CN201293319Y - Flame adjustable single thermal storage burner - Google Patents
Flame adjustable single thermal storage burner Download PDFInfo
- Publication number
- CN201293319Y CN201293319Y CNU2008201000761U CN200820100076U CN201293319Y CN 201293319 Y CN201293319 Y CN 201293319Y CN U2008201000761 U CNU2008201000761 U CN U2008201000761U CN 200820100076 U CN200820100076 U CN 200820100076U CN 201293319 Y CN201293319 Y CN 201293319Y
- Authority
- CN
- China
- Prior art keywords
- air
- gas
- flame
- coal gas
- current divider
- Prior art date
Links
- 239000003570 air Substances 0.000 claims abstract description 82
- 239000003034 coal gas Substances 0.000 claims abstract description 47
- 239000007789 gases Substances 0.000 claims abstract description 29
- 239000011449 bricks Substances 0.000 claims abstract description 18
- 230000001172 regenerating Effects 0.000 claims description 12
- 238000005338 heat storage Methods 0.000 claims description 11
- 238000002485 combustion reactions Methods 0.000 abstract description 8
- 238000002156 mixing Methods 0.000 abstract description 7
- 238000009825 accumulation Methods 0.000 abstract description 6
- 238000005516 engineering processes Methods 0.000 abstract description 5
- 239000004566 building materials Substances 0.000 abstract description 3
- 238000005272 metallurgy Methods 0.000 abstract description 3
- 229910001874 nitric oxide Inorganic materials 0.000 abstract description 3
- 229910052813 nitrogen oxides Inorganic materials 0.000 abstract description 3
- 238000007254 oxidation reactions Methods 0.000 abstract description 3
- 208000008918 Voyeurism Diseases 0.000 abstract 2
- 280000858870 Chemical Engineering companies 0.000 abstract 1
- 281000066869 Coke (fuel) companies 0.000 abstract 1
- 238000003889 chemical engineering Methods 0.000 abstract 1
- 239000003345 natural gases Substances 0.000 abstract 1
- 239000003209 petroleum derivatives Substances 0.000 abstract 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound 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[O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 4
- 239000003546 flue gases Substances 0.000 description 4
- 230000001105 regulatory Effects 0.000 description 4
- 239000000446 fuels Substances 0.000 description 3
- 238000005039 chemical industry Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000000034 methods Methods 0.000 description 2
- 238000006722 reduction reactions Methods 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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[C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 238000006243 chemical reactions Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000010586 diagrams Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 238000005755 formation reactions Methods 0.000 description 1
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitric oxide Chemical compound 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O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 1
- GQPLMRYTRLFLPF-UHFFFAOYSA-N nitrous Oxide Chemical compound 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[O-][N+]#N GQPLMRYTRLFLPF-UHFFFAOYSA-N 0.000 description 1
- 239000003921 oils Substances 0.000 description 1
- 239000007921 sprays Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
Abstract
Description
Technical field
The utility model belongs to field of combustion technology, relate to have low Nox, a kind of adjustable flame single regenerative burner of function such as suboxides scaling loss, flame can be regulated.
Background technology
Heat-accumulation combustion (HTAC) technology can realize that the limit of fume afterheat reclaims, and has energy-efficient and multiple advantage such as low pollution emission, can solve the contradiction of low yield and high consumption in the hot-working production process, is the advanced technology that satisfies current resource and environmental requirement.Single regenerative burner is generally used for the heat-accumulation combustion of middle and high calorific value of gas, has broad application prospects in industries such as metallurgy, building materials, chemical industry.
Most of industrial furnaces require characteristics such as furnace temperature height, temperature field uniformity height, thereby require heat-accumulating burner to possess performances such as high temperature resistant, corrosion-resistant, that flame status is good.At present, developed several single regenerative burners both at home and abroad, and dropped into industrial furnace and use, but had following technical barrier with own characteristic:
(1) existing single regenerative burner can not effectively solve the problem of air, coal gas mixing.
At present, the single regenerative burner of domestic and international design, air, coal gas have two kinds of hybrid modes, and a kind of is that coal gas passes through the middle ejection of high-temperature heat accumulation case from air port; Another kind is that coal gas certain position outside heat storage tank enters air port.The former advantage is to realize the even mixing of air, coal gas, and one of shortcoming is that gas pipe need pass through the high-temperature flue gas district, easy burn-out, even may cause leakage and the burning of coal gas in heat storage tank, damage heat storage or burner; Two of shortcoming is gas pipe problems in order to solve mixing and to cool off, and needs repeatedly air feed, pipeline and valve complexity before the burner, and cooling air has reduced fractional energy savings without accumulation of heat; Three of shortcoming is that gas-jet tube needs heatproof high, has increased cost of manufacture.The latter's advantage is effectively to have protected gas-jet tube, has reduced the use and the spoilage of heat resisting steel, reduced cost, but the mixed effect of its air and coal gas is relatively poor, and fired state is undesirable.
(2) existing single regenerative burner can not be realized the flame adjusting.Heat-accumulating burner is after completing, because solidify the shape of space gas spout and position, its flame profile, the length of flame all can't change, thereby heat-accumulating burner is little to the wide adaptability of stove, and the temperature field in the burner hearth is non-adjustable, and control of industrial furnace home is not high.
Summary of the invention
The purpose of this utility model provides a kind of adjustable flame single regenerative burner.Adjustable flame single regenerative burner is by mainly being made up of air heat storage tank, air duct, air port brick, ignition system and the flame system of spying on, the air port brick is provided with the tangential tiltedly spout of big straight spout and a plurality of annular configuration, the coal gas current divider is placed in the periphery of air duct, flame regulator is installed in the gas entry place of coal gas current divider, ignition system is placed in the end of coal gas current divider and leads to the space gas Mixed Zone, and the flame system of spying on is placed in the end of air duct.The utlity model has low Nox, low scaling loss, flame and characteristics such as can regulate, realized the even mixing of air, coal gas; Realized that fuel-staged combustion and flue gas entrainment the reduction reaction center district temperature that refluxes, and reduce the generation of nitrogen oxide; Realized that coal gas parcel air has reduced the scaling loss that is heated workpiece; Realized regulating of burner flame.
The purpose of this utility model realizes in the following way:
Cold air is flowed through and is become high-temperature hot air behind the heat storage in the air heat storage tank, and through spray orifice on the air port brick, becoming the center is direct current, is the air stream of multiply swirling eddy on every side.Coal gas is divided into two groups after entering the coal gas current divider, flow through respectively and be arranged in gas port on the current divider, two groups of coal gas streams that formation is circular layout, coal gas stream is when the air duct outer wall enters inwall, and one group of angle is bigger, and one group of angle is less, ring gas is wrapped in the outside of rotary air stream, realized the parcel of coal gas, obtained reducing atmosphere flame, reduced the heated parts oxidization burning loss air.Simultaneously, two groups of coal gas streams cross in different positions and air stream, under the stirring of rotary air stream, have realized that empty, coal gas mixes more uniformly, fractional combustion and the flue gas of also having realized fuel entrainment the reduction of backflow to reaction center district temperature, reduce the generation of nitrogen oxide.
Flame regulator is arranged on coal gas splitter inlet place, by regulating the valve plate aperture, changes the gas flow that enters each group, reaches the purpose of regulating flame; Ignition system is used for a burner, and the flame system of spying on is used to observe the burner working condition.
Description of drawings
Accompanying drawing 1 is a structural representation of the present utility model
Accompanying drawing 2 is that ignition system and flame regulator are arranged schematic diagram
Among the figure, part 1 is that air heat storage tank, part 2 are the air port brick for air duct, part 3, and part 4 is spied on system for ignition system, part 7 for flame for flame regulator, part 6 for coal gas current divider, part 5.
The specific embodiment
Be described further of the present invention below in conjunction with accompanying drawing:
Air heat storage tank 1 one ends are connected with air intake, the other end is connected with air duct 2, air port brick 3 is placed in the air duct 2, coal gas current divider 4 is placed in the outside of air duct 2, flame regulator 5 is installed in the gas entry place of coal gas current divider 4, ignition system 6 is placed in the end of coal gas current divider 4 and leads to the space gas Mixed Zone at air port brick 3 rear portions, and flame is spied on the end that system 7 is placed in air duct.Air port brick 3 centers are provided with big straight spout, are provided with the oblique spout of a plurality of annular configuration all around; Coal gas current divider 4 be provided with a plurality of evenly, the gas port of annular configuration, the coal gas stream that comes out from coal gas current divider 4 is divided into two groups, wherein one group of angle of cut inclination angle with air stream is β 1, and other one group of angle of cut inclination angle with air stream is β 2, and β 2 is greater than β 1.
Enter cold air of the present utility model from air intake, finish heat exchanging process behind the hole of heat storage in by air heat storage tank 1, be heated to form 900～1050 ℃ hot-air, hot-air continues to flow forward, is further heated by air duct 2 inwalls; When hot-air passes through air port brick 3, quickened and the change directions by the apertures that are provided with in the air port brick 3, a part of straight hole by the center becomes straight air stream, and a part becomes rotary air and flows by tangential hole; Coal gas enters gas entry, after flowing through flame regulator 5, be divided into two strands, enter respectively in each shunt group of coal gas current divider 4, after the little spout that is provided with in current divider 4 quickens, shunts, the coal gas stream that comes out from coal gas current divider 4 just becomes two groups of porous, high velocity air, and wherein one group of inclination angle is β 1, and other one group angle of cut inclination angle is β 2, these two groups of air-flows cross with the air stream that comes out from air port brick 3 in different positions, have realized that the fractional combustion of fuel and flue gas entrainment backflow.
By the multiply coal gas stream that coal gas current divider 4 produces, annular is wrapped in the periphery of air stream, annular airflow has increased the contact area of air, coal gas, has strengthened the mixing of air, coal gas.Coal gas stream at first crosses with the rotary air stream of air port brick 3 peripheries, produces reducing atmosphere flame, has reduced the oxidization burning loss that is heated workpiece, reducibility gas further with the direct current air mixed combustion at air port brick 3 centers, until after-flame.
Gas port does not directly pass through high temperature air passage 2, but enters inner chamber from the outer wall of air duct 2, has a little to contact in air port brick 3 exits with high temperature air stream, has improved the service life of gas-jet.
After air port brick 3 damages, can directly spy on the maintenance fire door turnover of settling at system 7 places, realize the quick replacing of consumable accessory by flame.
Ignition system 6 provides incendiary source, and incendiary source can be the band igniter burner of igniting automatically, also can be the fire hole that the igniter access way only is provided.
Spy on system 7 from flame and observe the flame burning situation, regulate the valve plate aperture of flame regulator 5, change enters the gas flow of each coal flow groups, thereby changes the flow size of different inclination angle coal gas stream, change the opportunity of air, coal gas mixing, realize the adjusting of flame profile.
The utility model can be widely used in the heat-processing equipment of a plurality of kinds of industries such as metallurgy, building materials, machinery, chemical industry, can gas-firing, multiple gases fuel such as hot dirty producer gas, coke-stove gas, mixed gas, oil gas, be a kind of novel burner of safe, efficient, energy-saving and environmental protection.
Claims (3)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008201000761U CN201293319Y (en) | 2008-09-23 | 2008-09-23 | Flame adjustable single thermal storage burner |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008201000761U CN201293319Y (en) | 2008-09-23 | 2008-09-23 | Flame adjustable single thermal storage burner |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201293319Y true CN201293319Y (en) | 2009-08-19 |
Family
ID=41006798
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2008201000761U CN201293319Y (en) | 2008-09-23 | 2008-09-23 | Flame adjustable single thermal storage burner |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201293319Y (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101639218B (en) * | 2009-09-01 | 2011-08-31 | 顾向涛 | Flameless combustion heat accumulating type flat flame combustion nozzle |
| CN102777915A (en) * | 2012-07-19 | 2012-11-14 | 马鞍山天洲节能工程科技有限公司 | Circumferentially distributed burner of natural gas channels |
| CN103939902A (en) * | 2013-01-18 | 2014-07-23 | 福建三能节能科技有限责任公司 | High-efficient energy-saving environmental protection type heat-storage flat flame combustor and combustion method thereof |
| CN104390460A (en) * | 2014-11-14 | 2015-03-04 | 北京神雾环境能源科技集团股份有限公司 | Heat accumulating type combustion device for bogie hearth furnace |
| CN110848675A (en) * | 2019-11-29 | 2020-02-28 | 朱冲 | Novel heat accumulating type combustor with sealing structure |
-
2008
- 2008-09-23 CN CNU2008201000761U patent/CN201293319Y/en not_active IP Right Cessation
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101639218B (en) * | 2009-09-01 | 2011-08-31 | 顾向涛 | Flameless combustion heat accumulating type flat flame combustion nozzle |
| CN102777915A (en) * | 2012-07-19 | 2012-11-14 | 马鞍山天洲节能工程科技有限公司 | Circumferentially distributed burner of natural gas channels |
| CN103939902A (en) * | 2013-01-18 | 2014-07-23 | 福建三能节能科技有限责任公司 | High-efficient energy-saving environmental protection type heat-storage flat flame combustor and combustion method thereof |
| CN104390460A (en) * | 2014-11-14 | 2015-03-04 | 北京神雾环境能源科技集团股份有限公司 | Heat accumulating type combustion device for bogie hearth furnace |
| CN110848675A (en) * | 2019-11-29 | 2020-02-28 | 朱冲 | Novel heat accumulating type combustor with sealing structure |
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