CN211706408U - Flue gas oxidation denitration device - Google Patents
Flue gas oxidation denitration device Download PDFInfo
- Publication number
- CN211706408U CN211706408U CN201922085325.5U CN201922085325U CN211706408U CN 211706408 U CN211706408 U CN 211706408U CN 201922085325 U CN201922085325 U CN 201922085325U CN 211706408 U CN211706408 U CN 211706408U
- Authority
- CN
- China
- Prior art keywords
- cavity
- flue gas
- absorption
- oxidation
- central column
- 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.)
- Active
Links
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 title claims abstract description 258
- 239000003546 flue gas Substances 0.000 title claims abstract description 258
- 238000007254 oxidation reaction Methods 0.000 title claims abstract description 224
- 230000003647 oxidation Effects 0.000 title claims abstract description 222
- 238000010521 absorption reaction Methods 0.000 claims abstract description 218
- 239000007788 liquid Substances 0.000 claims abstract description 182
- 230000001590 oxidative effect Effects 0.000 claims abstract description 100
- 238000005507 spraying Methods 0.000 claims abstract description 57
- 239000007921 spray Substances 0.000 claims abstract description 17
- 239000000243 solution Substances 0.000 claims description 22
- 238000005192 partition Methods 0.000 claims description 14
- 238000001514 detection method Methods 0.000 claims description 9
- 239000012670 alkaline solution Substances 0.000 claims description 7
- 125000004122 cyclic group Chemical group 0.000 claims description 7
- 239000000779 smoke Substances 0.000 claims description 7
- 239000007800 oxidant agent Substances 0.000 abstract description 8
- 238000006243 chemical reaction Methods 0.000 abstract description 4
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 136
- 238000000034 method Methods 0.000 description 23
- JCXJVPUVTGWSNB-UHFFFAOYSA-N nitrogen dioxide Inorganic materials O=[N]=O JCXJVPUVTGWSNB-UHFFFAOYSA-N 0.000 description 13
- 230000000052 comparative effect Effects 0.000 description 9
- 239000007789 gas Substances 0.000 description 8
- SUKJFIGYRHOWBL-UHFFFAOYSA-N sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 description 8
- 239000005708 Sodium hypochlorite Substances 0.000 description 7
- 238000004891 communication Methods 0.000 description 7
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- 230000002378 acidificating effect Effects 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 238000013461 design Methods 0.000 description 4
- LZDSILRDTDCIQT-UHFFFAOYSA-N dinitrogen trioxide Chemical compound [O-][N+](=O)N=O LZDSILRDTDCIQT-UHFFFAOYSA-N 0.000 description 4
- 239000003344 environmental pollutant Substances 0.000 description 4
- 231100000719 pollutant Toxicity 0.000 description 4
- 238000004064 recycling Methods 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- 239000003054 catalyst Substances 0.000 description 3
- 239000000835 fiber Substances 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonium chloride Substances [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 2
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 2
- GQPLMRYTRLFLPF-UHFFFAOYSA-N Nitrous Oxide Chemical compound [O-][N+]#N GQPLMRYTRLFLPF-UHFFFAOYSA-N 0.000 description 2
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 2
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 2
- 230000001133 acceleration Effects 0.000 description 2
- 235000011114 ammonium hydroxide Nutrition 0.000 description 2
- 239000004202 carbamide Substances 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- MGWGWNFMUOTEHG-UHFFFAOYSA-N 4-(3,5-dimethylphenyl)-1,3-thiazol-2-amine Chemical compound CC1=CC(C)=CC(C=2N=C(N)SC=2)=C1 MGWGWNFMUOTEHG-UHFFFAOYSA-N 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- 229910002651 NO3 Inorganic materials 0.000 description 1
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000002250 absorbent Substances 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 125000004429 atom Chemical group 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000012159 carrier gas Substances 0.000 description 1
- 235000019504 cigarettes Nutrition 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000002939 deleterious effect Effects 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 230000031700 light absorption Effects 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- QGZKDVFQNNGYKY-NJFSPNSNSA-N nitrogen-16 Chemical compound [16NH3] QGZKDVFQNNGYKY-NJFSPNSNSA-N 0.000 description 1
- 239000001272 nitrous oxide Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 125000004430 oxygen atom Chemical group O* 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 239000012286 potassium permanganate Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 150000003254 radicals Chemical class 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000000523 sample Substances 0.000 description 1
- 238000004088 simulation Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000005437 stratosphere Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Images
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
Landscapes
- Treating Waste Gases (AREA)
Abstract
The utility model provides a flue gas oxidation denitrification facility. The flue gas oxidation denitration device comprises an oxidation cavity and an absorption cavity connected with the oxidation cavity; an oxidizing liquid spraying device is arranged in the oxidation cavity, and an absorption liquid spraying device is arranged in the absorption cavity; at least one of the oxidation cavity and the absorption cavity is internally provided with a flue gas turbulence device; when the oxidation cavity is provided with the flue gas turbulence equipment, the flue gas turbulence equipment of the oxidation cavity is used for improving the turbulence degree of the flue gas entering the oxidation cavity in the oxidation cavity; when the absorption cavity is provided with a flue gas turbulence device, the absorption cavityThe flue gas turbulence equipment is used for improving the turbulence degree of the flue gas entering the absorption cavity in the absorption cavity. The utility model provides a flue gas denitration device has introduced turbulent equipment in order to increase the reaction efficiency who sprays liquid and flue gas, can be fine be applicable to with NaClO2Is the denitration treatment of the oxidant.
Description
Technical Field
The utility model belongs to the technical field of flue gas denitration, a flue gas oxidation denitrification facility is related to.
Background
Nitrogen oxides (NOx) are mainly nitrogen monoxide (NO) and nitrogen dioxide (NO)2) Pollution is formed when they are present in the atmosphere in amounts and for periods of time to the extent that they have a deleterious effect on humans, animals, plants and other materials. Other forms of nitrogen oxides in the atmosphere, such as nitrous oxide (N)2O) and dinitrogen trioxide (N)2O3) And the like.
NO can react with ozone in the atmosphere quickly to form NO2. NO is reacted directly with oxygen to form NO2The rate of (d) depends mainly on the concentration of NO and the ambient temperature. NO concentration of 10mg/m at below 20 deg.C3Under the condition (1), 10% of NO is oxidized to NO2It took 1.5 hours for 50% of the NO to oxidize to NO2It took 10.75 hours. NO concentration of 2mg/m at below 20 deg.C3Under the condition (1), 10% of NO is oxidized to NO2It takes more than 8 hours. It can be seen that when the NO content in the air is very low, it can remain in the air for a long time. NO may also be combined with NO2Reaction to produce dinitrogen trioxide (N)2O3) But the amount formed is small and has little effect on the quality of the atmosphere. NO2Is the most important light absorption molecule in the lower atmosphere and can absorb visible light and ultraviolet light of solar radiation. It absorbs ultraviolet light with wavelength less than 400 fiber meter and is decomposed into NO and oxygen atom, especially under the irradiation of light with wavelength of 300-370 fiber meter, over 90% NO2The molecule can be decomposed; due to NO2The bond energy (73 cal/mol) of the chemical bond between the mesooxygen atom and NO is greater than the photon energy at a wavelength of 400 km, so that NO2When the glass is irradiated by visible light with the wavelength of more than 420 fiber meters, the decomposition does not occur. The vast majority of atmospheric NOx is eventually converted to nitrate particulates and disappears from the atmosphere through processes such as wet or dry settling. N is a radical of2O is an inert gas which can be stored in the atmosphere for a long time and can be decomposed by reacting with ozone after entering the atmosphere of the stratosphere.
GB13223-2011 'emission Standard of atmospheric pollutants for thermal power plant' stipulates that the NOx emission Standard of a newly built boiler is 100mg/m3Increasingly stringent emission standards have prompted the continued push for new denitration technologies. For more than ten years, researchers at home and abroad try O in turn to realize low-temperature flue gas oxidation aiming at the defects of the SCR and SNCR technology adopted in the flue gas denitration of the industrial boiler3、H2O2、KMnO4、NaClO2Wherein NaClO2As an oxidant, has an optimum NOx removal capacity. The related research is mainly based on theoretical analysis and flue gas simulation experiments, and no report of practical application exists.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide an efficient flue gas oxidation denitrification facility and method.
In order to achieve the purpose, the utility model provides a flue gas oxidation denitration device, wherein, the device comprises an oxidation cavity and an absorption cavity (namely a denitration cavity) connected with the oxidation cavity; the flue gas oxidized by the oxidation cavity enters an absorption cavity to be absorbed;
an oxidizing liquid spraying device is arranged in the oxidizing cavity, and an absorbing liquid spraying device is arranged in the absorbing cavity;
at least one of the oxidation cavity and the absorption cavity is internally provided with a flue gas turbulence device;
when the oxidation cavity is provided with the flue gas turbulence equipment, the flue gas turbulence equipment of the oxidation cavity is used for improving the turbulence degree of the flue gas entering the oxidation cavity in the oxidation cavity;
when the absorption cavity is provided with the flue gas turbulence equipment, the flue gas turbulence equipment of the absorption cavity is used for improving the turbulence degree of the flue gas entering the absorption cavity in the absorption cavity.
In the flue gas oxidation and denitration device, flue gas enters the oxidation cavity so as to realize oxidation of nitrogen oxides in the flue gas, and the flue gas after oxidation treatment in the oxidation cavity enters the absorption cavity so as to realize absorption of the nitrogen oxides in the flue gas and realize denitration treatment; the flue gas turbulent flow equipment belt makes flue gas disorder degree promote, has realized that flue gas and oxidizing solution and/or absorption liquid fully contact, realizes the high-efficient oxidation denitration of flue gas.
In the above flue gas oxidation and denitration device, preferably, the flue gas turbulence equipment of the oxidation chamber comprises a partition board which divides the oxidation chamber into at least two chambers from top to bottom and a central column which penetrates the whole oxidation chamber from top to bottom; each chamber of the oxidation cavity is communicated with the central column through a grating arranged on the central column, and the central column is of a hollow structure, so that the communication among the chambers is realized; and the oxidizing liquid spraying equipment is arranged in each cavity, and a flue gas inlet of the oxidizing cavity is arranged at the bottommost cavity. The flue gas gets into bottommost cavity by the flue gas entry, the oxidation liquid contact that sprays with oxidation liquid spraying equipment, form the cyclone in bottommost cavity and increase contact time, then in the flue gas gets into the center post, flue gas after the post acceleration from the upper chamber in the center post grid efflux blowout get into the upper chamber in, very big increase the turbulent degree of the flue gas in the upper chamber, get into the flue gas in the upper chamber and spray the oxidation liquid that equipment sprayed with oxidation liquid more intensive mixing, realize the high-efficient oxidation of flue gas. In one embodiment, each portion of the central column located within each chamber of the oxidation chamber is provided with at least one grating.
In the above flue gas oxidation and denitration apparatus, preferably, the flue gas turbulence device of the absorption chamber comprises a partition plate which divides the absorption chamber into at least two chambers from top to bottom and a central column which vertically penetrates through the whole absorption chamber; each chamber of the absorption cavity is communicated with the central column through a grid arranged on the central column, and the central column is of a hollow structure, so that the communication among the chambers is realized; the absorption liquid spraying equipment is arranged in each cavity, and the smoke inlet of the absorption cavity is arranged at the bottommost cavity. The flue gas gets into bottommost cavity by the flue gas entry, the absorption liquid contact that sprays with absorption liquid spraying equipment, form the cyclone in bottommost cavity and increase contact time, then the flue gas gets into in the center post, flue gas after the post acceleration from the upper chamber in the center post grid efflux blowout get into the upper chamber in, very big increase the turbulent degree of the flue gas in the upper chamber, the flue gas that gets into the upper chamber sprays with absorption liquid spraying equipment absorption liquid intensive mixing more, realize the high-efficient absorption of flue gas, accomplish the oxidation denitration treatment. In a specific embodiment, each part of the central column located in each chamber of the absorption chamber is provided with at least one grating.
In the above flue gas oxidation and denitration device, preferably, the device is further provided with an oxidizing liquid circulating system, the oxidizing liquid circulating system comprises an oxidizing liquid pool arranged in the oxidation cavity and a circulating device connected with the oxidizing liquid pool, the oxidizing liquid pool is used for collecting the oxidizing liquid after the flue gas in the oxidation cavity is treated, and the circulating device is used for conveying the oxidizing liquid collected by the oxidizing liquid pool to the oxidizing liquid spraying device for recycling; more preferably, an oxidizing liquid pool stirring paddle is arranged in the oxidizing liquid pool. The circulating device can be a circulating pump.
In the above-mentioned flue gas oxidation and denitration device, preferably, the device is further provided with an absorption liquid circulation system, the absorption liquid absorption system includes an absorption liquid tank arranged in the absorption cavity and a circulation device connected to the absorption liquid tank, the absorption liquid tank is used for collecting the absorption liquid after the flue gas treatment in the absorption cavity, and the circulation device is used for conveying the absorption liquid collected by the absorption liquid tank to the absorption liquid spraying device for cyclic utilization. The circulating device can be a circulating pump.
In the above-mentioned flue gas oxidation denitrification facility, preferably, the absorption chamber and the oxidation chamber are arranged in the same absorption tower, and the oxidation chamber is located at the lower part of the absorption chamber.
In a specific embodiment, the flue gas oxidation and denitration device comprises a denitration tower body, wherein an oxidation cavity and an absorption cavity connected with the oxidation cavity are arranged in the denitration tower body, the oxidation cavity is positioned at the lower part of the absorption cavity, and the flue gas is oxidized by the oxidation cavity, enters the absorption cavity for absorption and then is discharged out of the denitration tower body through a flue gas outlet;
an oxidizing liquid spraying device and a flue gas turbulence device are arranged in the oxidation cavity; the flue gas turbulence equipment of the oxidation cavity comprises a partition board which divides the oxidation cavity into an upper cavity and a lower cavity and a central column which vertically penetrates through the whole oxidation cavity; each chamber of the oxidation chamber is communicated with the central column through a grating arranged on the central column, the central column is of a hollow structure, and the communication between the chambers is realized (preferably, at least one grating is arranged at each part of the central column, which is positioned in each chamber of the absorption chamber); the oxidation liquid spraying equipment is arranged in each cavity, and a flue gas inlet of the denitration tower body is arranged in the cavity at the bottommost part of the oxidation cavity; the flue gas enters an oxidation cavity to realize the oxidation of nitrogen oxides in the flue gas;
the absorption cavity is internally provided with absorption liquid spraying equipment and smoke turbulence equipment, and the smoke turbulence equipment of the absorption cavity comprises a partition board which divides the absorption cavity into an upper cavity and a lower cavity and a central column which vertically penetrates through the whole absorption cavity; each chamber of the absorption cavity is communicated with the central column through the grating arranged on the central column, the central column is of a hollow structure, and the communication between the chambers is realized (preferably, at least one grating is arranged on each part of the central column, which is positioned in each chamber of the absorption cavity); the absorption liquid spraying equipment is arranged in each cavity; the flue gas after oxidation treatment of the oxidation cavity enters the absorption cavity from the cavity at the bottommost part of the absorption cavity to absorb nitrogen oxides in the flue gas;
the denitration tower body is further provided with double circulating systems, namely an oxidizing liquid circulating system and an absorption liquid circulating system; the oxidizing liquid circulating system comprises an oxidizing liquid pool arranged in the oxidizing cavity and circulating equipment (such as a circulating pump) connected with the oxidizing liquid pool, the oxidizing liquid pool is used for collecting the oxidizing liquid after the flue gas in the oxidizing cavity is treated, and the circulating equipment is used for conveying the oxidizing liquid collected by the oxidizing liquid pool to oxidizing liquid spraying equipment for recycling; preferably, an oxidizing liquid pool stirring paddle is arranged in the oxidizing liquid pool; the absorption liquid absorption system comprises an absorption liquid pool arranged in the absorption cavity and circulating equipment (such as a circulating pump) connected with the absorption liquid pool, the absorption liquid pool is used for collecting absorption liquid after flue gas treatment in the absorption cavity, and the circulating equipment is used for conveying the absorption liquid collected by the absorption liquid pool to the absorption liquid spraying equipment for recycling.
In the flue gas oxidation and denitration device provided by the specific embodiment, the flue gas enters from the bottom layer cavity of the oxidation cavityAnd (4) the flue gas enters a denitration tower and is in reverse contact with the oxidizing liquid, and the oxidizing liquid is sprayed into an oxidation cavity through oxidizing liquid spraying equipment to perform oxidation reaction with the flue gas. The flue gas firstly enters a chamber at the lower layer of the clapboard, and the flue gas and oxidizing liquid (such as NaClO)2) The contact forms the cyclone in the region and increases contact time, then the flue gas gets into in the center post after accelerating from center post upper chamber baffle grid efflux blowout entering upper chamber, greatly increases the disorderly degree of flue gas in the upper chamber for flue gas and oxidizing liquid intensive mixing more realize the high-efficient oxidation of flue gas. The NO in the flue gas is fully oxidized and converted into NO by the oxidation of the oxidation cavity2With a small amount of Cl2HCl and untreated or untreated SO2The flue gas entering the absorption cavity is in reverse contact with the alkaline absorption liquid and also fully reacts with the flue gas through the central column-grating structure, and various pollutants including NOx can be almost completely removed at the position. In addition, the flue gas oxidation denitration device provided by the above specific embodiment adopts a single-tower double-circulation operation mode, the absorption liquid and the oxidation liquid are sprayed in different sections of the same tower in the oxidation denitration process, and the circulation systems respectively arranged in the oxidation cavity and the denitration cavity relatively and independently realize the recycling of the absorption liquid and the oxidation liquid. In addition, the single-tower double-circulation can effectively reduce the occupied area of the device.
In the above flue gas oxidation and denitration device, preferably, the top of the central column of the oxidation chamber is provided with an oxidizing liquid spraying device, and the flue gas is accelerated in the central column and can be further oxidized by the oxidizing liquid.
In the above flue gas oxidation and denitration device, preferably, the top of the central column of the absorption cavity is provided with an absorption liquid spraying device, and the flue gas is accelerated in the central column and can be further oxidized by the absorption liquid.
In the above flue gas oxidation and denitration device, preferably, the radius of the oxidation cavity is about 3-5 times of the radius of the central column of the oxidation cavity.
In the above flue gas oxidation and denitration device, preferably, the radius of the absorption cavity is about 3-5 times of the radius of the central column of the absorption cavity.
In the above flue gas oxidation and denitration device, preferably, the radius of the central column of the oxidation cavity is equal to the radius of the central column of the absorption cavity. The radius of the central column of the oxidation cavity is equal to that of the central column of the absorption cavity, so that the phenomenon that the flue gas is compressed too high in the central column can be better avoided.
In the above flue gas oxidation and denitration device, preferably, the radius of the oxidation cavity is equal to the radius of the absorption cavity. The radius of the oxidation cavity is equal to that of the absorption cavity, so that the oxidation cavity is convenient to process and transport.
In the above flue gas oxidation and denitration device, preferably, the opening ratio of the grating on the central column of the oxidation cavity (the opening ratio of the grating is the percentage of the opening area of the grating in the total area of the grating) is 50% -75%.
In the above flue gas oxidation and denitration device, preferably, the opening ratio of the grating on the central column of the absorption chamber (the opening ratio of the grating is the percentage of the opening area of the grating in the total area of the grating) is 50% -75%.
In the above flue gas oxidation and denitration device, preferably, the grid interval on the central column of the oxidation chamber is 0.05R-0.1R, where R is the radius of the central column.
In the above flue gas oxidation and denitration device, preferably, the grid interval on the central column of the absorption cavity is 0.05R-0.1R, where R is the radius of the central column.
In the above flue gas oxidation and denitration device, preferably, the oxidizing liquid spraying apparatus includes a spraying grid; more preferably, the spray grille comprises spray heads and a water delivery frame structure; further preferably, the spray grille is formed by connecting a circular frame body spray head to the bottom end of the frame.
In the above flue gas oxidation and denitration apparatus, preferably, the absorption liquid spraying device includes a spraying grid; more preferably, the spray grille comprises spray heads and a water delivery frame structure; further preferably, the spray grille is formed by connecting a circular frame body spray head to the bottom end of the frame.
In the above flue gas oxidation and denitration device, preferably, the oxidizing liquid sprayed by the oxidizing liquid spraying equipment is NaClO2A solution; more preferably, the NaClO2NaClO in solution2The concentration of (b) is 1mmol/L to 10 mmol/L.
At the upper partIn the flue gas oxidation and denitration device, preferably, the absorption liquid sprayed by the absorption liquid spraying equipment is an alkaline solution; more preferably, the alkaline solution comprises a NaOH solution, an ammonia solution, a urea solution, NaS2O8At least one of the solutions. Oxidation process generated Cl using alkaline solution as absorbent2And pollutants such as HCl and the like can be effectively removed, so that secondary pollution is avoided.
In the above flue gas oxidation and denitration device, preferably, the device further comprises a demister for treating the flue gas treated by the absorption chamber. When the absorption cavity and the oxidation cavity are arranged in the same absorption tower, the demister is preferably arranged between the absorption cavity and the flue gas outlet. The flue gas moisture content after spraying the processing through absorption liquid is higher, and direct emission can produce a large amount of white cigarette, sets up the defroster in denitration section upper end, can effectively reduce flue gas water content, and the flue gas after the purification is discharged through the exhanst gas outlet.
In the above flue gas denitration apparatus, preferably, the apparatus further comprises NOx concentration detection means for detecting the NOx concentration in the flue gas after the oxidation denitration treatment. More preferably, the device further comprises a flue gas circulation treatment device for introducing the flue gas with the unqualified NOx concentration inspection into the oxidation cavity for carrying out the flue gas oxidation denitration treatment again.
In the flue gas denitration device, the flue gas is oxidized by the oxidation cavity, and NO in the flue gas is fully oxidized and converted into NO2With a small amount of Cl2HCl and untreated or untreated SO2Entering the absorption cavity; the flue gas in the absorption cavity is in countercurrent contact with the alkaline absorption liquid, and various pollutants including NOx are almost completely removed in the absorption cavity.
In the flue gas denitration device, fillers such as Raschig rings, pall rings and the like can be properly arranged in the oxidation cavity and the absorption cavity to increase the contact area of gas and liquid phases.
Use the utility model provides an above-mentioned flue gas oxidation denitrification facility carries out flue gas oxidation denitrification treatment, can go on through following flue gas oxidation denitrification treatment method: the method comprises the steps that flue gas enters an oxidation cavity, a sodium hypochlorite solution is used as an oxidant to oxidize nitrogen oxides in the flue gas under the action of turbulent equipment, and/or the oxidized flue gas enters an absorption cavity, and NOx and other acidic gases in the flue gas are removed under the action of turbulent equipment by using an alkaline absorption liquid.
In a specific embodiment, the method for oxidation and denitration treatment of flue gas comprises: the flue gas enters the oxidation cavity, the oxidation of nitrogen oxides in the flue gas is realized under the action of turbulent equipment by using a sodium hypochlorite solution as an oxidant, the removal of NOx and other acidic gases in the flue gas is realized by using an alkaline absorption liquid after the oxidized flue gas enters the absorption cavity, and therefore the step of flue gas oxidation and denitration treatment is completed.
In a specific embodiment, the method for oxidation and denitration treatment of flue gas comprises: the flue gas enters the oxidation cavity, the oxidation of nitrogen oxides in the flue gas is realized by using a sodium hypochlorite solution as an oxidant, the oxidized flue gas enters the absorption cavity, and the removal of NOx and other acidic gases in the flue gas is realized by using an alkaline absorption liquid under the action of turbulent equipment, so that the step of flue gas oxidation and denitration treatment is completed.
In a specific embodiment, the method for oxidation and denitration treatment of flue gas comprises: the flue gas enters the oxidation cavity, the oxidation of nitric oxide in the flue gas is realized under the action of turbulent flow equipment by using a sodium hypochlorite solution as an oxidant, the removal of NOx and other acidic gases in the flue gas is realized under the action of turbulent flow equipment by using alkaline absorption liquid after the oxidation of the flue gas in the absorption cavity, and thus the step of flue gas oxidation and denitration treatment is completed.
In the above method for oxidation and denitration treatment of flue gas, preferably, the method further comprises a demisting treatment of flue gas treated with the absorption liquid.
In the above method for oxidizing and denitrating flue gas, preferably, the method further includes detecting NOx concentration of the flue gas after oxidation and denitration treatment, and the flue gas whose NOx concentration does not reach the emission standard enters the oxidation and denitration device again for secondary oxidation and denitration.
In the above method for oxidation and denitration treatment of flue gas, it is preferable that the sodium hypochlorite solution used for oxidation treatment is recycled.
In the above-described flue gas oxidation denitration treatment method, it is preferable that the alkaline solution used for the absorption treatment is recycled.
In the above-mentioned flue gas oxidation denitration treatment method, the SCR method is often used for denitration, and for flue gas with complex components such as coke oven flue gas and high dust content, if dust removal and desulfurization are not performed first, the flue gas will have adverse effect on the denitration catalyst, so that the catalyst life may be greatly reduced, the catalyst is expensive, and the cost is greatly increased. The utility model adopts NaClO2Oxidation method, and greatly improves the denitration capability and reduces the generated Cl by spraying alkali liquor2And secondary pollution such as HCl and the like, and turbulence equipment is introduced into the equipment to increase the reaction efficiency of the spray liquid and the flue gas, so that the denitration efficiency is obviously improved.
Compared with the prior art, the utility model has the advantages of as follows: the utility model provides a flue gas denitration device has introduced turbulent equipment in order to increase the reaction efficiency who sprays liquid and flue gas, can be fine be applicable to with NaClO2Is the denitration treatment of the oxidant.
Drawings
Fig. 1 is a schematic view of a flue gas oxidation and denitration device provided in embodiment 1.
Fig. 2 is a schematic diagram of a flue gas oxidation denitration device provided in comparative example 1.
FIG. 3A shows NO in Experimental example 1XThe result graph is removed.
FIG. 3B is a graph showing the results of NO oxidation rate in Experimental example 1.
Detailed Description
In order to clearly understand the technical features, objects and advantages of the present invention, the following detailed description is given to the technical solution of the present invention, but the technical solution of the present invention is not limited to the limit of the implementable range of the present invention.
Example 1
The embodiment provides a flue gas oxidation denitration device (as shown in fig. 1), which comprises a denitration tower body 1 and NOx concentration detection equipment 5, wherein an oxidation cavity 2, an absorption cavity 3 communicated with the oxidation cavity and a demister 4 communicated with the absorption cavity 3 are arranged in the denitration tower body 1 from bottom to top, a flue gas inlet 11 is arranged at the bottom of the denitration tower body 1, a flue gas outlet 12 is arranged at the top of the denitration tower body, and the NOx concentration detection equipment 5 is connected with the flue gas outlet 12;
an oxidizing liquid spraying device 21 and a flue gas turbulence device are arranged in the oxidation cavity 2; the flue gas turbulence equipment of the oxidation cavity comprises a partition plate 22 for dividing the oxidation cavity 2 into an upper cavity and a lower cavity and a central column 23 which vertically penetrates through the whole oxidation cavity 2; the radius of the center column 23 is 1/5 of the radius of the oxidation cavity 2, at least one center column grating 24 is arranged on the part of the center column 23 located in each cavity, the interval of the center column gratings 24 on the center column 23 is 0.1R, the height of each section of grating is 0.06R, R is the radius of the center column 23 (namely, 60% of the area of the surface of the center column 23 is the center column grating 24), and the aperture ratio of the center column grating 24 is 70% (the average aperture ratio of the whole center column 23 is 42%, namely, the total area of the apertures of all the center column gratings 24 on the whole center column 23 accounts for 42% of the total area of the center column 23); each chamber is communicated with a central column 23 through a central column grille 24, and the central column 23 is of a hollow structure, so that the communication among the chambers is realized; the oxidizing liquid spraying equipment 21 is arranged in each cavity, and the oxidizing liquid spraying equipment 21 is arranged at the top of the central column 23; a flue gas inlet 11 of the denitration tower body 1 is arranged in the bottommost cavity of the oxidation cavity 2; the oxidizing liquid spraying equipment 21 adopts a spraying grid which is formed by connecting a plurality of circular frame body nozzles at the bottom end of a water delivery frame structure;
the absorption cavity 3 is internally provided with absorption liquid spraying equipment 31 and flue gas turbulence equipment, and the flue gas turbulence equipment of the absorption cavity comprises a partition plate 32 for dividing the absorption cavity into an upper cavity and a lower cavity and a central column 33 vertically penetrating through the whole absorption cavity; the radius of the central column 33 is 1/5 of the radius of the absorption cavity 3, at least one central column grating 34 is arranged on the part of the central column 33 located in each cavity, the interval of the central column gratings 34 on the central column 33 is 0.1R, the height of each section of grating is 0.07R, R is the radius of the central column 33 (namely 70% of the area of the surface of the central column 33 is the central column grating 34), and the aperture ratio of the central column gratings 34 is 75% (the average aperture ratio of the whole central column 33 is 52.5%, namely the total area of the apertures of all the central column gratings 34 on the whole central column 33 accounts for 52.5% of the total area of the central column 33); each chamber is communicated with a central column 33 through a central column grating 34, and the central column 33 is of a hollow structure, so that the communication among the chambers is realized; the absorption liquid spraying equipment 31 is arranged in each cavity, and the oxidation liquid spraying equipment 31 is arranged at the top of the central column 33; the absorption liquid spraying equipment 31 adopts a spraying grid which is formed by connecting a plurality of circular frame body spray heads at the bottom end of a water delivery frame structure; the flue gas oxidized by the oxidation cavity 2 enters the absorption cavity 3 from the cavity at the bottommost part of the absorption cavity 3 to absorb nitrogen oxides in the flue gas; the radius of the absorption cavity 3 is the same as that of the oxidation cavity 2, and the radius of the central column 23 is the same as that of the central column 33;
the denitration tower body 1 is provided with double circulating systems, namely an oxidizing liquid circulating system and an absorption liquid circulating system;
the oxidizing liquid circulating system comprises an oxidizing liquid pool 25 arranged in the oxidizing cavity and a circulating pump 26 connected with the oxidizing liquid pool, the oxidizing liquid pool 25 is used for collecting the oxidizing liquid after the flue gas in the oxidizing cavity 2 is treated, and the circulating pump 26 is used for conveying the oxidizing liquid collected by the oxidizing liquid pool 25 to the oxidizing liquid spraying equipment 21 for cyclic utilization; an oxidizing liquid pool stirring paddle 27 and a waste liquid outlet 28 are arranged in the oxidizing liquid pool;
the absorption liquid absorption system comprises an absorption liquid pool 35 arranged in the absorption cavity 3, an absorption liquid storage pool 37 connected with the absorption liquid pool 35 and a circulating pump 36, wherein the absorption liquid pool 35 is used for collecting absorption liquid after the flue gas in the absorption cavity 3 is treated, the absorption liquid collected in the absorption liquid pool 35 is discharged into the absorption liquid storage pool 37, the circulating pump 36 is used for conveying the absorption liquid in the absorption liquid storage pool 37 to the absorption liquid spraying equipment 31 for cyclic utilization, and the absorption liquid storage pool 37 is provided with an absorption liquid stirring paddle 38;
the demister 4 is used for treating the flue gas treated by the absorption cavity 3;
the NOx concentration detection device 5 comprises a three-way control valve and a NOx concentration detection probe, wherein the three-way control valve is respectively communicated with a flue gas outlet 12, a flue gas inlet 11 of the denitration tower body 1 and the atmosphere; the device is used for detecting the concentration of NOx in the flue gas discharged from the flue gas outlet 12 after oxidation and denitration treatment, realizing the discharge of the flue gas qualified in NOx concentration check by controlling the communication state of the three-way control valve, and re-entering the flue gas unqualified in NOx concentration check into the denitration tower body 1 through the flue gas inlet 11 of the denitration tower body 1 for secondary flue gas oxidation and denitration treatment;
wherein the oxidizing solution sprayed by the oxidizing solution spraying equipment 21 is 1mmol/L-10mmol/L NaClO2A solution; the absorbing liquid sprayed by the absorbing liquid spraying equipment 31 is alkaline solution such as NaOH solution, ammonia solution, urea solution and/or NaS2O8And (3) solution.
The embodiment also provides a method for performing oxidation denitration treatment on flue gas by using the flue gas oxidation denitration device, wherein the method comprises the following steps:
flue gas enters an oxidation cavity 2 through a flue gas inlet 11, oxidation of nitric oxide in the flue gas is achieved under the action of turbulent equipment by using a sodium hypochlorite solution as an oxidant, the oxidized flue gas enters an absorption cavity 3, NOx and other acidic gases in the flue gas are removed under the action of turbulent equipment by using an alkaline absorption liquid, the flue gas treated by using the absorption liquid enters a demister 4 for demisting treatment, then the flue gas enters an NOx concentration detection device 5 through a flue gas outlet 12 for NOx concentration detection, the flue gas with the NOx concentration not reaching the emission standard passes through the flue gas inlet 11 of a denitration tower body 1 again to enter the denitration tower body 1 again for secondary flue gas oxidation denitration treatment, the flue gas with the qualified NOx concentration is discharged, and the whole oxidation denitration treatment process is completed;
wherein, the sodium hypochlorite solution used for the oxidation treatment is recycled by the oxidation liquid circulating system, and the alkaline solution used for the absorption treatment is recycled by the oxidation liquid circulating system.
Comparative example 1
The present comparative example provides a flue gas oxidation and denitration device (as shown in fig. 2), which is substantially the same as the flue gas oxidation and denitration device provided in example 1, except that no flue gas turbulence device is arranged in the oxidation chamber and the absorption chamber in the present comparative example.
Specifically, the oxidation chamber of the present comparative example is different from the oxidation chamber of example 1 in that no partition plate and no center column are provided; the comparative example absorption chamber is different from the absorption chamber of the example 1 in that no partition plate and no central column are arranged; the rest of the procedure was the same as in example 1.
Experimental example 1
Respectively using the flue gas oxidation and denitration devices provided in the embodiment 1 and the comparative example 1 to carry out flue gas denitration, wherein the flue gas to be treated is distributed by using steel bottle gas, and monitoring and analyzing NOx concentrations at a flue gas inlet and a flue gas outlet of the flue gas oxidation and denitration devices provided in the embodiment 1 and the comparative example 1 by using a theta 42i-Hl NOx flue gas analyzer; the experimental conditions are as follows: the composition of the flue gas is 700ppm NO and 16 vol% O2The carrier gas is N2(ii) a The temperature of the flue gas is 80 ℃; the smoke amount is 45m3H; the radius of the oxidation cavity and the absorption cavity is 200 mm.
The results of the experiment are shown in FIGS. 3A-3B. It can be seen that the average levels of the NO oxidation rate and the removal rate of the flue gas oxidation denitration device with the flue gas turbulence design shown in example 1 are higher than those of the flue gas oxidation denitration device without the flue gas turbulence design provided in comparative example 1, and the flue gas oxidation denitration device with the flue gas turbulence design shown in example 1 has higher data stability under the working conditions, so that the flue gas turbulence design shown in example 1 has a relatively obvious positive effect in the flue gas oxidation denitration device.
Claims (10)
1. A flue gas oxidation denitration device is characterized by comprising an oxidation cavity and an absorption cavity connected with the oxidation cavity; the flue gas oxidized by the oxidation cavity enters an absorption cavity to be absorbed;
an oxidizing liquid spraying device is arranged in the oxidizing cavity, and an absorbing liquid spraying device is arranged in the absorbing cavity;
at least one of the oxidation cavity and the absorption cavity is internally provided with a flue gas turbulence device;
when the oxidation cavity is provided with the flue gas turbulence equipment, the flue gas turbulence equipment of the oxidation cavity is used for improving the turbulence degree of the flue gas entering the oxidation cavity in the oxidation cavity;
when the absorption cavity is provided with the flue gas turbulence equipment, the flue gas turbulence equipment of the absorption cavity is used for improving the turbulence degree of the flue gas entering the absorption cavity in the absorption cavity.
2. The flue gas oxidation denitration apparatus according to claim 1,
the flue gas turbulence equipment of the oxidation cavity comprises a partition plate and a central column, wherein the partition plate divides the oxidation cavity into at least two cavities from top to bottom, and the central column penetrates through the whole oxidation cavity from top to bottom; each chamber of the oxidation cavity is communicated with the central column through a grating arranged on the central column, and the central column which vertically penetrates through the whole oxidation cavity is of a hollow structure; the oxidizing liquid spraying equipment is arranged in each cavity, and a flue gas inlet of the oxidizing cavity is arranged at the bottommost cavity;
the flue gas turbulence equipment of the absorption cavity comprises a partition board and a central column, wherein the partition board divides the absorption cavity into at least two cavities from top to bottom, and the central column penetrates through the whole absorption cavity from top to bottom; each cavity of the absorption cavity is communicated with the central column through a grid arranged on the central column, and the central column which vertically penetrates through the whole absorption cavity is of a hollow structure; the absorption liquid spraying equipment is arranged in each cavity, and the smoke inlet of the absorption cavity is arranged at the bottommost cavity.
3. The flue gas oxidation denitration apparatus according to claim 1,
the device is further provided with an oxidizing liquid circulating system, wherein the oxidizing liquid circulating system comprises an oxidizing liquid pool arranged in the oxidizing cavity and circulating equipment connected with the oxidizing liquid pool, the oxidizing liquid pool is used for collecting oxidizing liquid after flue gas treatment in the oxidizing cavity, and the circulating equipment is used for conveying the oxidizing liquid collected by the oxidizing liquid pool to oxidizing liquid spraying equipment for cyclic utilization;
the device further is equipped with absorption liquid circulation system, and absorption liquid absorption system is including locating the absorption liquid pond in the absorption chamber and the circulating equipment who is connected with the absorption liquid pond, and the absorption liquid pond is used for collecting the absorption liquid after the absorption intracavity flue gas is handled, and circulating equipment is used for carrying the absorption liquid that the absorption liquid pond was collected to absorption liquid spray equipment and carries out cyclic utilization.
4. The oxidation and denitration device for flue gas according to claim 1, wherein the oxidation and denitration device for flue gas comprises a denitration tower body, an oxidation cavity and an absorption cavity connected with the oxidation cavity are arranged in the denitration tower body, the oxidation cavity is positioned at the lower part of the absorption cavity, the flue gas is oxidized by the oxidation cavity, enters the absorption cavity for absorption, and then is discharged out of the denitration tower body through a flue gas outlet;
an oxidizing liquid spraying device and a flue gas turbulence device are arranged in the oxidation cavity; the flue gas turbulence equipment of the oxidation cavity comprises a partition board which divides the oxidation cavity into an upper cavity and a lower cavity and a central column which vertically penetrates through the whole oxidation cavity; each chamber of the oxidation cavity is communicated with the central column through a grating arranged on the central column, and the central column which vertically penetrates through the whole oxidation cavity is of a hollow structure; the oxidation liquid spraying equipment is arranged in each cavity, and a flue gas inlet of the denitration tower body is arranged in the cavity at the bottommost part of the oxidation cavity;
the absorption cavity is internally provided with absorption liquid spraying equipment and smoke turbulence equipment, and the smoke turbulence equipment of the absorption cavity comprises a partition board which divides the absorption cavity into an upper cavity and a lower cavity and a central column which vertically penetrates through the whole absorption cavity; each cavity of the absorption cavity is communicated with the central column through a grid arranged on the central column, and the central column which vertically penetrates through the whole absorption cavity is of a hollow structure; the absorption liquid spraying equipment is arranged in each cavity; the flue gas after oxidation treatment of the oxidation cavity enters the absorption cavity from the cavity at the bottommost part of the absorption cavity;
the denitration tower body is provided with double circulating systems, namely an oxidizing liquid circulating system and an absorption liquid circulating system; the oxidizing liquid circulating system comprises an oxidizing liquid pool arranged in the oxidizing cavity and circulating equipment connected with the oxidizing liquid pool, the oxidizing liquid pool is used for collecting the oxidizing liquid after the flue gas in the oxidizing cavity is treated, and the circulating equipment is used for conveying the oxidizing liquid collected by the oxidizing liquid pool to oxidizing liquid spraying equipment for cyclic utilization; the absorption liquid absorption system comprises an absorption liquid pool arranged in the absorption cavity and circulating equipment connected with the absorption liquid pool, the absorption liquid pool is used for collecting absorption liquid after flue gas treatment in the absorption cavity, and the circulating equipment is used for conveying the absorption liquid collected by the absorption liquid pool to absorption liquid spraying equipment for cyclic utilization.
5. The flue gas oxidation denitration apparatus according to claim 2 or 4,
an oxidizing liquid spraying device is arranged at the top of the central column of the oxidation cavity, and the flue gas can be accelerated in the central column and can be further oxidized by the oxidizing liquid;
the top of the central column of the absorption cavity is provided with absorption liquid spraying equipment, and the flue gas can be further oxidized by the absorption liquid while being accelerated in the central column.
6. The flue gas oxidation denitration apparatus according to claim 2 or 4,
the radius of the oxidation cavity is 3-5 times of that of the central column of the oxidation cavity;
the radius of the absorption cavity is 3-5 times of the radius of the central column of the absorption cavity.
7. The flue gas oxidation denitration apparatus according to claim 2 or 4,
the aperture ratio of the grating on the central column of the absorption cavity is 50-75%;
the grid interval on the central column of the oxidation cavity is 0.05R-0.1R, and R is the radius of the central column of the oxidation cavity;
the grid interval on the central column of the absorption cavity is 0.05R-0.1R, and R is the radius of the central column of the absorption cavity.
8. The flue gas oxidation denitration apparatus according to claim 2 or 4,
the radius of the central column of the oxidation cavity is equal to that of the central column of the absorption cavity;
the radius of the oxidation cavity is equal to the radius of the absorption cavity.
9. The flue gas oxidation denitration apparatus according to claim 1 or 4,
the oxidizing liquid sprayed by the oxidizing liquid spraying equipment is NaClO2A solution;
the absorption liquid sprayed by the absorption liquid spraying equipment is alkaline solution.
10. The flue gas oxidation denitration apparatus according to claim 1 or 4,
the device further comprises a demister used for treating the flue gas treated by the absorption cavity; when the absorption cavity and the oxidation cavity are arranged in the same absorption tower, the demister is arranged between the absorption cavity and the flue gas outlet;
the device further comprises NOx concentration detection equipment and flue gas circulation treatment equipment, wherein the NOx concentration detection equipment is used for detecting the NOx concentration in the flue gas after oxidation and denitration treatment, and the flue gas circulation treatment equipment is used for introducing the flue gas with unqualified NOx concentration check into the oxidation cavity to carry out flue gas oxidation and denitration treatment again.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201922085325.5U CN211706408U (en) | 2019-11-28 | 2019-11-28 | Flue gas oxidation denitration device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201922085325.5U CN211706408U (en) | 2019-11-28 | 2019-11-28 | Flue gas oxidation denitration device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN211706408U true CN211706408U (en) | 2020-10-20 |
Family
ID=72816017
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201922085325.5U Active CN211706408U (en) | 2019-11-28 | 2019-11-28 | Flue gas oxidation denitration device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN211706408U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112844013A (en) * | 2019-11-28 | 2021-05-28 | 中冶京诚工程技术有限公司 | Flue gas oxidation denitration device and method |
-
2019
- 2019-11-28 CN CN201922085325.5U patent/CN211706408U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112844013A (en) * | 2019-11-28 | 2021-05-28 | 中冶京诚工程技术有限公司 | Flue gas oxidation denitration device and method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| EP3401004A1 (en) | Method for controlling aerosol production during sulfur dioxide absorption with ammonium salts in flue gas desulfurization | |
| CN103801176B (en) | A kind of ozone oxidation is in conjunction with the flue-gas denitration process of spraying cooling and device | |
| CN101279185B (en) | Gas phase oxidation-liquid phase reduction method for absorbing and removing nitrous oxides in exhaust air | |
| CN104801178B (en) | Method for simultaneously desulfurizing, denitrifying and removing mercury by combining radical pre-oxidation with wet absorption | |
| CN1843575B (en) | Method and apparatus for optic catalytic oxidizing, desulfurizing and denitrifying flue gas simultaneously | |
| CN104785081B (en) | Desulfurization, denitrification and demercuration method by combining ozone with light radiation peroxide | |
| CN106693641A (en) | System integrating with waste heat recovery, dedusting, deodorization, desulfurization, denitration and white smoke removing and treating method of system | |
| CN105327612A (en) | Flue gas low-temperature combined desulfurization and denitration technology method | |
| CN103752151A (en) | Technology for flue gas denitration by magnesium sulfite | |
| CN103977681A (en) | Denitration method for high-concentration nitric oxide flue gas | |
| CN112058053A (en) | Flue gas wet denitration device and method | |
| CN107715666B (en) | Method and system for removing hydrogen sulfide by microwave activation persulfate spray induction of free radicals | |
| CN203123795U (en) | Flue gas denitration device using ozone oxidation method | |
| CN104492257A (en) | Comprehensive smoke treatment system | |
| CN211706408U (en) | Flue gas oxidation denitration device | |
| CN206911092U (en) | A kind of high-efficiency desulfurization denitrating system using ozone oxidation | |
| CN105311947A (en) | Boiler fume denitration and desulfuration dedusting device and process | |
| CN111036075A (en) | Method for treating high-concentration nitrogen oxide flue gas | |
| CN106853329B (en) | Method and device for generating hydroxyl free radical by ozone for low-temperature flue gas denitration | |
| CN106178725A (en) | The desulphurization denitration dust collecting process of a kind of glass kiln and device | |
| CN112844395B (en) | Oxidative denitration catalyst and flue gas catalytic oxidation denitration method and device | |
| CN104815538B (en) | Up-down opposite spraying fluidized bed desulfurization and denitrification method for photolysis of peroxide | |
| CN112844013A (en) | Flue gas oxidation denitration device and method | |
| CN111111401A (en) | Harmless and efficient treatment method for nitrogen oxides in industrial waste gas | |
| CN202845023U (en) | Heat treatment regeneration device of SCR (Selective Catalytic Reduction) denitration catalyst |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |