CN205261916U - 陶瓷热风炉的高效热能利用结构 - Google Patents
陶瓷热风炉的高效热能利用结构 Download PDFInfo
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- CN205261916U CN205261916U CN201520912345.4U CN201520912345U CN205261916U CN 205261916 U CN205261916 U CN 205261916U CN 201520912345 U CN201520912345 U CN 201520912345U CN 205261916 U CN205261916 U CN 205261916U
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- 239000002912 waste gas Substances 0.000 claims abstract description 22
- 239000000919 ceramic Substances 0.000 claims abstract description 17
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound 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[O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 8
- 238000010438 heat treatment Methods 0.000 claims abstract description 8
- 239000003546 flue gas Substances 0.000 claims abstract description 4
- 239000007789 gas Substances 0.000 claims description 17
- 239000000428 dust Substances 0.000 claims description 6
- 239000002699 waste material Substances 0.000 claims description 3
- 230000000694 effects Effects 0.000 abstract description 5
- 239000000446 fuel Substances 0.000 abstract description 3
- 239000003250 coal slurry Substances 0.000 abstract description 2
- 238000006213 oxygenation reaction Methods 0.000 abstract description 2
- 238000002485 combustion reaction Methods 0.000 abstract 1
- 239000000203 mixture Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 3
- 238000010583 slow cooling Methods 0.000 description 3
- FGIUAXJPYTZDNR-UHFFFAOYSA-N Potassium nitrate Chemical compound 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- 239000005864 Sulphur Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000003009 desulfurizing Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 238000005453 pelletization Methods 0.000 description 1
- 238000010791 quenching Methods 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
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
本实用新型公开了一种陶瓷热风炉的高效热能利用结构，包括从陶瓷窑炉延伸至热风炉下方的热气沟及废气沟，热风炉的炉顶与旋风除尘器连通，热气沟经风机向上与纵向的热气管连通，热气管与热风炉之间，从上到下经若干横向的分流管连通；热风炉的外壁从上到下，横向环绕有一根或两根以上废气的排气管，废气沟与每根排气管之间，以至少一根纵向的废气管连通,每根排气管与热风炉的内腔之间，以若干横向的小气管连通，所有小气管沿排气管的圆周均匀排布。上述结构能对热风炉中的水煤浆燃烧进行增氧助燃，并对热风炉中产生的热风实现增温，从而能减少燃料的消耗，达到非常良好的节能效果。
Description
技术领域
[0001]本实用新型涉及陶瓷设备，特别是一种陶瓷热风炉的高效热能利用结构。
背景技术
[0002]陶瓷窑炉依次包括干燥区、抽湿区、预热区、烧成区、急冷区、缓冷区和窑尾快冷区，陶瓷生产中，缓冷区和窑尾快冷区抽出的含氧量较高的热气，沿窑炉输送到起首的干燥区后，最后往往没有得到高效的利用，造成热能的大量浪费。
实用新型内容
[0003]本实用新型要解决的技术问题，是提供一种陶瓷热风炉的高效热能利用结构，能达到非常良好的节能效果。
[0004]为解决上述技术问题，本实用新型的技术方案为:提供一种陶瓷热风炉的高效热能利用结构，包括从陶瓷窑炉延伸至热风炉下方的热气沟及废气沟，热风炉的炉顶与旋风除尘器连通，热气沟经风机向上与纵向的热气管连通，热气管与热风炉之间，从上到下经若干横向的分流管连通；
[0005]热风炉的外壁从上到下，横向环绕有一根或两根以上废气的排气管，废气沟与每根排气管之间，以至少一根纵向的废气管连通，每根排气管与热风炉的内腔之间，以若干横向的小气管连通，所有小气管沿排气管的圆周均匀排布。
[0006]如上所述的陶瓷热风炉的高效热能利用结构，热气沟及废气沟均经自动或手动的控制阀门，与废气处理沟连通。
[0007]上述结构由于可利用输送至热气沟中的含氧量较高的热气，对热风炉中的水煤浆燃烧进行增氧助燃，并利用输送至废气沟中的部分高温废气，对热风炉中产生的热风实现增温，从而能减少燃料的消耗，达到非常良好的节能效果。
附图说明
[0008]下面结合附图和具体实施方式对本实用新型作进一步详细的说明。
[0009]图1为所述实施例的主视示意图；
[0010]图2为图1的A-A向剖视图；
[0011]图3为图1的B-B向剖视图。
具体实施方式
[0012]参见图1-图3，提供一种陶瓷热风炉的高效热能利用结构，包括从陶瓷窑炉延伸至热风炉下方的热气沟I及废气沟2，热风炉的炉顶与旋风除尘器3连通，热气沟I经风机4向上与纵向的热气管5连通，热气管5与热风炉之间，从上到下经四根横向的分流管6连通;热风炉的外壁从上到下，横向环绕有三根废气的排气管7，废气沟2与每根排气管7之间，以两根纵向的废气管8连通，每根排气管7与热风炉的内腔之间，以若干横向的小气管9连通，所有小气管9沿排气管7的圆周均匀排布。
[0013] 工作中:
[0014]缓冷区和窑尾快冷区抽出的含氧量较高的热气，沿窑炉传送至热气沟I中，经风机4抽至热气管5，再经四根分流管6输入热风炉内，可对热风炉中的水煤浆燃烧进行增氧助燃，从而能减少燃料的消耗，起到良好的节能作用，同时，从窑炉干燥区和抽湿区抽出的带有大量粉尘及含硫、硝等有害成份的高温废气，传送至废气沟2中，很大一部分经两根废气管8、三根排气管7及若干小气管9，排入热风炉中，一方面，对热风炉中产生的热风实现增温，同样有利于达到良好的节能效果，一方面，高温废气在热风炉内燃烧，可脱去一部分的硫、硝等有害成份。
[0015]由于上述热气经四根从上到下的分流管6，输入热风炉内，且三根排气管7在热风炉的外壁从上到下设置，且所有小气管9沿各排气管7的圆周均匀排布，因而热气及高温废气，能与热风均匀混合，热风增温非常迅速。混合后的热风经旋风除尘器3，除去水煤浆燃烧产生的一部分粉尘，从塔顶进入喷雾干燥塔，用于对陶瓷浆料进行干燥处理。
[0016] 参见图1，热气沟I及废气沟2均经自动或手动的控制阀门10，与废气处理沟11连通。陶瓷生产中，当传送至废气沟2中的热气量及废气量特别大时，控制阀门10可自动或手动打开，上述热风炉及喷雾干燥塔的工作过程中来不及处理的部分废气，会进入废气处理沟11，通过环保处理装置，例如干湿双重除尘系统、除硫塔，进行这部分废气的环保处理。
[0017]上述实施例为本实用新型的优选实施例，凡与本实用新型类似的结构及所作的等效变化，均应属于本实用新型的保护范畴。
Claims (2)
1.一种陶瓷热风炉的高效热能利用结构，包括从陶瓷窑炉延伸至热风炉下方的热气沟及废气沟，热风炉的炉顶与旋风除尘器连通，其特征在于:热气沟经风机向上与纵向的热气管连通，热气管与热风炉之间，从上到下经若干横向的分流管连通； 热风炉的外壁从上到下，横向环绕有一根或两根以上废气的排气管，废气沟与每根排气管之间，以至少一根纵向的废气管连通，每根排气管与热风炉的内腔之间，以若干横向的小气管连通，所有小气管沿排气管的圆周均匀排布。
2.根据权利要求1所述的陶瓷热风炉的高效热能利用结构，其特征在于:热气沟及废气沟均经自动或手动的控制阀门，与废气处理沟连通。
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