CN102721040A - Device for NOx reduction and grate firing by stokehold screening, gasifying and reburning - Google Patents
Device for NOx reduction and grate firing by stokehold screening, gasifying and reburning Download PDFInfo
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- 238000012216 screening Methods 0.000 title claims abstract description 16
- 230000009467 reduction Effects 0.000 title claims description 5
- 238000010304 firing Methods 0.000 title abstract 3
- 239000003245 coal Substances 0.000 claims abstract description 108
- 239000002245 particle Substances 0.000 claims abstract description 61
- 238000002309 gasification Methods 0.000 claims abstract description 41
- 238000002485 combustion reaction Methods 0.000 claims abstract description 31
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- 230000007704 transition Effects 0.000 claims description 7
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- 230000007613 environmental effect Effects 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000013618 particulate matter Substances 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000004939 coking Methods 0.000 description 1
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- 231100000719 pollutant Toxicity 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
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Abstract
Description
技术领域 technical field
本发明涉及一种降低NOx层燃设备,属于环保设备技术领域。The invention relates to equipment for reducing NOx layer combustion, which belongs to the technical field of environmental protection equipment.
背景技术 Background technique
我国现役燃煤工业锅炉约54.6万台,占目前在役工业锅炉总数的85%,且每年以1.5%左右的速度递增。燃煤工业锅炉年用煤量5-6亿吨,约占全国年用煤总量的18%。工业锅炉每年的总能源消耗和污染排放均位居全国工业行业第二。There are about 546,000 coal-fired industrial boilers in service in my country, accounting for 85% of the total number of industrial boilers currently in service, and increasing at a rate of about 1.5% every year. The annual coal consumption of coal-fired industrial boilers is 500-600 million tons, accounting for about 18% of the country's total annual coal consumption. The annual total energy consumption and pollution discharge of industrial boilers both rank second in the national industrial industry.
在工业锅炉污染物减排的研究中,SO2和烟尘的研究开展比较早,而且已经取得不少的研究成果,并已经工业化应用。由于工业锅炉低温燃烧等特点,使得其生成的NOx量相对较低(400-700mg/Nm3)。所以,工业锅炉的NOx减排工作一直未受到充分的重视(工业锅炉相对于电站煤粉锅炉NOx排放量是少的,所以目前重视程度不够并且不适用已有的电站煤粉锅炉的降低NOx排放技术)。近几年我国的环保要求逐年提高,使得工业锅炉的NOx排放问题越发凸显。特别是NOx在城市空气环境中对PM2.5(PM2.5是指大气中直径小于或等于2.5微米的颗粒物,也称为可入肺颗粒物。虽然PM2.5只是地球大气成分中含量很少的组分,但它对空气质量和能见度等有重要的影响。PM2.5粒径小,富含大量的有毒、有害物质且在大气中的停留时间长、输送距离远,因而对人体健康和大气环境质量的影响更大)的二次源贡献率逐渐受到关注。因此,开发与燃烧过程协同的经济型层燃锅炉低NOx燃烧技术,显得十分紧迫。In the research on the emission reduction of industrial boiler pollutants, the research on SO 2 and soot was carried out relatively early, and many research results have been obtained, and they have been applied industrially. Due to the low-temperature combustion of industrial boilers, the amount of NOx generated is relatively low (400-700mg/Nm3). Therefore, the NOx emission reduction work of industrial boilers has not received sufficient attention (the NOx emission of industrial boilers is less than that of power station pulverized coal boilers, so the current attention is not enough and it is not applicable to reduce NOx emissions of existing power station pulverized coal boilers technology). In recent years, my country's environmental protection requirements have been increasing year by year, making the NOx emission problem of industrial boilers more and more prominent. Especially NOx in the urban air environment has an effect on PM2.5 (PM2.5 refers to particulate matter with a diameter less than or equal to 2.5 microns in the atmosphere, also known as particulate matter that can enter the lungs. Although PM2.5 is only a small amount in the earth's atmospheric components components, but it has an important impact on air quality and visibility. PM2.5 has a small particle size, is rich in a large amount of toxic and harmful substances, and has a long residence time in the atmosphere and a long transportation distance, so it is harmful to human health and the atmosphere. The contribution rate of secondary sources that have a greater impact on environmental quality) has gradually drawn attention. Therefore, it is very urgent to develop an economical layer-fired boiler low-NOx combustion technology that is coordinated with the combustion process.
发明内容 Contents of the invention
本发明的目的是提供一种能够协同实现层燃工业锅炉低NOx排放与高效燃烧的炉前分选气化再燃降低NOx层燃设备The purpose of the present invention is to provide a kind of equipment for reducing NOx layer combustion by sorting, gasification and reburning in front of the furnace, which can realize low NOx emission and high-efficiency combustion of the layer-fired industrial boiler synergistically.
本发明为解决上述问题采取的技术方案是:The technical scheme that the present invention takes for solving the above problems is:
一种炉前分选气化再燃降低NOx层燃设备,所述设备包括锅炉煤斗、风机及燃煤输送装置,所述设备还包括炉前筛分分选装置、过渡管、气化气管路、助燃空气管路、固定床气化炉、螺旋物料输送机及气化气喷头;A pre-furnace sorting, gasification and recombustion equipment for reducing NOx layer combustion, the equipment includes a boiler coal hopper, a fan, and a coal-fired conveying device, and the equipment also includes a pre-furnace screening and sorting device, a transition pipe, and a gasification gas pipeline , Combustion air pipeline, fixed bed gasifier, screw material conveyor and gasification gas nozzle;
所述炉前筛分分选装置包括大颗粒煤斗、中颗粒煤斗和小颗粒煤斗,中颗粒煤斗设置在大颗粒煤斗与小颗粒煤斗之间,大颗粒煤斗、中颗粒煤斗和小颗粒煤斗三者的进料腔连通设置,大颗粒煤斗内设有大筛孔筛片、中颗粒煤斗内设有中筛孔筛片、小颗粒煤斗内设有小筛孔筛片,所述大筛孔筛片、中筛孔筛片和小筛孔筛片均设置在同一倾斜面内,所述倾斜面与锅炉煤斗相邻的一端高于该倾斜面远离所述锅炉煤斗的一端,燃煤输送装置的前端通过过渡管与炉前筛分分选装置的进料腔连通,小颗粒煤斗的出料口和中颗粒煤斗的出料口均与螺旋物料输送机的入料口连通,螺旋物料输送机的出料口一端高于螺旋物料输送机的入料口一端,螺旋物料输送机的出料口与锅炉煤斗连通,锅炉煤斗的出煤口与锅炉的进煤口连通,大颗粒煤斗的出料口与固定床气化炉连通,固定床气化炉的气化气出口经风机及气化气管路与气化气喷头连通,助燃空气管路与所述气化气喷头连通,所述气化气喷头设置在锅炉的炉膛内。The screening and sorting device in front of the furnace includes a large-grain coal hopper, a medium-grain coal hopper and a small-grain coal hopper, the medium-grain coal hopper is arranged between the large-grain coal hopper and the small-grain coal hopper, the large-grain coal hopper, the medium-grain coal hopper The feeding chambers of the coal hopper and the small particle coal hopper are connected. The large particle coal hopper is equipped with a large mesh screen, the medium particle coal hopper is equipped with a medium mesh mesh, and the small particle coal Mesh sieves, the large sieves, medium sieves and small sieves are all arranged in the same inclined plane, and the end of the inclined plane adjacent to the boiler coal hopper is higher than the inclined plane and away from the One end of the coal hopper of the boiler, the front end of the coal-fired conveying device communicates with the feeding chamber of the screening and sorting device in front of the furnace through a transition pipe, and the discharge port of the small particle coal hopper and the discharge port of the medium particle coal hopper are all connected to the The feed port of the screw conveyor is connected, one end of the discharge port of the screw conveyor is higher than the feed port of the screw conveyor, the discharge port of the screw conveyor is connected with the coal hopper of the boiler, and the discharge port of the boiler coal hopper The coal port is connected to the coal inlet of the boiler, the discharge port of the large particle coal hopper is connected to the fixed bed gasifier, and the gasification gas outlet of the fixed bed gasifier is connected to the gasification gas nozzle through the fan and the gasification gas pipeline. The combustion-supporting air pipeline communicates with the gasification gas nozzle, and the gasification gas nozzle is arranged in the furnace of the boiler.
本发明的有益效果是:一、采用炉前筛分分选装置将入炉煤进行粒度分类。依据《链条锅炉用煤技术条件》GB/T18342-2009,对于块煤:分为<6mm、6-15mm、15-25m三类,对于混煤:分为<6mm、6-20mm、20-50m三类。依次定义为小、中、大三类粒径。将中、小两类颗粒送入锅炉原有的锅炉煤斗内,再由锅炉煤斗给入炉膛燃烧。将大颗粒煤送入固定床气化炉内气化,送入炉膛内的煤粒径跨度范围缩小,有利于提高锅炉内燃烧的稳定性和均匀性,进而提高燃烧效率,降低固体不完全燃烧损失。大颗粒煤送入固定床气化炉内,有利于降低气化炉内流动阻力,减轻结焦的可能性。二、气化气的主要成分为CO、CH4、H2等,将气化气送入锅炉炉膛内的上方适宜位置燃烧,可实现对下部层燃燃烧产生的NO部分还原。反应机理如下:The beneficial effects of the present invention are as follows: 1. The furnace coal is subjected to particle size classification by adopting a screening and sorting device in front of the furnace. According to "Technical Conditions for Coal Used in Chain Boilers" GB/T18342-2009, for lump coal: it is divided into three categories: <6mm, 6-15mm, and 15-25m; for mixed coal: it is divided into <6mm, 6-20mm, 20-50m Three categories. It is defined in turn as small, medium and large particle sizes. The medium and small particles are fed into the original boiler coal hopper of the boiler, and then fed into the furnace for combustion by the boiler coal hopper. Send large-particle coal into the fixed-bed gasifier for gasification, and the particle size span of the coal fed into the furnace will be reduced, which will help improve the stability and uniformity of combustion in the boiler, thereby improving combustion efficiency and reducing incomplete combustion of solids loss. Large particle coal is fed into the fixed bed gasifier, which is beneficial to reduce the flow resistance in the gasifier and reduce the possibility of coking. 2. The main components of the gasification gas are CO, CH 4 , H 2 , etc., and the gasification gas is sent to a suitable position above the boiler furnace for combustion, which can realize the partial reduction of NO produced by the combustion of the lower layer. The reaction mechanism is as follows:
CO+NO→N2+CO2 CO+NO→N 2 +CO 2
CH4+NO→N2+CO2+H2OCH 4 +NO→N 2 +CO 2 +H 2 O
H2+NO→N2+H2OH 2 +NO→N 2 +H 2 O
三、气化气的燃烧可以提高炉膛空间的温度水平,增加了炉膛受热面的吸热量,根据气化气给入比例的不同,可以提高锅炉供热(蒸发能力)3-10%。通过布置适宜的燃尽风(助燃空气),可以实现对气体不完全燃烧损失的有效降低。四、本发明的设备能够实现层燃锅炉低NOx排放,本发明适用于各类层状燃烧的装置及设备。通过本设备的运行可以降低NOx排放30-50%以上,锅炉燃烧效率提高0.5-1%,锅炉供热(蒸发)能力提高3-10%。3. The combustion of gasification gas can increase the temperature level of the furnace space and increase the heat absorption of the heating surface of the furnace. According to the different ratios of gasification gas feeding, it can increase the heating (evaporation capacity) of the boiler by 3-10%. By arranging suitable burn-off air (combustion-supporting air), the incomplete combustion loss of gas can be effectively reduced. 4. The equipment of the present invention can realize low NOx emission of the layer fired boiler, and the present invention is applicable to various types of layered combustion devices and equipment. Through the operation of this equipment, NOx emissions can be reduced by more than 30-50%, the combustion efficiency of the boiler can be increased by 0.5-1%, and the heating (evaporation) capacity of the boiler can be increased by 3-10%.
附图说明 Description of drawings
图1为本发明的整体结构主视示意图。Figure 1 is a schematic front view of the overall structure of the present invention.
具体实施方式 Detailed ways
具体实施方式一:结合图1说明,本实施方式的一种炉前分选气化再燃降低NOx层燃设备,所述设备包括锅炉煤斗1、风机2及燃煤输送装置4,所述设备还包括炉前筛分分选装置5、过渡管6、气化气管路7、助燃空气管路8、固定床气化炉9、螺旋物料输送机10及气化气喷头11;Specific embodiment 1: In conjunction with Fig. 1, a kind of equipment for furnace separation, gasification and reburning to reduce NOx layer combustion in this embodiment, the equipment includes a boiler coal hopper 1, a
所述炉前筛分分选装置5包括大颗粒煤斗5-1、中颗粒煤斗5-2和小颗粒煤斗5-3,中颗粒煤斗5-2设置在大颗粒煤斗5-1与小颗粒煤斗5-3之间,大颗粒煤斗5-1、中颗粒煤斗5-2和小颗粒煤斗5-3三者的进料腔连通设置,大颗粒煤斗5-1内设有大筛孔筛片5-1-1、中颗粒煤斗5-2内设有中筛孔筛片5-2-1、小颗粒煤斗5-3内设有小筛孔筛片5-3-1,所述大筛孔筛片5-1-1、中筛孔筛片5-2-1和小筛孔筛片5-3-1均设置在同一倾斜面内,所述倾斜面与锅炉煤斗1相邻的一端高于该倾斜面远离所述锅炉煤斗1的一端,燃煤输送装置4的前端通过过渡管6与炉前筛分分选装置5的进料腔连通,小颗粒煤斗5-3的出料口和中颗粒煤斗5-2的出料口均与螺旋物料输送机10的入料口连通,螺旋物料输送机10的出料口一端高于螺旋物料输送机10的入料口一端,螺旋物料输送机10的出料口与锅炉煤斗1连通,锅炉煤斗1的出煤口与锅炉3的进煤口连通,大颗粒煤斗5-1的出料口与固定床气化炉9连通,固定床气化炉9的气化气出口经风机2及气化气管路7与气化气喷头11连通,助燃空气管路8与所述气化气喷头11连通,所述气化气喷头11设置在锅炉3的炉膛内。本实施方式中采用的螺旋物料输送机10为现有技术。The screening and
具体实施方式二:结合图1说明,本实施方式的小筛孔筛片5-3-1的孔径<6mm,中筛孔筛片5-2-1的孔径为6-15mm,大筛孔筛片5-1-1的孔径为15-25mm。适合对块煤筛分。其它与具体实施方式一相同。Specific embodiment two: In conjunction with Fig. 1 description, the aperture of the small mesh screen 5-3-1 of the present embodiment<6mm, the aperture of the medium mesh screen 5-2-1 is 6-15mm, and the large mesh screen The hole diameter of sheet 5-1-1 is 15-25mm. Suitable for screening lump coal. Others are the same as in the first embodiment.
具体实施方式三:结合图1说明,本实施方式的小筛孔筛片5-3-1的孔径<6mm,中筛孔筛片5-2-1的孔径为6-20mm,大筛孔筛片5-1-1的孔径为20-50mm。适合对混煤筛分。其它与具体实施方式一相同。Specific embodiment three: In conjunction with Fig. 1 description, the aperture of the small mesh screen 5-3-1 of the present embodiment<6mm, the aperture of the medium mesh screen 5-2-1 is 6-20mm, and the large mesh screen The hole diameter of sheet 5-1-1 is 20-50mm. Suitable for screening mixed coal. Others are the same as in the first embodiment.
具体实施方式四:结合图1说明,本实施方式的所述燃煤输送装置4为水平输送带输送装置。为现有技术。其它与具体实施方式一、二或三相同。Embodiment 4: In conjunction with FIG. 1 , the coal-fired
工艺过程如下:将公共输煤系统的燃煤经燃煤输送装置4输送燃煤,并经过渡管6进入至炉前筛分分选装置5内,将燃煤分为大、中、小三种粒径。中、小两种粒径燃煤经螺旋物料输送机10送回锅炉煤斗1入炉燃烧;大颗粒燃煤送入固定床气化炉9内进行气化。气化气经风机2及气化气管路7送入锅炉3的炉膛空间进行燃烧,助燃空气经助燃空气管路8送入锅炉3的炉膛内助燃。The process is as follows: the coal from the public coal delivery system is transported through the
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CN105003911A (en) * | 2015-08-05 | 2015-10-28 | 冯之军 | Biomass furnace and device for removing nitric oxide in same |
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