CN101592336A - A kind of fluidized-bed combustion boiler - Google Patents
A kind of fluidized-bed combustion boiler Download PDFInfo
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- CN101592336A CN101592336A CNA2009101005745A CN200910100574A CN101592336A CN 101592336 A CN101592336 A CN 101592336A CN A2009101005745 A CNA2009101005745 A CN A2009101005745A CN 200910100574 A CN200910100574 A CN 200910100574A CN 101592336 A CN101592336 A CN 101592336A
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- air
- flue gas
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- bed combustion
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Abstract
A kind of fluidized-bed combustion boiler, comprise fluidized bed combustion chamber, its bottom is provided with the air compartment of air distribution plate and is connected with air blast, the combustion product gases of combustion chamber is discharged from chimney through air-introduced machine, a flue gas recirculation pipe is connected in the air-introduced machine exit, it is connected with fluidized bed combustion chamber and air compartment respectively again, be provided with upper strata wind control valve between flue gas recirculation pipe and the fluidized bed combustion chamber, one upper strata blower fan is set between upper strata wind control valve and the combustion chamber, the aspiration channel that is connected a band air control valve between upper strata blower fan and the upper strata wind control valve, upper strata wind is mixed with flue gas by air and forms, air blast connects an air and flue gas mixing-chamber, the mixing chamber other end by cigarette again blower fan and cigarette again control valve be communicated with described flue gas recirculation pipe, this mixing chamber top is connected with air compartment again and constitutes a wind; Advantage of the present invention is can improve fuel availability and reduce pollutant emission, desulfuration efficiency is higher and has the advantage of using extensive coal fuel.
Description
Technical field
The present invention relates to a kind of technical field of boiler combustion device, especially relate to a kind of fluidized-bed combustion boiler with flue gas recirculation device.
Background technology
Existing fluidized-bed combustion boiler structure comprises that one is provided with the boiler body of fluidized bed combustion chamber, the bottom of this combustion chamber is provided with the air distribution plate of band blast cap, this blast cap is connected with the primary air flow air blast by air compartment, this air blast enters described combustion chamber with compressed air by described air compartment and blast cap, and the combustion product gases in the described boiler body causes chimney through deduster by air-introduced machine from described cyclone separator upper end again by the assembly that is heated and discharges.One side of this fluidized bed combustion chamber is communicated with a fuel tank.
Domestic middle-size and small-size fluidized-bed combustion boiler usually produces phenomenons such as the not enough and described air distribution plate leakage of described primary air flow slag because of component wear and the reduction of seal for pipe joints performance in running at present, causes the interior uncombusted thing second-time burning of the big feed back pipe with described cyclone separator of feed back amount again; And, numerous homemade middle-size and small-size fluidized-bed combustion boiler also exists desulfurization degree on the low side at present, these defectives have restricted inner mass transfer of existing fluidized-bed combustion boiler and heat-transfer effect, and furnace charge passes back into the function of burner hearth, thereby influence boiler output and economic benefit, pollute the excessive emissions of thing simultaneously.
Summary of the invention
Technical problem to be solved by this invention is the situation at prior art, provides a kind of and improves fuel availability and reduce pollutant emission and fluidized-bed combustion boiler that desulfuration efficiency is higher.
The present invention solves the problems of the technologies described above the technical scheme that is adopted: a kind of fluidized-bed combustion boiler, comprise that one is provided with the boiler body of fluidized bed combustion chamber, the bottom of this combustion chamber is provided with the air distribution plate of band blast cap, this blast cap is connected with an air blast by air compartment, this air blast enters described combustion chamber with compressed air by described air compartment and blast cap, combustion product gases in the described boiler body causes chimney through sack cleaner by air-introduced machine and discharges, it is characterized in that: a flue gas recirculation pipe is connected in described air-introduced machine exit, and this flue gas recirculation pipe is connected with described fluidized bed combustion chamber and described air compartment respectively; Be provided with devulcanizer between described cyclone separator and the described deduster.
Because the partial fume that adopts combustion process to produce inserts respectively in combustion chamber and the air compartment again, thereby realization is strengthened stove internal combustion effect and is not increased excess air; A part of flue gas recycled of while mixes with secondary wind sends into top, combustion chamber, with intensified response ability and realization air stage feeding; Exert oneself and desulfuration efficiency thereby improve fluidized-bed combustion boiler, and reduce pollutant emission.
Can be provided with upper strata wind smoke regulating valve between described flue gas recirculation pipe and the described fluidized bed combustion chamber.Upper strata wind control valve effect is to enter described flue gas recycled ratio in the described fluidized bed combustion chamber according to the load of boiler and regulating working conditions, and adding the flue gas recycled ratio in the wind of described upper strata is 0～100% scope.
Between described upper strata wind control valve and the described combustion chamber fluid bed upper strata blower fan can be set, this upper strata blower fan more helps upper strata wind is sent into the combustion chamber.Adopt " T " pipe to be connected an aspiration channel of being with air control valve between this upper strata blower fan and the described upper strata wind control valve; Described upper strata wind is mixed with described flue gas by described air and forms.After adopting flue gas recycled, the turbulent flow intensity in the fluid bed is increased, quicken the heat and mass transport process in the fluid bed, with the after-flame that impels fuel particle in the combustion chamber and improve nitrogen and desulfurization effect in the stove.This upper strata wind can promote the fluidisation intensity of air in fluid bed, to improve the effect of the abundant combustion conditions in the combustion chamber.
Described air blast connects an air and flue gas mixing-chamber by blast pipe, this mixing chamber other end by cigarette again blower fan be connected with described flue gas recirculation pipe; This mixing chamber top is connected with described air compartment again, to constitute wind of described fluidized bed combustion chamber.
Described upper strata blower fan is by upper strata wind ac variable frequency speed regulation Motor Drive, and this upper strata wind ac variable frequency speed regulation motor is by analysis of oxygen content sensor and oxygen content PLC control connection.
Described cigarette can be provided with cigarette control valve again between blower fan and the described flue gas recirculation pipe again.Control valve is as the flue gas recycled ratio of regulating a wind that enters mixing chamber again for cigarette, and it is in 5～50% scopes that a wind in the described mixing chamber adds the flue gas recycled ratio.After being mixed with a certain proportion of flue gas recycled in the wind, can reducing excess oxygen and do not influence fluidisation intensity in the fluid bed, and can not regulate bed temperature effectively by other means.
Described cigarette again blower fan by cigarette ac variable frequency speed regulation Motor Drive again, this cigarette again the ac variable frequency speed regulation motor by air compartment temperature sensor and air compartment temperature PLC control connection.
Described upper strata wind control valve, described cigarette control valve again can connect control by described PLC; Also can adopt operation control manually.
The present invention is because employing utilizes flue gas recycled and air stage feeding device, and compared with prior art its advantage is can improve fuel availability and reduce pollutant emission; Next is that desulfuration efficiency is higher, desulfurization degree can be brought up to about 90%; It three is can use various fuel in fluidized bed combustion chamber, has the advantage of using diversified fuel.
Description of drawings
Fig. 1 is a system schematic of the present invention;
The specific embodiment
Embodiment describes in further detail the present invention below in conjunction with accompanying drawing.
A kind of as shown in Figure 1 fluidized-bed combustion boiler, this boiler comprise that one is used to store the fuel tank 1 of coal or other fuel, and this fuel tank 1 is connected with boiler body 3.
This boiler body 3 comprises a circulating fluidized bed combustor 31, and this circulating fluidized bed combustor connects a cyclone separator 33; The district of fluidized bed height shown in the figure 32.These cyclone separator 33 exits are connected with the assembly 34 that is heated, and this assembly 34 that is heated includes superheater, economizer and air preheater.
The bottom of combustion chamber is provided with the air distribution plate 41 of band blast cap, and this blast cap is connected with an air blast 7 by air compartment 4, and this air blast enters described combustion chamber 31 with compressed air by air compartment and blast cap; The flue gas that combustion process in the combustion chamber produces leads to a dry type flue gas secondary devulcanizer 9 from the air preheater of the assembly that is heated, and the flue gas after the desulfurization enters sack cleaner 12, smoke regulating valve 14 and air-introduced machine 15 by connecting leg 11, and flue gas is discharged from chimney 16.
Coal in the fuel tank 1 or other solid fuel import in the combustion chamber 31 by fuel-supply pipe 2 after being ground into graininess.Import granular fuel in the combustion chamber 31 and be suspended in the combustion chamber in the fluidizing agent, and form a fluid bed.Combustion process mainly occurs in the fluidized bed height district 32 of combustion chamber.
Sack cleaner 12 is used for fuel was disposed wherein soot particle before the flue gas that combustion process produces is entering chimney 16, and this soot particle enters the dedusting ash storehouse 13 that is positioned at the sack cleaner below.
The present invention is in air-introduced machine 15 exits and be positioned at chimney 16 fronts and connect a flue gas recirculation pipe 17, and this flue gas recirculation pipe 17 is connected with combustion chamber 31 and air compartment 4 respectively.Air blast 7 is to connect an air and flue gas mixing-chamber 6 by blast pipe 23, and these air blast 7 front portions are provided with blow rate required control valve 8; This mixing chamber other end by cigarette again blower fan 22 be connected with flue gas recirculation pipe 17; This mixing chamber top is connected with described air compartment 4 again.Cigarette is provided with cigarette control valve 21 again between blower fan 22 and the flue gas recirculation pipe 17 again.
The partial fume that combustion process recited above produces inserts respectively in combustion chamber and the air compartment again, thereby constitutes feature of the present invention; Mix with a wind at the flue gas of air-introduced machine outlet exactly and send into the fluid bed bottom, in stove, strengthen fluid effect and do not increase excess air through air distribution plate; A part of flue gas recycled of while mixes with secondary wind sends into top, combustion chamber.
The present invention connects the flue gas recirculation pipe to obtain flue gas in the outlet of air-introduced machine 15.Thereby air-introduced machine 15 has enough pressure that flue gas is directly sent into air blast 7 in some case study on implementation, in this case, described cigarette blower fan again can be set again.
Utilize the CO in the flue gas recycled
2Strengthen SO in lime stone and the flue gas
2Respond and realize air stage feeding, and flue gas leads to a dry type flue gas secondary devulcanizer 9 from air preheater 34 and carries out the secondary desulfurization; This can improve the on the low side and higher phenomenon of pollutant emission of desulfurization degree of existing domestic middle-size and small-size fluidized-bed combustion boiler; Desulfurization degree of the present invention can be brought up to about 90%.
The present invention is to utilize remaining CaO in the boiler ash discharge in order further to improve desulfurized effect at the dry type flue gas secondary devulcanizer 9 that the fluidized-bed combustion boiler afterbody is set up, and 91 adds a part of lime stone from the desulfurizing agent porch, mixes removal SO with flue gas
2
The cloth bag of described fiber bag precipitator is installed in described dry type flue gas secondary devulcanizer 9 outlets, and connects by connecting leg 11.
The air compartment that the bottom of combustion chamber 31 is connected with air blast 7 forms a wind; After being mixed with a certain proportion of flue gas recycled in this wind, can reducing excess oxygen and do not influence fluidisation intensity in the fluid bed, and can not reduce bed temperature, cooling hearth effectively by other means.
In addition, behind the employing flue gas recycled, the turbulent flow intensity in the fluid bed is increased, quicken the heat and mass transport process in the fluid bed, this helps the after-flame and the interior nitrogen and desulfurization better effects if of stove of fuel particle.
Be provided with upper strata wind smoke regulating valve 18 between flue gas recirculation pipe 17 and combustion chamber, upper strata wind smoke regulating valve is used to adjust the flue gas quantity that enters the combustion chamber.
Between this upper strata wind smoke regulating valve 18 and the combustion chamber 31 a upper strata blower fan 20 is set again, the upper strata blower fan helps upper strata wind is successfully sent into the combustion chamber.Adopt the T-shape pipe to be connected an aspiration channel 24 of being with air control valve 19 between this upper strata blower fan and the upper strata wind smoke regulating valve 18; Upper strata wind is mixed with flue gas by air and forms thus, be injected in the combustion chamber in fluidized bed height district 32 as upper strata wind by airduct road, upper strata 25 again, this upper strata wind can promote the fluidisation intensity of air in fluid bed, to improve the abundant combustion conditions in the combustion chamber, for extra air is provided in the combustion process, also promptly provide extra oxygen simultaneously.
As mentioned above, it is to be mixed by air and flue gas recycled that upper strata wind is also promptly called secondary wind, and the free space of dilute phase provides extra air for burning in stove, realizes that the NOx that can lower in the combustion process behind the fractional combustion discharges.Air stage feeding and add the measure that flue gas recycled combines the excess oxygen of burning primary stage can be controlled at theoretical air requirement level or lower in a wind simultaneously is to manifest the effect of fractional combustion.
Cigarette again blower fan 22 by cigarette ac variable frequency speed regulation Motor Drive again, this cigarette again the ac variable frequency speed regulation motor by air compartment temperature PLC control connection.Adding the flue gas recycled ratio in the wind is roughly in 5～50% scopes.
In addition, upper strata wind can provide a metastable air parameter, and by controlling to reduce oxynitrides.Adding the flue gas recycled ratio in the wind of upper strata is roughly in 0～100% scope.Promptly can be 100% air, also can be 100% flue gas, but in most cases be to have a certain proportion of air and flue gas mist.The upper strata blower fan is by upper strata wind ac variable frequency speed regulation Motor Drive, and this upper strata wind ac variable frequency speed regulation motor is by oxygen content PLC control connection.
Air of the present invention mixes the upper strata wind injection fluidized-bed combustion boiler that constitutes with flue gas can cause the active more fuel fluid bed of chemical reaction and the excess air operating condition of lower quantity.Its beneficial effect is can reduce pollutant emission and more effectively utilize fuel.
Usually in fluidized-bed combustion boiler, lime stone (CaCO
3) blending joins in the fluid bed furnace together in coal and bed material, can be in stove with CO
2The concentration difference, and directly or through adding thermal decomposition generate CaO and SO
2Generation calcium sulfate CaSO is solidified in reaction
4These two kinds of reactions all with fire box temperature and CO
2Concentration is relevant, all along with CO
2The increase of concentration is reacted also strong more.The decomposition of lime stone also is relevant with this concentration.Thereby, increase CO
2Concentration is to absorbing the SO in the flue gas
2Be solidified into CaSO
4Favourable, be to increase some regional area CO in the stove and drop into flue gas recycled in the fluid bed
2The best method of concentration.
Have two zones of concentrated phase and dilute phase in the burner hearth of fluidized-bed combustion boiler, main heat transfer and sweetening process occur in the concentrated phase area.The flue gas recycled that mixes with secondary wind sprays in the burner hearth gas-solid phase mixture, promptly helps to reduce the discharging of sulfur dioxide, forms in the needed optimum temperature range of calcium sulfate combination reaction because it can be adjusted to bed temperature.
The device that the upper strata wind of band flue gas recirculation enters the combustion chamber and regulates its flue gas quantity can also adapt to the various application problems that contain fuel such as different ash contents, moisture and volatile materials; Thereby can realize that the present invention uses the function of diversified fuel.
Because the coal bed fluidizing velocity is the control that flowed by air, and flue gas quantity can control fluidized bed height in the fluidizing agent by increasing or reducing, thus can be to the accurate control of superfluous oxygen in the burning.So this makes to have the advantage of using various fuel in fluidized bed combustion chamber.
The superfluous oxygen in control combustion chamber is that the Measurement and Control System by oxygen in the flue gas recirculation realizes.The Measurement and Control System of this oxygen is connected with upper strata wind ac variable frequency speed regulation motor, and is controlled by oxygen content PLC.
The active more fluid bed of the present invention's reaction can reduce the discharging of smog and other particle.When flue gas reentered the combustion chamber, the burning again of more particles thing had reduced the carbon content of this particle in this flue gas, thereby realizes the purpose of full combustion of fuel, has also promptly reduced granular material discharged; Secondly, the minimizing of the quantity of oxygen will cause the minimizing of the pollutant emission quantity of nitrogen oxide in the combustion zone.
Claims (8)
1, a kind of fluidized-bed combustion boiler, comprise that one is provided with the boiler body (3) of fluidized bed combustion chamber (31), the bottom of this combustion chamber is provided with the air distribution plate (41) of band blast cap, this blast cap is connected with an air blast (7) by air compartment (4), this air blast enters described combustion chamber (31) with compressed air by described air compartment and blast cap, combustion product gases in the described boiler body (3) causes chimney (16) through sack cleaner (12) by air-introduced machine (15) and discharges, it is characterized in that: a flue gas recirculation pipe (17) is connected in described air-introduced machine (15) exit, and this flue gas recirculation pipe (17) is connected with described fluidized bed combustion chamber (31) and described air compartment (4) respectively; Be provided with dry type flue gas secondary devulcanizer (9) between described cyclone separator (33) and the described sack cleaner (12).
2, fluidized-bed combustion boiler according to claim 1 is characterized in that: be provided with upper strata wind smoke regulating valve (18) between described flue gas recirculation pipe (17) and the described fluidized bed combustion chamber (31); This upper strata wind smoke regulating valve (18) enters the ratio of flue gas recycled in the upper strata wind in the described fluidized bed combustion chamber (31) in order to adjusting, and this ratio is in 5～50% scopes.
3, fluidized-bed combustion boiler according to claim 2, it is characterized in that: a upper strata blower fan (20) is set between described upper strata wind smoke regulating valve (18) and described combustion chamber (31), adopts " T " pipe to be connected an aspiration channel (24) of being with air control valve (19) between this upper strata blower fan (20) and the described upper strata wind smoke regulating valve (18); Described upper strata wind is mixed with described flue gas by described air and forms.
4, fluidized-bed combustion boiler according to claim 1, it is characterized in that: described air blast (7) connects an air and flue gas mixing-chamber (6) by blast pipe (23), this mixing chamber (6) other end by cigarette again blower fan (22) be connected with described flue gas recirculation pipe (17); This mixing chamber (6) top is connected with described air compartment (4) again, to constitute wind one time.
5, fluidized-bed combustion boiler according to claim 3 is characterized in that: described upper strata blower fan (20) is by upper strata wind ac variable frequency speed regulation Motor Drive, and this upper strata wind ac variable frequency speed regulation motor is by analysis of oxygen content sensor and oxygen content PLC control connection.
6, fluidized-bed combustion boiler according to claim 4 is characterized in that: described cigarette is provided with cigarette control valve (21) again between blower fan (22) and the described flue gas recirculation pipe (17) again; This cigarette control valve (21) again is used for regulating the ratio of the flue gas recycled in the wind entering described mixing chamber (6), and this ratio is in 5～50% scopes.
7, fluidized-bed combustion boiler according to claim 6 is characterized in that: described cigarette again blower fan (22) by cigarette ac variable frequency speed regulation Motor Drive again, this cigarette again the ac variable frequency speed regulation motor by air compartment temperature sensor and air compartment temperature PLC control connection.
8, according to claim 3 or 6 described fluidized-bed combustion boilers, it is characterized in that: described upper strata wind smoke regulating valve (18), described cigarette control valve (21) are again controlled by described PLC control or employing operation manually.
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| Application Number | Priority Date | Filing Date | Title |
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| CNA2009101005745A CN101592336A (en) | 2009-07-06 | 2009-07-06 | A kind of fluidized-bed combustion boiler |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNA2009101005745A CN101592336A (en) | 2009-07-06 | 2009-07-06 | A kind of fluidized-bed combustion boiler |
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| CNA2009101005745A Pending CN101592336A (en) | 2009-07-06 | 2009-07-06 | A kind of fluidized-bed combustion boiler |
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Cited By (18)
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| CN102192498A (en) * | 2010-03-19 | 2011-09-21 | 杨文广 | Method of flue gas separation and depressurization as well as flue-returning and burning |
| CN102200276A (en) * | 2011-04-26 | 2011-09-28 | 清华大学 | Furnace-boiler separation system for combusting low-calorific-value solid fuel |
| CN102937290A (en) * | 2012-11-21 | 2013-02-20 | 中国东方电气集团有限公司 | External bed type double fluidized bed boiler-fouling preventing system |
| CN102944008A (en) * | 2012-11-21 | 2013-02-27 | 中国东方电气集团有限公司 | Boiler heating surface contamination preventing system of double-fluidized-bed combustion furnace |
| CN102966945A (en) * | 2012-11-02 | 2013-03-13 | 阳光凯迪新能源集团有限公司 | Method for reducing nitrogen oxide discharge of biomass circulating fluid bed boiler |
| CN103017329A (en) * | 2012-12-21 | 2013-04-03 | 哈尔滨工业大学 | Hot-blast stove system and method for different-speed circulating fluidized bed |
| CN103062785A (en) * | 2013-01-07 | 2013-04-24 | 宋朋泽 | System and method for flue gas dedusting and purifying |
| CN102116484B (en) * | 2010-01-05 | 2013-06-12 | 华北电力科学研究院有限责任公司 | Combustion control method and system for lignite-fired unit |
| CN103697466A (en) * | 2013-12-20 | 2014-04-02 | 哈尔滨锅炉厂有限责任公司 | Circulating fluidized bed boiler with smoke recirculating bypass, and NOX discharging method |
| CN103884013A (en) * | 2014-03-26 | 2014-06-25 | 东方电气集团东方锅炉股份有限公司 | Combustion method and device of coupled environment-friendly fluidized bed boiler |
| CN104006377A (en) * | 2014-03-04 | 2014-08-27 | 郭继会 | Treatment method for realizing zero release of fuel coal smoke dust in atmosphere |
| CN104197343A (en) * | 2014-08-29 | 2014-12-10 | 华北电力大学 | Oxygen-enriched combustion recycle flue gas catalytic desulfurization system and method |
| CN105509033A (en) * | 2016-02-02 | 2016-04-20 | 王立臣 | Pulverized-coal boiler multi-oxygen-combustion smoke recirculation system |
| CN105757699A (en) * | 2013-01-07 | 2016-07-13 | 宋朋泽 | Dust removal purifying system and method for flue gas |
| CN107152676A (en) * | 2017-06-15 | 2017-09-12 | 董磊 | Residual heat from boiler fume utilizes and reduced the air supply system of NO_x formation |
| CN107202319A (en) * | 2017-07-06 | 2017-09-26 | 烟台龙源电力技术股份有限公司 | A kind of differential fluidized-bed boiler system and its method for producing circulating flue gas |
| CN107355982A (en) * | 2016-05-09 | 2017-11-17 | 镇江北新建材有限公司 | Hot-blast stove residual neat recovering system |
| CN109611893A (en) * | 2018-11-16 | 2019-04-12 | 北京未来蓝天技术有限公司 | A kind of low-nitrogen discharged biomass granular fuel cooking warm |
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- 2009-07-06 CN CNA2009101005745A patent/CN101592336A/en active Pending
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| CN102116484B (en) * | 2010-01-05 | 2013-06-12 | 华北电力科学研究院有限责任公司 | Combustion control method and system for lignite-fired unit |
| CN102192498A (en) * | 2010-03-19 | 2011-09-21 | 杨文广 | Method of flue gas separation and depressurization as well as flue-returning and burning |
| CN102200276A (en) * | 2011-04-26 | 2011-09-28 | 清华大学 | Furnace-boiler separation system for combusting low-calorific-value solid fuel |
| WO2014067405A1 (en) * | 2012-11-02 | 2014-05-08 | 阳光凯迪新能源集团有限公司 | Method for reducing nitrogen oxide discharge of biomass circulating fluidized bed boiler |
| CN102966945A (en) * | 2012-11-02 | 2013-03-13 | 阳光凯迪新能源集团有限公司 | Method for reducing nitrogen oxide discharge of biomass circulating fluid bed boiler |
| CN102966945B (en) * | 2012-11-02 | 2016-03-02 | 阳光凯迪新能源集团有限公司 | Reduce the method for biomass recirculating fluidized bed boiler discharged nitrous oxides |
| CN102937290A (en) * | 2012-11-21 | 2013-02-20 | 中国东方电气集团有限公司 | External bed type double fluidized bed boiler-fouling preventing system |
| CN102944008A (en) * | 2012-11-21 | 2013-02-27 | 中国东方电气集团有限公司 | Boiler heating surface contamination preventing system of double-fluidized-bed combustion furnace |
| CN102944008B (en) * | 2012-11-21 | 2015-10-28 | 中国东方电气集团有限公司 | The system that a kind of double fluidized bed combustion stove prevents boiler heating surface from staiing |
| CN103017329A (en) * | 2012-12-21 | 2013-04-03 | 哈尔滨工业大学 | Hot-blast stove system and method for different-speed circulating fluidized bed |
| CN103017329B (en) * | 2012-12-21 | 2015-02-04 | 哈尔滨工业大学 | Hot-blast stove system and method for different-speed circulating fluidized bed |
| CN105757699A (en) * | 2013-01-07 | 2016-07-13 | 宋朋泽 | Dust removal purifying system and method for flue gas |
| CN103062785A (en) * | 2013-01-07 | 2013-04-24 | 宋朋泽 | System and method for flue gas dedusting and purifying |
| CN103697466A (en) * | 2013-12-20 | 2014-04-02 | 哈尔滨锅炉厂有限责任公司 | Circulating fluidized bed boiler with smoke recirculating bypass, and NOX discharging method |
| CN104006377A (en) * | 2014-03-04 | 2014-08-27 | 郭继会 | Treatment method for realizing zero release of fuel coal smoke dust in atmosphere |
| CN103884013A (en) * | 2014-03-26 | 2014-06-25 | 东方电气集团东方锅炉股份有限公司 | Combustion method and device of coupled environment-friendly fluidized bed boiler |
| CN104197343A (en) * | 2014-08-29 | 2014-12-10 | 华北电力大学 | Oxygen-enriched combustion recycle flue gas catalytic desulfurization system and method |
| CN105509033A (en) * | 2016-02-02 | 2016-04-20 | 王立臣 | Pulverized-coal boiler multi-oxygen-combustion smoke recirculation system |
| CN105509033B (en) * | 2016-02-02 | 2018-06-29 | 王立臣 | Pulverized-coal fired boiler polyoxy combustion product gases recirculating system |
| CN107355982A (en) * | 2016-05-09 | 2017-11-17 | 镇江北新建材有限公司 | Hot-blast stove residual neat recovering system |
| CN107152676A (en) * | 2017-06-15 | 2017-09-12 | 董磊 | Residual heat from boiler fume utilizes and reduced the air supply system of NO_x formation |
| CN107202319A (en) * | 2017-07-06 | 2017-09-26 | 烟台龙源电力技术股份有限公司 | A kind of differential fluidized-bed boiler system and its method for producing circulating flue gas |
| CN109611893A (en) * | 2018-11-16 | 2019-04-12 | 北京未来蓝天技术有限公司 | A kind of low-nitrogen discharged biomass granular fuel cooking warm |
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