CN209819528U - Biomass boiler multistage air distribution system capable of reducing nitrogen oxides - Google Patents
Biomass boiler multistage air distribution system capable of reducing nitrogen oxides Download PDFInfo
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Abstract
本实用新型涉及一种具有降低氮氧化物的生物质锅炉多级配风系统,属于锅炉环保技术领域。一次风系统位于炉排下部,烟气循环系统位于一次风系统的一侧,二次风系统、三次风系统分别位于前拱、后拱的上翻处;一次风系统包括风机、总管道、支管道、锅炉送风口、以及九个相互独立的风室B,所述风机通过总管道、支管道与锅炉送风口相连,风机将外部空气通过空气管道输送给总管道,再由总管道输送至九个风室B的支管道,支管道通过各风室B的风量自动调节阀控制管道供给空气量。优点在于:构思新颖,结构简单,使用安全方便。降低生物质锅炉氮氧化物的排放,节能环保,实用性强。
The utility model relates to a biomass boiler multi-stage air distribution system capable of reducing nitrogen oxides, which belongs to the technical field of boiler environmental protection. The primary air system is located at the lower part of the grate, the flue gas circulation system is located on one side of the primary air system, the secondary air system and the tertiary air system are respectively located at the upturned places of the front and rear arches; the primary air system includes fans, main pipes, branch Pipeline, boiler air outlet, and nine independent air chambers B, the fan is connected to the boiler air outlet through the main pipe and branch pipes, and the fan sends external air to the main pipe through the air pipe, and then sent to the nine air chambers by the main pipe. The branch pipes of each air chamber B, and the branch pipes control the air supply volume of the pipes through the air volume automatic adjustment valves of each air chamber B. The advantages are: novel conception, simple structure, safe and convenient use. Reduce nitrogen oxide emissions from biomass boilers, energy saving and environmental protection, and strong practicability.
Description
技术领域technical field
本实用新型涉及锅炉环保技术领域,特别涉及一种生物质锅炉多级配风系统,尤指一种具有降低氮氧化物的生物质锅炉多级配风系统。The utility model relates to the technical field of boiler environmental protection, in particular to a multi-stage air distribution system for a biomass boiler, in particular to a multi-stage air distribution system for a biomass boiler capable of reducing nitrogen oxides.
背景技术Background technique
目前生物质锅炉无论是从环保方面,还是从经济方面被越来越多的用能客户认可。作为第四大能源库,生物质在替代燃煤上有其独有的优势。生物质燃料具有低硫、低氮,挥发分高,易被引燃,二氧化碳零排放等特点。其烟气中的氮氧化物也主要是来自燃烧过程中热力型氮氧化物的生成,因此控制好炉膛燃烧温度,无需加装除硫脱硝设备就可以满足大部分地方环保排放要求。经济又环保。At present, biomass boilers are recognized by more and more energy-using customers both in terms of environmental protection and economical aspects. As the fourth largest energy pool, biomass has its unique advantages in replacing coal burning. Biomass fuel has the characteristics of low sulfur, low nitrogen, high volatile content, easy to ignite, and zero carbon dioxide emissions. The nitrogen oxides in the flue gas are also mainly from the generation of thermal nitrogen oxides during the combustion process. Therefore, controlling the combustion temperature of the furnace can meet the environmental protection emission requirements of most places without installing sulfur removal and denitrification equipment. Economical and environmentally friendly.
控制好炉膛温度,合理配风是关键。目前生物质锅炉的配风主要是在进料口提供送风,使得送风不均匀,局部出现温度过高,造成燃料燃烧不完全,热力型氮氧化物生成,使得烟气中的氮氧化物超标。To control the temperature of the furnace, reasonable air distribution is the key. At present, the air distribution of biomass boilers is mainly to provide air supply at the feed inlet, which makes the air supply uneven, and the local temperature is too high, resulting in incomplete combustion of fuel, and the generation of thermal nitrogen oxides, which makes the nitrogen oxides in the flue gas Exceeded the standard.
发明内容Contents of the invention
本实用新型的目的在于提供一种具有降低氮氧化物的生物质锅炉多级配风系统,解决了现有技术存在的上述问题。本实用新型将生物质燃料在炉膛内分段燃烧,减轻燃烧区域炉膛内温度,降低热力型氮氧化物的生成,解决生物质锅炉氮氧化物排放高的问题。The purpose of the utility model is to provide a biomass boiler multi-stage air distribution system with reduced nitrogen oxides, which solves the above-mentioned problems in the prior art. The utility model combusts the biomass fuel in sections in the furnace, reduces the temperature in the furnace in the combustion area, reduces the generation of thermal nitrogen oxides, and solves the problem of high nitrogen oxide emissions from the biomass boiler.
本实用新型的上述目的通过以下技术方案实现:Above-mentioned purpose of the utility model is realized through the following technical solutions:
具有降低氮氧化物的生物质锅炉多级配风系统,包括一次风系统、烟气循环系统、二次风系统和三次风系统,所述一次风系统位于炉排下部,烟气循环系统位于一次风系统的一侧,二次风系统、三次风系统分别位于前拱5、后拱6的上翻处;Biomass boiler multi-stage air distribution system with nitrogen oxide reduction, including primary air system, flue gas circulation system, secondary air system and tertiary air system, the primary air system is located at the bottom of the grate, and the flue gas circulation system is located at the On one side of the air system, the secondary air system and the tertiary air system are respectively located at the upturned places of the front arch 5 and the rear arch 6;
所述一次风系统包括风机8、总管道11、支管道12、锅炉送风口13、以及九个相互独立的风室B2,所述风机8通过总管道11、支管道12与锅炉送风口13相连,风机8将外部空气通过空气管道10输送给总管道11,再由总管道11输送至九个风室B2的支管道12,支管道12通过各风室B的风量自动调节阀14控制管道供给空气量。The primary air system includes a fan 8, a main duct 11, a branch duct 12, a boiler air outlet 13, and nine mutually independent air chambers B2, and the fan 8 is connected to the boiler air outlet 13 through the main duct 11 and the branch duct 12 , the fan 8 transports the external air to the main duct 11 through the air duct 10, and then the main duct 11 transports it to the branch ducts 12 of the nine air chambers B2, and the branch ducts 12 control the pipeline supply through the air volume automatic adjustment valve 14 of each air chamber B air volume.
所述烟气循环系统包括循环风机7、烟气管道9、烟气循环管道15以及一个独立的风室A1,所述烟气管道9与循环风机进口相连接,循环风机出口通过烟气循环管道15、风量自动调节阀14与风室A1内的锅炉送风口13相连接;所述风室A1位于炉排壳体给料处一旁,与一次风系统中的九个风室B2并列,均匀分布在炉排壳体两侧;循环风机7通过烟气管道9将除尘器处理后的烟气输入烟气循环管道15,烟气循环管道15再将烟气输送至风室A1,并通过风量自动调节阀14控制所需空气供给量。The flue gas circulation system includes a circulation fan 7, a flue gas pipe 9, a flue gas circulation pipe 15 and an independent air chamber A1, the flue gas pipe 9 is connected to the inlet of the circulation fan, and the outlet of the circulation fan passes through the flue gas circulation pipe 15. The air volume automatic regulating valve 14 is connected to the boiler air supply port 13 in the air chamber A1; the air chamber A1 is located beside the feeding place of the grate shell, paralleled with the nine air chambers B2 in the primary air system, and evenly distributed On both sides of the grate shell; the circulation fan 7 sends the flue gas processed by the dust collector into the flue gas circulation pipe 15 through the flue gas pipe 9, and the flue gas circulation pipe 15 transports the flue gas to the air chamber A1, and automatically passes through the air volume A regulator valve 14 controls the required air supply.
所述的二次风系统包括前拱输风管道16、前拱送风口17、前拱送风管3,所述前拱送风管3在前拱送风口17处与前拱输风管道16相连,前拱输风管道16与总管道11相连;前拱送风管3位于锅炉的前拱5上翻处,送风方向与炉膛下部烟气流动方向垂直。Described secondary air system comprises front arch air delivery duct 16, front arch air supply duct 17, front arch air supply duct 3, and front arch air supply duct 3 is connected to front arch air delivery duct 16 at front arch air delivery duct 17. The front arch air duct 16 is connected to the main duct 11; the front arch air supply pipe 3 is located at the upturned position of the front arch 5 of the boiler, and the air supply direction is perpendicular to the flue gas flow direction in the lower part of the furnace.
所述的三次风系统包括后拱输风管道18、后拱送风口19,后拱送风管4,所述后拱送风管4在后拱送风口19处与后拱输风管道18相连,后拱输风管道18与总管道11相连;后拱送风管4位于锅炉的后拱6上翻出,送风方向与炉膛上部烟气流动方向垂直。The tertiary air system comprises a rear arch air delivery duct 18, a rear arch air supply duct 19, and a rear arch air delivery duct 4, and the rear arch air delivery duct 4 is connected to the rear arch air delivery duct 18 at the rear arch air delivery duct 19 , the rear arch air duct 18 is connected to the main duct 11; the rear arch air supply pipe 4 is turned out on the rear arch 6 of the boiler, and the air supply direction is perpendicular to the flue gas flow direction on the upper part of the furnace.
本实用新型的有益效果在于:构思新颖,结构简单,节能环保,使用安全方便。一次风系统、烟气循环系统主要燃烧炉排中的碳,二、三次风系统主要燃烧挥发分。将高挥发分的生物质燃料进行分段燃烧,减轻燃烧区域炉膛温度。降低热力型氮氧化物的生成。烟气再循环系统,降低了烟气中的氧含量,从另一方面降低了氮氧化物的折算值。因而从整体上降低了氮氧化物的排放。实用性强。The beneficial effects of the utility model are: novel conception, simple structure, energy saving and environmental protection, and safe and convenient use. The primary air system and flue gas circulation system mainly burn carbon in the grate, and the secondary and tertiary air systems mainly burn volatile matter. The high volatile biomass fuel is burned in stages to reduce the furnace temperature in the combustion area. Reduces the formation of thermal nitrogen oxides. The flue gas recirculation system reduces the oxygen content in the flue gas, and on the other hand reduces the conversion value of nitrogen oxides. Thus reducing the emission of nitrogen oxides as a whole. Strong practicality.
附图说明Description of drawings
此处所说明的附图用来提供对本实用新型的进一步理解,构成本申请的一部分,本实用新型的示意性实例及其说明用于解释本实用新型,并不构成对本实用新型的不当限定。The accompanying drawings described here are used to provide a further understanding of the utility model and constitute a part of the application. The schematic examples and descriptions of the utility model are used to explain the utility model and do not constitute improper limitations to the utility model.
图1为本实用新型的配风结构锅炉主视图;Fig. 1 is the front view of the boiler with air distribution structure of the present utility model;
图2为本实用新型的一次风系统图;Fig. 2 is the primary air system diagram of the utility model;
图3为本实用新型的烟气循环系统图;Fig. 3 is the flue gas circulation system figure of the utility model;
图4为本实用新型的二次风系统图;Fig. 4 is the secondary air system diagram of the utility model;
图5为本实用新型的三次风系统图。Fig. 5 is the tertiary air system diagram of the utility model.
图中:1、风室A;2、风室B;3、前拱送风管;4、后拱送风管;5、前拱;6、后拱;7、循环风机;8、风机;9、烟气循环管道;10、空气管道;11、总管;12、支管;13、锅炉送风口;14、风量自动调节阀;15、烟气循环管道;16、前拱送风管道;17、前拱送风口;18、后拱送风管道;19、后拱送风口。In the figure: 1. Air chamber A; 2. Air chamber B; 3. Front arch air supply pipe; 4. Back arch air supply pipe; 5. Front arch; 6. Back arch; 7. Circulation fan; 8. Fan; 9. Flue gas circulation pipe; 10. Air pipe; 11. Main pipe; 12. Branch pipe; 13. Boiler air outlet; 14. Automatic air volume control valve; 15. Flue gas circulation pipe; 16. Front arch air supply pipe; 17. Front arch air supply port; 18, rear arch air supply duct; 19, rear arch air supply port.
具体实施方式Detailed ways
下面结合附图进一步说明本实用新型的详细内容及其具体实施方式。Further illustrate the detailed content of the utility model and its specific implementation below in conjunction with accompanying drawing.
参见图1至图5所示,本实用新型的具有降低氮氧化物的生物质锅炉多级配风系统,包括一次风系统、烟气循环系统、二次风系统和三次风系统,所述一次风系统位于炉排下部,烟气循环系统位于一次风系统的一侧,二次风系统、三次风系统分别位于前拱5、后拱6的上翻处;Referring to Fig. 1 to Fig. 5, the biomass boiler multi-stage air distribution system with nitrogen oxide reduction of the utility model includes a primary air system, a flue gas circulation system, a secondary air system and a tertiary air system. The air system is located at the lower part of the grate, the flue gas circulation system is located on one side of the primary air system, the secondary air system and the tertiary air system are respectively located at the upturned places of the front arch 5 and the rear arch 6;
参见图1及图2所示,所述一次风系统包括风机8、总管道11、支管道12、锅炉送风口13、以及九个相互独立的风室B2,所述风机8通过总管道11、支管道12与锅炉送风口13相连,总管道设有压力阀和止回阀,与各风室连接的支管设有流量调节阀。锅炉送风口位于炉排下部,由九个风室B构成,九个风室B均匀分布在炉排壳体两侧。风室B由风机将室外空气送入送风口。燃料随着炉排的运转,燃烧状态不同,通过变频风机调节各风室所需空气量。风机8不断地将外部空气通过空气管道10输送给总管道11,再由总管道11输送至九个风室B2的支管道12,支管道12通过各风室B的风量自动调节阀14控制管道供给空气量,将合理的风量送至九个风室B2。同一时间进入炉排上的燃料,随着炉排的运转,每个风室所对应的燃烧区域中,燃料燃烧程度不同,通过分区控制风量,使得燃料充分燃烧,并且提高锅炉热效率。Referring to Fig. 1 and shown in Fig. 2, described primary air system comprises fan 8, main duct 11, branch duct 12, boiler air outlet 13, and nine mutually independent air chambers B2, and described fan 8 passes through main duct 11, The branch pipe 12 is connected with the boiler air outlet 13, the main pipe is provided with a pressure valve and a check valve, and the branch pipe connected with each air chamber is provided with a flow regulating valve. The air supply port of the boiler is located at the lower part of the grate and consists of nine air chambers B, which are evenly distributed on both sides of the grate shell. The air chamber B sends the outdoor air into the air outlet by the fan. With the operation of the grate, the combustion state of the fuel is different, and the air volume required by each air chamber is adjusted by the frequency conversion fan. The fan 8 continuously transports the external air to the main duct 11 through the air duct 10, and then transports it to the branch ducts 12 of the nine air chambers B2 by the main duct 11. Supply air volume and send reasonable air volume to nine air chambers B2. The fuel entering the grate at the same time, with the operation of the grate, the degree of combustion of the fuel is different in the combustion area corresponding to each air chamber, and the air volume is controlled by partition to make the fuel fully burn and improve the thermal efficiency of the boiler.
参见图1及图3所示,所述烟气循环系统包括循环风机7、烟气管道9、烟气循环管道15以及一个独立的风室A1,所述烟气管道9与循环风机进口相连接,循环风机出口通过烟气循环管道15、风量自动调节阀14与风室A1内的锅炉送风口13相连接;所述风室A1位于炉排壳体靠近给料处一旁,与一次风系统中的九个风室B2并列,均匀分布在炉排壳体两侧管道总管设有压力阀和止回阀,与风室连接的支管设有流量调节阀。风源来自于经过除尘器处理的、锅炉内部燃烧产生的烟气。可以为初始燃烧阶段的生物质燃料提供相对稳定的供氧环境,同时降低烟气中的含氧量。循环风机7通过烟气管道9将除尘器处理后的烟气输入烟气循环管道15,烟气循环管道15再将烟气输送至风室A1,并通过风量自动调节阀14控制所需空气供给量;为锅炉内燃料燃烧提供空气的同时,降低烟气中的氧含量,控制热力型氮氧化物的生产。1 and 3, the flue gas circulation system includes a circulation fan 7, a flue gas duct 9, a flue gas circulation duct 15 and an independent air chamber A1, and the flue gas duct 9 is connected to the inlet of the circulation fan , the outlet of the circulating fan is connected to the boiler air supply port 13 in the air chamber A1 through the flue gas circulation pipe 15 and the automatic air volume control valve 14; The nine air chambers B2 are arranged side by side, and are evenly distributed on both sides of the grate shell. The main pipe is equipped with a pressure valve and a check valve, and the branch pipe connected to the air chamber is equipped with a flow regulating valve. The wind source comes from the flue gas produced by the internal combustion of the boiler after being treated by the dust collector. It can provide a relatively stable oxygen supply environment for the biomass fuel in the initial combustion stage, and at the same time reduce the oxygen content in the flue gas. The circulation fan 7 sends the flue gas processed by the dust collector into the flue gas circulation pipe 15 through the flue gas pipe 9, and the flue gas circulation pipe 15 transports the flue gas to the air chamber A1, and controls the required air supply through the air volume automatic adjustment valve 14 amount; while providing air for fuel combustion in the boiler, it reduces the oxygen content in the flue gas and controls the production of thermal nitrogen oxides.
生物质中的固定碳主要是一次风系统、烟气循环系统共同作用下,在炉排上完成燃烧的。燃料随着炉排行进方向,燃烧程度不同,所需氧量有所不同。通过独立风室的风量自动调节,合理控制风量供给。The fixed carbon in biomass is mainly burned on the grate under the joint action of the primary air system and the flue gas circulation system. Depending on the direction of the grate, the degree of combustion of the fuel is different, and the amount of oxygen required is different. Through the automatic adjustment of the air volume of the independent air chamber, the air volume supply is reasonably controlled.
参见图1及图4所示,所述的二次风系统包括前拱输风管道16、前拱送风口17、前拱送风管3,所述前拱送风管3在前拱送风口17处与前拱输风管道16相连,前拱输风管道16与总管道11相连;前拱送风管3位于锅炉的前拱5上翻处,送风方向与炉膛下部烟气流动方向垂直;二次风系统主要是将生物质燃料中析出的挥发分进行混合,在与一次风协同作用下,形成烟气扰动,强化燃烧。Referring to Figures 1 and 4, the secondary air system includes a front arch air duct 16, a front arch air supply port 17, and a front arch air supply pipe 3, and the front arch air supply pipe 3 is located at the front arch air supply port. 17 points are connected to the front arch air delivery pipe 16, and the front arch air delivery pipe 16 is connected to the main duct 11; the front arch air supply pipe 3 is located at the upward turning point of the front arch 5 of the boiler, and the air supply direction is perpendicular to the flue gas flow direction in the lower part of the furnace ; The secondary air system is mainly to mix the volatile matter precipitated from the biomass fuel, and under the synergy with the primary air, it forms flue gas disturbance and intensifies combustion.
参见图1及图5所示,所述的三次风系统包括后拱输风管道18、后拱送风口19,后拱送风管4,所述后拱送风管4在后拱送风口19处与后拱输风管道18相连,后拱输风管道18与总管道11相连;后拱送风管4位于锅炉的后拱6上翻出,送风方向与炉膛上部烟气流动方向垂直。三次风系统主要是将生物质析出的挥发分再一次进行强化混合,达到充分燃烧的目的。Referring to Fig. 1 and shown in Fig. 5, the described tertiary air system comprises a rear arch air supply duct 18, a rear arch air supply port 19, and a rear arch air supply pipe 4, and the rear arch air supply pipe 4 is located at the rear arch air supply port 19 The place is connected with the rear arch air duct 18, and the rear arch air duct 18 is connected with the main duct 11; the rear arch air supply pipe 4 is turned out on the rear arch 6 of the boiler, and the air supply direction is perpendicular to the flue gas flow direction on the upper part of the furnace. The tertiary air system is mainly to strengthen the mixing of the volatile matter precipitated from the biomass again to achieve the purpose of full combustion.
本实用新型的一次风主要燃烧炉排中的碳,二次风、三次风主要燃烧挥发分。将高挥发分的生物质燃料进行分段燃烧,减轻燃烧区域炉膛温度。降低热力型氮氧化物的生成。烟气再循环系统,降低了烟气中的氧含量,使氧含量≤9%,从另一方面降低了氮氧化物的折算值。因而从整体上降低了氮氧化物的排放。The primary air of the utility model mainly burns carbon in the fire grate, and the secondary air and the tertiary air mainly burn volatile matter. The high volatile biomass fuel is burned in stages to reduce the furnace temperature in the combustion area. Reduces the formation of thermal nitrogen oxides. The flue gas recirculation system reduces the oxygen content in the flue gas to make the oxygen content ≤ 9%, which reduces the conversion value of nitrogen oxides on the other hand. Thus reducing the emission of nitrogen oxides as a whole.
以上所述仅为本实用新型的优选实例而已,并不用于限制本实用新型,对于本领域的技术人员来说,本实用新型可以有各种更改和变化。凡对本实用新型所作的任何修改、等同替换、改进等,均应包含在本实用新型的保护范围之内。The above descriptions are only preferred examples of the utility model, and are not intended to limit the utility model. For those skilled in the art, the utility model can have various modifications and changes. Any modification, equivalent replacement, improvement, etc. made to the utility model shall be included in the protection scope of the utility model.
Claims (4)
Priority Applications (1)
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| TR01 | Transfer of patent right | ||
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Effective date of registration: 20260104 Address after: 130000 Jilin Province, Changchun City, Jingyue Development Zone, Jingyue Street, Jinping Street and Yinjin Road intersection, Guoxin Meiyi Building 93, Room 110 Patentee after: Jilin Shangxin Energy Co.,Ltd. Country or region after: China Address before: 130000 Jilin Province, Changchun City, Satellite Road 8722, High-tech Development Zone Patentee before: JILIN HONGRI NEW ENERGY CO.,LTD. Country or region before: China |