CN112138517A - A system and method for deep plume control - Google Patents
A system and method for deep plume control Download PDFInfo
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- 238000000034 method Methods 0.000 title claims abstract description 14
- 239000003814 drug Substances 0.000 claims abstract description 132
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 51
- 239000003546 flue gas Substances 0.000 claims abstract description 47
- 238000002347 injection Methods 0.000 claims abstract description 39
- 239000007924 injection Substances 0.000 claims abstract description 39
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- 239000003795 chemical substances by application Substances 0.000 claims abstract description 28
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- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/48—Sulfur compounds
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- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/77—Liquid phase processes
- B01D53/78—Liquid phase processes with gas-liquid contact
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/02—Other waste gases
- B01D2258/0283—Flue gases
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Abstract
Description
技术领域technical field
本发明涉及环境保护领域,具体为一种烟羽深度治理的系统及方法。The invention relates to the field of environmental protection, in particular to a system and method for deep treatment of smoke plumes.
背景技术Background technique
目前国内脱硫工艺90%是采用湿法脱硫,湿法烟气脱硫系统吸收塔出口净烟气由于处于湿饱和状态,在流经烟道、烟囱排入大气的过程中因温度降低,烟气中部分汽态水和污染物会发生凝结,在烟囱口形成雾状水汽,雾状水汽会因天空背景色和天空光照、观察角度等原因发生颜色的细微变化,形成有色烟羽。At present, 90% of the domestic desulfurization process adopts wet desulfurization. Since the net flue gas at the outlet of the absorption tower of the wet flue gas desulfurization system is in a wet saturated state, the temperature decreases during the process of flowing through the flue and chimney and discharging into the atmosphere, and the flue gas is in the flue gas. Part of the vaporous water and pollutants will condense, forming mist-like water vapor at the chimney mouth, and the mist-like water vapor will change slightly in color due to the background color of the sky, sky illumination, viewing angle, etc., forming colored plumes.
上海、浙江等地相继出台了地方环保标准《燃煤电厂大气污染物排放标准》,明确要求燃煤电厂采取有效措施消除有色烟羽。即通过采取相应技术降低排放的烟气含湿量,收集烟气中过饱和水蒸气水分、减少烟气中可溶性盐、硫酸酸雾、有机物等可凝结颗粒物的排放。Shanghai, Zhejiang and other places have successively issued the local environmental protection standard "Emission Standard of Air Pollutants for Coal-fired Power Plants", which clearly requires coal-fired power plants to take effective measures to eliminate colored plumes. That is, by adopting corresponding technologies to reduce the moisture content of the emitted flue gas, collect the supersaturated water vapor moisture in the flue gas, and reduce the emission of condensable particulate matter such as soluble salts, sulfuric acid mist, and organic matter in the flue gas.
采样烟气冷凝再热技术路线为当前普遍应用的烟气治理方案。该方案能有效降低烟气排放温度和含湿量,可收集烟气中过饱和水蒸气中水分,减少烟气中可溶性盐、硫酸酸雾、有机物等可凝结颗粒物的排放。现阶段烟气冷凝技术多采用在脱硫塔出口烟道设置烟道冷凝管式换热器或在浆液循环管道设置浆液板式换热器,现役电厂脱硫装置经超低排放改造后脱硫塔出口至烟囱入口之间的烟道空间难以布置烟道冷凝管式换热器,且烟道冷凝管式换热器布置位置高,配套循环水泵电耗大,改造工程量大,检修维护困难;浆液循环管道空间有限,增加了浆液在循环管道中的沿程阻力,浆液板式换热器有堵塞的风险,换热器故障时需停运其相应的浆液循环泵。The technical route of sampling flue gas condensation and reheating is currently a commonly used flue gas treatment scheme. This solution can effectively reduce the emission temperature and moisture content of flue gas, collect the moisture in the supersaturated water vapor in the flue gas, and reduce the emission of condensable particulate matter such as soluble salts, sulfuric acid mist, and organic matter in the flue gas. At present, the flue gas condensation technology mostly adopts the flue condensing tube heat exchanger at the outlet flue of the desulfurization tower or the slurry plate heat exchanger at the slurry circulation pipeline. It is difficult to arrange the flue condensing tube heat exchanger in the flue space between the inlets, and the arrangement position of the flue condensing tube heat exchanger is high, the power consumption of the supporting circulating water pump is large, the amount of renovation works is large, and the maintenance is difficult; the slurry circulation pipeline The space is limited, which increases the resistance along the path of the slurry in the circulating pipeline, and the slurry plate heat exchanger is at risk of blockage. When the heat exchanger fails, the corresponding slurry circulating pump needs to be shut down.
发明内容SUMMARY OF THE INVENTION
针对现有技术中存在的问题,本发明提供一种烟羽进行深度治理的系统及方法,设计合理,结构简单,且能有效消除白色烟羽。Aiming at the problems existing in the prior art, the present invention provides a system and method for in-depth treatment of smoke plumes, which has reasonable design, simple structure, and can effectively eliminate white smoke plumes.
本发明是通过以下技术方案来实现:The present invention is achieved through the following technical solutions:
一种烟羽深度治理的系统,包括沿烟气方向依次安装在脱硫塔的出口烟道上的超声团聚系统、药剂回落系统和药剂喷射系统,以及与药剂回落系统连接设置的药剂供给系统;A system for in-depth treatment of smoke plumes, comprising an ultrasonic agglomeration system, a pharmaceutical drop system and a pharmaceutical injection system, which are sequentially installed on the outlet flue of a desulfurization tower along the direction of the flue gas, and a pharmaceutical supply system connected with the pharmaceutical drop system;
所述的超声团聚系统设置在出口烟道的烟气入口处;所述的药剂喷射系统设置在出口烟道的烟气出口处,其药剂雾化喷射方向与烟气方向相反;The ultrasonic agglomeration system is arranged at the smoke inlet of the outlet flue; the pharmaceutical injection system is arranged at the smoke outlet of the outlet flue, and the spraying direction of the medicine is opposite to the direction of the smoke;
所述的药剂回落系统包括药剂回落池;药剂回落池连通设置在超声团聚系统和药剂喷射系统之间的出口烟道底部,且连接药剂供给系统。The medicament drop system includes a medicament drop pool; the medicament drop pool communicates with the bottom of the outlet flue arranged between the ultrasonic agglomeration system and the medicament injection system, and is connected to the medicament supply system.
进一步的,所述的药剂喷射系统包括分布在出口烟道的烟气出口处至少一层的药剂喷射层;每层药剂喷射层上均匀分布若干个药剂喷嘴,喷射方向与烟气方向相反,喷射扬程范围为3-5m。Further, the medicament injection system includes at least one medicament injection layer distributed at the flue gas outlet of the outlet flue; several medicament nozzles are evenly distributed on each layer of the medicament injection layer, and the injection direction is opposite to the direction of the flue gas. The lift range is 3-5m.
更进一步的,所述的药剂喷嘴通过药剂喷洒泵与药剂回落池连接。Furthermore, the medicament nozzle is connected to the medicament drop pool through a medicament spray pump.
更进一步的,所述的超声团聚系统包括分布在出口烟道的烟气入口处的多个超声发生装置;超声发生装置布置在药剂喷嘴的对面,且与药剂喷嘴间隔距离范围为3-4m。Further, the ultrasonic agglomeration system includes a plurality of ultrasonic generating devices distributed at the flue gas inlet of the outlet flue; the ultrasonic generating devices are arranged on the opposite side of the medicament nozzle, and the distance from the medicament nozzle is in the range of 3-4m.
进一步的,所述药剂回落池底部设置有药剂排出口,上部与药剂供给系统连接。Further, a medicament discharge port is provided at the bottom of the medicament falling pool, and the upper part is connected with a medicament supply system.
更进一步的,所述的药剂供给系统包括药剂池,其通过药剂给液泵与药剂回落池连通,其内盛装的药剂为阴离子表面活性剂和非离子表面活性剂中的至少一种。Further, the medicament supply system includes a medicament pool, which is communicated with the medicament drop pool through a medicament feeding pump, and the medicament contained therein is at least one of an anionic surfactant and a non-ionic surfactant.
一种烟羽深度治理的方法,药剂喷射系统将药剂回落系统中的药剂喷入出口烟道内,当脱硫塔出口烟气进入出口烟道后,与药剂喷射系统雾化喷射的药剂逆向对流接触,使湿饱和烟气转变成过饱和状态,并将湿烟气中的水蒸气、微细颗粒物和微量污染物团聚;A method for in-depth treatment of smoke plumes. The chemical injection system sprays the chemical in the chemical falling system into the outlet flue. When the flue gas from the outlet of the desulfurization tower enters the outlet flue, it is in reverse convection contact with the chemical sprayed by the chemical injection system. Transform wet saturated flue gas into a supersaturated state, and agglomerate water vapor, fine particles and trace pollutants in wet flue gas;
在超声团聚系统的作用下,使湿烟气中的水蒸气、微细颗粒物和微量污染物的团聚变大;Under the action of the ultrasonic agglomeration system, the agglomeration of water vapor, fine particles and trace pollutants in the wet flue gas becomes larger;
在重力的作用下,与药剂一起落入药剂回落系统,完成烟羽深度治理。Under the action of gravity, it falls into the medicine drop system together with the medicine to complete the deep control of the plume.
进一步的,当药剂回落系统的药剂回落池中药剂消耗到设定程度时,药剂供给系统的药剂池向药剂回落池补充新鲜药剂。Further, when the medicine in the medicine returning pool of the medicine returning system is consumed to a set level, the medicine pool of the medicine supplying system replenishes the medicine returning pool with fresh medicine.
更进一步的,所述药剂喷射量与烟气的液气比为0.05v/v-0.5v/v;药剂体积浓度为0.001%-0.2%w/v;所述的药剂为阴离子表面活性剂、非离子表面活性剂或二者复配物。Further, the liquid-to-gas ratio of the spray amount of the medicament to the flue gas is 0.05v/v-0.5v/v; the volume concentration of the medicament is 0.001%-0.2%w/v; the medicament is an anionic surfactant, Nonionic surfactants or a combination of the two.
更进一步的,超声发生装置的声场频率位0.5-5kHz。Furthermore, the frequency of the sound field of the ultrasonic generating device is 0.5-5 kHz.
与现有技术相比,本发明具有以下有益的技术效果:Compared with the prior art, the present invention has the following beneficial technical effects:
本发明系统采用在脱硫塔的出口烟道处设置药剂喷射系统和超声团聚系统的方式,使脱硫塔出口烟气经本发明的系统后,与药剂喷射系统雾化喷射的药剂逆向对流接触,一方面药剂的雾化喷射进一步降低烟温,促使湿饱和烟气转变成过饱和状态,另一方面,药剂降低湿烟气的表面张力,促进湿烟气中的水蒸气、微细颗粒物、微量污染物的团聚;同时在超声团聚系统的作用下,进一步促使湿烟气中的水蒸气、微细颗粒物、微量污染物的团聚变大,最后在重力的作用下,与药剂一起落入药剂回落池,同时达到烟羽深度治理的目的,能有效去处烟气中可溶性盐,去除率高达98%。The system of the present invention adopts the method of setting a chemical injection system and an ultrasonic agglomeration system at the outlet flue of the desulfurization tower, so that after the flue gas at the outlet of the desulfurization tower passes through the system of the present invention, it is in reverse convection contact with the chemical sprayed by the chemical injection system. On the one hand, the atomized spray of the medicament further reduces the smoke temperature and promotes the transformation of the wet saturated flue gas into a supersaturated state. At the same time, under the action of the ultrasonic agglomeration system, the agglomeration of water vapor, fine particles and trace pollutants in the wet flue gas is further promoted to become larger, and finally, under the action of gravity, it falls into the drug drop pool together with the drug, and at the same time To achieve the purpose of deep plume treatment, it can effectively remove soluble salts in the flue gas, and the removal rate is as high as 98%.
进一步,本发明系统的药剂喷嘴中的药剂雾化喷射方向与烟气方向相反,要求逆向喷射,增大传质效果;药剂喷射扬程为3-5米,保证药剂与湿烟气的停留反应时间。Further, the spraying direction of the medicament in the medicament nozzle of the system of the present invention is opposite to the direction of the flue gas, and the reverse spray is required to increase the mass transfer effect; the spray head of the medicament is 3-5 meters, which ensures the residence reaction time of the medicament and the wet flue gas. .
进一步,本发明系统使用的超声发生装置,要求在烟道内形成低频驻波声场,促使脱硫塔出口烟气中的水蒸气、微细颗粒物及微量污染物之间产生相对运动、发生碰撞并团聚。Further, the ultrasonic generating device used in the system of the present invention requires the formation of a low-frequency standing wave sound field in the flue to promote relative movement, collision and agglomeration of water vapor, fine particles and trace pollutants in the flue gas at the outlet of the desulfurization tower.
附图说明Description of drawings
图1为本发明实施例中所述的结构示意图。FIG. 1 is a schematic diagram of the structure described in the embodiment of the present invention.
图中:脱硫塔1、药剂池2、药剂给液泵3、药剂回落池4、药剂喷洒泵5、药剂排出口6、药剂喷嘴7、出口烟道8、超声发生装置9。In the figure: desulfurization tower 1,
具体实施方式Detailed ways
下面结合具体的实施例对本发明做进一步的详细说明,所述是对本发明的解释而不是限定。The present invention will be further described in detail below in conjunction with specific embodiments, which are to explain rather than limit the present invention.
本发明一种烟羽深度治理的系统,如图1所示,包括沿脱硫塔1的出口烟道8安装的超声团聚系统、药剂回落系统、药剂供给系统和药剂喷射系统;A system for deep plume treatment according to the present invention, as shown in FIG. 1 , includes an ultrasonic agglomeration system, a medicament fallback system, a medicament supply system and a medicament injection system installed along the outlet flue 8 of the desulfurization tower 1;
所述的超声团聚系统设置在出口烟道8的烟气入口处,其包括超声发生装置9;超声发生装置9至少两个,对称分布在出口烟道8的烟气入口处两侧,且与药剂喷嘴7正对,与药剂喷嘴7间隔距离范围为3-4m。The ultrasonic agglomeration system is arranged at the flue gas inlet of the outlet flue 8, and includes an ultrasonic generating device 9; there are at least two ultrasonic generating devices 9, which are symmetrically distributed on both sides of the flue gas inlet of the outlet flue 8, and are the same as those of the flue gas inlet. The medicine nozzle 7 is facing directly, and the distance from the medicine nozzle 7 is in the range of 3-4m.
所述的药剂回落系统设置在超声团聚系统和药剂喷射系统之间的出口烟道8上,且连接药剂供给系统;药剂回落系统包括药剂回落池4、药剂喷洒泵5以及设置在药剂回落池4底部的药剂排出口6;药剂回落池4连通设置在药剂喷嘴7和超声发生装置9之间的出口烟道8底部,并通过药剂喷洒泵5与药剂喷嘴7连通。The medicament fallback system is arranged on the outlet flue 8 between the ultrasonic agglomeration system and the medicament injection system, and is connected to the medicament supply system; the medicament fallback system includes a medicament fallback pool 4, a
所述的药剂供给系统包括药剂池2和药剂给液泵3;药剂池2通过药剂给液泵3与药剂回落池4连通,其内盛装的药剂为浓度0.001%-0.2%的阴离子表面活性剂、非离子表面活性剂或二者复配物。The medicament supply system includes a
所述的药剂喷射系统设置在出口烟道8的烟气出口处,其药剂雾化喷射方向与烟气方向相反;药剂喷射系统包括药剂喷射层、药剂喷嘴7和药剂喷洒泵5;药剂喷射层至少一层分布在出口烟道8的烟气出口处;每层药剂喷射层上均匀分布若干个通过药剂喷洒泵5与药剂回落系统连接的药剂喷嘴7,喷射方向与烟气方向相反,喷射扬程范围为3-5m。The medicament injection system is arranged at the flue gas outlet of the outlet flue 8, and its medicament spraying direction is opposite to the direction of the flue gas; the medicament injection system includes a medicament spray layer, a medicament nozzle 7 and a
其中,药剂为环境友好的阴离子表面活性剂和非离子表面活性剂中的一种或多种复配,其使用浓度为0.001%-0.2%w/v;Wherein, the medicament is one or more compounding of environment-friendly anionic surfactant and nonionic surfactant, and its use concentration is 0.001%-0.2% w/v;
其中,药剂回落池4中的药剂可重复使用,待药剂溶液中的药剂消耗到一定程度时,可向药剂回落池补充新鲜药剂,继续进行烟羽深度治理。Among them, the medicament in the medicament drop pool 4 can be reused. When the medicament in the medicament solution is consumed to a certain level, fresh medicament can be added to the medicament drop pool to continue the deep treatment of the plume.
本发明一种烟羽深度治理的方法,如下所述,A method for deep treatment of plume of the present invention is as follows,
药剂喷射系统将药剂回落系统中的药剂喷入出口烟道8内,当脱硫塔1出口烟气进入出口烟道8后,与药剂喷射系统雾化喷射的药剂逆向对流接触,使湿饱和烟气转变成过饱和状态,并将湿烟气中的水蒸气、微细颗粒物、微量污染物的团聚;同时在超声团聚系统的作用下,进一步促使湿烟气中的水蒸气、微细颗粒物、微量污染物的团聚变大,最后在重力的作用下,与药剂一起落入药剂回落系统,完成烟羽深度治理。The agent injection system sprays the agent in the agent drop system into the outlet flue 8. When the flue gas from the outlet of the desulfurization tower 1 enters the outlet flue 8, it contacts the agent atomized and sprayed by the agent injection system in reverse convection, so that the wet saturated flue gas is in contact with each other. Transform into a supersaturated state, and agglomerate the water vapor, fine particles, and trace pollutants in the wet flue gas; at the same time, under the action of the ultrasonic agglomeration system, further promote the water vapor, fine particles, and trace pollutants in the wet flue gas. The agglomeration becomes larger, and finally, under the action of gravity, it falls into the medicine drop system together with the medicine to complete the deep management of the plume.
其中,药剂回落系统的药剂回落池4中的药剂重复使用,当药剂回落系统的药剂回落池4中药剂消耗到一定程度时,药剂供给系统的药剂池2向药剂回落池4补充新鲜药剂。The medicament in the medicament drop pool 4 of the medicament return system is reused. When the medicament in the medicament drop pool 4 of the medicament drop system is consumed to a certain extent, the
其中,药剂喷射量与烟气的液气比为0.05v/v-0.5v/v,药剂池2中使用的药剂为阴离子表面活性剂、非离子表面活性剂或二者复配物,其表面活性剂的浓度为0.001%-0.2%w/v。Among them, the liquid-to-gas ratio of the spray amount of the agent to the flue gas is 0.05v/v-0.5v/v, and the agent used in the
其中,超声发生装置9的声场频率在0.5-5kHz内可调。The frequency of the sound field of the ultrasonic generating device 9 is adjustable within 0.5-5 kHz.
本优选实施例中,燃煤锅炉经脱硫塔1出后的烟气量为5000m3/h。未使用本发明系统前,可看到明显的白烟,对白色烟羽进行可溶物测试,得出其中可溶物的含量为10.5mg/m3;使用本发明系统后,药剂为0.05%的十二烷基硫酸钠和0.05%的烷基酚聚氧乙烯醚的混合物,药剂喷射量与烟气的液气比为0.5v/v,同时超声波声场频率为1.5kHz,不仅肉眼看不见白烟,而且测得烟气中的可溶解物的含量为0.37g/m3。In this preferred embodiment, the amount of flue gas discharged from the coal-fired boiler through the desulfurization tower 1 is 5000 m 3 /h. Before using the system of the present invention, obvious white smoke can be seen, and the soluble matter test of the white plume is carried out, and the content of the soluble matter is 10.5 mg/m 3 ; after the system of the present invention is used, the medicament is 0.05% The mixture of sodium lauryl sulfate and 0.05% alkylphenol polyoxyethylene ether, the liquid-gas ratio of the spray amount of the agent and the flue gas is 0.5v/v, and the frequency of the ultrasonic sound field is 1.5kHz, which is not only invisible to the naked eye. smoke, and the content of soluble matter in the smoke was measured to be 0.37 g/m 3 .
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