CN202237748U - SNCR (selective non catalytic reduction) flue gas denitration device taking carbamide as reducing agent - Google Patents
SNCR (selective non catalytic reduction) flue gas denitration device taking carbamide as reducing agent Download PDFInfo
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- CN202237748U CN202237748U CN201120294665XU CN201120294665U CN202237748U CN 202237748 U CN202237748 U CN 202237748U CN 201120294665X U CN201120294665X U CN 201120294665XU CN 201120294665 U CN201120294665 U CN 201120294665U CN 202237748 U CN202237748 U CN 202237748U
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- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 title claims abstract description 222
- 239000004202 carbamide Substances 0.000 title claims abstract description 221
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 title claims abstract description 21
- 239000003546 flue gas Substances 0.000 title claims abstract description 21
- 239000003638 chemical reducing agent Substances 0.000 title claims abstract description 14
- 238000010531 catalytic reduction reaction Methods 0.000 title description 3
- 235000013877 carbamide Nutrition 0.000 title 1
- 239000007787 solid Substances 0.000 claims abstract description 41
- 239000008235 industrial water Substances 0.000 claims abstract description 40
- 238000002360 preparation method Methods 0.000 claims abstract description 27
- 238000002485 combustion reaction Methods 0.000 claims abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 29
- 239000007921 spray Substances 0.000 claims description 21
- 239000007788 liquid Substances 0.000 claims description 13
- 238000001816 cooling Methods 0.000 claims 5
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims 3
- 238000010438 heat treatment Methods 0.000 claims 2
- 230000008676 import Effects 0.000 claims 1
- 239000000243 solution Substances 0.000 abstract description 58
- 230000001105 regulatory effect Effects 0.000 abstract description 56
- 238000002347 injection Methods 0.000 abstract description 26
- 239000007924 injection Substances 0.000 abstract description 26
- 230000000694 effects Effects 0.000 abstract description 4
- 238000009924 canning Methods 0.000 abstract 1
- 239000003595 mist Substances 0.000 abstract 1
- 238000002156 mixing Methods 0.000 description 22
- 238000000034 method Methods 0.000 description 6
- 239000002245 particle Substances 0.000 description 5
- 238000005260 corrosion Methods 0.000 description 4
- 230000007797 corrosion Effects 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 230000009286 beneficial effect Effects 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- 238000004090 dissolution Methods 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- 230000009466 transformation Effects 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000011362 coarse particle Substances 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000006722 reduction reaction Methods 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
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Abstract
本实用新型公开了一种以尿素为还原剂的SNCR烟气脱硝装置。包括固体尿素罐车、软管、活接头、固体尿素调节阀、固体尿素储罐、固体尿素给料机、压缩空气总管、压缩空气调节阀、搅拌器、尿素溶液制备罐、加热器、工业水总管、工业水调节阀、尿素输送泵、尿素溶液储存罐、尿素喷射泵、混合器、尿素回流调节阀、加压工业水调节阀、工业水泵、尿素稀溶液调节阀、雾化蒸汽调节阀、雾化蒸汽总管、尿素喷射单元。在罐装尿素时,实现全自动连续给料,保证尿素溶液的浓度和均匀性,根据燃烧设备NOx排放量自动调节尿素流量,使得燃烧设备NOx排放量在控制范围内,脱硝效果在60%;在袋装尿素供应时,由人工投入尿素溶液制备罐,尿素制备为间断运行。
The utility model discloses an SNCR flue gas denitrification device using urea as a reducing agent. Including solid urea tank truck, hose, union, solid urea regulating valve, solid urea storage tank, solid urea feeder, compressed air main pipe, compressed air regulating valve, agitator, urea solution preparation tank, heater, industrial water main pipe , industrial water regulating valve, urea delivery pump, urea solution storage tank, urea injection pump, mixer, urea return regulating valve, pressurized industrial water regulating valve, industrial water pump, urea dilute solution regulating valve, atomizing steam regulating valve, mist Steam header, urea injection unit. When canning urea, it realizes automatic continuous feeding to ensure the concentration and uniformity of urea solution, and automatically adjusts the urea flow rate according to the NOx emission of the combustion equipment, so that the NOx emission of the combustion equipment is within the control range, and the denitrification effect is 60%; When the bagged urea is supplied, the urea solution preparation tank is manually put into the urea preparation tank, and the urea preparation is intermittent operation.
Description
技术领域 technical field
本实用新型涉及一种烟气脱硝装置,特别是涉及一种以尿素为还原剂的SNCR烟气脱硝装置。 The utility model relates to a flue gas denitrification device, in particular to an SNCR flue gas denitrification device using urea as a reducing agent.
背景技术 Background technique
在烟气脱硝领域, 选择性催化还原(SCR)和非选择性催化还原(SNCR)两种方法得到了广泛应用。此两种方法均以NH3等为还原剂,把NOx还原为无害的N2和H2O。SNCR方法是将氨或尿素等还原剂水溶液喷入850~1150℃的烟气当中,实现NOx的还原反应。由于其基本不占用燃烧设备的空间,改造工作量小,改造周期短,因而得到较大的应用。由于尿素稳定性好,无毒无害,安全性高,便于储藏,因此采用尿素作为SNCR方法的还原剂是最佳选择。由于尿素是固体颗粒,在水中溶解需要吸热,而且具有一定的腐蚀性,尤其是稀释后的浓度、均匀性以及雾化颗粒粒度分布、喷入的温度窗口等对脱硝效果影响很大。目前SNCR技术的实际脱硝效率仅30%左右,而且已经发生喷入部位水冷壁腐蚀情况,这制约了SNCR技术的应用。 In the field of flue gas denitrification, two methods, selective catalytic reduction (SCR) and non-selective catalytic reduction (SNCR), have been widely used. These two methods both use NH 3 as a reducing agent to reduce NOx to harmless N 2 and H 2 O. The SNCR method is to spray a reducing agent aqueous solution such as ammonia or urea into the flue gas at 850~1150°C to realize the reduction reaction of NOx. Because it basically does not occupy the space of combustion equipment, the transformation workload is small, and the transformation period is short, so it has been widely used. Because urea has good stability, is non-toxic and harmless, has high safety and is easy to store, it is the best choice to use urea as the reducing agent in the SNCR method. Since urea is a solid particle, it needs to absorb heat when dissolving in water, and has a certain degree of corrosiveness, especially the diluted concentration, uniformity, particle size distribution of atomized particles, and sprayed temperature window have a great impact on the denitrification effect. At present, the actual denitrification efficiency of SNCR technology is only about 30%, and corrosion of the water wall at the injection site has already occurred, which restricts the application of SNCR technology.
发明内容 Contents of the invention
为了解决背景技术中存在的问题,本实用新型的目的在于提供一种以尿素为还原剂的SNCR烟气脱硝装置,解决固体尿素颗粒溶解、混合和喷射等问题,实现SNCR装置自动化高效可靠工作。 In order to solve the problems existing in the background technology, the purpose of this utility model is to provide an SNCR flue gas denitrification device using urea as a reducing agent to solve the problems of solid urea particle dissolution, mixing and spraying, and realize the automatic, efficient and reliable operation of the SNCR device.
本实用新型解决其技术问题所采用的技术方案是: The technical scheme that the utility model solves its technical problem adopts is:
本实用新型包括搅拌器、尿素溶液制备罐、加热器、工业水总管、工业水调节阀、尿素输送泵、尿素溶液储存罐、尿素喷射泵、混合器、尿素回流调节阀、加压工业水调节阀、工业水泵、尿素稀溶液调节阀、雾化蒸汽调节阀、雾化蒸汽总管和尿素喷射单元;尿素溶液制备罐上部经工业水调节阀和工业水总管相连通,尿素溶液制备罐内装设有第一加热器和搅拌器,通过尿素输送泵使尿素溶液制备罐和尿素溶液储存罐的连通;尿素溶液储存罐内设置第二加热器,尿素喷射泵入口与尿素溶液储存罐的下部相连通,尿素喷射泵出口分别与混合器和尿素回流调节阀的一端相连,尿素回流调节阀的另一端与尿素溶液储存罐的上部相连通;混合器的中间与加压工业水调节阀的一端相连通,加压工业水调节阀的另一端与工业水泵出口相连通,工业水泵的进口与工业水总管相连通;混合器的另一端与尿素稀溶液调节阀的一端连通,尿素稀溶液调节阀的另一端与尿素喷射单元相连通;尿素喷射单元还与雾化蒸汽调节阀的一端连通,雾化蒸汽调节阀的另一端与雾化蒸汽总管连通。 The utility model comprises a stirrer, a urea solution preparation tank, a heater, an industrial water main pipe, an industrial water regulating valve, a urea delivery pump, a urea solution storage tank, a urea injection pump, a mixer, a urea return regulating valve, and a pressurized industrial water regulating valve. Valve, industrial water pump, urea dilute solution regulating valve, atomizing steam regulating valve, atomizing steam main pipe and urea injection unit; the upper part of the urea solution preparation tank is connected with the industrial water main pipe through the industrial water regulating valve, and the urea solution preparation tank is equipped with The first heater and the agitator communicate with the urea solution preparation tank and the urea solution storage tank through the urea delivery pump; the second heater is arranged in the urea solution storage tank, and the urea injection pump inlet communicates with the lower part of the urea solution storage tank, The outlet of the urea injection pump is connected to the mixer and one end of the urea return regulating valve, and the other end of the urea return regulating valve is connected to the upper part of the urea solution storage tank; the middle of the mixer is connected to one end of the pressurized industrial water regulating valve, The other end of the pressurized industrial water regulating valve is connected with the outlet of the industrial water pump, and the inlet of the industrial water pump is connected with the industrial water main; the other end of the mixer is connected with one end of the urea dilute solution regulating valve, and the other end of the urea dilute solution regulating valve It communicates with the urea injection unit; the urea injection unit also communicates with one end of the atomizing steam regulating valve, and the other end of the atomizing steam regulating valve communicates with the atomizing steam main pipe.
在所述的尿素溶液制备罐上端还经固体尿素给料机与固体尿素储罐下端连通,固体尿素储罐上端经固体尿素调节阀、活接头、软管与固体尿素罐车连接。 The upper end of the urea solution preparation tank is also connected to the lower end of the solid urea storage tank through a solid urea feeder, and the upper end of the solid urea storage tank is connected to the solid urea tank truck through a solid urea regulating valve, a union, and a hose.
所述的混合器:包括尿素嘴、水管和混合嘴;尿素嘴的大端大孔与尿素喷射泵出口相连,尿素嘴的小端外部呈锥形,锥形内部开有小孔,尿素嘴大孔和小孔相连通;混合嘴的进口端与尿素嘴的凸肩相配合,混合嘴进口端向出口端方向外依次是大孔、锥孔、小孔,混合嘴出口端内部开有与混合嘴进口端内小孔相连通的大孔,混合嘴进口端内部的大孔与水管的一端相连通,水管的另一端与加压工业水调节阀的一端相连通,混合嘴出口端与尿素稀溶液调节阀的一端连通。 The mixer: includes a urea nozzle, a water pipe and a mixing nozzle; the large end of the urea nozzle is connected to the outlet of the urea injection pump, the small end of the urea nozzle is tapered, and there is a small hole inside the cone, and the urea nozzle is large The hole and the small hole are connected; the inlet end of the mixing nozzle matches the shoulder of the urea nozzle, and the inlet end of the mixing nozzle is followed by a large hole, a tapered hole, and a small hole in the direction of the outlet end, and there is a mixing hole inside the outlet end of the mixing nozzle. The small hole in the inlet end of the mixing nozzle is connected to the large hole, the large hole in the inlet end of the mixing nozzle is connected to one end of the water pipe, the other end of the water pipe is connected to one end of the pressurized industrial water regulating valve, and the outlet end of the mixing nozzle is connected to the urea dilute One end of the solution regulating valve is connected.
所述的尿素喷射单元:包括尿素喷枪、两块梳形板、两块侧墙板、盖板和水冷壁管束;第一梳形板、第一侧墙板、第二梳形板、第二侧墙板围成立方形框,立方形框的一侧盖有盖板,立方形框的另一侧是水冷壁管束的一侧,水冷壁管束的另一侧是高温烟气,每根水冷壁管安装在梳形板槽中定位;水冷壁管束的其中一根水冷壁管向盖板圆弧形弯曲,盖板中心开有圆孔,尿素喷枪穿过盖板中心圆孔和水冷壁管束圆弧形空隙。 The urea injection unit: includes a urea spray gun, two comb-shaped plates, two side wall plates, a cover plate and a water wall tube bundle; the first comb-shaped plate, the first side wall plate, the second comb-shaped plate, the second The side wall panels form a rectangular frame, one side of the cubic frame is covered with a cover plate, the other side of the cubic frame is one side of the water-cooled wall tube bundle, and the other side of the water-cooled wall tube bundle is high-temperature flue gas, each water-cooled wall The tubes are installed in the slot of the comb-shaped plate and positioned; one of the water-cooled wall tubes in the water-cooled wall tube bundle is bent toward the cover plate in an arc shape, and a round hole is opened in the center of the cover plate, and the urea spray gun passes through the center hole of the cover plate and the circle of the water-cooled wall tube bundle. arc gap.
所述的两个加热器采用电加热或采用蒸汽加热。所述的尿素喷射单元安装于燃烧设备850~1150℃烟气处。所述的尿素喷射单元为一个单元或是多个单元并联。 The two heaters are heated by electricity or by steam. The urea injection unit is installed at the flue gas of combustion equipment at 850-1150°C. The urea injection unit is one unit or multiple units connected in parallel.
本实用新型具有的有益效果是: The beneficial effect that the utility model has is:
在具备罐装尿素的条件下,可以实现罐装尿素的全自动连续给料,并保证尿素溶液的浓度和均匀性,根据燃烧设备NOx排放量自动调节尿素流量,使得燃烧设备NOx排放量在控制范围内,脱硝效果在60%左右,并有效防止水冷壁的腐蚀。在袋装尿素供应的条件下,由人工直接将袋装尿素破拆投入尿素溶液制备罐,尿素制备采用间断运行方式,其余与具备罐装尿素的方式相同。 Under the condition of canned urea, it can realize the automatic continuous feeding of canned urea, and ensure the concentration and uniformity of the urea solution, and automatically adjust the urea flow rate according to the NOx emission of the combustion equipment, so that the NOx emission of the combustion equipment is under control. Within the range, the denitrification effect is about 60%, and it can effectively prevent the corrosion of the water wall. Under the condition of bagged urea supply, the bagged urea is directly dismantled and put into the urea solution preparation tank manually, and the urea preparation adopts the intermittent operation mode, and the rest is the same as that with canned urea.
附图说明 Description of drawings
图1是本实用新型的SNCR尿素系统布置示意图。 Figure 1 is a schematic diagram of the layout of the SNCR urea system of the present invention.
图2是本实用新型的混合器正视图。 Fig. 2 is a front view of the mixer of the present invention.
图3是本实用新型的SNCR尿素系统布置示意图的A-A剖视图。 Fig. 3 is an A-A cross-sectional view of a schematic layout of the SNCR urea system of the present invention.
图中:1、固体尿素罐车,2、软管,3、活接头,4、固体尿素调节阀,5、固体尿素储罐,6、固体尿素给料机,7、压缩空气总管,8、压缩空气调节阀,9、搅拌器,10、尿素溶液制备罐,11、加热器,12、工业水总管,13、工业水调节阀,14、尿素输送泵,15、尿素溶液储存罐,16、尿素喷射泵,17、混合器,18、尿素回流调节阀,19、加压工业水调节阀,20、工业水泵,21、尿素稀溶液调节阀,22、雾化蒸汽调节阀,23、雾化蒸汽总管,24、尿素喷射单元,25、尿素嘴,26、水管,27、混合嘴,28、尿素喷枪,29、梳形板,30、侧墙板,31、盖板,32、水冷壁管束。 In the figure: 1. Solid urea tank truck, 2. Hose, 3. Union joint, 4. Solid urea regulating valve, 5. Solid urea storage tank, 6. Solid urea feeder, 7. Compressed air main pipe, 8. Compression Air regulating valve, 9. Agitator, 10. Urea solution preparation tank, 11. Heater, 12. Industrial water main, 13. Industrial water regulating valve, 14. Urea delivery pump, 15. Urea solution storage tank, 16. Urea Jet pump, 17, mixer, 18, urea reflux regulating valve, 19, pressurized industrial water regulating valve, 20, industrial water pump, 21, urea dilute solution regulating valve, 22, atomizing steam regulating valve, 23, atomizing steam Main pipe, 24, urea injection unit, 25, urea nozzle, 26, water pipe, 27, mixing nozzle, 28, urea spray gun, 29, comb plate, 30, side wall plate, 31, cover plate, 32, water wall tube bundle.
具体实施方式 Detailed ways
下面结合附图和实施例对本实用新型作进一步说明。 Below in conjunction with accompanying drawing and embodiment the utility model is further described.
如图1、图2、图3所示,本实用新型包括搅拌器9、尿素溶液制备罐10、加热器11、工业水总管12、工业水调节阀13、尿素输送泵14、尿素溶液储存罐15、尿素喷射泵16、混合器17、尿素回流调节阀18、加压工业水调节阀19、工业水泵20、尿素稀溶液调节阀21、雾化蒸汽调节阀22、雾化蒸汽总管23、尿素喷射单元24。尿素溶液制备罐10上部通过工业水调节阀13和相应管道与工业水总管12相连通。尿素溶液制备罐10内装设第一加热器11和搅拌器9。通过尿素输送泵14和相应管道实现尿素溶液制备罐10和尿素溶液储存罐15的连通。尿素溶液储存罐15内设置第二加热器11。尿素喷射泵16入口通过管道与尿素溶液储存罐15的下部相连通,尿素喷射泵16出口通过管道分别与混合器17和尿素回流调节阀18的一端相连,尿素回流调节阀18的另一端与尿素溶液储存罐15的上部相连通。混合器17的中间通过管道与加压工业水调节阀19的一端相连通,加压工业水调节阀19的另一端与工业水泵20出口相连通,工业水泵20的进口与工业水总管12相连通。混合器17的另一端通过管道与尿素稀溶液调节阀21的一端连通,尿素稀溶液调节阀21的另一端与尿素喷射单元24相连通。尿素喷射单元24还通过管道与雾化蒸汽调节阀22的一端连通,雾化蒸汽调节阀22的另一端与雾化蒸汽总管23连通。
As shown in Fig. 1, Fig. 2 and Fig. 3, the utility model comprises agitator 9, urea
如图1所示,如果在具备罐装尿素的条件下,它还包括固体尿素罐车1、软管2、活接头3、固体尿素调节阀4、固体尿素储罐5、固体尿素给料机6、压缩空气总管7、压缩空气调节阀8;通过软管2、活接头3、固体尿素调节阀4和相应管道使固体尿素罐车1和固体尿素储罐5相连通,通过气力输送可以把固体尿素送到固体尿素储罐5内,通过管道把固体尿素给料机6串联在固体尿素储罐5下部和尿素溶液制备罐10上部,固体尿素储罐5下部通过压缩空气调节阀8和相应管道与压缩空气总管7相连通。
As shown in Figure 1, if the canned urea is available, it also includes solid urea tank truck 1, hose 2,
如图2所示,所述混合器17:包括尿素嘴25、水管26和混合嘴27;尿素嘴25的大端大孔与尿素喷射泵16出口相连,尿素嘴25的大端外部为圆柱体,内部开有大孔,尿素嘴25的小端外部呈锥形,锥形内部开有小孔,尿素嘴25大孔和小孔相连通;混合嘴27的进口端与尿素嘴25的凸肩相配合,混合嘴27外部呈圆柱体,混合嘴27进口端向出口端方向外依次是大孔、锥孔、小孔,混合嘴27出口端内部开有与混合嘴27进口端内小孔相连通的大孔,混合嘴27进口端内部的大孔与水管26的一端相连通,水管26的另一端与加压工业水调节阀(19)的一端相连通,混合嘴27出口端与尿素稀溶液调节阀21的一端连通。
As shown in Figure 2, the mixer 17: includes a
如图1、图3所示,所述的尿素喷射单元24:包括尿素喷枪28、两块梳形板29、两块侧墙板30、盖板31和水冷壁管束32;第一梳形板29、第一侧墙板30、第二梳形板29、第二侧墙板30围成立方形框,立方形框的一侧盖有盖板31,立方形框的另一侧是水冷壁管束32的一侧,水冷壁管束32的另一侧是高温烟气,每根水冷壁管安装在梳形板槽中定位;水冷壁管束32的其中一根向盖板31圆弧形弯曲,盖板31中心开有圆孔,尿素喷枪28穿过盖板中心圆孔和水冷壁管束32圆弧形空隙。
As shown in Figures 1 and 3, the urea injection unit 24: includes a
所述的两个加热器11采用电加热或采用蒸汽加热。所述的尿素喷射单元24安装于燃烧设备850~1150℃烟气处。所述的尿素喷射单元24为一个单元或是多个单元并联。
The two heaters 11 are heated by electricity or by steam. The
本实用新型的工作过程如下: The working process of the present utility model is as follows:
一、在具备罐装尿素的条件下: 1. Under the condition of having canned urea:
可以把罐装尿素通过气力输送至固体尿素储罐5,通过固体尿素给料机6实现固体尿素的连续均匀计量给料,而采用压缩空气可以保证固体尿素颗粒给料的可靠性,避免尿素由于吸潮积块而导致给料堵塞。由于尿素在水中溶解需要吸热,因此尿素溶液制备罐10配置加热器11,控制其温度在50℃左右,配置搅拌器9可以加速尿素溶解。制备好的尿素溶液通过尿素输送泵14打到尿素溶液储存罐15备用,通过调节工业水调节阀13开度和固体尿素给料机6给料量可以维持尿素溶液制备罐10的液位和尿素溶液浓度不变。尿素溶液储存罐15配备加热器11,以保持温度不变。采用尿素喷射泵16、工业水泵20和混合器17对尿素溶液进行稀释,一般情况下,通过加压工业水调节阀保证混合器17前的压力不变,根据燃烧设备NOx的排放量通过尿素回流调节阀18调节尿素稀溶液浓度,保证NOx排放在控制范围内。混合器17的混合嘴进口由大孔逐渐收缩为小孔,一方面通过节流降低混合点的压力,有利于扩大尿素溶液的压力调节范围,另一方面有利于尿素溶液与工业水的均匀混合。尿素喷射单元包括尿素喷枪28、梳形板29、侧墙板30、盖板31、水冷壁管束32,由梳形板29、侧墙板30、盖板31、水冷壁管束32组成尿素喷枪固定支架,保证喷枪几何位置,避免尿素喷到水冷壁管而导致其腐蚀。采用雾化蒸汽对尿素稀溶液进行雾化,做到粗细颗粒按要求搭配,提高尿素稀溶液与烟气的混合效果。采用以上技术,可以实现SNCR系统全自动连续运行,并保证脱硝率在60%左右,有效避免水冷壁的腐蚀。
The canned urea can be conveyed to the solid urea storage tank 5 by pneumatic force, and the continuous and uniform metering and feeding of solid urea can be realized through the solid urea feeder 6, and the use of compressed air can ensure the reliability of solid urea particle feeding, avoiding the The feed blockage is caused by moisture absorption and accumulation. Since urea needs to absorb heat when dissolving in water, the urea
二、在袋装尿素供应的条件下: 2. Under the conditions of bagged urea supply:
取消固体尿素罐车1、软管2、活接头3、固体尿素调节阀4、固体尿素储罐5、固体尿素给料机6、压缩空气总管7、压缩空气调节阀8;由人工直接将袋装尿素破拆投入尿素溶液制备罐10,尿素制备采用间断运行方式,即首先调节并维持尿素溶液制备罐10的温度和液位,根据液位计算出工业水重量,按浓度要求人工投入相应重量的尿素,然后启动搅拌器8并运行一定时间,最后将尿素溶液通过尿素输送泵14打到尿素溶液储存罐15,其它与具备罐装尿素的条件相同。
Cancellation of solid urea tank car 1, hose 2,
上述具体实施方式用来解释说明本实用新型,而不是对本实用新型进行限制,在本实用新型的精神和权利要求的保护范围内,对本实用新型作出的任何修改和改变,都落入本实用新型的保护范围。 The above-mentioned specific embodiments are used to explain the utility model, rather than to limit the utility model. Within the spirit of the utility model and the scope of protection of the claims, any modifications and changes made to the utility model fall into the scope of the utility model. scope of protection.
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CN102274687A (en) * | 2011-08-15 | 2011-12-14 | 浙江大学 | SNCR (Selective Non-Catalytic Reduction) flue gas denitration device taking urea as reducting agent |
CN102824841A (en) * | 2012-08-21 | 2012-12-19 | 杨建华 | Selective non-catalytic reduction (SNCR) denitration system of coal-fired circulating fluidized bed boiler |
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CN102274687A (en) * | 2011-08-15 | 2011-12-14 | 浙江大学 | SNCR (Selective Non-Catalytic Reduction) flue gas denitration device taking urea as reducting agent |
CN102824841A (en) * | 2012-08-21 | 2012-12-19 | 杨建华 | Selective non-catalytic reduction (SNCR) denitration system of coal-fired circulating fluidized bed boiler |
CN102824841B (en) * | 2012-08-21 | 2015-04-29 | 郑州电力高等专科学校 | Selective non-catalytic reduction (SNCR) denitration system of coal-fired circulating fluidized bed boiler |
CN102921284A (en) * | 2012-10-11 | 2013-02-13 | 浙江省环境保护科学设计研究院 | A method and device for controlling NOx concentration in cement kiln flue gas |
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