CN107008143A - A kind of Novel SCR denitrating system of anti-gypsum rain - Google Patents
A kind of Novel SCR denitrating system of anti-gypsum rain Download PDFInfo
- Publication number
- CN107008143A CN107008143A CN201710346872.7A CN201710346872A CN107008143A CN 107008143 A CN107008143 A CN 107008143A CN 201710346872 A CN201710346872 A CN 201710346872A CN 107008143 A CN107008143 A CN 107008143A
- Authority
- CN
- China
- Prior art keywords
- heat
- heat exchanger
- flue gas
- rotary type
- absorbing end
- 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.)
- Pending
Links
- 229910052602 gypsum Inorganic materials 0.000 title claims abstract description 21
- 239000010440 gypsum Substances 0.000 title claims abstract description 21
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 40
- 239000003546 flue gas Substances 0.000 claims abstract description 40
- 230000003009 desulfurizing effect Effects 0.000 claims abstract description 23
- 239000007789 gas Substances 0.000 claims abstract description 10
- 235000019504 cigarettes Nutrition 0.000 claims abstract description 4
- 238000010438 heat treatment Methods 0.000 claims description 5
- 239000007788 liquid Substances 0.000 claims description 3
- 238000004064 recycling Methods 0.000 claims 1
- 239000003054 catalyst Substances 0.000 abstract description 11
- 238000006243 chemical reaction Methods 0.000 abstract description 5
- 239000000428 dust Substances 0.000 abstract description 3
- 230000000694 effects Effects 0.000 abstract description 3
- 150000003863 ammonium salts Chemical class 0.000 abstract 1
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 6
- 238000000034 method Methods 0.000 description 5
- 231100000572 poisoning Toxicity 0.000 description 5
- 230000000607 poisoning effect Effects 0.000 description 5
- 238000006477 desulfuration reaction Methods 0.000 description 4
- 230000023556 desulfurization Effects 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 230000009467 reduction Effects 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 229910001385 heavy metal Inorganic materials 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 230000000630 rising effect Effects 0.000 description 2
- 239000005864 Sulphur Substances 0.000 description 1
- 238000003916 acid precipitation Methods 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 239000006071 cream Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 231100001143 noxa Toxicity 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000012805 post-processing Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/86—Catalytic processes
- B01D53/8621—Removing nitrogen compounds
- B01D53/8625—Nitrogen oxides
- B01D53/8631—Processes characterised by a specific device
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/005—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by heat treatment
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/26—Drying gases or vapours
- B01D53/265—Drying gases or vapours by refrigeration (condensation)
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J15/00—Arrangements of devices for treating smoke or fumes
- F23J15/006—Layout of treatment plant
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J15/00—Arrangements of devices for treating smoke or fumes
- F23J15/02—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J15/00—Arrangements of devices for treating smoke or fumes
- F23J15/06—Arrangements of devices for treating smoke or fumes of coolers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J15/00—Arrangements of devices for treating smoke or fumes
- F23J15/08—Arrangements of devices for treating smoke or fumes of heaters
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/02—Other waste gases
- B01D2258/0283—Flue gases
-
- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/30—Technologies for a more efficient combustion or heat usage
Abstract
The invention discloses a kind of Novel SCR denitrating system of anti-gypsum rain, rotary type heat exchanger and heat-pipe heat exchanger are set between desulfurizing tower and SCR denitration system along tail flue gas flow, air preheater exiting flue gas is flowed through successively after deduster, desulfurizing tower, cooler, rotary type heat exchanger heat absorbing end, heat-pipe heat exchanger heat absorbing end, SCR reactors and rotary type heat exchanger release end of heat and empties.Extracting high-temperature stove cigarette sends into heat-pipe heat exchanger release end of heat out of stove, and circulation is melted down again after the flue gas heat release.The low-temperature flue gas come out from desulfurizing tower is heated through rotary type heat exchanger heat absorbing end and heat-pipe heat exchanger heat absorbing end reaches catalyst converter reaction temperature window.Compared with traditional SCR denitration technology, the present invention had both avoided the influence to catalyst such as flying dust, ammonium salt, it is ensured that the activity of catalyst, can control the exhaust gas temperature of flue gas by rotary type heat exchanger release end of heat again, eliminate " gypsum rain " problem.
Description
Technical field
The present invention relates to flue gas denitrification system, and in particular to a kind of Novel SCR denitrating system of anti-gypsum rain, belongs to boiler
Flue gas post-processing technology field.
Background technology
With the industrialized fast development of China, environmental problem turns into focus of concern.In recent years, nitrogen oxides
NOxAs cause atmosphere pollution, photochemical pollution, acid rain main contributor, its administer has become people concern and research
Focus.
The NO produced in current coal-burning power plant runningxIt is one of main source of nitrogen oxides.In December, 2015, state
The standing meeting of business institute is determined, minimum discharge is implemented in full to coal-burning power plant before the year two thousand twenty, by NOxConcentration of emission be limited to
50mg/m3Under.
At present, ammonia process SCR denitration technology is efficiency highest, technique the most ripe denitration technology, and it is at home and abroad obtained
It is widely applied.But SCR denitration technology exist in operation air preheater block, catalyst poisoning a series of problems, such as, because
This adverse effect for reducing or eliminating SCR device turns into the task of top priority.
At the same time, the gypsum rain problem that desulphurization system is brought also has obtained the extensive concern of people.As gas-gas exchanges heat
Device（Gas-gas Heater, abbreviation GGH）Cancellation, exhaust gas temperature is greatly reduced, and the row of entraining liquid pollutant easily occurs
Put, cause in the case of normal weather, decline droplet (i.e. " gypsum rain " problem) often occurs in chimney near zone, give common people's life
Living to bring very big influence, " gypsum rain " problem of solution is also extremely urgent.
The content of the invention
In order to overcome " gypsum rain " problem that background technology is present, the invention provides a kind of Novel SCR of anti-gypsum rain
Denitrating system.Its technical scheme is as follows：
To solve the above problems, a kind of Novel SCR denitrating system of anti-gypsum rain of the present invention, i.e., along tail flue gas flow de-
Rotary type heat exchanger and heat-pipe heat exchanger are set between sulphur tower and SCR denitration system, make the flue gas that air preheater is exported according to
It is secondary flow through deduster, desulfurizing tower, cooler, rotary type heat exchanger heat absorbing end, heat-pipe heat exchanger heat absorbing end, SCR reactors and
Emptying after rotary type heat exchanger release end of heat (" heat absorbing end " and " release end of heat " is defined from flue gas angle in the present invention).Taken out out of stove
High-temperature flue gas is taken to melt down circulation again after sending into heat-pipe heat exchanger release end of heat, flue gas release heat.From desulfurizing tower come out it is low
Warm flue gas reaches catalyst converter reaction temperature window through rotary type heat exchanger heat absorbing end and the heating of heat-pipe heat exchanger heat absorbing end.
Further, cooler is installed additional in desulfurizing tower outlet, condensate liquid is directed into desulfurizing tower by circulating pump and reused.
Further, along along flue gas stroke, the SCR reactors are arranged in after desulfurizing tower, and particular location is in revolution
After formula heat exchanger heat absorbing end and heat-pipe heat exchanger heat absorbing end, before rotary type heat exchanger release end of heat.
Further, heat-pipe heat exchanger release end of heat import flue gas is quoted from boiler high temperature area, this high-temperature flue gas release heat
It is discharged into again via the outlet of heat-pipe heat exchanger release end of heat to boiler high temperature area afterwards and carries out flue gas recirculation.
Further, the low-temperature flue gas of cooler outlet, first absorbs SCR reactors by means of rotary type heat exchanger heat absorbing end
The heat of exiting flue gas, realizes that primary heating controls exhaust gas temperature simultaneously；Absorb high by means of heat-pipe heat exchanger heat absorbing end again
The heat of warm stove cigarette, realization is heated again, so as to reach the temperature window of SCR reactors.
The present invention uses such scheme, and SCR denitration system is placed in after desulphurization system, need not introduce external heat source
In the case of, by rotary type heat exchanger and heat-pipe heat exchanger by flue gas to SCR denitration reaction temperature window.
Pass through the processes such as dedusting, desulfurization, therefore dust, SO due to entering the flue gas of SCR reactors2, heavy metal ion content significantly
Reduction, a series of problems, such as effectively prevent air preheater blocking, the catalyst poisoning that traditional SCR denitration system is present.
The present invention is equipped with cooler after desulfurizing tower simultaneously, when flue gas enters cooler, saturation cigarette after desulfurizing tower desulfurization
Water vapor condensation in gas, condensed water is squeezed into desulfurizing tower by circulating pump again and recycled again, and this measure can both disappear from source
Except " gypsum rain " problem, the effect of water saving is can reach again.And exhaust gas temperature can be controlled by rotary type heat exchanger, Ke Yishi
When reduction heat exchange amount, exhaust gas temperature is improved, the rising height of flue gas is improved, the shadow of " gypsum rain " to environment is technically reduced
Ring.
Brief description of the drawings
Fig. 1 is a kind of Novel SCR denitrating system structural representation of anti-gypsum rain of the present invention：1- boilers；2- dedusters；
3- desulfurizing towers；4- coolers；5- rotary type heat exchanger heat absorbing ends；6- rotary type heat exchanger release end of heat；7- heat-pipe heat exchangers are inhaled
Hot junction；8- heat-pipe heat exchanger release end of heat；9-SCR reactors；10- chimneys.
Fig. 2 is traditional SCR denitration system schematic diagram：11- boilers；12-SCR reactors；13- dedusters；14- desulfurizing towers；
15- chimneys.
Embodiment
The invention will be further described below in conjunction with the accompanying drawings.
Such as Fig. 1 institutes, the Novel SCR denitrating system of anti-gypsum rain of the invention, including boiler 1, deduster 2, desulfurizing tower 3,
Cooler 4, rotary type heat exchanger heat absorbing end 5, heat-pipe heat exchanger heat absorbing end 7, SCR reactors 9, rotary type heat exchanger release end of heat
6th, chimney 10.The inlet flue gas of heat-pipe heat exchanger heat absorbing end 7 comes from the high-temperature region of boiler 1, and exiting flue gas is discharged into the high temperature of boiler 1
Area.
Maximum innovation of the invention is SCR denitration system being placed in after desulphurization system, by means of in desulfurization system
Rotary type heat exchanger and heat-pipe heat exchanger are set between system and SCR denitration system, and realization is not introducing the condition of external heat source
It is issued to the phenomenon of preventing and treating " gypsum rain ".In addition, for traditional SCR denitration technology（As shown in Figure 2）Exist air preheater block,
A series of problems, such as catalyst poisoning, the present invention moves to SCR denitration system after deduster 2 and desulfurizing tower 3, and flue gas is through removing
The flue gas discharged after the processes such as dirt, desulfurization is neat stress, and now dust content, sulfur content, heavy metal ion content etc. be significantly
Reduction, effectively prevent catalyst poisoning problem.
The Suitable ranges of high temperature SCR process catalysts are 260-380 DEG C, to enable low-temperature flue gas to reach catalyst
Reaction temperature window, through rotary type heat exchanger heat absorbing end 5 and heat-pipe heat exchanger heat absorbing end 7 after the exiting flue gas elder generation of cooler 4
Heated.The heat of rotary type heat exchanger heat absorbing end 5 is exchanged heat by the exiting flue gas of SCR reactors 9 and provided.Heat-pipe heat exchanger is inhaled
The heat in hot junction 7 is provided by heat-pipe heat exchanger release end of heat 8, high temperature of the heat from boiler 1 of heat-pipe heat exchanger release end of heat 8
Flue gas.
Low-temperature flue gas from cooler 4, first passes through rotary type heat exchanger heat absorbing end 5 and is heated to 280 DEG C or so, and after pass through
Overheat pipe heat exchanger heat absorbing end 7 is heated to 340 DEG C or so, reaches optimal reaction temperature.7 need of heat-pipe heat exchanger heat absorbing end
There is provided less, the stability of boiler 1 will not be produced and significantly affected.
The present invention after desulfurizing tower equipped with one group of cooler 4, its it is condensable go out saturated flue gas in vapor, after processing
The utilization of the interior circulation of desulfurizing tower 3 can be squeezed into by circulating pump.This measure both reduces " gypsum rain " from source, and the work of water saving is played again
With.
Meanwhile, the present invention in rotary type heat exchanger release end of heat 6 thermal discharge it is controllable, when need improve flue gas exhaust gas temperature
When, it is possible to decrease the thermal discharge of rotary type heat exchanger release end of heat 6, improves the rising height of flue gas, technically effectively prevent " stone
The generation of cream rain ".
In summary, the invention provides a kind of new SCR denitration system, can be prevented effectively from catalyst poisoning etc. one is
Row problem.Meanwhile, this SCR denitration system can control the thermal discharge of rotary type heat exchanger release end of heat 6 again, and smoke evacuation is improved to reach
The purpose of temperature, effectively eliminates " gypsum rain ".
Above description and the cardinal principle for explaining the present invention, essential characteristic and its advantage, it is impossible to which the present invention is limited with this
The scope of implementation.The principle and feature of the simply present invention described in description above, is not departing from spirit and scope of the invention
On the premise of, the present invention also has many changes and improvement, and these are all in protection domain.
Claims (3)
1. a kind of Novel SCR denitrating system of anti-gypsum rain, including deduster（2）, desulfurizing tower（3）, cooler（4）, its feature
It is：Along flue gas flow in desulfurizing tower（3）With SCR reactors（9）Between be provided with rotary type heat exchanger heat absorbing end（5）And heat pipe-type
Heat exchanger heat absorbing end（7）, air preheater outlet flue gas flow through deduster successively（2）, desulfurizing tower（3）, cooler（4）, return
Rotatable heat exchanger heat absorbing end（5）, heat-pipe heat exchanger heat absorbing end（7）, SCR reactors（9）With rotary type heat exchanger release end of heat（6）
After empty；Extracting high-temperature stove cigarette sends into heat-pipe heat exchanger release end of heat out of stove（8）；From desulfurizing tower（3）Low-temperature flue gas out
Through rotary type heat exchanger heat absorbing end（5）With heat-pipe heat exchanger heat absorbing end（7）Heating reaches SCR reactors（9）Temperature window.
2. a kind of Novel SCR denitrating system of anti-gypsum rain according to claim 1, it is characterised in that：In desulfurizing tower（3）
Outlet install the cooler additional（4）, condensate liquid is directed into desulfurizing tower by circulating pump（3）Recycling.
3. a kind of Novel SCR denitrating system of anti-gypsum rain according to claim 1, it is characterised in that：Cooler（4）Go out
The low-temperature flue gas of mouth is first by means of rotary type heat exchanger heat absorbing end（5）The heat for absorbing SCR reactor outlet flue gases realizes primary
Heating, while exhaust gas temperature is controlled, then by means of heat-pipe heat exchanger heat absorbing end（7）The heat for absorbing high-temperature flue gas is realized again
Heating, so as to reach SCR reactors（9）Temperature window.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710346872.7A CN107008143A (en) | 2017-05-17 | 2017-05-17 | A kind of Novel SCR denitrating system of anti-gypsum rain |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710346872.7A CN107008143A (en) | 2017-05-17 | 2017-05-17 | A kind of Novel SCR denitrating system of anti-gypsum rain |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107008143A true CN107008143A (en) | 2017-08-04 |
Family
ID=59450152
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710346872.7A Pending CN107008143A (en) | 2017-05-17 | 2017-05-17 | A kind of Novel SCR denitrating system of anti-gypsum rain |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107008143A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108568210A (en) * | 2018-04-11 | 2018-09-25 | 山东大学 | Cooperate with the flue gas reheat eliminating white smoke technique and method of CO low-temperature denitrations |
| CN111617610A (en) * | 2020-06-16 | 2020-09-04 | 潘帅 | Energy-saving environment-friendly low-noise desulfurization, denitrification and dust removal device and treatment method |
| US20210220772A1 (en) * | 2019-10-29 | 2021-07-22 | Huaneng Clean Energy Research Institute | Flue gas low-temperature adsorption denitrification method |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104174287A (en) * | 2014-08-06 | 2014-12-03 | 北京京诚泽宇能源环保工程技术有限公司 | Partial flue gas denitrification system and method for sintering machine |
| CN105056671A (en) * | 2015-07-22 | 2015-11-18 | 江苏新中金环保科技有限公司 | Desulfurating, dust-removing, demisting and water-saving process for wet-type desulfurization tower and apparatus thereof |
| CN105509491A (en) * | 2015-12-09 | 2016-04-20 | 郑琨 | Environmental-protection and energy-conservation treatment technology of sintering flue gas |
| CN105841176A (en) * | 2016-05-06 | 2016-08-10 | 山东岱荣节能环保科技有限公司 | Desulfurization and denitration clean exhausting device for low-temperature waste gas |
| WO2016208717A1 (en) * | 2015-06-24 | 2016-12-29 | 三菱日立パワーシステムズ株式会社 | Denitration device and denitration method |
-
2017
- 2017-05-17 CN CN201710346872.7A patent/CN107008143A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104174287A (en) * | 2014-08-06 | 2014-12-03 | 北京京诚泽宇能源环保工程技术有限公司 | Partial flue gas denitrification system and method for sintering machine |
| WO2016208717A1 (en) * | 2015-06-24 | 2016-12-29 | 三菱日立パワーシステムズ株式会社 | Denitration device and denitration method |
| CN105056671A (en) * | 2015-07-22 | 2015-11-18 | 江苏新中金环保科技有限公司 | Desulfurating, dust-removing, demisting and water-saving process for wet-type desulfurization tower and apparatus thereof |
| CN105509491A (en) * | 2015-12-09 | 2016-04-20 | 郑琨 | Environmental-protection and energy-conservation treatment technology of sintering flue gas |
| CN105841176A (en) * | 2016-05-06 | 2016-08-10 | 山东岱荣节能环保科技有限公司 | Desulfurization and denitration clean exhausting device for low-temperature waste gas |
Non-Patent Citations (1)
| Title |
|---|
| 岳涛等: "《工业锅炉大气污染控制技术与应用》", 中国环境出版社, pages: 307 * |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108568210A (en) * | 2018-04-11 | 2018-09-25 | 山东大学 | Cooperate with the flue gas reheat eliminating white smoke technique and method of CO low-temperature denitrations |
| CN108568210B (en) * | 2018-04-11 | 2021-02-09 | 山东大学 | Smoke reheating white smoke eliminating process and method for cooperating with CO low-temperature denitration |
| US20210220772A1 (en) * | 2019-10-29 | 2021-07-22 | Huaneng Clean Energy Research Institute | Flue gas low-temperature adsorption denitrification method |
| US11925898B2 (en) * | 2019-10-29 | 2024-03-12 | Huaneng Clean Energy Research Institute | Flue gas low-temperature adsorption denitrification method |
| CN111617610A (en) * | 2020-06-16 | 2020-09-04 | 潘帅 | Energy-saving environment-friendly low-noise desulfurization, denitrification and dust removal device and treatment method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105169942B (en) | Flue gas of glass melting furnace dust-removal and desulfurizing denitration coprocessing system and processing method and application | |
| CN103585867B (en) | A kind of flue gas desulfurization and denitration method and device | |
| CN205340542U (en) | Low low temperature dust removal SOx/NOx control system | |
| WO2016045172A1 (en) | Denitration and waste heat recovery integrated furnace | |
| CN104162352B (en) | A kind of glass furnace fume dedusting, denitration, desulfurization integrated handling process | |
| CN105771638A (en) | Desulfurization and denitrification method and device for hot sparing of coke oven chimney by using coke oven flue gas | |
| CN204952670U (en) | Glass melting furnace flue gas dust removal SOx/NOx control concurrent processing system | |
| WO2022033512A1 (en) | Near-zero emission type flue gas multi-pollutant integrated removal system and method | |
| CN107008143A (en) | A kind of Novel SCR denitrating system of anti-gypsum rain | |
| CN106705090A (en) | SCR system based on flue gas waste heat gradient utilization and SCR denitration method | |
| KR20150067292A (en) | Exhaust gas treatment system and method | |
| CN108568210B (en) | Smoke reheating white smoke eliminating process and method for cooperating with CO low-temperature denitration | |
| CN110180386A (en) | A kind of flue gas spiral diffusion denitrification apparatus and method of denitration | |
| CN109404958A (en) | A kind of energy efficiency anti-blocking method and system based on air preheater bypass flue | |
| CN109603546A (en) | Sintering flue gas desulfurization denitration dust collecting disappears white technological process for purifying | |
| CN102980198A (en) | Washing condensing smoke triple recovery device | |
| CN206823460U (en) | Carbon workshop system for desulfuration and denitration | |
| CN202942807U (en) | Water-washing condensing-type smoke triple-recovery device | |
| CN110772915A (en) | Sintering flue gas SCR denitration and whitening system and process | |
| CN209490656U (en) | It is a kind of to disappear white device for fire coal tail gas desulphurization denitration dedusting | |
| CN212575985U (en) | Ultralow emission treatment system for coke oven flue gas | |
| CN208302512U (en) | Cooperate with the flue gas reheat eliminating white smoke system of CO low-temperature denitration | |
| CN206837854U (en) | A kind of Novel SCR denitrating system of anti-gypsum rain | |
| CN107420927A (en) | A kind of fire coal boiler fume high-efficient purification and UTILIZATION OF VESIDUAL HEAT IN technique | |
| CN208583169U (en) | A kind of sintering flue gas desulfurization denitration, flue gas disappear white total system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| CB03 | Change of inventor or designer information | ||
| CB03 | Change of inventor or designer information |
Inventor after: Ling Zhongqian Inventor after: Ling Bo Inventor after: Zeng Xianyang Inventor after: Jiang Yingjun Inventor after: Ling Shijie Inventor after: Ling Shijun Inventor before: Ling Bo Inventor before: Ling Zhongqian Inventor before: Zeng Xianyang Inventor before: Jiang Yingjun Inventor before: Ling Shijie Inventor before: Ling Shijun |
|
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20170804 |