CN207514925U - 一种泥饼用流化床干化焚烧炉 - Google Patents
一种泥饼用流化床干化焚烧炉 Download PDFInfo
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- CN207514925U CN207514925U CN201721533839.7U CN201721533839U CN207514925U CN 207514925 U CN207514925 U CN 207514925U CN 201721533839 U CN201721533839 U CN 201721533839U CN 207514925 U CN207514925 U CN 207514925U
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- 239000012530 fluid Substances 0.000 title claims abstract description 20
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- 239000004744 fabric Substances 0.000 claims abstract description 37
- 239000000463 material Substances 0.000 claims abstract description 7
- 239000004576 sand Substances 0.000 claims abstract description 6
- 238000000034 method Methods 0.000 abstract description 5
- 239000010865 sewage Substances 0.000 abstract description 2
- 239000007789 gas Substances 0.000 description 20
- 239000010802 sludge Substances 0.000 description 9
- 238000001035 drying Methods 0.000 description 7
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound 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- 206010021143 Hypoxia Diseases 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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Abstract
本实用新型公开了一种泥饼用流化床干化焚烧炉，包括炉体，炉体内的布风板将炉体内腔分隔为上燃烧腔和下进气腔，下进气腔与进气管和主燃烧器连通，上燃烧腔的炉体侧壁上设置有焚烧物料的进料口和炉渣的排渣口，布风板上设置有砂层，进料口下方设置有布气环，布气环的环面上设置有若干个排气孔；布气环将上燃烧腔分隔为干化燃烧区和位于干化燃烧区上方的二次燃烧区，干化燃烧区的炉体侧壁上连通有水汽导出管，布气环通过管道与鼓风机相通。该泥饼用流化床干化焚烧炉在进料口下方设置布气环，通过调节燃烧器和空气流量的大小，是焚烧炉兼具干化泥饼和焚烧泥饼双重功能，尤其适用于污水处理过程中的小批量泥饼的焚烧处理。
Description
一种泥饼用流化床干化焚烧炉
技术领域
[0001] 本实用新型涉及废水处理技术领域，具体涉及一种泥饼用流化床干化焚烧炉。
背景技术
[0002] 污泥焚烧是指在500-100(TC下，污泥固形物在无氧气或者低氧气氛中分解气体、 焦油及灰分的过程。污泥焚烧的对象为脱水泥饼。工业废水处理过程中所产生的污泥、废 渣、废气最终均需要导入到焚烧炉中进行焚烧，其中的污泥需要预先经过压滤机或者其他 等效设备压制成泥饼。现有技术中泥饼的含水率为45-86%，干燥后的污泥含水率可降至20-40%，含水量过大不利于泥饼的充分燃烧。
[0003] 现有技术中通常采用先干化后焚烧的处理，但是干化过程中能耗大，改进的技术 方案如CN20〇986l95、CN2〇39〇7628U等多篇专利文献中公开的，将焚烧炉产生的烟气导入到 换热机构对泥饼进行预烘干化处理，或者采用具有往复炉排片的焚烧炉，利用往复炉排片 的结构不同，对初入焚烧炉的泥饼进行干化。上述两种结构的焚烧炉结构较复杂，设备占地 面积大，往复炉排片的焚烧炉炉排片使用寿命低，一般多用于焚烧水分和灰分较高、热值较 低（12560kJ/kg)的劣质煤和一般易结焦的煤。相较而言，废水处理厂实际所采用的焚烧炉 处理量较小。
[0004] 《环境工程》2004年6月第22卷第3期“流化床焚烧炉污泥焚烧工艺特性研究”指出， 流化床形焚烧炉燃烧进料适用范围广、在处理含油污泥过程中安全系数高，为废水处理厂 的常用机型，并公开了常用极性的结构。现有技术中的流化床焚烧炉也进针对脱水物料，对 于含有一定水分的物料，同样需要经过预先处理，设备之间的物料转运需要耗费大量的人 工，生产效率较差。 实用新型内容
[0005]本实用新型的目的在于克服现有技术中存在的缺陷，提供一种泥饼用流化床干化 焚烧炉，该焚烧炉可分步实现泥饼的干化以及焚烧处理。
[0006]为实现上述技术效果，本实用新型的技术方案为:一种泥饼用流化床干化焚烧炉， 包括炉体，炉体内的布风板将炉体内腔分隔为上燃烧腔和下进气腔，下进气腔与进气管和 主燃烧器连通，上燃烧腔的炉体侧壁上设置有焚烧物料的进料口和炉渣的排渣口，布风板 上设置有砂层，其特征在于，进料口下方设置有布气环，布气环的环面上设置有若干个排气 孔;布气环将上燃烧腔分隔为干化燃烧区和位于干化燃烧区上方的二次燃烧区，干化燃烧 区的炉体侧壁上连通有水汽导出管，布气环通过管道与鼓风机相通。
[0007]将泥饼直接进料至炉体干化燃烧区中，由于下进气腔与空气的进气管和主燃烧器 相连通，通过调节主燃烧器的燃烧物质流量和空气流量，使干化燃烧区中的泥饼升温脱水， 布气环喷射出气流可控制含有水蒸气的湿气流上升至二次燃烧区中，最终湿气流经由水汽 导出管排出，同时还可以增加泥饼表面的空气流动速度，便于其中水分的蒸发。干化完成 后，加大主燃烧器的燃烧物质流量和空气流量，继续流化焚烧作业。
[0008] 为了保证布气环的喷出气流倾斜向下，使干化燃烧区中的气流形成热对流，优选 的技术方案为，排气孔在布气环内缘周向上均匀分布，布气环的排气孔倾斜设置，排气孔的 出料端朝向干化燃烧区。
[0009] 为了保证布气环的喷出气流倾斜向下，使干化燃烧区中的气流形成热对流，优选 的技术方案还可以为，排气孔在布气环内缘周向上均匀分布，排气孔固定连接有导气管，导 气管的出料端朝向干化燃烧区倾斜设置。
[0010] 优选的技术方案为，水汽导出管与冷凝器连通。通过监测冷凝器的冷凝液体流量， 或者监测盛装冷凝液体的容器液面变化，判断炉体中泥饼的干燥程度和千化处理结束时 间。
[0011] 为了提高布气环出风的温度，避免干化过程中冷热气流混合影响干化效率，优选 的技术方案为，下进气腔的炉体侧壁上设置有支管，支管与布气环相通，鼓风机连接设置在 支管上。
[0012] 优选的技术方案为，布气环的外轮廓为锥筒状。锥筒状的布气环还具有一定的导 流作用，将沿炉体侧壁上升的含水蒸气的湿气流导向炉体中心部分，直至与布气环喷射气 流混合。
[0013] 为了保证泥饼的彻底焚烧，优选的技术方案为，二次燃烧区的炉体侧壁上连通有 二次空气导入口和附加燃烧器。
[0014] 本实用新型的优点和有益效果在于：
[0015] 该泥饼用流化床干化焚烧炉结构合理紧凑，在进料口下方设置布气环，通过调节 燃烧器和空气流量的大小，是焚烧炉兼具干化泥饼和焚烧泥饼双重功能，尤其适用于污水 处理过程中的小批量泥饼的焚烧处理；
[0016]上述结构可用于现有技术中鼓泡式流化床焚烧炉的技术改造。
附图说明
[0017]图1是本实用新型泥饼用流化床干化焚烧炉实施例1的结构示意图；
[0018]图2是图1中A的局部放大图；
[0019]图3是实施例2的结构示意图。
[0020]图中：1、炉体；11、上燃烧腔；111、干化燃烧区；112、二次燃烧区；12、下进气腔;2、 布风板;3、进气管;4、主燃烧器;5、进料口；6、排渣口；7、砂层;8、布气环;9、排气孔；10、水汽 导出管;I3、鼓风机;14、冷凝器;15、支管;16、二次空气导入口； 17、附加燃烧器;18、导气管。
具体实施方式
[0021]下面结合附图和实施例，对本实用新型的具体实施方式作进一步描述。以下实施 例仅用于更加清楚地说明本实用新型的技术方案，而不能以此来限制本实用新型的保护范 围。
[0022] 实施例1
[0023]如图1和2所示，实施例丨泥饼用流化床干化焚烧炉，包括炉体丨，炉体i内的布风板2 将炉体内腔分隔为上燃烧腔11和下进气腔12,下进气腔12与进气管3和主燃烧器4连通，上 燃烧腔11的炉体侧壁上设置有焚烧物料的进料口 5和炉渣的排渣口 6，布风板2上设置有砂 层7，进料口 5下方设置有布气环8，布气环8的环面上设置有若干个排气孔9;布气环8彳寸上燃 烧腔11分隔为干化燃烧区II1和位于干化燃烧区111上方的二次燃烧区112,干化燃烧区111 的炉体侧壁上连通有水汽导出管10,布气环8通过管道与鼓风机13相通。
[0024] 排气孔9在布气环8内缘周向上均勾分布，布气环8的排气孔9倾斜设置，排气孔9的 出料端朝向干化燃烧区111;水汽导出管10与冷凝器14连通;布气环8的外轮廓为锥筒状。
[0025] 实施例1中管道导入的气体来源为冷空气，冷空气与炉内的热空气混合。
[0026] 实施例2
[0027] 如图3所示，实施例2与实施例1的区别在于，排气孔9固定连接有导气管18,导气管 18的出料端朝向干化燃烧区111倾斜设置。
[0028] 下进气腔12的炉体侧壁上设置有支管15,支管15与布气环8相通，鼓风机13连接设 置在支管15上。
[0029] 二次燃烧区112的炉体侧壁上连通有二次空气导入口 16和附加燃烧器17。
[0030]泥饼经由进料口导入至干化燃烧区中，关闭进料口，打开主燃烧器的燃烧器开关 和空气进气阀（连接在进气管上），通过控制系统或手动调节燃烧器的油或可燃气体的流 量，同时调节空气进气流量，打开布气环的鼓风机进气和水汽导出管排气，干化燃烧区保温 100〜120°C，含有水蒸气的热气流在干化燃烧区中呈热对流状态。当冷凝器无冷凝液滴落， 污泥干化操作完成。
[0031]调节燃烧器的油或可燃气体的流量，同时调节空气进气流量(过量空气），脱水后 的泥饼松散，焚烧颗粒在干化燃烧区和二次燃烧区中均形成悬浮的焚烧区，砂层呈沸腾状 态。焚烧烟气经由炉体顶端的烟气出口出料，由上燃烧腔的底端排渣口出料。
[0032]泥饼进料量相同且含水量一致的条件下，通过监测冷凝水量，实施例2中的泥饼干 化速度快。
[0033]进一步的，冷凝器的尾气还可导回焚烧炉中焚烧。
[0034i巧上所述、仅是本实用新型的优选实施方式，应当指出，对于本技术领域的普通技 术人贝来说，在不脱呙本实用新型技术原理的前提下，还可以做出若干改进和润饰这幽改 进和润饰也应视为本实用新型的保护范围。 丁义 ^
Claims (7)
1.一种泥饼用流化床干化焚烧炉，包括炉体，炉体内的布风板将炉体内腔分隔为上燃 烧腔和下进气腔，下进气腔与进气管和主燃烧器连通，上燃烧腔的炉体侧壁上设置有焚烧 物料的进料口和炉渣的排渣口，布风板上设置有砂层，其特征在于，进料口下方设置有布气 环，布气环的环面上设置有若干个排气孔•，布气环将上燃烧腔分隔为干化燃烧区和位于干 化燃烧区上方的二次燃烧区，干化燃烧区的炉体侧壁上连通有水汽导出管，布气环通过管 道与鼓风机相通。
2.根据权利要求1所述的泥饼用流化床干化焚烧炉，其特征在于，排气孔在布气环内缘 周向上均匀分布，布气环的排气孔倾斜设置，排气孔的出料端朝向干化燃烧区。
3.根据权利要求1所述的泥饼用流化床干化焚烧炉，其特征在于，排气孔在布气环内缘 周向上均匀分布，排气孔固定连接有导气管，导气管的出料端朝向干化燃烧区倾斜设置。
4.根据权利要求1所述的泥饼用流化床干化焚烧炉，其特征在于，水汽导出管与冷凝器 连通。
5.根据权利要求1所述的泥饼用流化床干化焚烧炉，其特征在于，下进气腔的炉体侧壁 上设置有支管，支管与布气环相通，鼓风机连接设置在支管上。
6.根据权利要求1所述的泥饼用流化床干化焚烧炉，其特征在于，布气环的外轮廓为锥 筒状。
7.根据权利要求1所述的泥饼用流化床干化焚烧炉，其特征在于，二次燃烧区的炉体侧 壁上连通有二次空气导入口和附加燃烧器。
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