CN107051199A - A kind of efficient SCR denitration system ammoniacal liquor ammonia system - Google Patents
A kind of efficient SCR denitration system ammoniacal liquor ammonia system Download PDFInfo
- Publication number
- CN107051199A CN107051199A CN201611236976.4A CN201611236976A CN107051199A CN 107051199 A CN107051199 A CN 107051199A CN 201611236976 A CN201611236976 A CN 201611236976A CN 107051199 A CN107051199 A CN 107051199A
- Authority
- CN
- China
- Prior art keywords
- ammonia
- ammoniacal liquor
- scr denitration
- flue gas
- efficient scr
- 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
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 title claims abstract description 129
- 229910021529 ammonia Inorganic materials 0.000 title claims abstract description 50
- 235000011114 ammonium hydroxide Nutrition 0.000 title claims abstract description 34
- 239000003546 flue gas Substances 0.000 claims abstract description 45
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 44
- 239000006200 vaporizer Substances 0.000 claims abstract description 21
- 239000003638 chemical reducing agent Substances 0.000 claims abstract description 17
- 238000010790 dilution Methods 0.000 claims abstract description 17
- 239000012895 dilution Substances 0.000 claims abstract description 17
- 238000005507 spraying Methods 0.000 claims abstract description 15
- 239000003054 catalyst Substances 0.000 claims description 40
- 239000007789 gas Substances 0.000 claims description 19
- 239000003085 diluting agent Substances 0.000 claims description 8
- 239000007788 liquid Substances 0.000 claims description 8
- 230000003068 static effect Effects 0.000 claims description 5
- 239000007921 spray Substances 0.000 claims description 4
- 235000019504 cigarettes Nutrition 0.000 claims description 3
- 238000002156 mixing Methods 0.000 claims description 3
- 238000009834 vaporization Methods 0.000 claims description 3
- 230000008016 vaporization Effects 0.000 claims description 3
- 238000006555 catalytic reaction Methods 0.000 claims 1
- 239000007800 oxidant agent Substances 0.000 claims 1
- 230000001590 oxidative effect Effects 0.000 claims 1
- 238000005265 energy consumption Methods 0.000 abstract description 3
- 238000010438 heat treatment Methods 0.000 abstract description 3
- 230000009466 transformation Effects 0.000 abstract description 3
- 239000003517 fume Substances 0.000 abstract description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 2
- 239000012159 carrier gas Substances 0.000 abstract 1
- 230000008676 import Effects 0.000 abstract 1
- 229910000069 nitrogen hydride Inorganic materials 0.000 description 9
- 238000005516 engineering process Methods 0.000 description 7
- 238000002360 preparation method Methods 0.000 description 7
- 238000006243 chemical reaction Methods 0.000 description 6
- 238000006722 reduction reaction Methods 0.000 description 6
- 230000009467 reduction Effects 0.000 description 5
- 239000003795 chemical substances by application Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- BIGPRXCJEDHCLP-UHFFFAOYSA-N ammonium bisulfate Chemical compound [NH4+].OS([O-])(=O)=O BIGPRXCJEDHCLP-UHFFFAOYSA-N 0.000 description 2
- 238000000889 atomisation Methods 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 230000008021 deposition Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 238000011144 upstream manufacturing Methods 0.000 description 2
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 1
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 239000004202 carbamide Substances 0.000 description 1
- 238000010531 catalytic reduction reaction Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 150000001875 compounds Chemical group 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000002779 inactivation Effects 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 230000035800 maturation Effects 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 239000012453 solvate Substances 0.000 description 1
- 235000015096 spirit Nutrition 0.000 description 1
- 239000013589 supplement 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
- B01D53/90—Injecting reactants
-
- 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
- B01D2251/00—Reactants
- B01D2251/20—Reductants
- B01D2251/206—Ammonium compounds
- B01D2251/2062—Ammonia
-
- 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
Abstract
The present invention proposes a kind of efficient SCR denitration system ammoniacal liquor ammonia system, including dilution air, ammoniacal liquor transfer pump, metering device, flue gas heat-exchange unit, atomising device, vaporizer, steam-water separator, swirl-flow devices, ammonia-spraying grid and tank used for storing ammonia, dilution air is connected with flue gas heat-exchange unit influent header, carrier gas after heating is connected with vaporizer, the entrance of ammoniacal liquor transfer pump is connected with tank used for storing ammonia, outlet is connected with atomising device, chamber outputs are connected with ammonia-spraying grid, steam-water separator import, outlet respectively with chamber outputs, ammonia-spraying grid entrance is connected, swirl-flow devices are arranged at chamber input.Fume afterheat is utilized, SO2/SO3 transformation rules, denitration rule are fully combined, while energy consumption prepared by reducing agent is reduced, reduce SO3, the generation of the escaping of ammonia, efficiently solve the problem of existing influence unit safety, reliable, economical operation.
Description
Technical field
The present invention relates to a kind of SCR flue gas denitrification systems reducing agent preparation system, particularly a kind of efficient SCR denitration system
Ammoniacal liquor ammonia system.
Background technology
SCR (Selective Catalytic Reduction, SCR) gas denitrifying technology is because of its denitration
Efficiency high, technology maturation, it has also become the one preferred technique of Large-scale fire-electricity unit denitration.Its technical principle is that reduction is sprayed into flue gas
Agent NH3, harmless N2 and H2O is generated under catalyst action with the NOx reactions in flue gas.SCR gas denitrifying technologies engineering should
One of key is the preparation of reducing agent, and the reducing agent of present domestic and international application mainly has liquefied ammonia, ammoniacal liquor, three kinds of urea, but
No matter the ammonia which kind of reducing agent is required to exist using outside heat by liquid or with other compound forms changes into ammonia, such as
What reduces hot issue of this portion of energy consumption as reducing agent Study on Preparation.
Catalyst has certain scope and requirement to running temperature in coal unit SCR denitration system, and cigarette temperature is less than minimum
Continuous running temperature (MOT) can cause NH4HSO4 generations and blocking catalyst internal-response micropore, cause catalyst inactivation.Cause
This, in actual denitration operation, in order to ensure the activity of catalyst, denitrification apparatus should operate in minimum continuous operation steadily in the long term
It is more than cigarette temperature；However, current country's unit generally existing rate of load condensate is low, denitrification apparatus entrance flue gas temperature is low, underrun
Under operating mode denitrification apparatus put into operation problem also more protrude.
Existing technology such as Chinese patent bulletin CN104548933A provides one kind and substitutes outside heat using fume afterheat
Source prepares the technique and device of ammonia to solve the above problems by ammoniacal liquor.Although the technique reduce the energy of ammonia preparation process
Consumption, but due to its flue gas heat using SCR first floor catalyst top, when can further reduce the operation of boiler at low load operating mode
The flue-gas temperature of SCR equipment for denitrifying flue gas first floor catalyst inlets, adds denitrating flue gas denitrification apparatus less than minimum continuous fortune
The risk of trip temperature.
Numerous studies think that minimum continuous running temperature mainly has with the NH3 concentration in inlet flue gas condition and SO3 concentration
Close, raised with the increase of SO3 and NH3 concentration, but because most NH3 is consumed after first floor catalyst, for
The second layer and with rear catalyst for, required minimum continuous running temperature is significantly reduced, the appropriate reduction second layer and with
Layer catalyst inlet flue-gas temperature will not influence on the generation that denitrification apparatus full load is run afterwards.Other SCR equipment for denitrifying flue gas
Middle SO2/SO3 conversion is mainly influenceed by reaction temperature and NH3 concentration, and flue-gas temperature is higher, and SO2/SO3 conversion ratio is got over
It is high；NH3 concentration is higher, and SO2/SO3 conversion ratio is lower.For SCR flue gas denitrification systems, due to first floor catalyst inlet NH3
Concentration is higher, and the SO2/SO3 of generation conversion is few, but the NH3 concentration of the second layer and catalyst below is relatively low, is that SO2/SO3 turns
The main generation area changed, if flue-gas temperature of the SCR equipment for denitrifying flue gas after first floor catalyst can be controlled rationally, for
Reduction SO3 generation has important influence.
Therefore, how SCR multi-layer catalyst SO2/SO3 transformation rules and denitration rule are correctly utilized, by reduction SO3 lifes
Joined together into, the preparation that reduces the escaping of ammonia and reducing agent, while ammonia cost processed is reduced, further alleviation SCR downstreams are set
Standby ABS phenomenons, a new focus as reducing agent preparation field research.
The content of the invention
The to be solved of the present invention is that reducing agent needs to change using outside heat by liquid or with other in the prior art
The problem of ammonia that solvate form is present changes into ammonia, while being advised using SCR multi-layer catalyst SO2/SO3 transformation rules and denitration
Rule, the preparation for reducing SO3 generations, reduction the escaping of ammonia and reducing agent is joined together, while ammonia cost processed is reduced, further
Alleviate SCR upstream device ABS phenomenons.
The present invention includes：
The ammonia-gas spraying device that is set gradually along flue gas direction of advance, at least include first layer catalyst and second layer catalyst
Catalyst layer；And
Dilution air, flue gas heat-exchange unit, vaporizer, institute that pipeline connection is set are passed sequentially through along diluent gas direction of advance
Flue gas heat-exchange unit is stated to be arranged between first layer catalyst and second layer catalyst；And
Tank used for storing ammonia, the atomising device set gradually along ammonia spirit direction of advance, the atomising device and vaporizer lead to
Piping is connected, and the vaporizer and ammonia-gas spraying device are connected by pipeline.
The present invention increases one or more levels between SCR equipment for denitrifying flue gas first layer catalyst and second layer catalyst
Flue gas heat-exchange unit, reduces 20-50 DEG C by second layer catalyst inlet temperature, not only reduces SO3's from SO3 formation mechanism angles
Growing amount, and do not influence equipment for denitrifying flue gas full load to put into operation.In addition, newly-increased flue gas heat-exchange unit can optimize first layer and urge
Flow field between agent and second layer catalyst, is further ensured that the Effec-tive Function of SCR equipment for denitrifying flue gas, reduces the escaping of ammonia
Amount, reduces deposition of the hydrogen sulfate ammonia on the upstream device surface of SCR equipment for denitrifying flue gas, alleviates the risk blocked.Flue gas is released
Heat be used for heating cold air, air after heating is used to prepare reducing agent NH3.
Further, the flue gas heat-exchange unit is pipe heat exchanger.
Further, the vaporizer is provided with swirl-flow devices.Swirl-flow devices be used to solving flow field is uneven and the temperature that causes
Degree is uneven, improves evaporation efficiency, is arranged in the porch of vaporizer；
Further, vapour liquid separator is set before the ammonia-gas spraying device.Vapour liquid separator is used to reduce in mixed gas
Moisture content, be arranged on the confession ammonia pipeline between vaporizer and ammonia-gas spraying device；
Further, be additionally provided between the tank used for storing ammonia and vaporizer filter, ammoniacal liquor transfer pump, metering device,
Reducing agent pressure-regulating valve, dilution gas pressures control valve is additionally provided between the dilution air and flue gas heat-exchange unit.
Further, the flue gas heat-exchange unit heats diluent gas to more than 260 DEG C.
Further, the mass concentration of ammoniacal liquor is 20-30% in the tank used for storing ammonia.
Further, it is additionally provided with static mixing device between ammonia-gas spraying device and the first layer catalyst.
Further, the dilution air is composed in parallel by Liang Tai.
Further, the ammoniacal liquor transfer pump is composed in parallel by Liang Tai.
The present invention compared with the existing technology has advantages below and effect：
1st, it is rational in infrastructure, install and easy to implement.
2nd, substantially reduce enterprise's reducing agent and prepare energy consumption.
3rd, the generation of SO3 and the escaping of ammonia is effectively reduced.
4th, ABS deposition problems are effectively alleviated.
Brief description of the drawings
In order to illustrate more clearly about the embodiment of the present invention or technical scheme of the prior art, below will be to embodiment or existing
There is the accompanying drawing used required in technology description to be briefly described, it should be apparent that, drawings in the following description are only this
Some embodiments of invention, for those of ordinary skill in the art, without having to pay creative labor, may be used also
To obtain other accompanying drawings according to these accompanying drawings.
A kind of efficient SCR denitration system ammoniacal liquor ammonia system schematic diagram of Fig. 1 present invention.
Mark explanation：
1- ammonia-gas spraying device 2- static mixer 3- first layer catalyst 4- flue gas heat-exchange units
5- second layer catalyst 6- dilution gas pressures control valve 7- atomising devices
8- reducing agent pressure-regulating valve 9- metering device 10- ammoniacal liquor transfer pump 11- filters
12- tank used for storing ammonia 13- swirl-flow devices 14- vaporizer 15- dilution airs
16- vapour liquid separators.
Embodiment
This patent is described in detail with reference to specific embodiment：
Embodiment 1：With reference to Fig. 1, the present embodiment ammonia-gas spraying device 1, catalyst layer, catalyst layer at least includes first layer and is catalyzed
Agent 3 and second layer catalyst 5, it is possibility to have three layers and more than three layers catalyst；The present embodiment also includes dilution air 15, flue gas
Heat exchanger 4, vaporizer 14, flue gas heat-exchange unit 4 are arranged between first layer catalyst 3 and second layer catalyst 5, diluent gas warp
Cross dilution air 15 and arrive vaporizer 14 again to flue gas heat-exchange unit 4, the present embodiment also includes tank used for storing ammonia 12, atomising device 7, atomization
Device 7 and vaporizer 14 are connected, and the ammoniacal liquor that storage tank 12 comes out sprays into vaporizer 14 after being atomized through atomising device 7.
Embodiment 2：In the present embodiment, flue gas heat-exchange unit 4 is pipe heat exchanger.
Embodiment 3：With reference to Fig. 1, in the present embodiment, the porch of vaporizer 14 is provided with swirl-flow devices 13.
Embodiment 4：With reference to Fig. 1, in the present embodiment, vapour liquid separator 16 is set before ammonia-gas spraying device 1.
Embodiment 5：With reference to Fig. 1, in the present embodiment, be additionally provided between tank used for storing ammonia 12 and vaporizer 14 filter 11,
Ammoniacal liquor transfer pump 10, metering device 9, reducing agent pressure-regulating valve 8, are additionally provided with dilute between dilution air 15 and flue gas heat-exchange unit 4
Release gas-pressure controlling valve 6.
Embodiment 6：In the present embodiment, flue gas heat-exchange unit 4 heats diluent gas to more than 260 DEG C.
Embodiment 7：In the present embodiment, the mass concentration of ammoniacal liquor is 20-30% in tank used for storing ammonia.
Embodiment 8：With reference to Fig. 1, in the present embodiment, static mixing is additionally provided between ammonia-gas spraying device 1 and first layer catalyst 3
Device 2.
Embodiment 9：With reference to Fig. 1, in the present embodiment, dilution air 15 is composed in parallel by Liang Tai.
Embodiment 10：With reference to Fig. 1, in the present embodiment, ammoniacal liquor transfer pump 10 is composed in parallel by Liang Tai.
The present invention enough diluent gas are provided by dilution air 15, by the ammonia after vaporization be diluted to volumetric concentration 5% with
Under, diluent gas enters flue gas heat-exchange unit 4, and heat exchange is carried out with high-temperature flue gas, is heated to the temperature of vaporization ammonia spirit enough
Spend (more than 260 DEG C), the boil-off gas as evaporation ammoniacal liquor；Mass concentration passes through for 20%-30% ammonia spirits in tank used for storing ammonia 12
Filter 11 is crossed, atomising device 7 is sent into by ammoniacal liquor transfer pump 10, metering device 9, reducing agent pressure-regulating valve 8, after atomization
Ammonia spirit spray into vaporizer 14 in, be sufficiently mixed, vaporize by swirl-flow devices 13 and boil-off gas, formation ammonia mass concentration
The mixed gas of 5% ammonia, air and vapor, mixed gas enters spray after vapour liquid separator 16 is further removed water
Ammonia device 1, is injected in flue gas, and catalyst is carried out after static mixer 2, carries out reduction reaction.
Furthermore, it is necessary to explanation, the specific embodiment described in this specification, is named the shape of its parts and components
Title etc. can be different.The equivalent or simple change that all construction, feature and principles according to described in inventional idea of the present invention are done, is wrapped
Include in the protection domain of patent of the present invention.Those skilled in the art can be to described specific implementation
Example is made various modifications or supplement or substituted using similar mode, structure without departing from the present invention or surmounts this
Scope as defined in the claims, all should belong to protection scope of the present invention.
Claims (10)
1. a kind of efficient SCR denitration system ammoniacal liquor ammonia system, it is characterised in that including：
The ammonia-gas spraying device that is set gradually along flue gas direction of advance, at least include the catalysis of first layer catalyst and second layer catalyst
Oxidant layer；And
Dilution air, flue gas heat-exchange unit, vaporizer, the cigarette that pipeline connection is set are passed sequentially through along diluent gas direction of advance
Gas heat exchanger is arranged between first layer catalyst and second layer catalyst；And
Tank used for storing ammonia, the atomising device set gradually along ammonia spirit direction of advance, the atomising device and vaporizer pass through pipe
Road is connected, and the vaporizer and ammonia-gas spraying device are connected by pipeline.
2. a kind of efficient SCR denitration system ammoniacal liquor ammonia system according to claim 1, it is characterised in that the flue gas
Heat exchanger is pipe heat exchanger.
3. a kind of efficient SCR denitration system ammoniacal liquor ammonia system according to claim 1, it is characterised in that the vaporization
Swirl-flow devices are provided with chamber inlet.
4. a kind of efficient SCR denitration system ammoniacal liquor ammonia system according to claim 1, it is characterised in that the spray ammonia
Vapour liquid separator is set before device.
5. a kind of efficient SCR denitration system ammoniacal liquor ammonia system according to claim 1, it is characterised in that the ammoniacal liquor
Filter, ammoniacal liquor transfer pump, metering device, reducing agent pressure-regulating valve, the dilution are additionally provided between storage tank and vaporizer
Dilution gas pressures control valve is additionally provided between blower fan and flue gas heat-exchange unit.
6. a kind of efficient SCR denitration system ammoniacal liquor ammonia system according to claim 1, it is characterised in that the flue gas
Heat exchanger heats diluent gas to more than 260 DEG C.
7. a kind of efficient SCR denitration system ammoniacal liquor ammonia system according to claim 1, it is characterised in that the ammoniacal liquor
The mass concentration of ammoniacal liquor is 20-30% in storage tank.
8. a kind of efficient SCR denitration system ammoniacal liquor ammonia system according to claim any one of 1-7, it is characterised in that
Static mixing device is additionally provided between ammonia-gas spraying device and the first layer catalyst.
9. a kind of efficient SCR denitration system ammoniacal liquor ammonia system according to claim any one of 1-7, it is characterised in that
The dilution air is composed in parallel by Liang Tai.
10. a kind of efficient SCR denitration system ammoniacal liquor ammonia system according to claim 5, it is characterised in that the ammoniacal liquor
Transfer pump is composed in parallel by Liang Tai.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611236976.4A CN107051199A (en) | 2016-12-28 | 2016-12-28 | A kind of efficient SCR denitration system ammoniacal liquor ammonia system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611236976.4A CN107051199A (en) | 2016-12-28 | 2016-12-28 | A kind of efficient SCR denitration system ammoniacal liquor ammonia system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107051199A true CN107051199A (en) | 2017-08-18 |
Family
ID=59624301
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201611236976.4A Pending CN107051199A (en) | 2016-12-28 | 2016-12-28 | A kind of efficient SCR denitration system ammoniacal liquor ammonia system |
Country Status (1)
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| CN (1) | CN107051199A (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107894003A (en) * | 2017-09-30 | 2018-04-10 | 北京中电联环保股份有限公司 | Application of the gas-gas heat exchanger in SCR denitration mixed flow system |
| CN108069440A (en) * | 2018-01-23 | 2018-05-25 | 华北电力大学（保定） | A kind of ammonium hydrogen sulfate reaction generating means based on high temperature process furnances |
| CN109764695A (en) * | 2018-12-18 | 2019-05-17 | 西安交通大学 | A kind of condensing heat exchanger and method for gas fired-boiler denitrating flue gas |
| CN110064287A (en) * | 2019-04-12 | 2019-07-30 | 华电电力科学研究院有限公司 | It is a kind of using spray gun cooling water as the SNCR device and its working method of dilution water |
| CN111229037A (en) * | 2020-03-16 | 2020-06-05 | 西安西热锅炉环保工程有限公司 | Denitration device and method for gas-steam combined cycle unit by using ammonia water as reducing agent |
| CN112240560A (en) * | 2019-07-30 | 2021-01-19 | 青岛诺瑞尔节能环保科技有限公司 | Energy-saving SNCR (selective non-catalytic reduction) denitration device and denitration method |
| WO2021046880A1 (en) * | 2019-09-11 | 2021-03-18 | 唐山维数科技有限公司 | Flue gas denitrification system |
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| US20050118084A1 (en) * | 2003-12-02 | 2005-06-02 | J. Edward Cichanowicz | Multi-stage heat absorbing reactor and process for SCR of NOx and for oxidation of elemental mercury |
| CN104548933A (en) * | 2015-01-14 | 2015-04-29 | 福建紫荆环境工程技术有限公司 | Ammonia water ammonia production reducing agent supply device and method for SCR denitration |
| CN106178950A (en) * | 2016-08-25 | 2016-12-07 | 华电电力科学研究院 | A kind of low SO2/ SO3the SCR denitration system of conversion ratio |
| CN206535430U (en) * | 2016-12-28 | 2017-10-03 | 华电电力科学研究院 | A kind of efficient SCR denitration system ammoniacal liquor ammonia system |
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| US20050118084A1 (en) * | 2003-12-02 | 2005-06-02 | J. Edward Cichanowicz | Multi-stage heat absorbing reactor and process for SCR of NOx and for oxidation of elemental mercury |
| CN104548933A (en) * | 2015-01-14 | 2015-04-29 | 福建紫荆环境工程技术有限公司 | Ammonia water ammonia production reducing agent supply device and method for SCR denitration |
| CN106178950A (en) * | 2016-08-25 | 2016-12-07 | 华电电力科学研究院 | A kind of low SO2/ SO3the SCR denitration system of conversion ratio |
| CN206535430U (en) * | 2016-12-28 | 2017-10-03 | 华电电力科学研究院 | A kind of efficient SCR denitration system ammoniacal liquor ammonia system |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107894003A (en) * | 2017-09-30 | 2018-04-10 | 北京中电联环保股份有限公司 | Application of the gas-gas heat exchanger in SCR denitration mixed flow system |
| CN108069440A (en) * | 2018-01-23 | 2018-05-25 | 华北电力大学（保定） | A kind of ammonium hydrogen sulfate reaction generating means based on high temperature process furnances |
| CN109764695A (en) * | 2018-12-18 | 2019-05-17 | 西安交通大学 | A kind of condensing heat exchanger and method for gas fired-boiler denitrating flue gas |
| CN109764695B (en) * | 2018-12-18 | 2021-01-19 | 西安交通大学 | Condensing heat exchanger and method for denitration of flue gas of gas-fired boiler |
| CN110064287A (en) * | 2019-04-12 | 2019-07-30 | 华电电力科学研究院有限公司 | It is a kind of using spray gun cooling water as the SNCR device and its working method of dilution water |
| CN110064287B (en) * | 2019-04-12 | 2023-07-11 | 华电电力科学研究院有限公司 | SNCR device using spray gun cooling water as dilution water and working method thereof |
| CN112240560A (en) * | 2019-07-30 | 2021-01-19 | 青岛诺瑞尔节能环保科技有限公司 | Energy-saving SNCR (selective non-catalytic reduction) denitration device and denitration method |
| WO2021046880A1 (en) * | 2019-09-11 | 2021-03-18 | 唐山维数科技有限公司 | Flue gas denitrification system |
| CN111229037A (en) * | 2020-03-16 | 2020-06-05 | 西安西热锅炉环保工程有限公司 | Denitration device and method for gas-steam combined cycle unit by using ammonia water as reducing agent |
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Application publication date: 20170818 |