CN105716076A - Electrolysis oxy-hydrogen gas pulverized coal igniting burner - Google Patents
Electrolysis oxy-hydrogen gas pulverized coal igniting burner Download PDFInfo
- Publication number
- CN105716076A CN105716076A CN201610081600.4A CN201610081600A CN105716076A CN 105716076 A CN105716076 A CN 105716076A CN 201610081600 A CN201610081600 A CN 201610081600A CN 105716076 A CN105716076 A CN 105716076A
- Authority
- CN
- China
- Prior art keywords
- pulverized coal
- pipe
- hydrogen
- electrolysis
- tubular shell
- 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
- 239000003245 coal Substances 0.000 title claims abstract description 34
- 238000005868 electrolysis reaction Methods 0.000 title claims abstract description 11
- 239000001257 hydrogen Substances 0.000 claims abstract description 27
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 27
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 25
- 239000007789 gas Substances 0.000 claims abstract description 17
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 14
- 239000001301 oxygen Substances 0.000 claims abstract description 14
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 14
- 239000000203 mixture Substances 0.000 claims abstract description 13
- 239000002817 coal dust Substances 0.000 claims description 25
- 238000002485 combustion reaction Methods 0.000 claims description 16
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 claims description 13
- 229910001882 dioxygen Inorganic materials 0.000 claims description 13
- 230000007062 hydrolysis Effects 0.000 claims description 3
- 238000006460 hydrolysis reaction Methods 0.000 claims description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 8
- 230000009286 beneficial effect Effects 0.000 abstract description 4
- 238000010304 firing Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 230000033228 biological regulation Effects 0.000 description 2
- 239000000470 constituent Substances 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 150000002431 hydrogen Chemical class 0.000 description 2
- 230000006698 induction Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 2
- 229910052721 tungsten Inorganic materials 0.000 description 2
- 239000010937 tungsten Substances 0.000 description 2
- 238000001816 cooling Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000005474 detonation Methods 0.000 description 1
- 239000002283 diesel fuel Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000011819 refractory material Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 238000009736 wetting Methods 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D1/00—Burners for combustion of pulverulent fuel
- F23D1/02—Vortex burners, e.g. for cyclone-type combustion apparatus
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D2201/00—Burners adapted for particulate solid or pulverulent fuels
- F23D2201/20—Fuel flow guiding devices
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D2207/00—Ignition devices associated with burner
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
Abstract
An electrolysis oxy-hydrogen gas pulverized coal igniting burner comprises a tubular shell, a burning board, a water electrolysis oxy-hydrogen gas production tube and a flame drawing tube. The electrolysis oxy-hydrogen gas pulverized coal igniting burner is technically characterized in that a primary pulverized coal air casing tube is sleeved with the tubular shell; the flame drawing tube is sleeved with the primary pulverized coal air casing tube; a burning board with burning fire columns is arranged in the flame drawing tube, wherein the burning fire columns are perpendicular to the heading direction of a mixture of pulverized coal and air; and the tubular shell communicates with a secondary air inflow tube. The electrolysis oxy-hydrogen gas pulverized coal igniting burner has the beneficial effects that pipeline connection is easy, and leakage is unlikely to happen; output gas produced by a water electrolysis device exactly comprises two parts of hydrogen and one part of oxygen, and the ratio of burning gas is just right; and the burnt gas burns violently and fire is unlikely to be extinguished through the pulverized coal, the temperature can reach about 3000 DEG C, the size of flames can be controlled, operation is convenient, control is easy, pulverized coal of various types can be ignited, the requirement for ignition of the pulverized coal of various types can be met, operation is easy, control is convenient, energy is saved, and the environment is protected.
Description
Technical field
The invention belongs to coal dust and light equipment technical field, particularly to a kind of hydrogen and oxygen electrolyzing gas ignition coal burner.
Background technology
It is known that the igniting of existing thermal power plant large coal powder boiler and combustion-supporting, it is mostly device Large Oil rifle in the secondary air duct of coal burner, complete oil firing during ignition trigger.The evaporation capacity 670 each ignition oil of ton hour boiler of one 200,000 kilowatts of unit is more than 50 tons, and power plant of China is many lights a fire for power plant with light diesel fuel, and this is a kind of serious high-rank fuel waste.
Currently available make to replace fuel ignition burner and main burner have plasma non-oil ignition surely to fire, high temperature air non-oil ignition surely fires, three kinds of technical approach of hydrogen or oxygen gas ignition smooth combustion technology.
nullPlasma non-oil ignition smooth combustion apparatus is by ignition spout、Negative electrode、Anode、Water-cooling system、The part composition such as large power supply,Use the large power supply of about 120kW~400kW,Ignition temperature is up to the plasma arc of degree up to ten thousand,Realize coal dust heating、Reliable ignition and steady combustion,There is igniting fast、Reliable and stable、Coal adaptability more extensively waits various features,It is disadvantageous in that,High-power、Degree high temperature up to ten thousand cause negative electrode、Anode scaling loss is serious,Even if taking water-cooled measure,The most tens of hours of tungsten cathode life-span,The most hundreds of hours of anode life,Need to frequently change negative electrode and anode,Rather bother,Once fault,Affect the safe and reliable operation of station boiler,And consume the strategic materials materials such as more valuable tungsten,And power consumption is higher,As a example by the power station of corner tangential firing,Separate unit boiler configuration four set plasma burner,Power reaches 480kW~1600kW,Separate unit boiler annual operating cost is up to about 5,000,000.
High temperature air non-oil ignition smooth combustion apparatus, by port, high-frequency induction head, large power supplies etc. form, use the high-frequency induction system of tens of kilowatt, by the eddy current electrocaloric effect of metal pipe-wall, air is heated high temperature, realize lighting and surely firing of coal dust, there is host inorganic tool moving component, reliability is higher, various features, it is disadvantageous in that, the temperature of air heating, the restriction of metal of originally experiencing license wall temperature, and the thermal capacity of air own is relatively low, ature of coal is the poorest, water content is the highest, its thermal capacity is the biggest, coal dust possibly cannot be heated to burning-point and be lighted by high temperature air at any time, loss of ignition rate is higher, apply bigger by effect on coal quality, coal adaptability is poor.
Hydrogen or oxygen gas ignition smooth combustion apparatus, it is in charge of by the regulation and control hydrogen of specific proportioning, carrier of oxygen and mixes merga pass electricity ignition device at the burning column of flame after burner and ignite, the mode that this hydrogen, carrier of oxygen are in charge of into burner regulates and controls proportioning inconvenience, they generally use gas tank storage, frequently change, even if in order to reduce replacing during use, multiple gas tanks are connected, its pipeline connected once leaks, and detonation easily occurs, even explodes, be absolutely unsafe;The direct of travel of coal dust-air mixture is parallel with burning column of flame flame direction or has less angle, cannot the high temperature of fully utilized oxyhydrogen flame, burn insufficient through oxyhydrogen flame at coal dust-air mixture, bigger combustion zone cannot be formed, and then need the continual continuous work of oxyhydrogen flame, to reach the purpose surely fired, thus cause the raising of job costs.
Summary of the invention
For solving above-mentioned technical problem, the present invention proposes a kind of hydrogen and oxygen electrolyzing gas ignition coal burner, and it uses the hydrogen and oxygen gas mixture of electrolysis unit electrolysis water directly to enter stove Vertical Flame and lights, it is not necessary to regulation and control, safe and reliable, environmental protection and energy saving.
The technical scheme is that and be achieved in that:
A kind of hydrogen and oxygen electrolyzing gas ignition coal burner, it includes tubular shell, burner plate, electrolysis aquatic product hydrogen or oxygen gas pipe and holds together combustion pipe, a coal dust windband pipe it is set with in described tubular shell, in a coal dust windband pipe, it is set with combustion pipe, the burner plate of the band burning column of flame it is provided with in holding together to fire pipe, this burning column of flame is perpendicular to the direct of travel of coal dust-air mixture, and the burning column of flame is connected with electrolytic water oxyhydrogen generator by being electrolysed aquatic product hydrogen or oxygen gas pipe;It is communicated with secondary wind inleting tube on described tubular shell.
Preferably, it is additionally provided with a point windband pipe between described tubular shell and a coal dust windband pipe.
Preferably, the port of export of described point of windband pipe and a coal dust windband pipe is provided with rotary wind guide grid.
The hydrogen and oxygen electrolyzing gas ignition coal burner of the present invention has pipeline connection compared with tradition hydrogen or oxygen gas ignition smooth combustion apparatus and is simply not susceptible to reveal;Electrolysis wetting system aerogenesis output gas is exactly one oxygen of two hydrogen, and the proportioning of burning gases is just right;The gas combustion being ignited fiercely is difficult to be gone out by coal dust wind, temperature controls up to the size of the size available current of about 3000 degree flames, easy to operate control is easy, any of the above for fugitive constituent 24 coal dust can be lighted with 10-20 degree electricity, if fugitive constituent can suitably increase electric current output less than less than 24, increase flame.Lighting of various coal dust can be met, have simple to operate easy to control, the advantage of energy-conserving and environment-protective.
Accompanying drawing explanation
Fig. 1 is the structural representation sketch of the present invention;
Fig. 2 is the left view end view drawing of Fig. 1.
In figure: 1, tubular shell;2, windband pipe is divided;3, a coal dust windband pipe;4, combustion pipe is held together;5, it is electrolysed aquatic product hydrogen or oxygen gas pipe;6, electrolytic water oxyhydrogen generator;7, secondary wind inleting tube;8, burner plate;9, the burning column of flame;10, rotary wind guide grid.
Detailed description of the invention
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is clearly and completely described, it is clear that described embodiment is only a part of embodiment of the present invention rather than whole embodiments.Based on the embodiment in the present invention, the every other embodiment that those of ordinary skill in the art are obtained under not making creative work premise, broadly fall into the scope of protection of the invention.
As shown in Figure 1-2, for one hydrogen and oxygen electrolyzing gas ignition coal burner of the present invention, including:
Tubular shell 1, burner plate 8, it is electrolysed aquatic product hydrogen or oxygen gas pipe 5 and holds together to fire pipe 4, a coal dust windband pipe 3 it is set with in described tubular shell 1, in a coal dust windband pipe 3, it is set with combustion pipe 4, the burner plate 8 of the band burning column of flame 9 it is provided with in holding together to fire pipe 4, this burning column of flame 9 is perpendicular to the direct of travel of coal dust-air mixture, and the burning column of flame 9 is connected with lioh hydrolysis generator 6 by being electrolysed aquatic product hydrogen or oxygen gas pipe 5;It is communicated with secondary wind inleting tube 7 on described tubular shell 1.It is additionally provided with a point windband pipe 2 between described tubular shell 1 and a coal dust windband pipe 3.The port of export of described point of windband pipe 2 and a coal dust windband pipe 3 is provided with rotary wind guide grid 10.
nullDuring use,This device is installed in pulverized-coal fired boiler,It is electrolysed the hydrogen and oxygen of water by electrolytic water oxyhydrogen generator 6 and sends into burner plate 8 by being electrolysed aquatic product hydrogen or oxygen gas pipe 5,The burning column of flame 9 being made up of special refractory material sprays,After being ignited by electronic-igniting device,Coal dust-air mixture passes through to hold together combustion pipe 4 and a coal dust windband pipe 3 simultaneously enters,Hold together to fire the coal dust in pipe 4-air mixture and be ignited into existing high-temperature region through oxyhydrogen flame,Hold together to fire coal dust-air mixture between pipe 4 and a coal dust windband pipe 3 to be also ignited behind high-temperature region,And then expand burning step by step,Coal dust-air the mixture of burning is sufficiently mixed with secondary air under the effect of rotary wind guide grid 10,Improve efficiency of combustion,And secondary air point between windband pipe 2 with tubular shell 1 and a coal dust wind mix and can extend the length of flame,When fire box temperature reaches to throw powder temperature,Close lioh hydrolysis generator 6.
The invention has the beneficial effects as follows that the hydrogen or oxygen gas produced by lighting hydro-electrolytic hydroxide generator ignites coal dust so that it is trouble-free burning heat release and sufficiently reliable firing power is provided;Economic and environment-friendly, safe and reliable.In short supply at current crude resources, expensive in the case of, the present invention had both saved country's crude resources, and the cost decreasing enterprise puts into, and is one and is beneficial to current, was beneficial to again following invention.
These are only presently preferred embodiments of the present invention, not in order to limit the present invention, all within the spirit and principles in the present invention, any modification, equivalent substitution and improvement etc. made, should be included within the scope of the present invention.
Claims (3)
1. a hydrogen and oxygen electrolyzing gas ignition coal burner, it includes tubular shell, burner plate, electrolysis aquatic product hydrogen or oxygen gas pipe and holds together combustion pipe, it is characterized in that: in described tubular shell, be set with a coal dust windband pipe, in a coal dust windband pipe, it is set with combustion pipe, the burner plate of the band burning column of flame it is provided with in holding together to fire pipe, this burning column of flame is perpendicular to the direct of travel of coal dust-air mixture, and the burning column of flame is connected with lioh hydrolysis generator by being electrolysed aquatic product hydrogen or oxygen gas pipe;It is communicated with secondary wind inleting tube on described tubular shell.
Hydrogen and oxygen electrolyzing gas ignition coal burner the most according to claim 1, it is characterised in that: it is additionally provided with a point windband pipe between described tubular shell and a coal dust windband pipe.
Hydrogen and oxygen electrolyzing gas ignition coal burner the most according to claim 2, it is characterised in that: the port of export of described point of windband pipe and a coal dust windband pipe is provided with rotary wind guide grid.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201610081600.4A CN105716076A (en) | 2016-02-05 | 2016-02-05 | Electrolysis oxy-hydrogen gas pulverized coal igniting burner |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610081600.4A CN105716076A (en) | 2016-02-05 | 2016-02-05 | Electrolysis oxy-hydrogen gas pulverized coal igniting burner |
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CN105716076A true CN105716076A (en) | 2016-06-29 |
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Family Applications (1)
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CN201610081600.4A Pending CN105716076A (en) | 2016-02-05 | 2016-02-05 | Electrolysis oxy-hydrogen gas pulverized coal igniting burner |
Country Status (1)
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107869731A (en) * | 2017-10-12 | 2018-04-03 | 国网河北能源技术服务有限公司 | A kind of wind curtain type water power of pulverized-coal fired boiler is vented one's spleen igniter |
CN113958950A (en) * | 2021-11-15 | 2022-01-21 | 上海电力大学 | Device for coal and hydrogen oxygen synergistic strengthening and stable combustion of coal-fired power plant |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
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JP2000257811A (en) * | 1999-03-03 | 2000-09-22 | Hitachi Ltd | Method and device for burning pulverized coal, and pulverized coal burning burner |
CN1963310A (en) * | 2006-11-30 | 2007-05-16 | 艾佩克斯科技(北京)有限公司 | Micro-oil plasma composite ignition and combustion-stabilization method and device therefor |
CN201233008Y (en) * | 2008-07-02 | 2009-05-06 | 北京光耀电力设备有限公司 | Coal powder burner |
CN101532678A (en) * | 2009-03-02 | 2009-09-16 | 章礼道 | Brown gas (oxyhydrogen gas) ignition system of coal burning boiler of power plant |
CN202048592U (en) * | 2011-05-17 | 2011-11-23 | 北京京能热电股份有限公司 | Alternating-current plasma ignition device for coal-fired boiler in power plant |
CN202229181U (en) * | 2011-07-27 | 2012-05-23 | 北京远东四维系统工程技术有限公司 | Tiny-oil ignition and stable combustion device |
-
2016
- 2016-02-05 CN CN201610081600.4A patent/CN105716076A/en active Pending
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2000257811A (en) * | 1999-03-03 | 2000-09-22 | Hitachi Ltd | Method and device for burning pulverized coal, and pulverized coal burning burner |
CN1963310A (en) * | 2006-11-30 | 2007-05-16 | 艾佩克斯科技(北京)有限公司 | Micro-oil plasma composite ignition and combustion-stabilization method and device therefor |
CN201233008Y (en) * | 2008-07-02 | 2009-05-06 | 北京光耀电力设备有限公司 | Coal powder burner |
CN101532678A (en) * | 2009-03-02 | 2009-09-16 | 章礼道 | Brown gas (oxyhydrogen gas) ignition system of coal burning boiler of power plant |
CN202048592U (en) * | 2011-05-17 | 2011-11-23 | 北京京能热电股份有限公司 | Alternating-current plasma ignition device for coal-fired boiler in power plant |
CN202229181U (en) * | 2011-07-27 | 2012-05-23 | 北京远东四维系统工程技术有限公司 | Tiny-oil ignition and stable combustion device |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107869731A (en) * | 2017-10-12 | 2018-04-03 | 国网河北能源技术服务有限公司 | A kind of wind curtain type water power of pulverized-coal fired boiler is vented one's spleen igniter |
CN113958950A (en) * | 2021-11-15 | 2022-01-21 | 上海电力大学 | Device for coal and hydrogen oxygen synergistic strengthening and stable combustion of coal-fired power plant |
CN113958950B (en) * | 2021-11-15 | 2023-10-13 | 上海电力大学 | Device for coal-fired power plant coal-hydrogen-oxygen synergistic strengthening stable combustion |
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Effective date of registration: 20170419 Address after: 110000 Liaoning Province, Shenyang city Tiexi District Xunye four Road No. 14 2-3-3 Applicant after: Shi Xiang Address before: 110000 Dongping Lake Street, Yuhong District, Liaoning, China, No. 75, Applicant before: SHENYANG SHIDAI CLEANING ENERGY TECHNOLOGY CO., LTD. |
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Application publication date: 20160629 |