CN105311925A - Large-scale adsorbent modification coupling jet system for controlling heavy metal pollutant emission in flue gas - Google Patents

Large-scale adsorbent modification coupling jet system for controlling heavy metal pollutant emission in flue gas Download PDF

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CN105311925A
CN105311925A CN201410261836.7A CN201410261836A CN105311925A CN 105311925 A CN105311925 A CN 105311925A CN 201410261836 A CN201410261836 A CN 201410261836A CN 105311925 A CN105311925 A CN 105311925A
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adsorbent
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CN105311925B (en
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张永生
顾永正
曹晏
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North China Electric Power University
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Abstract

本发明公开了属于烟气重金属污染物控制技术领域的吸附剂大规模改性耦合喷射系统。该系统主要包括:储料罐、给料器、进料装置、改性药剂罐、改性主机、旋风分离器、收集料斗、进料器、气固混合加速器、喷射管道及空气压缩机等。工作中吸附剂和药剂按照一定比例加入改性主机中,发生反应并进行化学改性;改性后的吸附剂由进料器控制进入气固混合加速器;在气固混合加速器中吸附剂和气体按照一定的比例混合,然后沿着输送管道喷入烟道中吸附脱除烟气中污染物。该系统适用于烟气中重金属(汞、砷、铅、镉、铬等)污染物及酸性气体如三氧化硫和氯化氢等污染物的脱除。本发明能够实现吸附剂现场大规模改性,具有连续性及封闭性的特点。

The invention discloses a large-scale modified coupling injection system for adsorbents, which belongs to the technical field of flue gas heavy metal pollutant control. The system mainly includes: storage tank, feeder, feeding device, modified agent tank, modified host, cyclone separator, collecting hopper, feeder, gas-solid mixing accelerator, injection pipeline and air compressor, etc. During work, the adsorbent and medicament are added to the modified host according to a certain proportion, react and undergo chemical modification; the modified adsorbent is controlled by the feeder and enters the gas-solid mixing accelerator; in the gas-solid mixing accelerator, the adsorbent and gas Mix according to a certain ratio, and then spray it into the flue along the conveying pipeline to absorb and remove pollutants in the flue gas. The system is suitable for the removal of heavy metals (mercury, arsenic, lead, cadmium, chromium, etc.) and acid gases such as sulfur trioxide and hydrogen chloride in flue gas. The invention can realize large-scale on-site modification of the adsorbent, and has the characteristics of continuity and sealing.

Description

控制烟气重金属污染物排放的大规模吸附剂改性耦合喷射系统Large-Scale Adsorbent Modification Coupled Injection System for Controlling the Emission of Heavy Metal Pollutants in Flue Gas

技术领域 technical field

本发明专利属于烟气重金属污染物排放控制技术领域,特别涉及一种控制烟气中重金属污染物排放的大规模吸附剂改性耦合喷射系统。具体是指在燃煤电厂等现场实现吸附剂大规模改性的耦合气力输送及喷射系统,通过吸附实现脱除烟气中多种污染物,如重金属(汞、砷、铅、镉、铬)以及强酸性气体(三氧化硫和氯化氢)等。 The patent of the invention belongs to the technical field of emission control of heavy metal pollutants in flue gas, and in particular relates to a large-scale adsorbent modified coupling injection system for controlling the emission of heavy metal pollutants in flue gas. Specifically, it refers to the coupled pneumatic conveying and injection system that realizes large-scale modification of adsorbents in coal-fired power plants and other sites, and removes various pollutants in flue gas through adsorption, such as heavy metals (mercury, arsenic, lead, cadmium, chromium) And strong acid gases (sulfur trioxide and hydrogen chloride), etc.

背景技术 Background technique

重金属具有富集性,很难在环境中降解,排放到外界的重金属及其化合物对人体健康以及生态环境有危害大。以重金属汞为例,汞污染物具有化学性质稳定、挥发性强等特点,同时汞污染物在自然环境和生物有机体中具有累积性,所以大气中汞污染问题逐渐引起人们的重视。燃煤电厂等烟气所释放的汞是大气汞污染的主要来源,煤燃烧过程中会形成大量气态汞,气态汞会随着烟气一起排放到大气中。通过吸附剂吸附烟气中的气态汞是主流的燃煤烟气汞污染控制技术之一。该技术中,一般是将吸附剂喷射到烟道中吸附烟气中的气态汞。常用的吸附剂包括碳基吸附剂活性炭以及非碳基吸附剂如飞灰吸附剂等。吸附包括物理吸附和化学吸附,物理吸附能力相对较弱,为了提高吸附剂的吸附能力,通常需要对吸附剂进行化学改性。 Heavy metals are enriched and difficult to degrade in the environment. The heavy metals and their compounds discharged to the outside world are very harmful to human health and the ecological environment. Taking the heavy metal mercury as an example, mercury pollutants have the characteristics of stable chemical properties and strong volatility. At the same time, mercury pollutants are cumulative in the natural environment and biological organisms, so the problem of mercury pollution in the atmosphere has gradually attracted people's attention. Mercury released from flue gas from coal-fired power plants is the main source of atmospheric mercury pollution. A large amount of gaseous mercury will be formed during coal combustion, and gaseous mercury will be emitted into the atmosphere along with the flue gas. Adsorption of gaseous mercury in flue gas by adsorbent is one of the mainstream mercury pollution control technologies in coal-fired flue gas. In this technology, the adsorbent is generally injected into the flue to absorb the gaseous mercury in the flue gas. Commonly used adsorbents include carbon-based adsorbents such as activated carbon and non-carbon-based adsorbents such as fly ash adsorbents. Adsorption includes physical adsorption and chemical adsorption. The physical adsorption capacity is relatively weak. In order to improve the adsorption capacity of the adsorbent, it is usually necessary to chemically modify the adsorbent.

活性炭比表面积较大,吸附能力较强,但价格昂贵。非碳基吸附剂如飞灰是燃煤电厂的煤粉经过燃烧后排出的一种工业固体废弃物,价格便宜,同时有很大的存量。我国对粉煤灰的利用率仅在30%~40%之间,主要用于建筑、水泥等行业。但飞灰对气态汞吸附性差,所以更需要对飞灰进行改性,开发出新型的飞灰基吸附剂。 Activated carbon has a large specific surface area and strong adsorption capacity, but it is expensive. Non-carbon-based adsorbents such as fly ash are industrial solid wastes discharged from coal-fired power plants after combustion. They are cheap and have a large stock. The utilization rate of fly ash in our country is only between 30% and 40%, and it is mainly used in construction, cement and other industries. However, fly ash has poor adsorption to gaseous mercury, so it is more necessary to modify fly ash and develop new fly ash-based adsorbents.

中国专利CN102120174A公开了一种利用卤盐对粉煤灰进行浸渍改性处理的方法,这种方法中吸附剂需要在卤盐溶液中浸渍3~12小时,然后晾干12小时,最后需要放入真空烘箱中烘干24小时。该改性方法适用于实验室规模的研究,难以满足烟气量较大的燃煤电厂等所需吸附剂的喷射量。因此,如何在燃煤电厂对吸附剂进行大规模改性是目前急需解决的问题。 Chinese patent CN102120174A discloses a method of impregnating and modifying fly ash using halogen salts. In this method, the adsorbent needs to be immersed in the halogen salt solution for 3 to 12 hours, then dried for 12 hours, and finally put into Dry in a vacuum oven for 24 hours. This modification method is suitable for laboratory-scale research, but it is difficult to meet the injection volume of adsorbent required by coal-fired power plants with large flue gas volume. Therefore, how to carry out large-scale modification of adsorbents in coal-fired power plants is an urgent problem to be solved.

中国专利CN201614359U公开了一种连续粉体表面改性剂,这种改性剂适用于对无机非金属矿粉填料进行表面改性,物料在改性过程中,通过定子、转子之间的强烈摩擦产生的温度为100~125℃,药剂的熔点一般低于100℃,改性主机中物料和药剂的混合是固体和液体的混合以达到粉体表面改性的效果。 Chinese patent CN201614359U discloses a continuous powder surface modifier. This modifier is suitable for surface modification of inorganic non-metallic mineral powder fillers. During the modification process, the material passes through strong friction between the stator and the rotor. The generated temperature is 100-125°C, and the melting point of the agent is generally lower than 100°C. The mixing of materials and agents in the modified host is a mixture of solid and liquid to achieve the effect of powder surface modification.

目前吸附剂喷射脱汞技术所使用的吸附剂都是以离线生产方式生产,自动化程度较低,并且改性后吸附剂含水率比原吸附剂高,堆积时间过长易造成结块,较难满足燃煤电厂等现场连续运行脱除汞等重金属污染物需求。为了实现对烟气中汞等重金属污染物以及强酸性气体污染物的控制,开发大规模吸附剂现场改性耦合喷射系统具有重要意义。 At present, the adsorbents used in the adsorbent injection mercury removal technology are all produced in an off-line production mode, with a low degree of automation, and the moisture content of the modified adsorbent is higher than that of the original adsorbent. If the accumulation time is too long, it will easily cause agglomeration, which is difficult. It meets the needs of coal-fired power plants and other on-site continuous operations to remove heavy metal pollutants such as mercury. In order to realize the control of heavy metal pollutants such as mercury and strong acid gas pollutants in flue gas, it is of great significance to develop a large-scale adsorbent on-site modification coupling injection system.

发明内容 Contents of the invention

本发明目的是提出一种实现控制烟气中重金属污染物排放的大规模吸附剂改性耦合喷射系统。其特征在于,吸附剂的改性与喷射同时进行,可在现场实现大规模改性,所述系统全部采用电控进行实时控制。经示范电厂试验,所述系统控制重金属(汞、砷、铅、镉、铬)污染以及强酸性气体如三氧化硫和氯化氢等污染物能力强,适用于工业过程烟气中多污染物的控制。 The purpose of the invention is to propose a large-scale adsorbent modification coupled injection system for controlling the emission of heavy metal pollutants in flue gas. It is characterized in that the modification of the adsorbent is carried out at the same time as the spraying, and large-scale modification can be realized on site, and all the systems are electronically controlled for real-time control. After the test of the demonstration power plant, the system has a strong ability to control heavy metal (mercury, arsenic, lead, cadmium, chromium) pollution and strong acid gas such as sulfur trioxide and hydrogen chloride, and is suitable for the control of multiple pollutants in industrial process flue gas .

本发明通过以下方式来实现大规模改性耦合喷射: The present invention realizes large-scale modified coupling injection in the following ways:

所述的吸附剂储料罐1中存放着原始未改性吸附剂,工作时通过给料器2进入变频进料装置3中,改性药剂置于改性药剂罐4中。 The original unmodified adsorbent is stored in the adsorbent storage tank 1, and enters the frequency conversion feeding device 3 through the feeder 2 during operation, and the modifying agent is placed in the modifying agent tank 4.

吸附剂和改性药剂按照一定比例加入改性主机5中,未改性吸附剂在改性主机中发生高速碰撞并发生反应,改性后的吸附剂吸附能力大大提高,同时不会出现吸附剂结块现象。 The adsorbent and the modified agent are added to the modified host 5 according to a certain proportion, and the unmodified adsorbent collides and reacts at a high speed in the modified host, and the adsorption capacity of the modified adsorbent is greatly improved, and at the same time, no adsorbent Agglomeration phenomenon.

所述的改性药剂罐4和改性主机5材料是不锈钢或内部喷上铁氟龙涂层,耐腐蚀和耐磨损性强。 The material of the modified agent tank 4 and the modified host 5 is stainless steel or Teflon coating is sprayed inside, which has strong corrosion resistance and wear resistance.

所述的引风机7为大规模改性系统提供负压,改性后吸附剂受到引风机7的作用进入旋风分离器6中,引风机7出口与输送管道连接,这样可以保证吸附剂改性耦合喷射系统的封闭性,不存在物料质量损失。 The induced draft fan 7 provides negative pressure for the large-scale modification system. After modification, the adsorbent enters the cyclone separator 6 under the action of the induced draft fan 7, and the outlet of the induced draft fan 7 is connected with the delivery pipeline, so that the modified adsorbent can be guaranteed. Coupled with the sealing of the injection system, there is no loss of material quality.

所述的旋风分离器6中的改性吸附剂进入收集料斗8后,由进料器11控制进入气固混合加速器12,进料器11的进料速度与给料器2的进料速度基本一致,保证大规模改性耦合喷射系统的连续性。 After the modified adsorbent in the described cyclone separator 6 enters the collection hopper 8, it is controlled by the feeder 11 to enter the gas-solid mixing accelerator 12, and the feed rate of the feeder 11 is basically the same as that of the feeder 2. Consistent, to ensure the continuity of large-scale modified coupling injection system.

所述的输送弯头13曲率半径是管径的6~12倍,管道内壁衬着3~5mm陶瓷管,有效地提高了输送弯头的使用寿命。 The radius of curvature of the delivery elbow 13 is 6-12 times of the pipe diameter, and the inner wall of the pipeline is lined with a 3-5mm ceramic tube, which effectively improves the service life of the delivery elbow.

所述的罗茨风机9是吸附剂喷射系统的驱动元件,排空阀10起到调节输送管路所需风量的作用。系统压力损失过大时,罗茨风机9可换用空气压缩机。 The Roots blower 9 is the driving element of the adsorbent injection system, and the emptying valve 10 plays the role of adjusting the required air volume of the conveying pipeline. When the system pressure loss is too large, the Roots blower 9 can be replaced with an air compressor.

所述的喷射管道14进料方式为两端同时进料,此时管道内部颗粒和压力分布更加均匀,喷射到烟道15内的吸附剂分散效果好,防止管道堵塞。所述的吸附剂大规模改性耦合喷射系统中所有控制元件由电控系统16控制,操作简单,提高工作效率。 The feeding method of the injection pipeline 14 is that both ends are fed at the same time. At this time, the distribution of particles and pressure inside the pipeline is more uniform, and the sorbent sprayed into the flue 15 has a good dispersion effect, preventing pipeline blockage. All control components in the large-scale adsorbent modification coupling injection system are controlled by the electronic control system 16, which is easy to operate and improves work efficiency.

所述的止回阀17用于防止输送管道中的气体和吸附剂逆流。 The check valve 17 is used to prevent backflow of gas and adsorbent in the delivery pipeline.

所述的空气压缩机18起吹堵的作用,喷射管道14发生堵塞时,系统自动停止运行,空气压缩机18开始工作,对喷射管道进行吹堵。 The air compressor 18 plays the role of blowing and plugging. When the injection pipeline 14 is blocked, the system automatically stops running, and the air compressor 18 starts to work to blow and block the injection pipeline.

本发明实施的有益效果包括: The beneficial effects of the implementation of the present invention include:

1)本发明实现了现场大规模吸附剂改性耦合喷射,吸附剂的改性与喷射同时进行,保证通过吸附方法降低污染物工艺过程的连续性; 1) The present invention realizes on-site large-scale adsorbent modification coupling injection, and the modification of the adsorbent and the injection are carried out at the same time, ensuring the continuity of the technological process of reducing pollutants through the adsorption method;

2)本发明保证了系统的封闭性,无粉尘飞溢,吸附剂改性和喷射耦合的效果好,不存在物料质量损失,防止物料污染环境; 2) The present invention ensures the sealing of the system, no dust spillage, good effect of adsorbent modification and spray coupling, no loss of material quality, and prevents material from polluting the environment;

3)本发明保证经过大规模改性后的吸附剂含水率低于3%,满足气力输送的要求,同时吸附剂在改性机中发生高速碰撞,结块现象减少,整个输送及喷射过程不易发生堵塞,系统运行可靠度高; 3) The present invention ensures that the moisture content of the adsorbent after large-scale modification is lower than 3%, which meets the requirements of pneumatic transportation. At the same time, the adsorbent collides at a high speed in the modification machine, and the caking phenomenon is reduced, and the entire conveying and spraying process is not easy. Blockage occurs, and the system operates with high reliability;

4)本发明实现了自动化,主要工作元件置于地面上,不需要搬运到平台上工作,整套系统控制元件由电控系统控制,操作简单。 4) The present invention realizes automation, and the main working components are placed on the ground without being transported to work on the platform. The control components of the whole system are controlled by the electric control system, and the operation is simple.

附图说明 Description of drawings

图1为本发明所述吸附剂大规模改性耦合喷射系统的工艺流程图。 Fig. 1 is a process flow chart of the coupled injection system for large-scale modification of adsorbents in the present invention.

其中图中标号: Among them, the labels in the figure are:

1、储料罐;2、给料器;3、变频进料装置;4、改性药剂罐;5、改性主机;6、旋风分离器;7、引风机;8、收集料斗;9、罗茨风机;10、排空阀;11、进料器;12、气固混合加速器;13、输送弯头;14、喷射管道;15、烟道;16、电控系统;17、止回阀;18、空气压缩机。 1. Storage tank; 2. Feeder; 3. Frequency conversion feeding device; 4. Modified agent tank; 5. Modified host; 6. Cyclone separator; 7. Induced fan; 8. Collection hopper; 9. Roots blower; 10. Evacuation valve; 11. Feeder; 12. Gas-solid mixing accelerator; 13. Delivery elbow; 14. Injection pipe; 15. Flue; 16. Electric control system; 17. Check valve ; 18. Air compressor.

具体实施方式 detailed description

下面结合附图和具体实施例进一步详细描述本发明。 The present invention will be further described in detail below in conjunction with the accompanying drawings and specific embodiments.

本发明提出一种大规模吸附剂改性耦合喷射系统,如图1所示,包括:吸附剂储料罐1、旋给料器2、变频进料装置3、改性药剂罐4、改性主机5、旋风分离器6、引风机7、收集料斗8、罗茨风机9、排空阀10、进料器11、气固混合加速器12、输送弯头13、喷射管道14、烟道15、电控系统16、止回阀17和空气压缩机18。所述的系统包括两个部分:大规模改性系统和喷射系统,两个系统配合运行,保证了耦合系统的连续性和封闭性。 The present invention proposes a large-scale adsorbent modified coupling injection system, as shown in Figure 1, comprising: adsorbent storage tank 1, rotary feeder 2, frequency conversion feeding device 3, modified agent tank 4, modified Main engine 5, cyclone separator 6, induced draft fan 7, collection hopper 8, Roots blower 9, emptying valve 10, feeder 11, gas-solid mixing accelerator 12, conveying elbow 13, injection pipe 14, flue 15, Electric control system 16, check valve 17 and air compressor 18. The system includes two parts: a large-scale modification system and an injection system, and the two systems work together to ensure the continuity and sealing of the coupling system.

所述大规模改性系统包括进料装置和改性及集料装置,1、2、3、4组成改性前吸附剂和药剂进料装置,吸附剂和药剂按照一定比例加入改性主机5中,在改性主机5中完成改性;受到引风机7的作用,从改性主机5中出来的改性后吸附剂沿着连接管道进入旋风分离器6中进行分离,其中吸附剂落到旋风分离器的底部,空气由引风机7出口进入输送管道中。 The large-scale modification system includes a feeding device and a modification and collection device. 1, 2, 3, and 4 form an adsorbent and medicament feeding device before modification, and the sorbent and medicament are added to the modified host according to a certain ratio 5 In the process, the modification is completed in the modified host 5; under the action of the induced draft fan 7, the modified adsorbent coming out of the modified host 5 enters the cyclone separator 6 along the connecting pipe for separation, wherein the adsorbent falls to At the bottom of the cyclone separator, the air enters the delivery pipeline from the outlet of the induced draft fan 7.

所述喷射系统包括气力输送装置和喷射管道,9和10组成进气装置;8和11组成吸附剂进料装置。气固混合加速器12中吸附剂和气体按照一定的比例混合,然后沿着输送管道流到喷射管道14处,均匀的喷入烟道15中。 The injection system includes a pneumatic conveying device and an injection pipeline, 9 and 10 form an air inlet device; 8 and 11 form an adsorbent feeding device. The adsorbent and the gas in the gas-solid mixing accelerator 12 are mixed according to a certain ratio, and then flow to the injection pipe 14 along the delivery pipe, and are evenly sprayed into the flue 15 .

所述的变频进料装置3带有加热装置,在寒冷的工作环境下工作时,开启加热装置,保证改性系统正常运行。 The frequency conversion feeding device 3 is equipped with a heating device. When working in a cold working environment, the heating device is turned on to ensure the normal operation of the modification system.

所述改性药剂罐4材质为不锈钢或内部喷上铁氟龙涂层,并带有电加热棒,保证改性系统可在寒冷的工作环境下运行。 The modified agent tank 4 is made of stainless steel or coated with Teflon inside, and has an electric heating rod to ensure that the modified system can operate in a cold working environment.

所述改性主机5材质为不锈钢或内部喷上铁氟龙涂层,耐磨损、耐腐蚀。 The modified host 5 is made of stainless steel or coated with Teflon inside, which is wear-resistant and corrosion-resistant.

所述的输送弯头13在管道内壁衬着3~5mm厚陶瓷管,增强输送弯头的耐磨损性。 The delivery elbow 13 is lined with a 3-5 mm thick ceramic tube on the inner wall of the pipeline to enhance the wear resistance of the delivery elbow.

所述的喷射管道14发生堵塞时,系统自动停止运行,空气压缩机18开始工作,对喷射管道进行吹堵。 When the injection pipeline 14 is blocked, the system automatically stops running, and the air compressor 18 starts to work to blow the injection pipeline to blockage.

本发明可用其他的不违背本发明的精神和主要特征的具体形式来概述。因此,本发明的上述实施方案都只能认为是对本发明的说明而不能限制本发明,权利要求书指出了本发明的范围,而上述的说明并未全部指出本发明的范围。因此,在与本发明的权利要求书相当的含义和范围内的任何改变,都应认为是包括在权利要求书的范围内。 The present invention may be embodied in other specific forms without departing from the spirit and main characteristics of the invention. Therefore, the above-mentioned embodiments of the present invention can only be considered as descriptions of the present invention and can not limit the present invention, and the claims point out the scope of the present invention, but the above description does not all point out the scope of the present invention. Therefore, any changes within the meaning and scope equivalent to the claims of the present invention should be considered to be included in the scope of the claims.

Claims (10)

1.一种实现控制烟气中重金属污染物排放的大规模吸附剂改性耦合喷射系统,其特征在于,系统耦合改性系统和喷射系统,改性后的吸附剂直接输送到喷射系统,形成在现场开展改性及喷射一体化的工艺,喷射系统将吸附剂喷射到烟道中吸附烟气中的污染物,如重金属(汞、砷、铅、镉、铬)以及强酸性气体(三氧化硫和氯化氢)等,系统具体组成包括:吸附剂储料罐1,给料器2,变频进料装置3,改性药剂罐4,改性主机5,旋风分离器6,引风机7,收集料斗8,罗茨风机9,排空阀10,进料器11,气固混合加速器12,输送弯头13,喷射管道14,烟道15,电控系统16,止回阀17,空气压缩机18,其中吸附剂储料罐1、给料器2、变频进料装置3、改性药剂罐4、改性主机5、旋风分离器6和引风机7组成改性系统,收集料斗8、罗茨风机9、排空阀10、进料器11、气固混合加速器12、输送弯头13和喷射管道14组成喷射系统。1. A large-scale adsorbent modification coupling injection system for controlling the emission of heavy metal pollutants in flue gas, characterized in that the system is coupled with the modification system and the injection system, and the modified adsorbent is directly transported to the injection system to form Carry out the process of modification and injection integration on site. The injection system injects the adsorbent into the flue to absorb pollutants in the flue gas, such as heavy metals (mercury, arsenic, lead, cadmium, chromium) and strong acid gases (sulfur trioxide) and hydrogen chloride), etc., the specific composition of the system includes: adsorbent storage tank 1, feeder 2, frequency conversion feeding device 3, modified agent tank 4, modified host 5, cyclone separator 6, induced draft fan 7, collection hopper 8. Roots blower 9, exhaust valve 10, feeder 11, gas-solid mixing accelerator 12, delivery elbow 13, injection pipe 14, flue 15, electric control system 16, check valve 17, air compressor 18 , wherein the adsorbent storage tank 1, the feeder 2, the frequency conversion feeding device 3, the modified agent tank 4, the modified host 5, the cyclone separator 6 and the induced draft fan 7 form a modified system, and the collection hopper 8, Roots Fan 9, emptying valve 10, feeder 11, gas-solid mixing accelerator 12, delivery elbow 13 and injection pipe 14 form an injection system. 2.根据权利要求1所述的吸附剂改性耦合喷射系统,其特征在于,吸附剂从吸附剂储料罐1经给料器2进入变频进料装置3中,从变频进料装置3中出来的吸附剂和改性药剂罐4中的改性药剂按照一定比例加入改性主机5中,并在改性主机5中发生反应改性,在引风机7的作用下,从改性主机5出来的改性后的吸附剂由旋风分离器6收集,旋风分离器6中的吸附剂进入收集料斗8后,由进料器11控制进入气固混合加速器12,改性后的吸附剂和从罗茨风机9吸入的空气在气固混合加速器12中按照一定的比例混合,然后沿着输送管道流到喷射管道14处,通过多个喷射管道将改性后的吸附剂均匀的喷入烟道15中。2. The adsorbent modified coupling injection system according to claim 1, wherein the adsorbent enters the frequency conversion feeding device 3 from the adsorbent storage tank 1 through the feeder 2, and from the frequency conversion feeding device 3 The adsorbent that comes out and the modifying agent in the modifying agent tank 4 are added in the modified host 5 according to a certain ratio, and reaction modification occurs in the modified host 5, and under the action of the induced draft fan 7, from the modified host 5 The modified adsorbent that comes out is collected by cyclone separator 6, after the adsorbent in cyclone separator 6 enters collection hopper 8, enters gas-solid mixing accelerator 12 by the control of feeder 11, the adsorbent after modified and from The air inhaled by the Roots blower 9 is mixed according to a certain ratio in the gas-solid mixing accelerator 12, and then flows along the delivery pipe to the injection pipe 14, and the modified adsorbent is uniformly sprayed into the flue through multiple injection pipes 15 in. 3.根据权利要求1所述的吸附剂改性耦合喷射系统,其特征在于,系统实现了吸附剂现场大规模连续改性,改性过程中通过混合及反应,吸附剂的物理化学性质和机构发生变化,提高了吸附剂的活性。3. The coupling injection system for adsorbent modification according to claim 1, characterized in that the system realizes large-scale continuous modification of the adsorbent on site, and the physical and chemical properties and mechanism of the adsorbent are improved through mixing and reaction during the modification process. changes to increase the activity of the adsorbent. 4.根据权利要求1所述的吸附剂改性耦合喷射系统,其特征在于,变频进料装置3带有加热装置,药剂罐4材质为不锈钢或内部喷上铁氟龙涂层,并带有电加热棒,保证改性系统可在寒冷的工作环境下运行。4. The adsorbent modified coupling injection system according to claim 1, characterized in that, the frequency conversion feeding device 3 has a heating device, and the medicine tank 4 is made of stainless steel or sprayed with a Teflon coating inside, and has a Electric heating rods ensure that the modified system can operate in cold working environments. 5.根据权利要求1所述的吸附剂改性耦合喷射系统,其特征在于,改性主机5材质为不锈钢或内部喷上铁氟龙涂层,耐磨损、耐腐蚀,未改性吸附剂在改性主机内部经过高速搅拌、碰撞,不会出现结块等现象。5. The adsorbent modified coupling injection system according to claim 1, characterized in that, the material of the modified host 5 is stainless steel or the interior is sprayed with Teflon coating, which is wear-resistant and corrosion-resistant, and the unmodified adsorbent After high-speed stirring and collision inside the modified host, there will be no agglomeration and other phenomena. 6.根据权利要求1所述的吸附剂改性耦合喷射系统,其特征在于,系统压力损失过大时,罗茨风机9可换用空气压缩机。6. The adsorbent modified coupling injection system according to claim 1, characterized in that, when the system pressure loss is too large, the Roots blower 9 can be replaced with an air compressor. 7.输送弯头13在管道内壁衬着3~5mm厚陶瓷管,增强输送弯头的耐磨损性,提高系统使用寿命。7. The conveying elbow 13 is lined with a 3-5 mm thick ceramic tube on the inner wall of the pipeline, which enhances the wear resistance of the conveying elbow and improves the service life of the system. 8.根据权利要求1所述的吸附剂改性耦合喷射系统,其特征在于,喷射管道14的进料方式为两端同时进料,促进管道内部颗粒和压力分布更加均匀,喷射到烟道15内的吸附剂分散效果好,并防止管道堵塞。8. The adsorbent modified coupling injection system according to claim 1, characterized in that, the feeding mode of the injection pipeline 14 is feeding at both ends simultaneously, which promotes a more uniform particle and pressure distribution inside the pipeline, and sprays it into the flue 15 The adsorbent inside has a good dispersion effect and prevents the pipeline from clogging. 9.根据权利要求1所述的吸附剂改性耦合喷射系统,其特征在于,所述的止回阀17用于防止输送管道中的气体和吸附剂逆流。9 . The coupled injection system for adsorbent modification according to claim 1 , wherein the check valve 17 is used to prevent backflow of gas and adsorbent in the delivery pipeline. 10.根据权利要求1所述的吸附剂改性耦合喷射系统,其特征在于,所述的空气压缩机18起吹堵的作用,喷射管道14发生堵塞时,系统自动停止运行,空气压缩机18开始工作,对喷射管道进行吹堵。10. The adsorbent modified coupling injection system according to claim 1, characterized in that, the air compressor 18 plays the role of blowing plugging, when the injection pipeline 14 is blocked, the system automatically stops running, and the air compressor 18 Start to work and blow off the injection pipe.
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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106178834A (en) * 2016-08-26 2016-12-07 福建龙净环保股份有限公司 Active carbon powder injection apparatus
JP2018066523A (en) * 2016-10-21 2018-04-26 日立造船株式会社 Chemical charging device and combustion exhaust gas treatment facility
CN109821350A (en) * 2019-02-18 2019-05-31 浙江菲达环保科技股份有限公司 A kind of Hg/SO based on intermediate injection3The electric-bag complex dust collector of cooperation-removal
CN110772931A (en) * 2019-11-19 2020-02-11 华南理工大学 Modified kaolin injection system and method for removing heavy metal pollutants in flue gas

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1665947A (en) * 2002-05-06 2005-09-07 小西德尼·G·尼尔逊 Adsorbent for removing mercury in flue gas and corresponding mercury removal method
CN1943842A (en) * 2004-10-08 2007-04-11 阿尔斯托姆科技有限公司 Control of mercury emissions from solid fuel combustion
US20070180990A1 (en) * 2004-03-22 2007-08-09 William Downs Dynamic halogenation of sorbents for the removal of mercury from flue gases
CN101496980A (en) * 2009-01-08 2009-08-05 重庆大学 Method for removing mercury from flue gas
CN201545512U (en) * 2009-06-10 2010-08-11 陈毅 A continuous limestone conveying system
CN202038725U (en) * 2011-05-03 2011-11-16 陈和平 Material pipeline drying or pneumatic conveying equipment with abrasion-free device
CN202609584U (en) * 2012-03-30 2012-12-19 日氟荣航空新材料(上海)有限公司 Vacuum suction device

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1665947A (en) * 2002-05-06 2005-09-07 小西德尼·G·尼尔逊 Adsorbent for removing mercury in flue gas and corresponding mercury removal method
US20070180990A1 (en) * 2004-03-22 2007-08-09 William Downs Dynamic halogenation of sorbents for the removal of mercury from flue gases
CN1943842A (en) * 2004-10-08 2007-04-11 阿尔斯托姆科技有限公司 Control of mercury emissions from solid fuel combustion
CN101496980A (en) * 2009-01-08 2009-08-05 重庆大学 Method for removing mercury from flue gas
CN201545512U (en) * 2009-06-10 2010-08-11 陈毅 A continuous limestone conveying system
CN202038725U (en) * 2011-05-03 2011-11-16 陈和平 Material pipeline drying or pneumatic conveying equipment with abrasion-free device
CN202609584U (en) * 2012-03-30 2012-12-19 日氟荣航空新材料(上海)有限公司 Vacuum suction device

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106178834A (en) * 2016-08-26 2016-12-07 福建龙净环保股份有限公司 Active carbon powder injection apparatus
JP2018066523A (en) * 2016-10-21 2018-04-26 日立造船株式会社 Chemical charging device and combustion exhaust gas treatment facility
CN109821350A (en) * 2019-02-18 2019-05-31 浙江菲达环保科技股份有限公司 A kind of Hg/SO based on intermediate injection3The electric-bag complex dust collector of cooperation-removal
CN110772931A (en) * 2019-11-19 2020-02-11 华南理工大学 Modified kaolin injection system and method for removing heavy metal pollutants in flue gas

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