CN103115357A - Circulating fluidized bed fire coal (waste incineration) boiler oxygen enrichment pulverized coal igniting steady burning device - Google Patents
Circulating fluidized bed fire coal (waste incineration) boiler oxygen enrichment pulverized coal igniting steady burning device Download PDFInfo
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- CN103115357A CN103115357A CN2013100175459A CN201310017545A CN103115357A CN 103115357 A CN103115357 A CN 103115357A CN 2013100175459 A CN2013100175459 A CN 2013100175459A CN 201310017545 A CN201310017545 A CN 201310017545A CN 103115357 A CN103115357 A CN 103115357A
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- coal
- coal dust
- fluidized bed
- waste incineration
- circulating fluidized
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- 239000003245 coal Substances 0.000 title claims abstract description 110
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 title claims abstract description 65
- 229910052760 oxygen Inorganic materials 0.000 title claims abstract description 65
- 239000001301 oxygen Substances 0.000 title claims abstract description 65
- 238000004056 waste incineration Methods 0.000 title claims abstract description 56
- 238000002485 combustion reaction Methods 0.000 claims abstract description 102
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 claims abstract description 25
- 239000002817 coal dust Substances 0.000 claims description 129
- 239000000843 powder Substances 0.000 claims description 51
- 238000010304 firing Methods 0.000 claims description 45
- 230000001105 regulatory effect Effects 0.000 claims description 7
- 230000000977 initiatory effect Effects 0.000 claims description 6
- 239000003921 oil Substances 0.000 description 29
- 238000005516 engineering process Methods 0.000 description 6
- 239000000295 fuel oil Substances 0.000 description 6
- 239000004519 grease Substances 0.000 description 5
- 239000002245 particle Substances 0.000 description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 239000000470 constituent Substances 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000003546 flue gas Substances 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- 230000003044 adaptive effect Effects 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 239000010779 crude oil Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000001360 synchronised effect Effects 0.000 description 1
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- 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
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
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- Fluidized-Bed Combustion And Resonant Combustion (AREA)
- Combustion Of Fluid Fuel (AREA)
Abstract
The invention relates to a circulating fluidized bed fire coal (waste incineration) boiler oxygen enrichment pulverized coal igniting steady burning device. The circulating fluidized bed fire coal (waste incineration) boiler oxygen enrichment pulverized coal igniting steady burning device is characterized in that according to the circulating fluidized bed fire coal (waste incineration) boiler oxygen enrichment pulverized coal igniting steady burning device, a primary air moving direction is a primary air fan (1), a primary air pipeline (2), a wind power mixer (6), a primary wind power pipeline (7), a pulverized coal combustion gun shell (8), an oil oxygen pipeline (9), a pure oxygen oil premix burning nozzle (10), a pulverized coal burning gun nozzle (11), and a circulating fluidized bed fire coal (waste incineration) boiler (12) in sequence. A pulverized coal moving direction is a pulverized coal transiting cabin (3), a pulverized coal feeder (4), a pulverized coal pipeline (5), the wind power mixer (6), the primary wind power pipeline (7), the pulverized coal combustion gun shell (8), the oil oxygen pipeline (9), the pure oxygen oil premixed combustion nozzle (10), the pulverized coal combustion gun nozzle (11), and the circulating fluidized bed fire coal (waste incineration) boiler (12) in sequence. The pulverized coal pipeline (5) is intersected with the primary air pipeline (2) in the wind power mixer (6), and the primary wind power pipeline (7) is composed and moves along a same direction.
Description
Technical field
The present invention relates to a kind of circulating fluidized bed combustion coal (waste incineration) boiler oxygen-rich coal dust ignition smooth combustion apparatus, refer in particular to the application in circulating fluidized bed combustion coal boiler and refuse incinerator of circulating fluid bed.
Background technology
Circulating fluidized bed combustion coal (waste incineration) boiler is wide due to its combustion adaptive, direct desulfurization denitration in stove, boiler load are regulated than all many-sides such as large, that boiler thermal output is high has outstanding advantages and is day by day attracted attention by thermal technology circle.Circulating fluidized bed combustion coal (waste incineration) boiler all adopts large grease gun igniting surely to fire, and when ignition of the boiler is surely fired, consumes great amount of fuel oil, not the fuel oil of combustion can cause environmental protecting device can't with the synchronous operation of ignition of the boiler device, can not reach national requirements for environmental protection.Enter 21st century, the fast development of national economy, China increases day by day to the demand of the energy, and the Global Oil resource is day by day in short supply constantly soaring with crude oil price, and controlling fuel consume has been the realistic problem that China's power industry has to face.Adopt oxygen-rich coal dust ignition smooth combustion technology to replace large grease gun igniting stable combustion technology, realize that " replace oil with coal " is an instant major issue of circulating fluidized bed combustion coal (waste incineration) boiler.
To sum up, circulating fluidized bed combustion coal (waste incineration) boiler adopts large grease gun igniting surely to fire and restricted national fuel-economizing implementation on sizable degree.
Summary of the invention
Adopt the deficiency of the steady combustion of large grease gun igniting for circulating fluidized bed combustion coal (waste incineration) boiler, the present invention proposes oxygen-rich coal dust ignition smooth combustion technology and replace large grease gun igniting stable combustion technology, circulating fluidized bed combustion coal (waste incineration) boiler oxygen-rich coal dust ignition smooth combustion apparatus has been invented in design.
For reaching above purpose, the solution of the present invention is:
A kind of circulating fluidized bed combustion coal (waste incineration) boiler oxygen-rich coal dust ignition smooth combustion apparatus, it is characterized in that this circulating fluidized bed combustion coal (waste incineration) boiler oxygen-rich coal dust ignition smooth combustion apparatus by a wind traffic direction, is successively: a wind blower fan (1), an airduct line (2), air and powder mixer (6), primary wind and powder pipeline (7), coal dust firing rifle housing (8), oily oxygen pipeline (9), pure oxygen oil premixed combustion spout (10), coal dust firing rifle spout (11), circulating fluidized bed combustion coal (waste incineration) boiler (12); Press the coal dust traffic direction, be successively: roll-over in coal dust (3), machine supplying powder (4), coal dust pipeline (5), air and powder mixer (6), primary wind and powder pipeline (7), coal dust firing rifle housing (8), oily oxygen pipeline (9), pure oxygen oil premixed combustion spout (10), coal dust firing rifle spout (11), circulating fluidized bed combustion coal (waste incineration) boiler (12); Coal dust pipeline (5) is located to intersect at air and powder mixer (6) with an airduct line (2), synthetic primary wind and powder pipeline (7), and operation in the same direction.
Further, a wind blower fan (1) is positioned at an airduct line (2) initiating terminal along a wind traffic direction, and a wind blower fan (1) provides power and the coal dust firing oxygen used of coal dust transportation, can control primary air flow by regulating a wind blower fan (1) rotating speed.
Further, roll-over in coal dust (3) is positioned at the initiating terminal of coal dust pipeline (5) along the coal dust traffic direction, this device ignition smooth combustion coal dust used is housed in roll-over in coal dust (3), fineness of pulverized coal is R75 ~ R100, and the coal dust in roll-over in coal dust (3) makes by coal pulverizer or vehicles drive obtains.
Further, machine supplying powder (4) is arranged between roll-over in coal dust (3) and air and powder mixer (6), and is arranged under coal dust roll-over (3), can control the coal dust amount by regulating machine supplying powder (4) rotating speed.
Further, air and powder mixer (6) is arranged on coal dust pipeline (5) and an airduct line (2) intersection, wind and coal dust are mixed in air and powder mixer (6), regulate the interior pulverized coal density of primary air of air and powder mixer (6) by a wind blower fan (1) and machine supplying powder (4), make pulverized coal density of primary air maintain 0 ~ 1kg/kg.
Further, coal dust firing rifle housing (8) is arranged on the lower former oil gun of circulating fluidized bed combustion coal (waste incineration) boiler (12) bed place, perhaps be arranged on circulating fluidized bed combustion coal (waste incineration) boiler (12) bed former oil gun place or the upper Secondary Air of bed exit, perhaps be arranged on simultaneously the lower former oil gun of circulating fluidized bed combustion coal (waste incineration) boiler (12) bed, the upper former oil gun of bed or bed upper Secondary Air exit.
Further, coal dust firing rifle housing (8), coal dust firing rifle spout (11) and pure oxygen oil premixed combustion spout (10) be all circle perpendicular to the profile on wind traffic direction, and axial line all is on same axial line.
Further, oil oxygen pipeline (9) axial line and pure oxygen oil premixed combustion spout (10) axial line are 0 ° ~ 90 ° angles, and two axial lines intersect, and pure oxygen oil premixed combustion spout (10) external diameter and oily oxygen pipeline (9) external diameter are all less than coal dust firing rifle housing (8) internal diameter.
Further, coal dust firing rifle housing (8) axial line and a wind traffic direction are 0 ° ~ 90 ° angles, and are connected with primary wind and powder pipeline (7).
Principle of the present invention and characteristics are: the flame that utilizes micro-fuel oil fully to burn and produce under the pure oxygen condition, this flame temperature is high, rigidity is strong, make the shallow bid that passes this flame be that in the pulverized coal flow of oxygen enrichment state, Pulverized Coal obtains the fast pyrogenation burning, wherein, the not only contained fugitive constituent burning of coal dust, because pulverized coal flow is the oxygen enrichment state, thereby also burning simultaneously of the contained solid carbon of this part coal dust, and then this part heat that coal dust firing produces, the whole pulverized coal flow that ignites is realized " replace oil with coal; with oxygen and aiding combustion ", reaches with the direct firing coal-dust stream of little oil firing; The pulverized coal flow of lighting is emitted heat, heat cycles fluidized bed burned-coal (waste incineration) furnace and burner hearth, and then ignite or light coal particle on circulating fluidized bed combustion coal (waste incineration) furnace, realize circulating fluidized bed combustion coal (waste incineration) boiler oxygen-rich coal dust ignition smooth combustion apparatus to circulating fluidized bed combustion coal (waste incineration) ignition of the boiler surely fire.
The coal dust that wind that a wind blower fan (1) provides and machine supplying powder (4) provide is located to mix at air and powder mixer (6), forms pulverized coal flow, and pulverized coal flow enters coal dust firing rifle housing (8) through primary wind and powder pipeline (7).
Pure oxygen penetrates from oily oxygen pipeline (9) high speed, is formed strong Rotary Oxygen air-flow by coal dust firing rifle housing (8) constraint, and when pulverized coal flow passed through this strong Rotary Oxygen air-flow, pulverized coal flow and the abundant premix of Rotary Oxygen air-flow formed oxygen-rich coal dust stream.
Oxygen-rich coal dust stream passes fuel oil and pure oxygen and locates to form thermal-flame at pure oxygen oil premixed combustion spout (10) and directly burn, and locates to form oxygen-rich coal dust flame at coal dust firing rifle spout (11).
Oxygen-rich coal dust flame sprays from coal dust firing rifle spout (11), emit heat, heat cycles fluidized bed burned-coal (waste incineration) boiler (12) siege and burner hearth, and then ignite or light coal particle on circulating fluidized bed combustion coal (waste incineration) boiler (12) siege.
Above principle and characteristics make the pulverized coal flow sufficient combustion, the burning heat that produces ignites or puts coal-burning particle, the amount of flue gas emission and the temperature that produce after the pulverized coal flow burning are equal to amount of flue gas emission and the temperature that oil firing produces, and are conducive to the application at circulating fluidized bed combustion coal boiler and refuse incinerator of circulating fluid bed.
Description of drawings:
Fig. 1 is a kind of circulating fluidized bed combustion coal (waste incineration) boiler oxygen-rich coal dust ignition smooth combustion apparatus.
Specific embodiments:
Below in conjunction with specification and Fig. 1, circulating fluidized bed combustion coal (waste incineration) boiler oxygen-rich coal dust ignition smooth combustion apparatus is described further.
Circulating fluidized bed combustion coal (waste incineration) boiler oxygen-rich coal dust ignition smooth combustion apparatus by a wind traffic direction is successively: a wind blower fan (1), an airduct line (2), air and powder mixer (6), primary wind and powder pipeline (7), coal dust firing rifle housing (8), oily oxygen pipeline (9), pure oxygen oil premixed combustion spout (10), coal dust firing rifle spout (11), circulating fluidized bed combustion coal (waste incineration) boiler (12); Press the coal dust traffic direction, be successively: roll-over in coal dust (3), machine supplying powder (4), coal dust pipeline (5), air and powder mixer (6), primary wind and powder pipeline (7), coal dust firing rifle housing (8), oily oxygen pipeline (9), pure oxygen oil premixed combustion spout (10), coal dust firing rifle spout (11), circulating fluidized bed combustion coal (waste incineration) boiler (12); Coal dust pipeline (5) is located to intersect at air and powder mixer (6) with an airduct line (2), synthetic primary wind and powder pipeline (7), and operation in the same direction.
A wind blower fan (1) is positioned at an airduct line (2) initiating terminal along a wind traffic direction, and a wind blower fan (1) provides power and the coal dust firing oxygen used of coal dust transportation, can control primary air flow by regulating a wind blower fan (1) rotating speed.
Roll-over in coal dust (3) is positioned at the initiating terminal of coal dust pipeline (5) along the coal dust traffic direction, this device ignition smooth combustion coal dust used is housed in roll-over in coal dust (3), fineness of pulverized coal is R75 ~ R100, and the coal dust in roll-over in coal dust (3) makes by coal pulverizer or vehicles drive obtains.
Machine supplying powder (4) is arranged between roll-over in coal dust (3) and air and powder mixer (6), and is arranged under coal dust roll-over (3), can control the coal dust amount by regulating machine supplying powder (4) rotating speed.
Air and powder mixer (6) is arranged on coal dust pipeline (5) and an airduct line (2) intersection, wind and coal dust are mixed in air and powder mixer (6), regulate the interior pulverized coal density of primary air of air and powder mixer (6) by a wind blower fan (1) and machine supplying powder (4), make pulverized coal density of primary air maintain 0 ~ 1kg/kg.
Coal dust firing rifle housing (8) is arranged on the lower former oil gun of circulating fluidized bed combustion coal (waste incineration) boiler (12) bed place, perhaps be arranged on circulating fluidized bed combustion coal (waste incineration) boiler (12) bed former oil gun place or the upper Secondary Air of bed exit, perhaps be arranged on simultaneously the lower former oil gun of circulating fluidized bed combustion coal (waste incineration) boiler (12) bed, the upper former oil gun of bed or bed upper Secondary Air exit.
Coal dust firing rifle housing (8), coal dust firing rifle spout (11) and pure oxygen oil premixed combustion spout (10) be all circle perpendicular to the profile on wind traffic direction, and axial line all is on same axial line.
Oil oxygen pipeline (9) axial line and pure oxygen oil premixed combustion spout (10) axial line are 0 ° ~ 90 ° angles, and two axial lines are crossing, and pure oxygen oil premixed combustion spout (10) external diameter and oily oxygen pipeline (9) external diameter are all less than coal dust firing rifle housing (8) internal diameter.
Coal dust firing rifle housing (8) axial line and a wind traffic direction are 0 ° ~ 90 ° angles, and are connected with primary wind and powder pipeline (7).
The flame that utilizes micro-fuel oil fully to burn and produce under the pure oxygen condition, this flame temperature is high, rigidity is strong, make the shallow bid that passes this flame be that in the pulverized coal flow of oxygen enrichment state, Pulverized Coal obtains the fast pyrogenation burning, wherein, the not only contained fugitive constituent burning of coal dust, because pulverized coal flow is the oxygen enrichment state, thereby also burning simultaneously of the contained solid carbon of this part coal dust, and then this part heat that coal dust firing produces, the whole pulverized coal flow that ignites is realized " replace oil with coal; with oxygen and aiding combustion ", reaches with the direct firing coal-dust stream of little oil firing; The pulverized coal flow of lighting is emitted heat, heat cycles fluidized bed burned-coal (waste incineration) furnace and burner hearth, and then ignite or light coal particle on circulating fluidized bed combustion coal (waste incineration) furnace, realize circulating fluidized bed combustion coal (waste incineration) boiler oxygen-rich coal dust ignition smooth combustion apparatus to circulating fluidized bed combustion coal (waste incineration) ignition of the boiler surely fire.
The coal dust that wind that a wind blower fan (1) provides and machine supplying powder (4) provide is located to mix at air and powder mixer (6), forms pulverized coal flow, and pulverized coal flow enters coal dust firing rifle housing (8) through primary wind and powder pipeline (7).
Pure oxygen penetrates from oily oxygen pipeline (9) high speed, is formed strong Rotary Oxygen air-flow by coal dust firing rifle housing (8) constraint, and when pulverized coal flow passed through this strong Rotary Oxygen air-flow, pulverized coal flow and the abundant premix of Rotary Oxygen air-flow formed oxygen-rich coal dust stream.
Oxygen-rich coal dust stream passes fuel oil and pure oxygen and locates to form thermal-flame at pure oxygen oil premixed combustion spout (10) and directly burn, and locates to form oxygen-rich coal dust flame at coal dust firing rifle spout (11).
Oxygen-rich coal dust flame sprays from coal dust firing rifle spout (11), emit heat, heat cycles fluidized bed burned-coal (waste incineration) boiler (12) siege and burner hearth, and then ignite or light coal particle on circulating fluidized bed combustion coal (waste incineration) boiler (12) siege.
Above enforcement; only to general description of the present invention; be not that scope of the present invention is limited; design under the prerequisite of spirit not breaking away from the present invention; anyone all should fall in the definite protection domain of claims of the present invention various distortion and improvement that technical scheme of the present invention is made.
Claims (9)
1. a circulating fluidized bed combustion coal (waste incineration) boiler oxygen-rich coal dust ignition smooth combustion apparatus, it is characterized in that this circulating fluidized bed combustion coal (waste incineration) boiler oxygen-rich coal dust ignition smooth combustion apparatus by a wind traffic direction, is successively: a wind blower fan (1), an airduct line (2), air and powder mixer (6), primary wind and powder pipeline (7), coal dust firing rifle housing (8), oily oxygen pipeline (9), pure oxygen oil premixed combustion spout (10), coal dust firing rifle spout (11), circulating fluidized bed combustion coal (waste incineration) boiler (12); Press the coal dust traffic direction, be successively: roll-over in coal dust (3), machine supplying powder (4), coal dust pipeline (5), air and powder mixer (6), primary wind and powder pipeline (7), coal dust firing rifle housing (8), oily oxygen pipeline (9), pure oxygen oil premixed combustion spout (10), coal dust firing rifle spout (11), circulating fluidized bed combustion coal (waste incineration) boiler (12); Coal dust pipeline (5) is located to intersect at air and powder mixer (6) with an airduct line (2), synthetic primary wind and powder pipeline (7), and operation in the same direction.
2. a kind of circulating fluidized bed combustion coal as claimed in claim 1 (waste incineration) boiler oxygen-rich coal dust ignition smooth combustion apparatus, it is characterized in that a wind blower fan (1) is positioned at an airduct line (2) initiating terminal along a wind traffic direction, a wind blower fan (1) provides power and the coal dust firing oxygen used of coal dust transportation, can control primary air flow by regulating a wind blower fan (1) rotating speed.
3. a kind of circulating fluidized bed combustion coal as claimed in claim 1 (waste incineration) boiler oxygen-rich coal dust ignition smooth combustion apparatus, it is characterized in that roll-over in coal dust (3) is positioned at the initiating terminal of coal dust pipeline (5) along the coal dust traffic direction, this device ignition smooth combustion coal dust used is housed in roll-over in coal dust (3), fineness of pulverized coal is R75 ~ R100, and the coal dust in roll-over in coal dust (3) makes by coal pulverizer or vehicles drive obtains.
4. a kind of circulating fluidized bed combustion coal as claimed in claim 1 (waste incineration) boiler oxygen-rich coal dust ignition smooth combustion apparatus, it is characterized in that machine supplying powder (4) is arranged between roll-over in coal dust (3) and air and powder mixer (6), and be arranged under coal dust roll-over (3), can control the coal dust amount by regulating machine supplying powder (4) rotating speed.
5. a kind of circulating fluidized bed combustion coal as claimed in claim 1 (waste incineration) boiler oxygen-rich coal dust ignition smooth combustion apparatus, it is characterized in that air and powder mixer (6) is arranged on coal dust pipeline (5) and an airduct line (2) intersection, wind and coal dust are mixed in air and powder mixer (6), regulate the interior pulverized coal density of primary air of air and powder mixer (6) by a wind blower fan (1) and machine supplying powder (4), make pulverized coal density of primary air maintain 0 ~ 1kg/kg.
6. a kind of circulating fluidized bed combustion coal as claimed in claim 1 (waste incineration) boiler oxygen-rich coal dust ignition smooth combustion apparatus, it is characterized in that coal dust firing rifle housing (8) is arranged on the lower former oil gun of circulating fluidized bed combustion coal (waste incineration) boiler (12) bed place, perhaps be arranged on circulating fluidized bed combustion coal (waste incineration) boiler (12) bed former oil gun place or the upper Secondary Air of bed exit, perhaps be arranged on simultaneously the lower former oil gun of circulating fluidized bed combustion coal (waste incineration) boiler (12) bed, the upper former oil gun of bed or bed upper Secondary Air exit.
7. a kind of circulating fluidized bed combustion coal as claimed in claim 1 (waste incineration) boiler oxygen-rich coal dust ignition smooth combustion apparatus, it is characterized in that coal dust firing rifle housing (8), coal dust firing rifle spout (11) and pure oxygen oil premixed combustion spout (10) be all circle perpendicular to the profile on wind traffic direction, and axial line is in all on same axial line.
8. a kind of circulating fluidized bed combustion coal as claimed in claim 1 (waste incineration) boiler oxygen-rich coal dust ignition smooth combustion apparatus, it is characterized in that oily oxygen pipeline (9) axial line and pure oxygen oil premixed combustion spout (10) axial line is 0 ° ~ 90 ° angles, and two axial lines intersect, and pure oxygen oil premixed combustion spout (10) external diameter and oily oxygen pipeline (9) external diameter are all less than coal dust firing rifle housing (8) internal diameter.
9. a kind of circulating fluidized bed combustion coal as claimed in claim 1 (waste incineration) boiler oxygen-rich coal dust ignition smooth combustion apparatus, it is characterized in that coal dust firing rifle housing (8) axial line and a wind traffic direction are 0 ° ~ 90 ° angles, and be connected with primary wind and powder pipeline (7).
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| CN2013100175459A CN103115357A (en) | 2013-01-17 | 2013-01-17 | Circulating fluidized bed fire coal (waste incineration) boiler oxygen enrichment pulverized coal igniting steady burning device |
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| CN2013100175459A CN103115357A (en) | 2013-01-17 | 2013-01-17 | Circulating fluidized bed fire coal (waste incineration) boiler oxygen enrichment pulverized coal igniting steady burning device |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103386413A (en) * | 2013-07-26 | 2013-11-13 | 上海宝锋工程技术有限公司 | Garbage incinerating device and garbage incinerating method |
| CN105318326A (en) * | 2015-06-16 | 2016-02-10 | 湖南联新能源环保科技股份有限公司 | High-low circulating fluidized bedboiler |
| CN106322365A (en) * | 2015-07-01 | 2017-01-11 | 重庆市富燃科技有限责任公司 | Apparatus and method for generating carbon monoxide through igniting coal dust at nozzle |
| CN107543196A (en) * | 2017-08-31 | 2018-01-05 | 山东英电环保科技有限公司 | Coal unit depth peak regulation surely fires system |
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| CN106322365A (en) * | 2015-07-01 | 2017-01-11 | 重庆市富燃科技有限责任公司 | Apparatus and method for generating carbon monoxide through igniting coal dust at nozzle |
| CN107543196A (en) * | 2017-08-31 | 2018-01-05 | 山东英电环保科技有限公司 | Coal unit depth peak regulation surely fires system |
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