing web plate between the air inlet and the gas outlet
Through at least one mesh of the splashing web plate,
And spray assemblies, the spray assemblies are mounted on the absorption tower, the spray assemblies are used to fly to the nethike embrane
Splash component liquid-spraying purified liquid.
2. desulphurization denitration gas wash tower nethike embrane splinter device according to claim 1, which is characterized in that each splashing net
It is provided at least one lug boss on plate, is provided with the mesh at least one described lug boss.
3. desulphurization denitration gas wash tower nethike embrane splinter device according to claim 2, which is characterized in that the lug boss is circle
Conical shell.
4. desulphurization denitration gas wash tower nethike embrane splinter device according to claim 2, which is characterized in that the splashing web plate is
The edge of bending plate, the splashing web plate extends perpendicular to the section in its bending line direction in nonlinear type.
5. desulphurization denitration gas wash tower nethike embrane splinter device according to claim 4, which is characterized in that the splashing web plate
Extend along the section perpendicular to its bending line direction in fold-line-shaped.
6. desulphurization denitration gas wash tower nethike embrane splinter device according to claim 5, which is characterized in that the splashing web plate packet
The first web plate and the second web plate being arranged alternately, adjacent first web plate and the second web plate is included to be arranged in angle, it is adjacent described
The angle of first web plate and the second web plate is 60 degree to 90 degree.
7. desulphurization denitration gas wash tower nethike embrane splinter device according to claim 4, which is characterized in that the splashing web plate
Extend along the section perpendicular to its bending line direction in wave.
8. desulphurization denitration gas wash tower nethike embrane splinter device according to claim 1, which is characterized in that the splashing web plate is set
At least two are equipped with, at least two splashing web plates are intervally arranged along the central axes direction of the flow channel.
9. desulphurization denitration gas wash tower nethike embrane splinter device according to claim 1, which is characterized in that the spray assemblies packet
Spray tube and at least one spray head are included, the spray tube protrudes into the flow channel, at least one described spray head is mounted on
On the spray tube, at least one described spray head is located in the flow channel, and the splashing web plate is located at the spray head and institute
It states between air inlet.
10. a kind of desulphurization denitration gas wash tower, which is characterized in that including air-introduced machine and according to claim 1 described in -9 any one
Desulphurization denitration gas wash tower nethike embrane splinter device, the air-introduced machine is used to flue gas introducing the flow channel from the air inlet
In.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820738699.5U CN208389734U (en) | 2018-05-17 | 2018-05-17 | Desulphurization denitration gas wash tower nethike embrane splinter device and desulphurization denitration gas wash tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820738699.5U CN208389734U (en) | 2018-05-17 | 2018-05-17 | Desulphurization denitration gas wash tower nethike embrane splinter device and desulphurization denitration gas wash tower |
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| Publication Number | Publication Date |
|---|---|
| CN208389734U true CN208389734U (en) | 2019-01-18 |
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| CN201820738699.5U Active CN208389734U (en) | 2018-05-17 | 2018-05-17 | Desulphurization denitration gas wash tower nethike embrane splinter device and desulphurization denitration gas wash tower |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108421379A (en) * | 2018-05-17 | 2018-08-21 | 大连铭晟环保设备有限公司 | Desulphurization denitration gas wash tower nethike embrane splinter device and desulphurization denitration gas wash tower |
| CN110787544A (en) * | 2019-11-07 | 2020-02-14 | 安徽天顺环保设备股份有限公司 | Semi-dry desulfurization and denitrification device bag-type dust collector |
-
2018
- 2018-05-17 CN CN201820738699.5U patent/CN208389734U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108421379A (en) * | 2018-05-17 | 2018-08-21 | 大连铭晟环保设备有限公司 | Desulphurization denitration gas wash tower nethike embrane splinter device and desulphurization denitration gas wash tower |
| CN110787544A (en) * | 2019-11-07 | 2020-02-14 | 安徽天顺环保设备股份有限公司 | Semi-dry desulfurization and denitrification device bag-type dust collector |
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