CN101182217A - Rich-oxygen and pure oxygen burning roller-way kiln - Google Patents
Rich-oxygen and pure oxygen burning roller-way kiln Download PDFInfo
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- CN101182217A CN101182217A CNA2007101686437A CN200710168643A CN101182217A CN 101182217 A CN101182217 A CN 101182217A CN A2007101686437 A CNA2007101686437 A CN A2007101686437A CN 200710168643 A CN200710168643 A CN 200710168643A CN 101182217 A CN101182217 A CN 101182217A
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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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P40/00—Technologies relating to the processing of minerals
- Y02P40/60—Production of ceramic materials or ceramic elements, e.g. substitution of clay or shale by alternative raw materials, e.g. ashes
Abstract
The invention provides an oxygen-enriched and total-oxygen burning roller kiln, comprising a preheating area (2), a sintering area (3), a fuel and combustion-support feeding system (4), a smoke exhaust system (5), a quench area, a cooling area, a temperature control system, a burning system and a waste heat system. The roller kiln is used for a combustion-supporting medium with the volume concentration of at least 21 percent of oxygen and the fuel to burn together inside a burner (6), no air combustion-supporting fan is required, the burner (6) is installed at the position of a burner brick (7). In order to solve the problem that the exhaust emission quantity of a ceramic roller kiln is large, the invention adopts the high concentration oxygen burning roller kiln which has high thermal efficiency, so compared with the combustion which considers the air as the combustion-supporting medium, the burning product quantity is reduced more than 50 percent, the nitrogen oxide produced by the invention is reduced greatly, the invention can reduce the energy consumption more than 10 percent, and the harmful substance emission can be reduced to the minimum.
Description
Technical field
The present invention relates to ceramic kiln, particularly relate to and a kind ofly comprise the roller kiln of high purity oxygen as combustion-supporting medium with high oxygen concentration.
Background technology
Global warming is on the rise, and the discharging of greenhouse gases has caused the concern of countries in the world and Chinese Government.The quickening of climate warming speed has seriously influenced expanding economy.China is the big producing country of world's pottery and refractory materials, and the ultimate production of pottery is near 50 percent of Gross World Product, and carbonic acid gas, oxynitride and exhaust gas discharging amount also are the rich anies influential family at world's ceramic industry.Just energy consumption, carbonic acid gas, oxynitride and the exhaust gas discharging amount of roller kiln and tunnel furnace have become the direction of countries in the world research and development to reduce pottery and refractory materials kiln.The burning of traditional industry stove is to be combustion-supporting medium with the air, the content of oxygen is 21% in the air, the content of nitrogen is 78%, be in the combustion processes of combustion-supporting medium with the air, burning produces hot a large amount of heated nitrogens that are used for, thermo-efficiency is low, and energy consumption is big, the products of combustion amount is big, and particularly the generation to the very harmful oxynitride of atmosphere is big.
Summary of the invention
Technical problem to be solved by this invention is: be energy consumption that solves above-mentioned existing industrial furnace and the products of combustion quantity discharged problem that reduces kiln, the spy provides a kind of oxygen enrichment and all-oxygen combustion roller kiln, these roller kiln are that the combustion system of combustion-supporting medium replaces with the combustion system of air as combustion-supporting medium with oxygen concn greater than 21% oxygen, thereby can reduce existing pottery and refractory materials kiln roller kiln products of combustion quantity discharged just greatly, energy consumption also reduces simultaneously.
The present invention solves the technical scheme that its technical problem adopts: provide a kind of combustion-supporting medium that is at least 21% oxygen with volumetric concentration to burn in burner with fuel, and do not need the oxygen enrichment and the all-oxygen combustion roller kiln of air-breathing blower fan.These roller kiln comprise heating zone, firing zone, quench zone, cooling area, fuel and combustion-supporting delivery system, temperature controlling system, firing system, fume exhaust system, waste heat system.Burner is installed in the burner block place.
The present invention is to provide with the high oxygen concentration is the oxygen enrichment and the all-oxygen combustion roller kiln (abbreviation kiln) of combustion-supporting medium, is that the ceramic kiln of air is compared with traditional employing combustion-supporting medium, has following major advantage:
One. is that the combustion system of combustion-supporting medium replaces with the combustion system of air as combustion-supporting medium with concentration greater than 21% oxygen, therefore the products of combustion of this kiln reduces more than 50% than traditional ceramic kiln, the total power of the fume exhaust system of this kiln is reduced greatly, volume also reduces more, to atmospheric quantity discharged bigger reduction is arranged.
They are two years old. and the high-temperature gas after the high-temperature gas after the burning of this kiln burns than traditional ceramic kiln is clean, so this kiln can be produced high-quality ceramic product.
They are three years old. and after combustion-supporting medium adopted high oxygen concentration, the preparation of oxygen and kiln can separate, so this kiln does not need burner blower, the noise of whole kiln decreases.
They are four years old. and when this kiln adopted the high oxygen concentration burning, the content of oxygen was greater than 21% in the combustion-supporting medium, and the content of nitrogen is less than 15%.Increase concentration of oxygen, thermo-efficiency will improve.Because concentration of oxygen and temperature of reaction are determining the physical-chemical reaction in the kiln, when oxygen concn increased, rate of oxidation increased, and was very beneficial for the oxidation of carbon in the base substrate, quickened the eliminating of carbon, quickened the burning of fuel and guaranteed that CO perfect combustion is CO
2, improve efficiency of combustion greatly, can reduce the firing period of burnt product simultaneously.
They are five years old. during the burning of this kiln oxygen, because the reduction of a nitrogen content in the combustion-supporting medium, under identical energy consumption, flame temperature raises, and the efficient of radiative transfer is just high in the kiln, and the volume of products of combustion reduces, reduced the thermosteresis that waste gas is taken away, so, improve outside the output except improving oxidizing reaction speed, also can improve the efficient of burner, reduce firing rate, cut down the consumption of energy, reduce quantity discharged, more uniform temperature in the kiln, product percent of pass is higher.
They are six years old. and when this kiln adopted the oxygen burning, the content of oxygen was greater than 21% in the combustion-supporting medium, and the content of nitrogen is less than 15%, and in products of combustion, the content of oxynitride is than reducing more than 60% with air during as combustion-supporting medium.
In a word, the present invention has adopted high oxygen concentration incendiary roller kiln for the big problem of discharge amount of exhaust gas that solves ceramic roller kiln, this roller kiln thermo-efficiency height, reduce more than 50% so the products of combustion amount is the burning of combustion-supporting medium than with the air, the oxynitride that produces reduces greatly, capable of reducing energy consumption more than 10%, can drop to lower-most point to the emission of harmful substances amount.
Description of drawings
Fig. 1 is the preheating zone 2 of oxygen enrichment of the present invention and all-oxygen combustion roller kiln and the layout synoptic diagram of firing zone 3.
Fig. 2 is an A-A sectional view among Fig. 1, and this figure has reflected the layout of the cross-section structure and the burner 6 of these roller kiln.
Among the figure: 1. kiln body; 2. preheating zone; 3. firing zone; 4. high oxygen concentration combustion-supporting medium and fuel channel; 5. fume exhaust system; 6. burner; 7. burner block; 8. fuel inlet; 9. combustion-supporting medium enters the mouth
Embodiment
The invention will be further described below in conjunction with embodiment and accompanying drawing, but do not limit the present invention.
Oxygen enrichment provided by the invention and all-oxygen combustion roller kiln, its structure is as shown in Figure 1 and Figure 2: be that a kind of combustion-supporting medium that is at least 21% oxygen with volumetric concentration burns in burner 6 with fuel, and do not need the oxygen enrichment and the all-oxygen combustion roller kiln of air-breathing blower fan; Burner 6 is installed in burner block 7 places.The kiln body 1 of these roller kiln comprises preheating zone 2, firing zone 3, fuel and combustion-supporting delivery system 4, fume exhaust system 5, quench zone, cooling area, temperature controlling system, firing system, and wherein preheating zone 2 links to each other with fuel channel 4 by the high oxygen concentration combustion-supporting medium with firing zone 3.
Described combustion-supporting medium, the content volume concentration of its oxygen is 21% to 99%; The content volume concentration of its nitrogen is at least less than 15%.
Described burner 6, burner block 7, it is arranged as shown in Figure 2: in the both sides up and down of kiln, be respectively equipped with several burners 6 and burner block 7, and burner 6 and burner block 7 mounted in pairing mode.Products of combustion sprays at a high speed in the kiln inner chamber of firing zone 3, in the heating burnt product, also hot gas in the kiln is stirred the companion, reduces the upper and lower temperature difference of kiln inner chamber, increases the temperature homogeneity of kiln inner chamber.Burner block 7 exit diameters are generally less than or equal 40mm.
The quench zone of oxygen enrichment of the present invention and all-oxygen combustion roller kiln, cooling area, waste heat system equal and existing wall floor tile roller kiln are identical, as identical with the wall floor tile roller kiln of Mona Lisa group.
Claims (3)
1. burning roller-way kiln, comprise preheating zone (2), firing zone (3), fuel and combustion-supporting medium delivery system (4), fume exhaust system (5), quench zone, cooling area, temperature controlling system, firing system, waste heat system, it is characterized in that described roller kiln are that a kind of combustion-supporting medium that is at least 21% oxygen with volumetric concentration burns in burner (6) with fuel, and do not need the oxygen enrichment and the all-oxygen combustion roller kiln of air-breathing blower fan; Burner (6) is installed in burner block (7) and locates.
2. burning roller-way kiln according to claim 1 is characterized in that described combustion-supporting medium, and the content volume concentration of its oxygen is 21% to 99%.
3. burning roller-way kiln according to claim 1 is characterized in that described combustion-supporting medium, and the content volume concentration of its nitrogen is at least less than 15%.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNA2007101686437A CN101182217A (en) | 2007-12-06 | 2007-12-06 | Rich-oxygen and pure oxygen burning roller-way kiln |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNA2007101686437A CN101182217A (en) | 2007-12-06 | 2007-12-06 | Rich-oxygen and pure oxygen burning roller-way kiln |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN101182217A true CN101182217A (en) | 2008-05-21 |
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| Application Number | Title | Priority Date | Filing Date |
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| CNA2007101686437A Pending CN101182217A (en) | 2007-12-06 | 2007-12-06 | Rich-oxygen and pure oxygen burning roller-way kiln |
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Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101344264B (en) * | 2008-08-22 | 2010-06-02 | 武汉理工大学 | Mixed combustion control system of oxygen-enriched and full-oxygen combustion ceramic roller kiln |
| CN101445372B (en) * | 2008-12-15 | 2012-05-23 | 王儒林 | Method for applying membrane oxygen enrichment technology in roller kiln |
| CN103134313A (en) * | 2011-12-02 | 2013-06-05 | 中国科学院金属研究所 | Low carbon and energy-saving gas heat treatment tunnel kiln |
| CN104792157A (en) * | 2015-03-31 | 2015-07-22 | 佛山市三水宏源陶瓷企业有限公司 | Low-emission ceramic roller kiln |
| CN104949505A (en) * | 2015-05-25 | 2015-09-30 | 绥阳县华夏陶瓷有限责任公司 | Oxygen-enriched combustion roller kiln system |
| CN107902698A (en) * | 2017-12-20 | 2018-04-13 | 四川省银河化学股份有限公司 | A kind of method for cleaning static continuous and automatic calcining production chrome oxide green |
| CN108716852A (en) * | 2018-06-13 | 2018-10-30 | 佛山市中晨窑炉设备有限公司 | A kind of kiln firing oxidation panel secondary combustion system |
| CN116398878A (en) * | 2023-06-01 | 2023-07-07 | 南京思墨能源科技有限公司 | Combined type total oxygen combustion system for steel rolling heating furnace and combustion method thereof |
-
2007
- 2007-12-06 CN CNA2007101686437A patent/CN101182217A/en active Pending
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101344264B (en) * | 2008-08-22 | 2010-06-02 | 武汉理工大学 | Mixed combustion control system of oxygen-enriched and full-oxygen combustion ceramic roller kiln |
| CN101445372B (en) * | 2008-12-15 | 2012-05-23 | 王儒林 | Method for applying membrane oxygen enrichment technology in roller kiln |
| CN103134313A (en) * | 2011-12-02 | 2013-06-05 | 中国科学院金属研究所 | Low carbon and energy-saving gas heat treatment tunnel kiln |
| CN104792157A (en) * | 2015-03-31 | 2015-07-22 | 佛山市三水宏源陶瓷企业有限公司 | Low-emission ceramic roller kiln |
| CN104949505A (en) * | 2015-05-25 | 2015-09-30 | 绥阳县华夏陶瓷有限责任公司 | Oxygen-enriched combustion roller kiln system |
| CN107902698A (en) * | 2017-12-20 | 2018-04-13 | 四川省银河化学股份有限公司 | A kind of method for cleaning static continuous and automatic calcining production chrome oxide green |
| CN107902698B (en) * | 2017-12-20 | 2023-07-21 | 四川省银河化学股份有限公司 | Method for producing chromium oxide green by clean static continuous automatic calcination |
| CN108716852A (en) * | 2018-06-13 | 2018-10-30 | 佛山市中晨窑炉设备有限公司 | A kind of kiln firing oxidation panel secondary combustion system |
| CN116398878A (en) * | 2023-06-01 | 2023-07-07 | 南京思墨能源科技有限公司 | Combined type total oxygen combustion system for steel rolling heating furnace and combustion method thereof |
| CN116398878B (en) * | 2023-06-01 | 2024-03-12 | 南京林普热能科技有限公司 | Combined type total oxygen combustion system for steel rolling heating furnace and combustion method thereof |
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Open date: 20080521 |