CN103343965A - Heating furnace system with oxygen-enriched combustion - Google Patents
Heating furnace system with oxygen-enriched combustion Download PDFInfo
- Publication number
- CN103343965A CN103343965A CN2013102939626A CN201310293962A CN103343965A CN 103343965 A CN103343965 A CN 103343965A CN 2013102939626 A CN2013102939626 A CN 2013102939626A CN 201310293962 A CN201310293962 A CN 201310293962A CN 103343965 A CN103343965 A CN 103343965A
- Authority
- CN
- China
- Prior art keywords
- gas
- combustion
- oxygen
- supporting
- enriched
- 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.)
- Granted
Links
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 title claims abstract description 78
- 239000001301 oxygen Substances 0.000 title claims abstract description 78
- 229910052760 oxygen Inorganic materials 0.000 title claims abstract description 78
- 238000002485 combustion reaction Methods 0.000 title claims abstract description 26
- 238000010438 heat treatment Methods 0.000 title claims abstract description 23
- 239000007789 gas Substances 0.000 claims abstract description 107
- 239000003034 coal gas Substances 0.000 claims description 24
- 229910000831 Steel Inorganic materials 0.000 claims description 14
- 239000010959 steel Substances 0.000 claims description 14
- 238000005096 rolling process Methods 0.000 claims description 7
- 238000000034 method Methods 0.000 claims description 4
- 238000005516 engineering process Methods 0.000 abstract description 7
- 238000004519 manufacturing process Methods 0.000 abstract description 6
- 230000001105 regulatory effect Effects 0.000 abstract description 6
- 230000000694 effects Effects 0.000 abstract description 2
- 238000004134 energy conservation Methods 0.000 abstract description 2
- 239000006227 byproduct Substances 0.000 description 5
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 3
- 239000003546 flue gas Substances 0.000 description 3
- 230000005855 radiation Effects 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 239000003345 natural gas Substances 0.000 description 2
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 2
- 239000000779 smoke Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000005242 forging Methods 0.000 description 1
- 238000005338 heat storage Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000001172 regenerating effect Effects 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
Images
Classifications
-
- 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
Abstract
The invention relates to a heating furnace system with oxygen-enriched combustion. The heating furnace system comprises a gas pipeline system, a combustion-supporting gas pipeline system, a gas heat exchanger (12), a combustion-supporting gas heat exchanger (13), a combustion system and a furnace body (14), wherein the combustion system comprises an oxygen-enriched combustor (15), a combustion-supporting gas regulating valve (16), a gas regulating valve (17) and a control system; gas introduced into the gas pipeline system is preheated through the gas heat exchanger (12) and then is introduced into the oxygen-enriched combustor (15); combustion-supporting gas introduced into the combustion-supporting gas pipeline system is preheated through the combustion-supporting gas heat exchanger (13) and then is introduced into the oxygen-enriched combustor (15); the supply flow of the gas and the combustion-supporting gas is regulated through the combustion-supporting gas regulating valve (16), the gas regulating valve (17) and the combustor control system. By virtue of the oxygen-enriched combustion technology, the effective utilization of low-heat value gas can be realized, and the heating furnace system is higher in efficiency and has the better effects of energy conservation and environment protection; meanwhile, the heating furnace system with oxygen-enriched combustion is simple, low in manufacturing cost and high in production stability.
Description
Technical field
The present invention relates to the heating furnace technical field, more particularly, relate to a kind of reheat furnace system that utilizes oxygen-enriched combustion technology.
Background technology
At present, heating furnace is widely used in billet rolling, the forging line.Utilize heating furnace that steel billet is heated, burn till red steel, it is reached satisfy rolling, as to forge needs steel billet temperature, then be rolled or forge.In China, the heating furnace One's name is legion, the traditional heating stove modes that adopt conventional diffusion combustion more, the energy consumption height, seriously polluted.
In recent years, developed regenerative combustion technology at heater for rolling steel, recuperative heater can be applied to heater for rolling steel with iron and steel enterprise's by-product blast furnace gas, has saved high heating value fat coal gas such as natural gas, coke-stove gas, has realized effective utilization of by-product blast furnace gas.But still there are many shortcomings in recuperative heater: (1) power consumption is higher, a large amount of electric energy of its hold over system reversal valve frequent operation consumption, and the more powerful air-introduced machine of system configuration also consumes a large amount of electric energy; (2) reversal valve, heat storage weak point in service life are changed frequently, have increased production cost, have reduced operational use time; (3) CO content is higher in the smoke evacuation, the coal gas side smoke evacuation of especially two thermal storage heating stoves, and its CO content is up to several thousand ppm, and is local even surpass 10,000 ppm, serious environment pollution.
Summary of the invention
The technical problem to be solved in the present invention is, the reheat furnace system that utilizes oxygen-enriched combustion technology of a kind of burning highly effective, energy-conserving and environment-protective is provided, and can realize effective utilization of low-heat value gas.
The technical solution adopted for the present invention to solve the technical problems is: construct a kind of reheat furnace system that utilizes oxygen-enriched combusting, comprise the gaspipe line system, combustion-supporting air pipe system, gas change heater, combustion-supporting gas heat exchanger, combustion system and body of heater, described combustion system comprises oxygen-enriched burner, help gas control valve, gas regulator and control system, feed in the oxygen-enriched burner after the coal gas process gas change heater preheating that the gaspipe line system feeds, the combustion-supporting gas that combustion-supporting air pipe system feeds feeds in the oxygen-enriched burner, by the described gas control valve that helps after through the preheating of combustion-supporting gas heat exchanger, gas regulator and burner control system are regulated the infeed flow of coal gas and combustion-supporting gas.
In the reheat furnace system that utilizes oxygen-enriched combusting of the present invention, described gaspipe line system comprises gaspipe line and is arranged on gas valve on the described gaspipe line that described gaspipe line is connected with described gas change heater.
In the reheat furnace system that utilizes oxygen-enriched combusting of the present invention, described combustion-supporting air pipe system comprises combustion-supporting air pipe and first oxygen valve, second oxygen valve and the air door that are connected with described combustion-supporting air pipe respectively, described first oxygen valve is connected with the oxygen pipe network, described second oxygen valve is connected with the oxygenerator group, and described air door is connected with combustion fan.
In the reheat furnace system that utilizes oxygen-enriched combusting of the present invention, the oxygen concentration scope of carrying in the described combustion-supporting air pipe system is 21～60%.
In the reheat furnace system that utilizes oxygen-enriched combusting of the present invention, described body of heater is provided with flue, and described gas change heater and combustion-supporting gas heat exchanger are connected with described flue.
In the reheat furnace system that utilizes oxygen-enriched combusting of the present invention, described combustion-supporting gas heat exchanger is pipe heat exchanger, plate type heat exchanger or heat exchange of heat pipe.
In the reheat furnace system that utilizes oxygen-enriched combusting of the present invention, described gas change heater be pipe heat exchanger, plate type heat exchanger or heat exchange of heat pipe.
In the reheat furnace system that utilizes oxygen-enriched combusting of the present invention, the coal gas that feeds in the described gaspipe line system is mixed gas, coal gas of converter or blast furnace gas.
In the reheat furnace system that utilizes oxygen-enriched combusting of the present invention, described body of heater is heater for rolling steel, rotary heating furnace or forge furnace.
Implement the reheat furnace system that the present invention utilizes oxygen-enriched combusting, have following beneficial effect:
1, the present invention adopts oxygen-enriched combustion technology, efficient more, energy-saving and environmental protection.
2, utilize oxygen-enriched combusting and combustion-supporting gas, gas double pre-heating mode that low-heat value gas such as blast furnace gas, coal gas of converter, mixed gas are applied to the heating furnace burning, realize effective utilization of steel plant's by-product low-heat value gas, save high heating value fat coal gas such as natural gas, coke-stove gas.
3, the present invention utilizes the reheat furnace system of oxygen-enriched combusting simple, low cost of manufacture, and production stability is good.
Description of drawings
The invention will be further described below in conjunction with drawings and Examples, in the accompanying drawing:
Fig. 1 is the structural representation that the present invention utilizes the reheat furnace system of oxygen-enriched combusting.
The specific embodiment
Understand for technical characterictic of the present invention, purpose and effect being had more clearly, now contrast accompanying drawing and describe the specific embodiment of the present invention in detail.
As shown in Figure 1, the present invention utilizes the reheat furnace system of oxygen-enriched combusting to comprise gaspipe line system, combustion-supporting air pipe system, gas change heater 12, combustion-supporting gas heat exchanger 13, combustion system and body of heater 14.
Combustion system comprises oxygen-enriched burner 15, helps gas control valve 16, gas regulator 17 and control system.Feed in the oxygen-enriched burner 15 after coal gas process gas change heater 12 preheatings that feed in the gaspipe line system, coal gas can be low-heat value gas such as mixed gas, coal gas of converter or blast furnace gas.The combustion-supporting gas that combustion-supporting air pipe system feeds is through feeding in the oxygen-enriched burner 15 after combustion-supporting gas heat exchanger 13 preheatings, and combustion-supporting gas is oxygen-enriched air.Coal gas and combustion-supporting gas mix after-combustion in oxygen-enriched burner 15.Regulate the infeed flow of coal gas and combustion-supporting gas by helping gas control valve 16, gas regulator 17 and burner control system.Every heating furnace arranges the number of oxygen-enriched burner 15 and determines according to heating furnace production capacity and body of heater 14 sizes.Body of heater 14 can be the heating furnace of various steel billets such as heater for rolling steel, rotary heating furnace or forge furnace, steel part.
The present invention utilizes coal gas in the reheat furnace system of oxygen-enriched combusting, the two preheatings of combustion-supporting gas, and the burning form is oxygen-enriched combusting, can improve the ignition temperature of coal gas and the radiation intensity of flue gas, has characteristics such as efficient, energy-conservation, low-nitrogen oxide discharging.According to heating furnace technology needs, rational coal gas, combustion-supporting gas preheat temperature are set, ignition temperature and gas radiation intensity that rational combustion-supporting gas oxygen concentration can improve low-heat value gas such as blast furnace gas, coal gas of converter are set, thereby steel plant's by-product low-heat value gas such as blast furnace gas, coal gas of converter can be applied in the heating furnace, realize efficient application and the energy-saving and emission-reduction of steel plant's by-product low-heat value gas.
Further, the gaspipe line system comprises gaspipe line 8 and the gas valve 9 that is arranged on the gaspipe line 8, and gaspipe line 8 is connected with gas change heater 12.Gaspipe line 8 is connected with gaspipe network 10.Coal gas is heated in gas change heater 12 more than 200 ℃, supplies in the combustion system through gaspipe line 8 then.
Further, combustion-supporting air pipe system comprises combustion-supporting air pipe 7 and first oxygen valve 2 that is connected with combustion-supporting air pipe 7 respectively, second oxygen valve 6 and air door 3, first oxygen valve 2 is connected with oxygen pipe network 1, second oxygen valve 6 is connected with oxygenerator group 5, and air door 3 is connected with combustion fan 4.Producing the oxygen of oxygen-enriched air can supply with by oxygen pipe network 1, also can produce by oxygenerator group 5 is set.Oxygen mixes in pipeline with the air that combustion fan 4 is supplied with, and obtains oxygen-enriched air.Combustion-supporting air pipe system comprises first oxygen valve 2, oxygenerator group 5, second oxygen valve 6, air door 3, combustion fan 4 and combustion-supporting air pipe 7.Oxygen-enriched air is as the combustion-supporting gas of burning, and the oxygen of oxygenerator group 5 or oxygen pipe network 1 mixes in pipeline with the air that combustion fan 4 is supplied with, and obtains oxygen-enriched air.Combustion-supporting gas feeds in the combustion-supporting gas heat exchanger 13 through combustion-supporting air pipe 7, and combustion-supporting gas is heated to more than 300 ℃ in combustion-supporting gas heat exchanger 13, supplies in the combustion system through combustion-supporting air pipe 7 then.
Further, the oxygen concentration scope of carrying in the combustion-supporting air pipe system is 21～60%, can improve ignition temperature and the gas radiation intensity of low-heat value gas such as blast furnace gas, coal gas of converter greatly.
Further, body of heater 14 is provided with flue 11, and gas change heater 12 and combustion-supporting gas heat exchanger 13 are connected with flue 11.Discharging flue gas from body of heater 14 at first is preheated to combustion-supporting gas more than 300 ℃ by combustion-supporting gas heat exchanger 13, then by gas change heater 12 with more than the gas preheating to 200 ℃, temperature is down to below 300 ℃ after the heat exchange of flue gas process two-stage, discharges through air-introduced machine or chimney, has reduced thermal pollution.
Further, combustion-supporting gas heat exchanger 13 and gas change heater 12 are the heat exchanger of forms such as pipe heat exchanger, plate type heat exchanger or heat exchange of heat pipe.
By reference to the accompanying drawings embodiments of the invention are described above; but the present invention is not limited to the above-mentioned specific embodiment; the above-mentioned specific embodiment only is schematic; rather than it is restrictive; those of ordinary skill in the art is under enlightenment of the present invention; not breaking away under the scope situation that aim of the present invention and claim protect, also can make a lot of forms, these all belong within the protection of the present invention.
Claims (9)
1. a reheat furnace system that utilizes oxygen-enriched combusting is characterized in that, comprises gaspipe line system, combustion-supporting air pipe system, gas change heater (12), combustion-supporting gas heat exchanger (13), combustion system and body of heater (14),
Described combustion system comprises oxygen-enriched burner (15), helps gas control valve (16), gas regulator (17) and control system, feed in the oxygen-enriched burner (15) after coal gas process gas change heater (12) preheating that the gaspipe line system feeds, the combustion-supporting gas that combustion-supporting air pipe system feeds feeds in the oxygen-enriched burner (15) after through combustion-supporting gas heat exchanger (13) preheating, by the described infeed flow that helps gas control valve (16), gas regulator (17) and burner control system to regulate coal gas and combustion-supporting gas.
2. the reheat furnace system that utilizes oxygen-enriched combusting according to claim 1, it is characterized in that, described gaspipe line system comprises gaspipe line (8) and is arranged on gas valve (9) on the described gaspipe line (8) that described gaspipe line (8) is connected with described gas change heater (12).
3. the reheat furnace system that utilizes oxygen-enriched combusting according to claim 1, it is characterized in that, described combustion-supporting air pipe system comprises combustion-supporting air pipe (7) and first oxygen valve (2) that is connected with described combustion-supporting air pipe (7) respectively, second oxygen valve (6) and air door (3), described first oxygen valve (2) is connected with oxygen pipe network (1), described second oxygen valve (6) is connected with oxygenerator group (5), and described air door (3) is connected with combustion fan (4).
4. the reheat furnace system that utilizes oxygen-enriched combusting according to claim 1 is characterized in that, the oxygen concentration scope of carrying in the described combustion-supporting air pipe system is 21～60%.
5. the reheat furnace system that utilizes oxygen-enriched combusting according to claim 1 is characterized in that, described body of heater (14) is provided with flue (11), and described gas change heater (12) and combustion-supporting gas heat exchanger (13) are connected with described flue (11).
6. the reheat furnace system that utilizes oxygen-enriched combusting according to claim 1 is characterized in that, described combustion-supporting gas heat exchanger (13) is pipe heat exchanger, plate type heat exchanger or heat exchange of heat pipe.
7. the reheat furnace system that utilizes oxygen-enriched combusting according to claim 1 is characterized in that, described gas change heater (12) be pipe heat exchanger, plate type heat exchanger or heat exchange of heat pipe.
8. the reheat furnace system that utilizes oxygen-enriched combusting according to claim 1 is characterized in that, the coal gas that feeds in the described gaspipe line system is mixed gas, coal gas of converter or blast furnace gas.
9. the reheat furnace system that utilizes oxygen-enriched combusting according to claim 1 is characterized in that, described body of heater (14) is heater for rolling steel, rotary heating furnace or forge furnace.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310293962.6A CN103343965B (en) | 2013-07-12 | 2013-07-12 | A kind of reheat furnace system utilizing oxygen-enriched combusting |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310293962.6A CN103343965B (en) | 2013-07-12 | 2013-07-12 | A kind of reheat furnace system utilizing oxygen-enriched combusting |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN103343965A true CN103343965A (en) | 2013-10-09 |
| CN103343965B CN103343965B (en) | 2016-04-20 |
Family
ID=49278781
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201310293962.6A Active CN103343965B (en) | 2013-07-12 | 2013-07-12 | A kind of reheat furnace system utilizing oxygen-enriched combusting |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN103343965B (en) |
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104748568A (en) * | 2015-04-03 | 2015-07-01 | 首钢总公司 | Heating method and system based on steel rolling heating furnace |
| CN105066114A (en) * | 2015-08-27 | 2015-11-18 | 四川德胜集团钒钛有限公司 | Boiler oxygen-enriched combustion system for power generation set |
| CN105241262A (en) * | 2015-11-03 | 2016-01-13 | 中冶东方工程技术有限公司 | Pure oxygen combustion and carbon dioxide capturing system and process of heating furnace |
| CN105953409A (en) * | 2016-06-27 | 2016-09-21 | 河南中托力合化学有限公司 | Vertical energy saving device for fuel gas heating medium furnace |
| CN106545846A (en) * | 2015-09-17 | 2017-03-29 | 鞍钢股份有限公司 | A kind of low NO of heating furnacexFlue gas recirculation oxygen-enriched burning device and method |
| CN108893127A (en) * | 2018-07-03 | 2018-11-27 | 西安建筑科技大学 | A kind of method that routine internal heat type low-temperature dry distillation furnace transform oxygen-enriched gas retort as |
| CN109556416A (en) * | 2018-11-28 | 2019-04-02 | 重庆赛迪热工环保工程技术有限公司 | A kind of pure oxygen flue gas circular heating furnace control system and its control method |
| CN110145741A (en) * | 2019-06-03 | 2019-08-20 | 重庆赛迪热工环保工程技术有限公司 | A kind of oxygen-enriched burner suitable for a variety of calorific value of gas |
| CN110440593A (en) * | 2019-08-13 | 2019-11-12 | 蚌埠市昆宇机械加工厂 | A kind of glass processing heating device |
| CN111219994A (en) * | 2019-10-31 | 2020-06-02 | 鞍钢股份有限公司 | Oxygen-enriched combustion safety protection control method for heating furnace |
| CN115354142A (en) * | 2022-08-18 | 2022-11-18 | 重庆赛迪热工环保工程技术有限公司 | Combustion control method for heating furnace |
| CN115354140A (en) * | 2022-08-18 | 2022-11-18 | 重庆赛迪热工环保工程技术有限公司 | Oxygen-enriched heating furnace system and control process |
| CN116576683A (en) * | 2023-05-15 | 2023-08-11 | 广东维正环保机电工程有限公司 | Environment-friendly energy-saving system for graphite production |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101650133A (en) * | 2009-09-01 | 2010-02-17 | 北京沃克能源科技有限公司 | Recycling system of smoke gas energy for realizing high-temperature and low-oxygen combustion |
| CN102062394A (en) * | 2010-12-21 | 2011-05-18 | 鞍山普贝达科技有限公司 | Intensive oxygen enriched supply device for implementing oxygen enriched combustion of heating furnace |
| CN203454110U (en) * | 2013-07-12 | 2014-02-26 | 中冶南方(武汉)威仕工业炉有限公司 | Heating furnace system utilizing oxygen-enriched combustion |
-
2013
- 2013-07-12 CN CN201310293962.6A patent/CN103343965B/en active Active
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101650133A (en) * | 2009-09-01 | 2010-02-17 | 北京沃克能源科技有限公司 | Recycling system of smoke gas energy for realizing high-temperature and low-oxygen combustion |
| CN102062394A (en) * | 2010-12-21 | 2011-05-18 | 鞍山普贝达科技有限公司 | Intensive oxygen enriched supply device for implementing oxygen enriched combustion of heating furnace |
| CN203454110U (en) * | 2013-07-12 | 2014-02-26 | 中冶南方(武汉)威仕工业炉有限公司 | Heating furnace system utilizing oxygen-enriched combustion |
Cited By (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104748568A (en) * | 2015-04-03 | 2015-07-01 | 首钢总公司 | Heating method and system based on steel rolling heating furnace |
| CN105066114A (en) * | 2015-08-27 | 2015-11-18 | 四川德胜集团钒钛有限公司 | Boiler oxygen-enriched combustion system for power generation set |
| CN106545846A (en) * | 2015-09-17 | 2017-03-29 | 鞍钢股份有限公司 | A kind of low NO of heating furnacexFlue gas recirculation oxygen-enriched burning device and method |
| CN105241262A (en) * | 2015-11-03 | 2016-01-13 | 中冶东方工程技术有限公司 | Pure oxygen combustion and carbon dioxide capturing system and process of heating furnace |
| CN105953409A (en) * | 2016-06-27 | 2016-09-21 | 河南中托力合化学有限公司 | Vertical energy saving device for fuel gas heating medium furnace |
| CN108893127A (en) * | 2018-07-03 | 2018-11-27 | 西安建筑科技大学 | A kind of method that routine internal heat type low-temperature dry distillation furnace transform oxygen-enriched gas retort as |
| CN109556416A (en) * | 2018-11-28 | 2019-04-02 | 重庆赛迪热工环保工程技术有限公司 | A kind of pure oxygen flue gas circular heating furnace control system and its control method |
| CN110145741A (en) * | 2019-06-03 | 2019-08-20 | 重庆赛迪热工环保工程技术有限公司 | A kind of oxygen-enriched burner suitable for a variety of calorific value of gas |
| CN110440593A (en) * | 2019-08-13 | 2019-11-12 | 蚌埠市昆宇机械加工厂 | A kind of glass processing heating device |
| CN111219994A (en) * | 2019-10-31 | 2020-06-02 | 鞍钢股份有限公司 | Oxygen-enriched combustion safety protection control method for heating furnace |
| CN115354142A (en) * | 2022-08-18 | 2022-11-18 | 重庆赛迪热工环保工程技术有限公司 | Combustion control method for heating furnace |
| CN115354140A (en) * | 2022-08-18 | 2022-11-18 | 重庆赛迪热工环保工程技术有限公司 | Oxygen-enriched heating furnace system and control process |
| CN115354140B (en) * | 2022-08-18 | 2023-08-15 | 重庆赛迪热工环保工程技术有限公司 | Oxygen-enriched heating furnace system |
| CN115354142B (en) * | 2022-08-18 | 2023-11-28 | 重庆赛迪热工环保工程技术有限公司 | Combustion control method of heating furnace |
| CN116576683A (en) * | 2023-05-15 | 2023-08-11 | 广东维正环保机电工程有限公司 | Environment-friendly energy-saving system for graphite production |
Also Published As
| Publication number | Publication date |
|---|---|
| CN103343965B (en) | 2016-04-20 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103343965B (en) | A kind of reheat furnace system utilizing oxygen-enriched combusting | |
| CN110793032B (en) | Oxygen-enriched combustion system of heating furnace and control method thereof | |
| CN202012913U (en) | Novel flue gas self-reflux low-oxygen combustor | |
| CN204165045U (en) | Warm flue gas recirculation coal powder burner in one | |
| CN109945669B (en) | Method and system for recycling and burning oxygen-enriched flue gas of tempering furnace | |
| CN103363811A (en) | Combustion method of high-temperature oxygen-mixed flue gas | |
| CN105222585A (en) | The combustion-supporting energy-saving aluminium-melting furnace of small-sized flue gas | |
| CN105114951A (en) | Tail edge backflow dual-classification low-nitrogen-oxygen gas burner | |
| CN101839473A (en) | Flue gas recirculation high temperature air energy-saving and environmental protection combustion technology | |
| CN103088178B (en) | Blast furnace hot-blast stove flue gas self-circulation combustion method and system | |
| CN104728830A (en) | Compound recycling low-nitrogen combustion method for chain boiler | |
| CN203454110U (en) | Heating furnace system utilizing oxygen-enriched combustion | |
| CN103673592A (en) | Method and system for parallel preheating of fuel gas and combustion air for sintering ignition furnace | |
| CN203112858U (en) | Bleeding oxygen reutilization device in metallurgical production | |
| CN203373366U (en) | Hot-blast stove system for achieving high blast temperature by only burning blast furnace | |
| CN102721276B (en) | Energy-saving transformation system for ceramic kiln | |
| CN212581984U (en) | Energy-saving emission-reducing roasting system of belt type pellet roasting machine | |
| CN202912990U (en) | Hot blast stove system | |
| CN101928797A (en) | High-blast-temperature energy-saving and emission-reducing combined type preheating system for blast furnace | |
| CN209263628U (en) | A kind of disperse formula renewable aluminum raw material accumulation of heat smelting furnace | |
| CN102381830B (en) | A kind of method and system of supporting combustion by using oxygen-enriched air in production of float glass | |
| CN208038322U (en) | A kind of lime shaft kiln cooling air cyclic utilization system | |
| CN202692726U (en) | Heating combustion air equipment for ceramic kiln | |
| CN203174129U (en) | Flue gas self-circulation combustion system of blast furnace hot blast stove | |
| CN201867081U (en) | Waste heat utilization system for low-temperature smoke of heating furnace |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 430223 No. 33 University Park Road, Donghu Development Zone, Wuhan City, Hubei Province Patentee after: WISDRI (WUHAN) THERMAL INDUSTRY Co.,Ltd. Address before: 430223 No. 33 University Park Road, Donghu Development Zone, Wuhan City, Hubei Province Patentee before: WISDRI (WUHAN) WISFUR THERMAL TECHNOLOGY CO.,LTD. |
|
| CP01 | Change in the name or title of a patent holder | ||
| CP03 | Change of name, title or address |
Address after: 430223 No. 33 University Park Road, Donghu Development Zone, Wuhan City, Hubei Province Patentee after: WISDRI (WUHAN) WISFUR THERMAL TECHNOLOGY CO.,LTD. Address before: 430205 No. 33 University Park Road, Donghu New Technology Development Zone, Wuhan City, Hubei Province Patentee before: WISDRI (WUHAN) WIS INDUSTRIAL FURNACE Co.,Ltd. |
|
| CP03 | Change of name, title or address |