CN201521952U - A multi-stage secondary air supply device sandwiching a partition wall in a circulating fluidized bed - Google Patents
A multi-stage secondary air supply device sandwiching a partition wall in a circulating fluidized bed Download PDFInfo
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- CN201521952U CN201521952U CN2009201974195U CN200920197419U CN201521952U CN 201521952 U CN201521952 U CN 201521952U CN 2009201974195 U CN2009201974195 U CN 2009201974195U CN 200920197419 U CN200920197419 U CN 200920197419U CN 201521952 U CN201521952 U CN 201521952U
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- 238000005192 partition Methods 0.000 title claims abstract description 44
- 239000000463 material Substances 0.000 claims description 9
- 230000009970 fire resistant effect Effects 0.000 claims description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 7
- 239000000203 mixture Substances 0.000 claims description 4
- 238000002485 combustion reaction Methods 0.000 abstract description 11
- 239000012530 fluid Substances 0.000 abstract description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 5
- 239000001301 oxygen Substances 0.000 abstract description 5
- 229910052760 oxygen Inorganic materials 0.000 abstract description 5
- 239000013589 supplement Substances 0.000 abstract description 4
- 230000000694 effects Effects 0.000 abstract description 2
- 238000004519 manufacturing process Methods 0.000 abstract 1
- 238000010586 diagram Methods 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- 206010021143 Hypoxia Diseases 0.000 description 3
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 239000010881 fly ash Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000007954 hypoxia Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
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Abstract
本实用新型涉及一种循环流化床中隔墙夹心多级二次风供风装置。它具有炉顶二次风箱、至少一根二次风管和炉底二次风箱,二次风管连接炉顶二次风箱和炉底二次风箱,所述二次风管布置于炉膛中隔墙的管屏工质流通管的间隔中,每根二次风管在炉膛不同高度处朝中隔墙的两侧开有多个二次风喷口。本实用新型通过在中隔墙管屏工质流通管的间隔中布置二次风管,向炉膛补充供给二次风,在二次风管上可以沿炉膛高度根据需要开设二次风口,实现多级供风,改善炉膛燃烧中心区域氧浓度场分布,提高锅炉的燃烧效率。本实用新型直接从锅炉炉膛的燃烧中心区域补充燃烧所需的二次风,效果直接可靠,同时依附于中隔墙,结构简单,制造安装方便。
The utility model relates to a multi-stage secondary air air supply device sandwiching a partition wall in a circulating fluidized bed. It has a furnace top secondary air box, at least one secondary air pipe and a furnace bottom secondary air box, the secondary air pipe is connected to the furnace top secondary air box and the furnace bottom secondary air box, and the secondary air pipe is arranged in the middle partition of the furnace In the interval of the working medium circulation pipes of the tube panel of the wall, each secondary air pipe has a plurality of secondary air nozzles on both sides of the middle partition wall at different heights of the furnace. The utility model arranges the secondary air pipe in the interval of the working fluid flow pipe of the tube panel of the middle partition wall to supplement and supply the secondary air to the furnace, and the secondary air port can be set up on the secondary air pipe along the height of the furnace according to the need, so as to realize multiple Level air supply, improve the distribution of oxygen concentration field in the furnace combustion center area, and improve the combustion efficiency of the boiler. The utility model directly supplements the secondary air required for combustion from the combustion center area of the boiler furnace, and the effect is direct and reliable. At the same time, it is attached to the middle partition wall, has a simple structure, and is convenient to manufacture and install.
Description
技术领域technical field
本实用新型涉及一种循环流化床中隔墙夹心多级二次风供风装置。The utility model relates to a multi-stage secondary air air supply device sandwiching a partition wall in a circulating fluidized bed.
背景技术Background technique
随着循环流化床技术的发展,流化床锅炉二次风射程和扩散的问题越来越受到人们的关注。尤其随着循环流化床锅炉的容量不断增大,炉膛截面不断增大,炉膛高度不断增加,二次风难以到达炉膛中心区域,使炉膛中心区域处于严重缺氧状态。试验证明,炉膛中心缺氧在大型循环流化床锅炉中普遍存在,由于炉膛中心广大区域缺氧,导致燃料燃烧不充分,特别是锅炉飞灰可燃物高,降低了锅炉的燃烧效率。因此,随着循环流化床大型化的发展,重点需要解决的就是炉膛燃烧中心区域的二次风不足问题。With the development of circulating fluidized bed technology, the issue of range and diffusion of secondary air in fluidized bed boilers has attracted more and more attention. Especially as the capacity of circulating fluidized bed boilers continues to increase, the cross-section of the furnace continues to increase, and the height of the furnace continues to increase. It is difficult for the secondary air to reach the central area of the furnace, which makes the central area of the furnace in a state of severe hypoxia. Tests have proved that the lack of oxygen in the furnace center is common in large circulating fluidized bed boilers. Due to the lack of oxygen in the large area of the furnace center, fuel combustion is insufficient, especially the boiler fly ash is high in combustibles, which reduces the combustion efficiency of the boiler. Therefore, with the development of large-scale circulating fluidized bed, the key problem that needs to be solved is the lack of secondary air in the combustion center area of the furnace.
申请人哈尔滨工业大学提出一种壁面-中心复合供给二次风的流化床燃烧装置(专利公开号CN 101196295A),该装置利用炉膛壁面上的若干个下倾式二次风管和由炉膛底端伸入炉膛燃烧中心区域的逆流型二次风柱联合供风的形式,补充锅炉的炉膛中央区域燃烧所需要的空气。但是这种装置不适应大型循环流化床锅炉的结构,裤衩腿结构和中隔墙都阻碍了这种装置的应用。The applicant Harbin Institute of Technology proposed a fluidized bed combustion device (patent publication number CN 101196295A) for a wall-center composite supply of secondary air. The counterflow secondary air column combined with air supply extending into the combustion center area of the furnace supplements the air needed for combustion in the central area of the furnace. But this device is not suitable for the structure of large-scale circulating fluidized bed boiler, and the underpants leg structure and the partition wall all hinder the application of this device.
申请人西安热工研究院有限公司提出一种内凹式循环流化床锅炉二次风供风方法及其装置(专利公开号CN 101225954A),该方法将炉膛下部二次风喷口附近的壁面向炉膛内凹入,使二次风供风喷口由离炉膛中心更近的位置向炉膛内供风,以此改善炉膛燃烧中心区域氧浓度场的分布,消除炉膛中心区域缺氧的现象。但这种方法结构复杂,改变了炉膛结构,直接影响炉膛内部的物质流动。The applicant Xi'an Thermal Engineering Research Institute Co., Ltd. proposed a secondary air supply method and device for an inner concave circulating fluidized bed boiler (patent publication number CN 101225954A). The furnace is recessed so that the secondary air supply nozzle is closer to the center of the furnace to supply air to the furnace, thereby improving the distribution of the oxygen concentration field in the combustion center area of the furnace and eliminating the phenomenon of oxygen deficiency in the center area of the furnace. However, this method has a complicated structure, changes the structure of the furnace, and directly affects the material flow inside the furnace.
申请人福斯特韦德能源股份公司提出一种“裤衩”式炉膛布置结构(专利公开号CN 1270664A),该结构利用中间隔板壁形成二次风室供风,同时在炉膛底部形成两个燃烧室,燃烧室之间或者独立,或者利用通道进行连接。这种结构得到广泛的应用,但炉膛上部气量补充困难,此外结构相对复杂。The applicant Foster Wade Energy Co., Ltd. proposed a "pants" type furnace layout structure (patent publication number CN 1270664A), which uses the middle partition wall to form a secondary air chamber for air supply, and at the same time forms two combustion chambers at the bottom of the furnace. Chambers and combustion chambers are either independent or connected by passages. This structure is widely used, but it is difficult to replenish the gas volume in the upper part of the furnace, and the structure is relatively complicated.
发明内容Contents of the invention
本实用新型的目的是针对现有技术存在的上述不足,提供一种循环流化床锅炉中隔墙夹心多级二次风供风装置。The purpose of this utility model is to provide a partition wall sandwich multi-stage secondary air supply device for circulating fluidized bed boilers in view of the above-mentioned shortcomings in the prior art.
循环流化床锅炉中隔墙夹心多级二次风供风装置具有炉顶二次风箱、至少一根二次风管和炉底二次风箱,二次风管连接炉顶二次风箱和炉底二次风箱,炉膛中设有中隔墙,所述二次风管布置于炉膛中隔墙的管屏工质流通管的间隔中,在管屏工质流通管中的工质为水、蒸汽或汽水的混合物,每根二次风管在炉膛不同高度处朝中隔墙的两侧开有多个二次风喷口。The partition wall sandwich multi-stage secondary air supply device in the circulating fluidized bed boiler has a secondary air box on the furnace top, at least one secondary air pipe and a secondary air box on the furnace bottom. The secondary air pipe is connected to the secondary air box on the furnace top and the furnace Bottom secondary bellows, the furnace is provided with a middle partition wall, and the secondary air pipe is arranged in the interval of the working fluid flow pipe of the tube panel in the middle partition wall of the furnace, and the working fluid in the tube panel working medium flow tube is water, A mixture of steam or soda, each secondary air pipe has multiple secondary air nozzles on both sides of the middle partition wall at different heights of the furnace.
所述的二次风喷口轴线与水平线的夹角在±45°以内。所述的二次风喷口的气流流通面积a与二次风管气流流通面积A之比a/A为1.6×10-3~3.25。所述的二次风喷口上布置有风帽,所述风帽为侧置箭头型风帽或钟罩型风帽。所述的二次风管上的多个二次风喷口可平行或交错布置。所述的二次风管上敷设有耐火耐磨材料层。The included angle between the axis of the secondary air nozzle and the horizontal line is within ±45°. The ratio a/A of the air flow area a of the secondary air nozzle to the air flow area A of the secondary air pipe is 1.6×10 -3 -3.25. A wind cap is arranged on the secondary air nozzle, and the wind cap is a side arrow type wind cap or a bell type wind cap. The multiple secondary air nozzles on the secondary air pipe can be arranged in parallel or alternately. A refractory and wear-resistant material layer is laid on the secondary air pipe.
本实用新型具有以下有益效果:本实用新型为循环流化床锅炉中隔墙夹心多级二次风供风装置。本实用新型利用大型循环流化床锅炉炉膛内存在的中隔墙,通过在中隔墙管屏工质流通管间隔中布置二次风管来补充供给二次风,同时在二次风管上可以根据需要开设二次风口,沿炉膛高度实现多级供风,通过这种中隔墙夹心式多级的供风系统,补充了锅炉炉膛燃烧中心区域不同高度处燃烧所需要的空气,改善了燃烧区域氧浓度场分布,解决日益增大炉膛面积和高度的大型循环流化床锅炉炉膛中心缺氧现象,促进锅炉内气固两相的充分混合和反应,提高锅炉的燃烧效率。同时,本实用新型的供风方法和装置结构简单,效果明显,适应大型循环流化床的要求。The utility model has the following beneficial effects: the utility model is a multi-stage secondary air supply device sandwiching a partition wall in a circulating fluidized bed boiler. The utility model utilizes the middle partition wall existing in the furnace of a large-scale circulating fluidized bed boiler to supplement and supply the secondary air by arranging a secondary air pipe in the middle partition wall tube panel working medium circulation pipe interval, and at the same time, on the secondary air pipe Secondary air outlets can be opened as needed to realize multi-stage air supply along the height of the furnace. Through this sandwich-type multi-stage air supply system in the middle partition wall, the air required for combustion at different heights in the combustion center area of the boiler furnace is supplemented, improving the The distribution of oxygen concentration field in the combustion area solves the phenomenon of oxygen deficiency in the hearth center of large circulating fluidized bed boilers with increasing furnace area and height, promotes the full mixing and reaction of gas-solid two-phase in the boiler, and improves the combustion efficiency of the boiler. At the same time, the air supply method and device of the utility model have simple structure and obvious effect, and can meet the requirements of large circulating fluidized bed.
附图说明Description of drawings
图1是单炉膛循环流化床锅炉中隔墙夹心多级二次风供风装置结构示意图;Figure 1 is a structural schematic diagram of a multi-stage secondary air supply device with a partition wall sandwiched in a single furnace circulating fluidized bed boiler;
图2是裤衩式炉膛循环流化床锅炉中隔墙夹心多级二次风供风装置结构示意图;Fig. 2 is a structural schematic diagram of a partition wall sandwich multi-stage secondary air supply device in a pant-type furnace circulating fluidized bed boiler;
图3是本实用新型的实施例1的A向结构示意图;Fig. 3 is the structural schematic view of A to the
图4是本实用新型的实施例2的A向结构示意图;Fig. 4 is the structural schematic diagram of A to the
图5是本实用新型的实施例3的A向结构示意图;Fig. 5 is a structural schematic view of A direction of
图6是本实用新型的实施例4的A向结构示意图;Fig. 6 is a structural schematic diagram of A direction of Embodiment 4 of the present utility model;
图7是本实用新型的实施例5的A向结构示意图;Fig. 7 is a structural schematic diagram of A direction of
图中,炉顶二次风箱1、二次风管2、炉底二次风箱3、炉膛4、中隔墙5管屏工质流通管6、二次风喷口7。In the figure, the furnace top
具体实施方式Detailed ways
如图1、2所示,循环流化床锅炉中隔墙夹心多级二次风供风装置具有炉顶二次风箱1、至少一根二次风管2和炉底二次风箱3,二次风管2连接炉顶二次风箱1和炉底二次风箱3,炉膛4中设有中隔墙5,所述的二次风管2布置于中隔墙5的管屏工质流通管6的间隔中,在管屏工质流通管中的工质为水、蒸汽或汽水的混合物,每根二次风管2在炉膛不同高度处朝中隔墙的两侧开有多个二次风喷口7。As shown in Figures 1 and 2, the partition wall sandwich multi-stage secondary air supply device in the circulating fluidized bed boiler has a furnace top
所述二次风管2可根据中隔墙5的结构以及供风需要选择管屏工质流通管6间隔的其中几个间隔进行夹心布置。所述的二次风喷口7轴线与水平线的夹角在±45°以内。二次风喷口7的气流流通面积a与二次风管2气流流通面积A之比a/A为1.6×10-3~3.25。二次风喷口7上布置有风帽,所述风帽为侧置箭头型风帽或钟罩型风帽。所述的二次风管2上的多个二次风喷口7可平行或交错布置。二次风管2上敷设有耐火耐磨材料层。The
实施例1:如图3所示,循环流化床锅炉中隔墙夹心多级二次风供风装置具有炉顶二次风箱1、至少一根二次风管2和炉底二次风箱3,二次风管2连接炉顶二次风箱1和炉底二次风箱3,炉膛4中设有中隔墙5,所述的二次风管2布置于中隔墙5的管屏工质流通管6的间隔中,在管屏工质流通管中的工质为水、蒸汽或汽水的混合物,每根二次风管2在合适高度处朝中隔墙的两侧开有多个二次风喷口7。所述的二次风喷口7轴线与水平线的夹角在±45°以内。二次风喷口7的气流流通面积a与二次风管2气流流通面积A之比a/A为1.6×10-3~3.25。所述的二次风管2上的多个二次风喷口7可平行或交错布置。二次风管2上敷设有耐火耐磨材料层。Embodiment 1: As shown in Figure 3, the partition wall sandwich multi-stage secondary air supply device in the circulating fluidized bed boiler has a furnace top
实施例2:如图4所示,每根二次风管2根据供风需要在几个不同高度处朝中隔墙的两侧开有多个二次风喷口7。所述的二次风喷口7轴线与水平线的夹角在±45°以内。二次风喷口7的气流流通面积a与二次风管2气流流通面积A之比a/A为1.6×10-3~3.25。所述的二次风管2上的多个二次风喷口7可平行或交错布置。二次风管2上敷设有耐火耐磨材料层。Embodiment 2: As shown in FIG. 4 , each
实施例3:如图5所示,每根二次风管2在合适高度处朝中隔墙的两侧开有多个二次风喷口7。所述的二次风喷口7轴线与水平线的夹角在±45°以内。二次风喷口7的气流流通面积a与二次风管2气流流通面积A之比a/A为1.6×10-3~3.25。二次风喷口7上布置有风帽,所述风帽为侧置箭头型风帽。所述的二次风管2上的多个二次风喷口7可平行或交错布置。二次风管2上敷设有耐火耐磨材料层。Embodiment 3: As shown in FIG. 5 , each
实施例4:如图6所示,每根二次风管2在合适高度处朝中隔墙的两侧开有多个二次风喷口7。所述的二次风喷口7轴线与水平线的夹角在±45°以内。二次风喷口7的气流流通面积a与二次风管2气流流通面积A之比a/A为1.6×10-3~3.25。二次风喷口7上布置有风帽,所述风帽为侧置钟罩型风帽。所述的二次风管2上的多个二次风喷口7可平行或交错布置。二次风管2上敷设有耐火耐磨材料层。Embodiment 4: As shown in FIG. 6 , each
实施例5:每根二次风管2在合适高度处朝中隔墙的两侧开有多个二次风喷口7。所述二次风管2可根据中隔墙5的结构以及供风需要选择管屏工质流通管6间隔的其中几个间隔进行夹心布置。所述的二次风喷口7轴线与水平线的夹角在±45°以内。二次风喷口7的气流流通面积a与二次风管2气流流通面积A之比a/A为1.6×10-3~3.25。所述的二次风管2上的多个二次风喷口7可平行或交错布置。二次风管2上敷设有耐火耐磨材料层。Embodiment 5: Each
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CN108413385A (en) * | 2018-03-06 | 2018-08-17 | 浙江哲丰能源发展有限公司 | A kind of low nitrogen burning method of circulating fluidized bed boiler |
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