CN206184231U - Novel high efficiency SOx/NOx control system - Google Patents
Novel high efficiency SOx/NOx control system Download PDFInfo
- Publication number
- CN206184231U CN206184231U CN201620884944.4U CN201620884944U CN206184231U CN 206184231 U CN206184231 U CN 206184231U CN 201620884944 U CN201620884944 U CN 201620884944U CN 206184231 U CN206184231 U CN 206184231U
- Authority
- CN
- China
- Prior art keywords
- less
- tower
- sox
- desulphurization denitration
- desulfuration
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Landscapes
- Treating Waste Gases (AREA)
Abstract
The utility model discloses a novel high efficiency SOx/NOx control system belongs to SOx/NOx control technical field, including intake pipe, cyclone, connecting pipe, filter chamber, active carbon, ozone generator, oxygen cylinder, high -pressure discharge ware, oxidizing chamber, electric squib, mouthpiece, SOx/NOx control tower, column plate, alkaline solution, alkali lye shower nozzle and outlet duct, the last fixed intake pipe that is equipped with of cyclone, novel high efficiency SOx/NOx control system includes cyclone, filter chamber, oxidizing chamber and SOx/NOx control tower, and the connecting pipe alternates wherein, the inside active carbon of evenly having loaded of filter chamber, the inside electric squib that is provided with of oxidizing chamber, even fixed mounting has the column plate in the SOx/NOx control tower, fixed mounting has the outlet duct on the SOx/NOx control tower, and this novel high efficiency SOx/NOx control system cost is low, simple structure, and the modern design, convenient to use, SOx/NOx control is efficient, can effectively purify the flue gas, reduces the harm that the flue gas brought to the human body.
Description
Technical field
The utility model belongs to distribution box field, and in particular to a kind of novel efficient system for desulfuration and denitration.
Background technology
At present, China's energy is based on fire coal, and metal smelt process, can produce a large amount of sulfur dioxide, at present, I
The annual SO2 emissions of state have been up to 40,000,000 tons, and this is to cause haze one of the main reasons today, and in these flue gases
Sulfur dioxide concentration it is high more than 10%, and low less than 1%, it is very big that this results in recovery difficult.For many years, China's input
With in the desulfurization project built, major part is all that to use with calcium base wet-process flue gas desulfurization be main Treatment process.Calcium base wet-process flue gas
Generally using calcium carbonate and calcium oxide as desulfurizing agent, desulfurization product is gypsum for desulfurization, and the gypsum resource of China is abundant, after desulfurization
Its impurity of gypsum is too many, and canopy pine is unreal, does not have use value, but cannot process, as pollution source, in fact,
This is the technology that another pollution is substituted with a kind of pollution modes, even so, because the cost of the sulfur removal technology technology is too high,
Desulfurization product can not bring benefits again, it has also become the great burden that can't stand is held by enterprise,【One large desulfurization denitration device, year
Operating cost is up to tens million of units, and a small-sized heating station, the operating cost in a winter also needs millions of units】This just forces the producer to be
Cost-effective, using desulphurization plant mostly as dealing with inspection, the ostentatious project all not put into operation really actually makes cigarette
Sulfur dioxide in gas, is not all just stolen by the directly row of stealing through treatment and is put into air mostly, and this is already well-known in industry
The fact;This is also China's main basic reason that today, haze was administered more serious and more serious!But, on the one hand, sulphur is again China's work
The essential important source material of agricultural production, and China due to sulphur mineral resources very little, China's gas washing in SA production is always to rely on big
Imported sulphur is measured to process, if, a kind of low cost of invention, the novel desulphurization technique of process is simple is set, by industry
Sulfur dioxide in flue gas is used for being produced into sulfuric acid, to substitute the sulfuric acid of sulfur cream!This just can directly by this main air
The malicious source of pollution, transforms into huge resource, therefore, the sulfur dioxide low cost conversion in industrial smoke is produced into sulfuric acid work
Skill, is the green technology of most preferable doulbe-sides' victory.Consequently, it is possible to this will make desulfurization emission reduction, voluntarily give as manufacturing enterprise
The profit project for changing harmful to treasure for receiving, occurs so as to will thoroughly prevent the row of stealing and steal Fang Shi parts!Effected a radical cure in haze
While, can also be that country saves the huge foreign exchange for buying sulphur.
Sulfur dioxide in industrial smoke is processed into sulfuric acid, this at home and abroad early has sub-fraction producer and has this
Aspect transformation technology facility, but all because its technique excessively complicated, operating cost is too high, the cost for especially producing ozone is too high,
Therefore, so far also only only tens of thousands of, ten tens of thousands of low discharges set and applied, it is difficult in the large-scale generating of millions of air quantity
Application is realized in factory, therefore, haze to be made obtains real improvement, need a kind of new skills of new and effective cheap sulfur removal technology of Chong
Art method.
Utility model content
The purpose of this utility model is to provide a kind of novel efficient desulfuring and denitrifying apparatus, to solve above-mentioned background technology
The problem of middle proposition.
To realize the utility model purpose, the technical scheme of use is:A kind of novel efficient system for desulfuration and denitration, belongs to
Desulphurization denitration technical field, including air inlet pipe, cyclone separator, connecting tube, filter chamber, activated carbon, ozone generator, oxygen
Bottle, high-voltage discharger, oxidizing chamber, electric plug, ozzle, desulphurization denitration tower, column plate, alkaline solution, alkali lye shower nozzle and escaping pipe,
Air inlet pipe is fixed with the cyclone separator, the novel efficient system for desulfuration and denitration includes cyclone separator, filtering
Room, oxidizing chamber and desulphurization denitration tower, connecting tube are interspersed wherein, and filter chamber's inner homogeneous are filled with activated carbon, the ozone
Generator is internally provided with oxygen cylinder and high-voltage discharger, and the oxidizing chamber is internally provided with electric plug, the desulphurization denitration
Ozzle is installed with tower, uniformly column plate is installed with the desulphurization denitration tower, the desulphurization denitration tower top end is fixed
Alkali lye shower nozzle is installed, alkaline solution is sprayed in the alkali lye shower nozzle, escaping pipe is installed with the desulphurization denitration tower.
Preferably, cyclone separator, filter chamber, oxidizing chamber and desulphurization denitration in the novel efficient system for desulfuration and denitration
Tower shell is made up of high-quality Q235 stainless steels, and cyclone separator, filter chamber, oxidizing chamber and all corners of desulphurization denitration tower shell are complete
Portion is molded using special fillet mould, wherein, cyclone separator is a kind of vertical cylinder structure, and wall thickness is 1cm, is highly
2m, drum diameter 30cm, filter chamber are a kind of vertical shuttle-type cylindrical structure, and oxidizing chamber is a kind of horizontal cylinder structure, and desulfurization takes off
Nitre tower is a kind of scrubbing tower, and cyclone separator, filter chamber, oxidizing chamber and desulphurization denitration tower shell wall thickness are no more than 1cm, filtering
Room, oxidizing chamber and desulphurization denitration tower volume are not less than 1 cubic metre.
Preferably, the air inlet pipe, connecting tube, ozzle and escaping pipe are made by Q235 stainless steels, specially a kind of circle
Cylindrical pipes, air inlet pipe, connecting tube and escaping pipe caliber are no more than 8cm, and length is not less than 10cm, and ozzle caliber is no more than 8cm,
Length is not less than 10cm, and outside is provided with flange gasket, and thickness is 1.6cm, and a diameter of 9.6cm, ozzle number is not less than 4.
Preferably, the activated carbon is a kind of metamict crystals activated carbon, is fine particulate structure, can be approximately spheroid,
Particle effective diameter is no more than 1mm, and duct is dispersed with inside activated carbon, and duct effective diameter is no more than 1um, inner surfaces of pores product
It is not less than 10cm2, duct number is not less than 100.
Preferably, the ozone generator is specifically made up of oxygen cylinder and high-voltage discharger, and ozone generator is a kind of long
Square three-dimensional-structure, fills the gas that oxygen purity is 99.2% in the oxygen cylinder, specific volume is 10L, and pressure is no more than 150
Individual atmospheric pressure, the high-voltage discharger work effective voltage is not less than 10KV, and power consumption is no more than 1000W.
Preferably, the electric plug is the electric plug of a kind of ceramic package and interior insulation body formula, and work effective voltage
1KV is not less than, power consumption is no more than 1000W, wherein, the number of the electric plug in oxidizing chamber is not less than 15 pairs.
Preferably, the column plate is a kind of plastic plate, is specifically made by vinyon system, the leakage of column plate middle setting
Fluid apertures, liquid-leaking nozzle aperture is 1cm, and individual layer column plate liquid-leaking nozzle hole count is not less than 500, and column plate thickness is no more than 1cm, is a kind of circle
Slab organization, plate number is not less than 20 pieces.
Preferably, the alkaline solution is the strong alkali solution such as NaOH, potassium hydroxide and calcium hydroxide, or several
Soda-wash solution mixed liquor, specific flow is not less than 1m3/ h, wherein, alkaline solution is pumped to desulphurization denitration by corrosion resisting centrifugal pump
Top of tower.
Preferably, the alkali lye shower nozzle is specifically made up of high brass, specially a kind of furred ceiling type shower nozzle, on alkali lye shower nozzle
Spray orifice is provided with, spray orifice aperture is no more than 1mm, and hole count is not less than 500, and alkali lye shower nozzle is not less than 30.
Compared with prior art, the beneficial effects of the utility model are:This novel efficient system for desulfuration and denitration low cost,
Simple structure, easy processing is novel in design, easy to use, and novel efficient system for desulfuration and denitration is taken off using four sections of removing formulas, desulfurization
Nitre efficiency high, can effective purifying smoke, reduce the harm that flue gas brings to human body.
Brief description of the drawings
Fig. 1 is the utility model structural representation.
Fig. 2 is the utility model functional sequence structural representation.
In figure:1. the ozone generator 7. of 2. cyclone separator of air inlet pipe, 3. connecting tube, 4. filter chamber, 5. activated carbon 6.
The alkali of 13. column plate of oxygen cylinder 8. high-voltage discharger, 9. oxidizing chamber, 10. electric plug, 11. ozzle, 12. desulphurization denitration tower 14.
The escaping pipe of 15. alkali lye shower nozzle of property solution 16.
Specific embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the utility model embodiment is carried out
Clearly and completely describe, it is clear that described embodiment is only a part of embodiment of the utility model, rather than whole
Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are not under the premise of creative work is made
The every other embodiment for being obtained, belongs to the scope of the utility model protection.
Refer to shown in Fig. 1 and Fig. 2, the utility model provides a kind of technical scheme:A kind of novel efficient desulphurization denitration
System, belongs to desulphurization denitration technical field, including air inlet pipe 1, cyclone separator 2, connecting tube 3, filter chamber 4, activated carbon 5, smelly
Oxygen Generator 6, oxygen cylinder 7, high-voltage discharger 8, oxidizing chamber 9, electric plug 10, ozzle 11, desulphurization denitration tower 12, column plate 13,
Alkaline solution 14, alkali lye shower nozzle 15 and escaping pipe 16, are fixed with air inlet pipe 1 on the cyclone separator 2, described new and effective
Rate desulfurization removing nitric system includes cyclone separator 2, filter chamber 4, oxidizing chamber 9 and desulphurization denitration tower 12, and connecting tube 3 is interspersed wherein,
The inner homogeneous of the filter chamber 4 are filled with activated carbon 5, and the ozone generator 6 is internally provided with oxygen cylinder 7 and high-voltage discharger
8, the oxidizing chamber 9 is internally provided with electric plug 10, and ozzle 11, the desulfurization are installed with the desulphurization denitration tower 12
Column plate 13 uniformly is installed with denitrating tower 12, the top of desulphurization denitration tower 12 is installed with alkali lye shower nozzle 15, described
Alkaline solution 14 is sprayed in alkali lye shower nozzle 15, escaping pipe 16 is installed with the desulphurization denitration tower 12.
Operation principle:During work, the flue gas of sulfur-bearing, nitrogen is entered into novel efficient system for desulfuration and denitration, cigarette from air inlet pipe 1
Gas enters cyclone separator 2, and under the centrifugation of cyclone separator 2, most solid particles are separated to be left, and flows through rotation
The flue gas of wind separator 2 introduces filter chamber 4 by connecting tube 3, under the suction-operated of activated carbon 5, remaining fine solid particles
Also it is filtered, in ozone generator 6, the release oxygen of oxygen cylinder 7, under the arc discharge effect of high-voltage discharger 8, oxygen
React to each other generation ozone, is passed through to connecting tube 3, and flue gas enters in oxidizing chamber 9 together, and in oxidizing chamber 9, flue gas is in electricity
Under the arc discharge effect of spark plug 10, and there are redox reaction, sulfur compound, nitrogenate and hydrocarbons etc. in ozone
Sour gas is oxidized to, sour gas and flue gas are introduced in ozzle 11 by connecting tube 3, subsequently enter desulphurization denitration tower 12
Interior, in desulphurization denitration tower 12, alkaline solution 14 sprays from the alkali lye shower nozzle 15 at the top of desulphurization denitration tower 12, on column plate 13 with
Flue gas and sour gas mix, and sour gas is absorbed by alkaline solution 14, generate salt, last from going out through the flue gas of desulphurization denitration
Tracheae 16 is discharged.
While there has been shown and described that embodiment of the present utility model, for the ordinary skill in the art,
It is appreciated that these embodiments can be carried out various changes in the case where principle of the present utility model and spirit is not departed from, repaiies
Change, replace and modification, scope of the present utility model is defined by the appended claims and the equivalents thereof.
Claims (9)
1. a kind of novel efficient system for desulfuration and denitration, belongs to desulphurization denitration technical field, including air inlet pipe (1), cyclonic separation
Device (2), connecting tube (3), filter chamber (4), activated carbon (5), ozone generator (6), oxygen cylinder (7), high-voltage discharger (8), oxygen
Change room (9), electric plug (10), ozzle (11), desulphurization denitration tower (12), column plate (13), alkaline solution (14), alkali lye shower nozzle
(15) air inlet pipe (1), the novel efficient desulphurization denitration and escaping pipe (16), are fixed with the cyclone separator (2)
System includes cyclone separator (2), filter chamber (4), oxidizing chamber (9) and desulphurization denitration tower (12), and connecting tube (3) is interspersed wherein,
Filter chamber (4) inner homogeneous are filled with activated carbon (5), and the ozone generator (6) is internally provided with oxygen cylinder (7) and height
Electrical equipment (8) is pressed, the oxidizing chamber (9) is internally provided with electric plug (10), fixedly mounted on the desulphurization denitration tower (12)
There is ozzle (11), uniformly column plate (13), desulphurization denitration tower (12) top are installed with the desulphurization denitration tower (12)
It is installed with ejection alkaline solution (14), the desulphurization denitration tower (12) in alkali lye shower nozzle (15), the alkali lye shower nozzle (15)
On be installed with escaping pipe (16).
2. a kind of novel efficient system for desulfuration and denitration according to claim 1, it is characterised in that:The novel efficient
Cyclone separator (2), filter chamber (4), oxidizing chamber (9) and desulphurization denitration tower (12) housing are by high-quality Q235 in system for desulfuration and denitration
Stainless steel is made, cyclone separator (2), filter chamber (4), oxidizing chamber (9) and all corner wholes of desulphurization denitration tower (12) housing
It is molded using special fillet mould, wherein, cyclone separator (2) is a kind of vertical cylinder structure, and wall thickness is 1cm, height
It is 2m, drum diameter 30cm, filter chamber (4) are a kind of vertical shuttle-type cylindrical structure, and oxidizing chamber (9) is a kind of horizontal cylinder knot
Structure, desulphurization denitration tower (12) is a kind of scrubbing tower, cyclone separator (2), filter chamber (4), oxidizing chamber (9) and desulphurization denitration tower
(12) housing wall thickness is no more than 1cm, and filter chamber (4), oxidizing chamber (9) and desulphurization denitration tower (12) volume are not less than 1 cubic metre.
3. a kind of novel efficient system for desulfuration and denitration according to claim 1, it is characterised in that:The air inlet pipe (1),
Connecting tube (3), ozzle (11) and escaping pipe (16) are made by Q235 stainless steels, specially a kind of cylindrical tube member, air inlet pipe
(1), connecting tube (3) and escaping pipe (16) caliber are no more than 8cm, and length is not less than 10cm, and ozzle (11) caliber is no more than 8cm,
Length is not less than 10cm, and outside is provided with flange gasket, and thickness is 1.6cm, a diameter of 9.6cm, and ozzle (11) number is not less than 4
It is individual.
4. a kind of novel efficient system for desulfuration and denitration according to claim 1, it is characterised in that:The activated carbon (5)
It is a kind of metamict crystals activated carbon, is fine particulate structure, concrete shape is spheroid, and particle effective diameter is no more than 1mm, living
Property charcoal (5) inside be dispersed with duct, duct effective diameter is no more than 1um, and inner surfaces of pores product is not less than 10cm2, duct number
It is not less than 100.
5. a kind of novel efficient system for desulfuration and denitration according to claim 1, it is characterised in that:The ozone generator
(6) specifically it is made up of oxygen cylinder (7) and high-voltage discharger (8), ozone generator (6) is a kind of cuboid-type structure, the oxygen
The gas that oxygen purity is 99.2% is filled in gas cylinder (7), specific volume is 10L, and pressure is no more than 150 atmospheric pressure, described
High-voltage discharger (8) work effective voltage is not less than 10KV, and power consumption is no more than 1000W.
6. a kind of novel efficient system for desulfuration and denitration according to claim 1, it is characterised in that:The electric plug
(10) be a kind of ceramic package and interior insulation body formula electric plug (10), work effective voltage be not less than 1KV, power consumption is not
More than 1000W, wherein, the number of the electric plug (10) in oxidizing chamber (9) is not less than 15 pairs.
7. a kind of novel efficient system for desulfuration and denitration according to claim 1, it is characterised in that:The column plate (13) is
A kind of plastic plate, is specifically made by vinyon system, column plate (13) middle setting liquid-leaking nozzle, and liquid-leaking nozzle aperture is 1cm,
Individual layer column plate (13) liquid-leaking nozzle hole count is not less than 500, and column plate (13) thickness is no more than 1cm, is a kind of disc structure, column plate
(13) number is not less than 20 pieces.
8. a kind of novel efficient system for desulfuration and denitration according to claim 1, it is characterised in that:The alkaline solution
(14) be NaOH, the strong alkali solution such as potassium hydroxide and calcium hydroxide, or several soda-wash solution mixed liquors, specific flow
1m3/h is not less than, wherein, alkaline solution (14) is pumped to desulphurization denitration top of tower by corrosion resisting centrifugal pump.
9. a kind of novel efficient system for desulfuration and denitration according to claim 1, it is characterised in that:The alkali lye shower nozzle
(15) specifically it is made up of high brass, specially a kind of furred ceiling type shower nozzle is provided with spray orifice, spray orifice aperture on alkali lye shower nozzle (15)
No more than 1mm, hole count is not less than 500, and alkali lye shower nozzle (15) is not less than 30.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620884944.4U CN206184231U (en) | 2016-08-15 | 2016-08-15 | Novel high efficiency SOx/NOx control system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620884944.4U CN206184231U (en) | 2016-08-15 | 2016-08-15 | Novel high efficiency SOx/NOx control system |
Publications (1)
Publication Number | Publication Date |
---|---|
CN206184231U true CN206184231U (en) | 2017-05-24 |
Family
ID=58736973
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201620884944.4U Expired - Fee Related CN206184231U (en) | 2016-08-15 | 2016-08-15 | Novel high efficiency SOx/NOx control system |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN206184231U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107583422A (en) * | 2017-10-23 | 2018-01-16 | 安徽金森源环保工程有限公司 | A kind of low-temperature plasma desulfuring and denitrifying apparatus and desulfurization denitration method |
CN108187480A (en) * | 2018-01-23 | 2018-06-22 | 青岛双瑞海洋环境工程股份有限公司 | Marine exhaust desulphurization system |
-
2016
- 2016-08-15 CN CN201620884944.4U patent/CN206184231U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107583422A (en) * | 2017-10-23 | 2018-01-16 | 安徽金森源环保工程有限公司 | A kind of low-temperature plasma desulfuring and denitrifying apparatus and desulfurization denitration method |
CN108187480A (en) * | 2018-01-23 | 2018-06-22 | 青岛双瑞海洋环境工程股份有限公司 | Marine exhaust desulphurization system |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101862583B (en) | Flue gas desulfurization process suitable for sintering machine of steel mill | |
CN104258719A (en) | Desulfuration, denitration and dust removal (PM2.5 removal) three-in-one technical system for boiler exhaust gas by adopting ammonia method | |
CN102240500A (en) | System and process for desulfuration and denitration by pure oxygen dielectric barrier discharge in flue | |
CN104959034A (en) | Flue gas desulfurization method, flue gas desulfurization device as well as integrated flue gas desulfurization and denitration system and method | |
CN107051158A (en) | A kind of hydrogen peroxide desulfurizer handled for sulfuric acid tail gas and method | |
CN206184231U (en) | Novel high efficiency SOx/NOx control system | |
CN105363340A (en) | Activated carbon dry-method smoke purifying method and device capable of achieving simultaneous desulfurization and denitrification | |
CN102160961A (en) | Dielectric barrier discharge reactor, fume desulfurization and denitration system and desulfurizating and denitrating process | |
CN102151475B (en) | Two-tower ammonia method desulfurization device and method | |
CN107158910A (en) | A kind of denitrating flue gas ozone reaction device | |
CN105107366A (en) | Direct flow spraying semi-dry type flue gas desulfurization method | |
CN204320092U (en) | A kind of flue gas washing mechanism with convergent-divergent shape orifice plate | |
CN203916446U (en) | Desulphurization denitration enriched flue gas cooling device | |
CN108854499A (en) | A kind of furfural dregs boiler smoke magnesia FGD purification device | |
CN102872693B (en) | Processing method of waste nitric acid fume and device thereof | |
CN107096378A (en) | The flue gas desulphurization system and sulfur method of a kind of floatation glass production line | |
CN107051171A (en) | A kind of double tower magnesium method flue gas desulphurization technique | |
CN203944281U (en) | Flue gas desulfur device | |
CN106422712A (en) | High-pressure spray desulfurization, denitration and dust removal method | |
CN203963977U (en) | The ammonia desulfuration equipment of smoke treatment desulfurization band liquid | |
CN204170616U (en) | Process of desulfurization for boiler flue gas denitration dust collecting Trinity process system | |
CN202169136U (en) | Integrated equipment for conducting desulfurization by adopting ammonia wet method and collecting desulfurization products by adopting dry method | |
CN101549245A (en) | Desulfurizing method of spraying flue gas purifier for flue gas desulfurization of sintering machines | |
CN204412054U (en) | A kind of wet flue gas desulfurization tower | |
CN105833694B (en) | Electric arc devulcanizer |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170524 Termination date: 20170815 |