CN110090523A - One kind being used for the quenched reforming apparatus of sintering flue gas - Google Patents
One kind being used for the quenched reforming apparatus of sintering flue gas Download PDFInfo
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Abstract
一种用于烧结烟气调质改性装置,包括有粉仓,粉仓与压缩空气系统通过管道连接,粉仓底部的管道上有手动插板门和旋转给料阀,旋转给料阀与喷射器连接,喷射器与风机连接,风机来的自然风与粉仓内的调质粉料在喷射器内混合;喷射器还通过管道与气均布器连接,气均布器与粉料喷枪连接,粉料喷枪与压缩空气系统连接并安装在烧结烟气脱硝前烟道上。通过烧结烟气调质剂装置,有效的解决了烧结烟气中烟尘在高温下熔融粘结,堵塞催化剂的问题,同时保障了烧结烟气SCR脱硝系统的安全稳定运行、保证SCR的脱硝效率,保证烧结机系统的安全稳定运行,使烧结烟气NOx达到环保部门要求的排放标准。
A device for tempering and modifying sintering flue gas, including a powder bin, which is connected to the compressed air system through pipelines. The pipeline at the bottom of the powder bin has a manual sliding door and a rotary feeding valve. The rotary feeding valve is connected to the The injector is connected, the injector is connected with the fan, the natural wind from the fan is mixed with the tempered powder in the powder bin in the injector; the injector is also connected with the gas distributor through the pipeline, and the gas distributor is connected with the powder spray gun Connection, the powder spray gun is connected with the compressed air system and installed on the flue before the denitrification of the sintering flue gas. Through the sintering flue gas conditioner device, the problem of soot in the sintering flue gas melting and bonding at high temperature and blocking the catalyst is effectively solved, and at the same time, the safe and stable operation of the sintering flue gas SCR denitrification system is guaranteed, and the denitrification efficiency of SCR is guaranteed. Ensure the safe and stable operation of the sintering machine system, so that the NOx of the sintering flue gas can meet the emission standards required by the environmental protection department.
Description
技术领域technical field
本发明涉及烟气处理技术领域,特别涉及一种用于烧结烟气调质改性装置。The invention relates to the technical field of flue gas treatment, in particular to a conditioning and tempering device for sintering flue gas.
背景技术Background technique
烧结烟气脱硝主流工艺采用SCR(选择性催化还原技术)脱硝工艺,因烧结烟气温度低无法满足SCR脱硝的温度要求,需对烟气进行加热至300℃左右,在此温度下烧结烟气中含有的大量Na+、K+等碱金属物质在高温下发生熔融现象,烟尘发生粘结搭桥,灰尘粘附在催化剂表面,堵塞催化剂孔洞,烟气阻力增大,影响系统的正常运行。The mainstream process of sintering flue gas denitrification adopts SCR (Selective Catalytic Reduction Technology) denitrification process. Because the temperature of sintering flue gas is low, it cannot meet the temperature requirements of SCR denitrification. It is necessary to heat the flue gas to about 300°C. A large amount of alkali metal substances such as Na + and K + contained in the gas will melt at high temperature, and the smoke and dust will bond and bridge.
烧结烟气脱硝在国内刚刚开始,世界范围内对烧结烟气进行脱硝处理的仅有几家,可以说烧结烟气脱硝处于探索阶段,无成熟的技术经验进行参照。国家政策要求烧结烟气脱硝必须进行,在此背景下,只能引用电厂烟气脱硝技术,由于两种烟气特性差别很大,在烧结烟气脱硝建成运行以后,发生堵塞等问题,严重影响脱硝效率及烧结机的安全稳定运行。Sintering flue gas denitrification has just started in China, and there are only a few companies in the world that have denitrified sintering flue gas. It can be said that sintering flue gas denitrification is in the exploratory stage, and there is no mature technical experience for reference. The national policy requires that denitrification of sintering flue gas must be carried out. In this context, only power plant flue gas denitrification technology can be used. Due to the great difference in the characteristics of the two flue gases, after the completion and operation of sintering flue gas denitrification, problems such as blockage will occur, seriously affecting The denitrification efficiency and the safe and stable operation of the sintering machine.
面对这一急需解决的难题,通过拦截,加大吹扫力度等措施,对催化剂的堵塞有一定的效果,但收效甚微,不能从根本上解决堵塞问题。纯机械措施无法解决粘结堵塞问题。Faced with this problem that needs to be solved urgently, measures such as interception and increased blowing intensity have certain effects on catalyst clogging, but the effect is very small, and the clogging problem cannot be fundamentally solved. Purely mechanical measures cannot solve the problem of sticky clogging.
目前国内无通过对脱硝烟气进行调质的技术,本发明从根本上解决烧结烟气高温下熔融搭接堵塞催化剂技术。At present, there is no technology of conditioning and tempering denitrification flue gas in China, and the present invention fundamentally solves the technology of sintering flue gas melting and lapping and clogging the catalyst at high temperature.
发明内容Contents of the invention
为克服现有技术中存在的问题,本发明提供了一种用于烧结烟气调质改性装置。In order to overcome the problems in the prior art, the present invention provides a device for tempering and modifying sintering flue gas.
本发明解决其技术问题所采取的技术方案是:该种用于烧结烟气调质改性装置,包括有粉仓,粉仓与压缩空气系统通过管道连接,粉仓底部的管道上有手动插板门和旋转给料阀,旋转给料阀与喷射器连接,喷射器与风机连接,风机来的自然风与粉仓内的调质粉料在喷射器内混合;喷射器还通过管道与气均布器连接,气均布器与粉料喷枪连接,粉料喷枪与压缩空气系统连接并安装在烧结烟气脱硝前烟道上。The technical solution adopted by the present invention to solve the technical problem is: the device for tempering and modifying sintering flue gas includes a powder bin, which is connected to the compressed air system through a pipeline, and there is a manual plug on the pipeline at the bottom of the powder bin. The plate door and the rotary feed valve, the rotary feed valve is connected with the injector, the injector is connected with the fan, the natural wind from the fan is mixed with the tempered powder in the powder bin in the injector; the injector is also connected with the air through the pipeline The uniform distributor is connected, the gas distributor is connected with the powder spray gun, the powder spray gun is connected with the compressed air system and installed on the flue before the sintering flue gas denitrification.
进一步地,所述粉仓顶部安装有布袋除尘器。Further, a bag filter is installed on the top of the powder bin.
进一步地,压缩空气系统与粉仓之间的管道上安装有电加热器。Further, an electric heater is installed on the pipeline between the compressed air system and the powder bin.
进一步地,所述旋转给料阀为变频,布置于喷射泵的上部,将来自粉仓的粉料均匀定量的送入到喷射器内。Further, the rotary feeding valve is frequency-variable, arranged on the upper part of the jet pump, and sends the powder from the powder bin into the jet evenly and quantitatively.
进一步地,所述粉仓底部设流化装置,流化装置包括均布在粉仓底部的流化板,对应每一流化板设有开关阀,来自压缩空气系统的风通过流化板对粉仓内的粉料进行流化。Further, a fluidization device is provided at the bottom of the powder silo, and the fluidization device includes fluidization plates evenly distributed at the bottom of the powder silo, and a switch valve is provided corresponding to each fluidization plate, and the wind from the compressed air system passes through the fluidization plate to the powder. The powder in the bin is fluidized.
进一步地,所述风机为罗茨风机,罗茨风机包括两台,两台罗茨风机通过管道与喷射器连接。Further, the blower is a Roots blower, and there are two Roots blowers, and the two Roots blowers are connected to the injector through a pipeline.
综上,本发明的上述技术方案的有益效果如下:In summary, the beneficial effects of the technical solution of the present invention are as follows:
通过烧结烟气调质剂装置,有效的解决了烧结烟气中烟尘在高温下熔融粘结,堵塞催化剂的问题,同时保障了烧结烟气SCR脱硝系统的安全稳定运行、保证SCR的脱硝效率,保证烧结机系统的安全稳定运行,使烧结烟气NOx达到环保部门要求的排放标准。Through the sintering flue gas conditioner device, the problem of soot in the sintering flue gas melting and bonding at high temperature and blocking the catalyst is effectively solved, and at the same time, the safe and stable operation of the sintering flue gas SCR denitrification system is guaranteed, and the denitrification efficiency of SCR is guaranteed. Ensure the safe and stable operation of the sintering machine system, so that the NOx of the sintering flue gas can meet the emission standards required by the environmental protection department.
附图说明Description of drawings
图1为本发明结构示意图。Fig. 1 is a schematic diagram of the structure of the present invention.
图2为喷枪与烟气管道的安装位置关系示意图。Fig. 2 is a schematic diagram of the installation position relationship between the spray gun and the flue gas pipe.
图中:In the picture:
1.罗茨风机,2.喷射器3.旋转给料阀,4.手动插板门,5.流化装置,6.粉仓,7.布袋除尘器,8.气均布器,9.喷枪,10.电加热器,11.压缩空气系统,12.烟道。1. Roots blower, 2. Ejector 3. Rotary feeding valve, 4. Manual sliding door, 5. Fluidization device, 6. Powder bin, 7. Bag filter, 8. Gas uniform distributor, 9. Spray gun, 10. Electric heater, 11. Compressed air system, 12. Flue.
具体实施方式Detailed ways
以下结合附图对本发明的特征和原理进行详细说明,所举实施例仅用于解释本发明,并非以此限定本发明的保护范围。The features and principles of the present invention will be described in detail below in conjunction with the accompanying drawings, and the examples given are only used to explain the present invention, not to limit the protection scope of the present invention.
如图1和图2所示,该种用于烧结烟气调质改性装置,包括有粉仓6,粉仓6与压缩空气系统11通过管道连接,粉仓6底部的管道上有手动插板门4 和旋转给料阀3,旋转给料阀3与喷射器2连接,喷射器2与风机连接,风机来的自然风与粉仓6内的调质粉料在喷射器2内混合;喷射器2还通过管道与气均布器8连接,气均布器8与粉料喷枪9连接,粉料喷枪9与压缩空气系统 11连接并安装在烧结烟气脱硝前烟道12上。As shown in Figure 1 and Figure 2, this kind of device for sintering flue gas conditioning and modification includes a powder bin 6, which is connected to the compressed air system 11 through pipelines, and there is a manual insert on the pipeline at the bottom of the powder bin 6 Plate door 4 and rotary feed valve 3, rotary feed valve 3 is connected with injector 2, injector 2 is connected with fan, the natural wind from fan is mixed with the tempered powder in powder bin 6 in injector 2; The injector 2 is also connected to the gas distributor 8 through the pipeline, the gas distributor 8 is connected to the powder spray gun 9, and the powder spray gun 9 is connected to the compressed air system 11 and installed on the flue 12 before the sintering flue gas denitrification.
在粉仓6顶部安装有布袋除尘器7。A bag filter 7 is installed on the top of the powder bin 6 .
压缩空气系统11与粉仓6之间的管道上安装有电加热器10,电加热器10 对来自压缩空气系统11的压缩空气进行加热后通入粉仓6内。An electric heater 10 is installed on the pipeline between the compressed air system 11 and the powder bin 6 , and the electric heater 10 passes into the powder bin 6 after heating the compressed air from the compressed air system 11 .
粉仓6底部设流化装置5,流化装置5包括均布在粉仓6底部的流化板,对应每一流化板设有开关阀,来自压缩空气系统11的风通过流化板对粉仓6 内的粉料进行流化。A fluidization device 5 is arranged at the bottom of the powder bin 6, and the fluidization device 5 includes a fluidization plate evenly distributed at the bottom of the powder bin 6, and an on-off valve is provided corresponding to each fluidization plate, and the wind from the compressed air system 11 passes through the fluidization plate to the powder. The powder in bin 6 is fluidized.
旋转给料阀3为变频,布置于喷射泵的上部,将来自粉仓6的粉料均匀定量的送入到喷射器2内。The rotary feeding valve 3 is frequency-converted, and is arranged on the upper part of the jet pump, and sends the powder from the powder bin 6 into the injector 2 evenly and quantitatively.
风机为罗茨风机1,罗茨风机1包括两台,两台罗茨风机1通过管道与喷射器2连接。The blower is a Roots blower 1, and the Roots blower 1 includes two sets, and the two Roots blowers 1 are connected to the ejector 2 through a pipeline.
该装置的工作原理:How the device works:
调质剂粉料储存在粉仓6内,本系统采用稀相输送(当流化介质速度较大时,固体颗粒开始带出。随着流化介质速度增大,颗粒夹带也愈多;这时空隙率增大,压降下降;固体颗粒在流体中形成悬浮状态的稀相,并与流体从流化床中一起夹带出去,这一个阶段就叫做气流输送阶段,也叫做稀相输送),设有两台罗茨风机1用于输送调质剂粉料,罗茨风机1来的自然风与调质剂粉料在喷射器2(喷射器2,又名:引射器、射流真空泵、射流真空喷射器2、喷射泵、水喷射器2、真空喷射器2,是利用流体来传递能量和质量的真空获得装置,采用有一定压力的水流通过对称均布成一定侧斜度的喷嘴喷出,聚合在一个焦点上;由于喷射水流速特别高,将压力能转变为速度能,使吸气区压力降低产生真空)内混合,在罗茨风机1的作用下以一定的速度由喷射器2的喷射泵喷出,通过输送管道输送到气均布器8,将粉气混合料均匀的分布到粉料喷枪9内。同时,粉料喷枪9还设有一个压缩空气接口,压缩空气的作用是将粉气混合物雾化成细小的颗粒,在压缩空气的推动下粉气混合物高速喷入到烟道中,在烟道内细微的调质粉颗粒与烟气中的灰尘快速进行反应,在短时间内完成烟尘改性的目的。The conditioner powder is stored in the powder bin 6, and the system adopts dilute phase transportation (when the velocity of the fluidized medium is high, the solid particles begin to be carried out. As the velocity of the fluidized medium increases, more particles are entrained; this When the void ratio increases, the pressure drop decreases; the solid particles form a suspended dilute phase in the fluid, and are entrained out of the fluidized bed together with the fluid. This stage is called the airflow conveying stage, also known as dilute phase conveying), There are two Roots blowers 1 for transporting conditioner powder, the natural wind from Roots blower 1 and the conditioner powder are in the ejector 2 (ejector 2, also known as: ejector, jet vacuum pump, Jet vacuum ejector 2, jet pump, water ejector 2, and vacuum ejector 2 are vacuum obtaining devices that use fluid to transfer energy and quality. out, aggregated at a focal point; due to the particularly high flow rate of the jet water, the pressure energy is converted into velocity energy, so that the pressure in the suction area is reduced to generate a vacuum) and mixed in, under the action of the Roots blower 1, the ejector is blown at a certain speed 2, the jet pump sprays out, and transports it to the gas uniform distributor 8 through the delivery pipeline, and evenly distributes the powder-air mixture into the powder spray gun 9. At the same time, the powder spray gun 9 is also provided with a compressed air interface. The function of the compressed air is to atomize the powder-air mixture into fine particles. The tempering powder particles react quickly with the dust in the flue gas, and the purpose of dust modification is completed in a short time.
粉料喷枪9为双流体喷枪9,设有两个接口,一个是粉气混合物接口,一个是压缩空气接口。调质剂粉仓6底部设流化装置5,经过电加热器10加热的流化风通过流化板对粉料起流化作用,以防粉在仓内板结,系统运行。The powder spray gun 9 is a dual-fluid spray gun 9, and is provided with two interfaces, one is a powder-air mixture interface, and the other is a compressed air interface. A fluidization device 5 is installed at the bottom of the conditioner powder bin 6, and the fluidization wind heated by the electric heater 10 fluidizes the powder through the fluidization plate to prevent the powder from compacting in the bin and the system operates.
喷枪9布置在进入SCR反应器前的烟道壁上,在烟道上的布置需要做流场模拟,数量、布置形式、安装形式均需要满足流场的要求,保证粉气混合物能在烟道内与烟气中的烟气以最大面积接触,尽可能混合均匀。The spray gun 9 is arranged on the wall of the flue before entering the SCR reactor. The arrangement on the flue needs to be simulated on the flow field. The quantity, layout and installation form must meet the requirements of the flow field, so as to ensure that the powder-gas mixture can flow in the flue. The flue gas in the flue gas is in contact with the largest area and mixed as evenly as possible.
粉喷射雾化器根据流场模拟布置在烟气壁上,进入粉雾化装置的气粉混合物在压缩空气的作用下被雾化成细微颗粒,喷入到烟道内,调质粉在烟道内与烟气中的烟尘进行均匀混合,在调质剂的作用下,烧结烟气的烟尘特性被改性,原烧结烟尘在高温下熔融粘结,改性后不在粘结,流动性好。本装置可以有效的改变烧结烟气中的烟尘特性,从而避免了烧结烟尘在高温下粘结搭桥,易堵塞催化剂的问题,保证了烧结烟气SCR脱硝系统的正常高效运行。The powder jet atomizer is arranged on the flue gas wall according to the flow field simulation. The gas-powder mixture entering the powder atomization device is atomized into fine particles under the action of compressed air and sprayed into the flue. The soot in the flue gas is uniformly mixed. Under the action of the conditioner, the soot characteristics of the sintering flue gas are modified. The original sintering soot is melted and bonded at high temperature, and after modification, it is no longer bonded and has good fluidity. The device can effectively change the characteristics of the soot in the sintering flue gas, thereby avoiding the problem of the sintering fume bonding and bridging at high temperature, and easily blocking the catalyst, and ensuring the normal and efficient operation of the sintering flue gas SCR denitrification system.
本烧结烟气调质改性装置可以有效的改变烧结烟气中的Na+、K+等碱金属物质在高温下发生熔融粘结特性,烟尘由原来的粘结搭桥变的流动性好,不粘结不粘附,可以很容易的通过催化剂孔洞,从而避免了其对催化剂的堵塞,催化剂失活降低脱硝效率的问题,保证了烧结烟气SCR脱硝系统及烧结机系统的正常高效运行。The sintering flue gas conditioning modification device can effectively change the melting and bonding characteristics of Na+, K+ and other alkali metal substances in the sintering flue gas at high temperature, and the flue dust will change from the original bonding bridging to good fluidity and non-sticking It is not sticky, and can easily pass through the catalyst pores, thus avoiding the blockage of the catalyst and the deactivation of the catalyst to reduce the denitrification efficiency, ensuring the normal and efficient operation of the sintering flue gas SCR denitrification system and the sintering machine system.
上述实施例仅仅是对本发明的优选实施方式进行的描述,并非对本发明的范围进行限定,在不脱离本发明设计精神的前提下,本领域相关技术人员对本发明的各种变形和改进,均应扩入本发明权利要求书所确定的保护范围内。The above-mentioned embodiments are only descriptions of preferred implementations of the present invention, and are not intended to limit the scope of the present invention. On the premise of not departing from the design spirit of the present invention, those skilled in the art should make various modifications and improvements of the present invention. Into the scope of protection defined by the claims of the present invention.
Claims (6)
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| CN201910488697.4A CN110090523A (en) | 2019-06-05 | 2019-06-05 | One kind being used for the quenched reforming apparatus of sintering flue gas |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111068485A (en) * | 2019-12-25 | 2020-04-28 | 天津天钢联合特钢有限公司 | Method for preventing denitration catalyst from being blocked |
| CN111068516A (en) * | 2020-01-18 | 2020-04-28 | 浙江大学 | System and method for multi-strengthened coupled intelligent regulation to prevent deposition of highly viscous ash on catalyst surface |
| CN116242154A (en) * | 2023-03-28 | 2023-06-09 | 首钢集团有限公司 | A method and device for suppressing clogging of a dust collector in a sintering flue gas circulation system |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN202893146U (en) * | 2012-11-21 | 2013-04-24 | 江苏中建材环保研究院有限公司 | Novel flue gas conditioning device for glass melting furnace |
| CN105126540A (en) * | 2015-09-25 | 2015-12-09 | 山东默锐环境产业股份有限公司 | Coal-fired flue gas powder adsorbent jetting mercury removing device |
| CN105817136A (en) * | 2016-06-03 | 2016-08-03 | 镇江京华电力环保工程公司 | Desulphurization system in circulating fluidized bed boiler |
| CN106422748A (en) * | 2016-09-05 | 2017-02-22 | 光大环保(中国)有限公司 | Dry denitrification system |
| CN207076306U (en) * | 2017-04-25 | 2018-03-09 | 广州冉升环保工程有限公司 | The device that a kind of sulfur trioxide in flue gas is administered |
| CN207533026U (en) * | 2017-11-21 | 2018-06-26 | 江苏华本环境科技有限公司 | A kind of high-temperature flue gas Dry denitration device |
| CN210410024U (en) * | 2019-06-05 | 2020-04-28 | 山东国舜建设集团有限公司 | Be used for modified device of sintering flue gas quenching and tempering |
-
2019
- 2019-06-05 CN CN201910488697.4A patent/CN110090523A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN202893146U (en) * | 2012-11-21 | 2013-04-24 | 江苏中建材环保研究院有限公司 | Novel flue gas conditioning device for glass melting furnace |
| CN105126540A (en) * | 2015-09-25 | 2015-12-09 | 山东默锐环境产业股份有限公司 | Coal-fired flue gas powder adsorbent jetting mercury removing device |
| CN105817136A (en) * | 2016-06-03 | 2016-08-03 | 镇江京华电力环保工程公司 | Desulphurization system in circulating fluidized bed boiler |
| CN106422748A (en) * | 2016-09-05 | 2017-02-22 | 光大环保(中国)有限公司 | Dry denitrification system |
| CN207076306U (en) * | 2017-04-25 | 2018-03-09 | 广州冉升环保工程有限公司 | The device that a kind of sulfur trioxide in flue gas is administered |
| CN207533026U (en) * | 2017-11-21 | 2018-06-26 | 江苏华本环境科技有限公司 | A kind of high-temperature flue gas Dry denitration device |
| CN210410024U (en) * | 2019-06-05 | 2020-04-28 | 山东国舜建设集团有限公司 | Be used for modified device of sintering flue gas quenching and tempering |
Non-Patent Citations (1)
| Title |
|---|
| 徐志毅主编: "《环境保护技术和设备》", 上海交通大学出版社, pages: 359 - 360 * |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111068485A (en) * | 2019-12-25 | 2020-04-28 | 天津天钢联合特钢有限公司 | Method for preventing denitration catalyst from being blocked |
| CN111068516A (en) * | 2020-01-18 | 2020-04-28 | 浙江大学 | System and method for multi-strengthened coupled intelligent regulation to prevent deposition of highly viscous ash on catalyst surface |
| CN111068516B (en) * | 2020-01-18 | 2023-11-14 | 浙江大学 | System and method for preventing the deposition of highly viscous ash on the catalyst surface using multi-enhanced coupled intelligent control |
| CN116242154A (en) * | 2023-03-28 | 2023-06-09 | 首钢集团有限公司 | A method and device for suppressing clogging of a dust collector in a sintering flue gas circulation system |
| CN116242154B (en) * | 2023-03-28 | 2025-08-15 | 首钢集团有限公司 | Method and device for inhibiting blockage of dust remover in sintering flue gas circulation system |
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