CN103291419B - A kind of tail gas purification device of combustion engine - Google Patents
A kind of tail gas purification device of combustion engine Download PDFInfo
- Publication number
- CN103291419B CN103291419B CN201210050162.7A CN201210050162A CN103291419B CN 103291419 B CN103291419 B CN 103291419B CN 201210050162 A CN201210050162 A CN 201210050162A CN 103291419 B CN103291419 B CN 103291419B
- Authority
- CN
- China
- Prior art keywords
- box
- urea
- filter cartridge
- compressed air
- combustion engine
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 238000002485 combustion reaction Methods 0.000 title claims abstract description 24
- 238000000746 purification Methods 0.000 title claims description 19
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims abstract description 145
- 229910021529 ammonia Inorganic materials 0.000 claims abstract description 68
- 239000002245 particle Substances 0.000 claims abstract description 24
- 239000007921 spray Substances 0.000 claims abstract description 21
- 239000003054 catalyst Substances 0.000 claims abstract description 14
- 238000006555 catalytic reaction Methods 0.000 claims abstract description 13
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 claims abstract description 11
- 239000004202 carbamide Substances 0.000 claims abstract description 11
- 239000007787 solid Substances 0.000 claims abstract description 9
- 238000001914 filtration Methods 0.000 claims abstract description 8
- 230000009471 action Effects 0.000 claims abstract description 7
- 239000003595 mist Substances 0.000 claims abstract description 6
- 238000006722 reduction reaction Methods 0.000 claims abstract description 3
- 239000000243 solution Substances 0.000 claims description 69
- WTHDKMILWLGDKL-UHFFFAOYSA-N urea;hydrate Chemical compound O.NC(N)=O WTHDKMILWLGDKL-UHFFFAOYSA-N 0.000 claims description 52
- 239000000919 ceramic Substances 0.000 claims description 28
- 238000002347 injection Methods 0.000 claims description 28
- 239000007924 injection Substances 0.000 claims description 28
- 230000003197 catalytic effect Effects 0.000 claims description 26
- 238000003860 storage Methods 0.000 claims description 24
- 238000007664 blowing Methods 0.000 claims description 15
- 229910001220 stainless steel Inorganic materials 0.000 claims description 15
- 239000010935 stainless steel Substances 0.000 claims description 15
- 239000003365 glass fiber Substances 0.000 claims description 6
- 238000005192 partition Methods 0.000 claims description 6
- 239000013618 particulate matter Substances 0.000 claims description 5
- 230000035939 shock Effects 0.000 claims description 2
- 238000000034 method Methods 0.000 abstract description 21
- 238000010531 catalytic reduction reaction Methods 0.000 abstract description 12
- 238000004519 manufacturing process Methods 0.000 abstract description 6
- 239000007789 gas Substances 0.000 description 46
- 229910000831 Steel Inorganic materials 0.000 description 10
- 239000010959 steel Substances 0.000 description 10
- 239000003344 environmental pollutant Substances 0.000 description 9
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 9
- 231100000719 pollutant Toxicity 0.000 description 9
- 239000000203 mixture Substances 0.000 description 6
- 125000006297 carbonyl amino group Chemical group [H]N([*:2])C([*:1])=O 0.000 description 5
- 238000006243 chemical reaction Methods 0.000 description 5
- 238000006477 desulfuration reaction Methods 0.000 description 5
- 230000023556 desulfurization Effects 0.000 description 5
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 4
- OHJMTUPIZMNBFR-UHFFFAOYSA-N biuret Chemical compound NC(=O)NC(N)=O OHJMTUPIZMNBFR-UHFFFAOYSA-N 0.000 description 4
- 239000000376 reactant Substances 0.000 description 4
- 238000005507 spraying Methods 0.000 description 4
- 239000007864 aqueous solution Substances 0.000 description 3
- 238000000354 decomposition reaction Methods 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 230000001105 regulatory effect Effects 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 229910001868 water Inorganic materials 0.000 description 3
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 2
- PQUCIEFHOVEZAU-UHFFFAOYSA-N Diammonium sulfite Chemical compound [NH4+].[NH4+].[O-]S([O-])=O PQUCIEFHOVEZAU-UHFFFAOYSA-N 0.000 description 2
- 235000011114 ammonium hydroxide Nutrition 0.000 description 2
- BFNBIHQBYMNNAN-UHFFFAOYSA-N ammonium sulfate Chemical compound N.N.OS(O)(=O)=O BFNBIHQBYMNNAN-UHFFFAOYSA-N 0.000 description 2
- 229910052921 ammonium sulfate Inorganic materials 0.000 description 2
- 235000011130 ammonium sulphate Nutrition 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 229910002091 carbon monoxide Inorganic materials 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 230000001276 controlling effect Effects 0.000 description 2
- 238000004880 explosion Methods 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 230000001681 protective effect Effects 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000001066 destructive effect Effects 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000013067 intermediate product Substances 0.000 description 1
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 229910000069 nitrogen hydride Inorganic materials 0.000 description 1
- 150000002897 organic nitrogen compounds Chemical class 0.000 description 1
- 230000035945 sensitivity Effects 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/12—Improving ICE efficiencies
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/40—Engine management systems
Landscapes
- Exhaust Gas After Treatment (AREA)
Abstract
本发明公开了一种内燃机尾气净化装置,包括顺次相连的气态氨生成系统、颗粒物去除系统和催化反应系统;气态氨生成系统前端与内燃机尾气排放口相连,以气流式或高压喷雾的方式将尿素溶液喷成极细微的雾状,在高温尾气的作用下产生气态氨;颗粒物去除系统前端与气态氨生成系统相连,后端与催化反应系统相连,以过滤的方式去除内燃机尾气中的固态颗粒物;催化反应系统内设置有催化剂载体,其上涂覆还原反应所需的催化剂。本发明装置结构简单、体积小、重量轻,仅需一套精巧的气流式喷雾装置或高压喷雾装置即可实现气态氨生成功能,实用性强;从根本上解决了选择性催化还原法的安全性问题;解决了选择性催化还原法的气态氨生成量不稳定的弊病。
The invention discloses a device for purifying exhaust gas of an internal combustion engine, which comprises a gaseous ammonia generating system, a particle removal system and a catalytic reaction system connected in sequence; The urea solution is sprayed into a very fine mist, and gaseous ammonia is generated under the action of high-temperature exhaust gas; the front end of the particle removal system is connected to the gaseous ammonia generation system, and the rear end is connected to the catalytic reaction system to remove solid particles in the exhaust gas of the internal combustion engine by filtering ; The catalytic reaction system is provided with a catalyst carrier on which the catalyst required for the reduction reaction is coated. The device of the invention is simple in structure, small in size and light in weight. It only needs a set of exquisite airflow spray device or high-pressure spray device to realize the function of gaseous ammonia generation, and has strong practicability; it fundamentally solves the safety of the selective catalytic reduction method It solves the problem of unstable gaseous ammonia production in the selective catalytic reduction method.
Description
技术领域 technical field
本发明涉及环保技术领域,特别是涉及一种内燃机尾气净化装置。The invention relates to the technical field of environmental protection, in particular to an exhaust gas purification device of an internal combustion engine.
背景技术 Background technique
对于内燃机的尾气排放污染,以柴油机为例进行介绍,柴油机排放的废气中包含有气态及固态的污染物,气态污染物中主要为NOX、SO2、CO、HC、氧化物,有机氮化物及含硫混合物等;固态污染物最主要的是碳化颗粒物。在上述污染物中,最主要的是NOX、CO、SO2、HC以及固体微粒(pm)。在现有技术中,净化上述气态污染物的方法主要采用选择性催化还原法(SelectiveCatalyticReduction,简称SCR)净化气态污染物中的NOX和CO;采用这种方法时,反应物是气态氨(NH3)。为了获得气态氨的方法是采用氨水在常温下(因氨气生成量与温度之间存在敏感性,要求控制温度范围非常窄,温度高氨气过量,造成氨污染,温度低反应物量少,净化效率低)自然蒸发为氨气,这套气态氨生成装置包括氨气蒸发器、氨气缓冲罐、气体流量阀等,这些装置相对与柴油机来言,显得体积过于庞大,同时氨气是一种易爆气体,若氨气在空气中浓度为5%~15%的范围内,遇明火即可发生破坏力和危险性都很大的爆炸,柴油机尾气排放处又是处于高温状态,因此,在柴油机尾气净化装置中采用氨气蒸发器、氨气缓冲罐等来获得气态氨是不现实的和危险的。For the exhaust emission pollution of internal combustion engines, the diesel engine is taken as an example. The exhaust gas emitted by diesel engines contains gaseous and solid pollutants. The gaseous pollutants are mainly NO X , SO 2 , CO, HC, oxides, and organic nitrogen compounds. and sulfur-containing mixtures, etc.; the most important solid pollutants are carbonized particles. Among the above-mentioned pollutants, the most important ones are NOx , CO , SO2, HC and solid particles (pm). In the prior art, the method for purifying the above-mentioned gaseous pollutants mainly adopts Selective Catalytic Reduction (SCR) to purify NO X and CO in the gaseous pollutants; when using this method, the reactant is gaseous ammonia (NH3 ). The method for obtaining gaseous ammonia is to adopt ammonia water at normal temperature (because there is sensitivity between the amount of ammonia gas generation and the temperature, it is required to control the temperature range very narrowly, the high temperature ammonia gas is excessive, causing ammonia pollution, and the low temperature reactant amount is few. Low purification efficiency) naturally evaporates into ammonia. This set of gaseous ammonia generating devices includes ammonia evaporator, ammonia buffer tank, gas flow valve, etc. Compared with diesel engines, these devices are too bulky. At the same time, ammonia is a An explosive gas, if the concentration of ammonia in the air is within the range of 5% to 15%, it will explode with great destructive power and danger when it encounters an open flame, and the diesel engine exhaust is in a high temperature state. Therefore, It is unrealistic and dangerous to use ammonia evaporator, ammonia buffer tank, etc. to obtain gaseous ammonia in diesel engine exhaust purification equipment.
发明内容 Contents of the invention
(一)要解决的技术问题(1) Technical problems to be solved
本发明要解决的技术问题是如何实现安全高效地对内燃机所排放的尾气进行及时处理,以避免其排放到空气中造成污染。The technical problem to be solved by the present invention is how to safely and efficiently process the tail gas discharged from the internal combustion engine in time, so as to avoid pollution from being discharged into the air.
(二)技术方案(2) Technical solutions
为了解决上述技术问题,本发明提供一种内燃机尾气净化装置,包括顺次相连的气态氨生成系统、颗粒物去除系统和催化反应系统;所述气态氨生成系统前端与内燃机尾气排放口相连,后端与颗粒物去除系统相连,气态氨生成系统以气流式或高压喷雾的方式将尿素溶液喷成极细微的雾状,在高温尾气的作用下产生气态氨;所述颗粒物去除系统前端与气态氨生成系统相连,后端与催化反应系统相连,以过滤的方式去除内燃机尾气中的固态颗粒物;所述催化反应系统内设置有催化剂载体,其内壁上涂覆还原反应所需的催化剂。In order to solve the above technical problems, the present invention provides an internal combustion engine tail gas purification device, which includes a gaseous ammonia generation system, a particle removal system and a catalytic reaction system connected in sequence; the front end of the gaseous ammonia generation system is connected to the exhaust port of the internal combustion engine, and the rear end Connected with the particle removal system, the gaseous ammonia generation system sprays the urea solution into a very fine mist in the form of air flow or high-pressure spray, and generates gaseous ammonia under the action of high-temperature exhaust gas; the front end of the particle removal system is connected with the gaseous ammonia generation system The rear end is connected to the catalytic reaction system to remove solid particles in the exhaust gas of the internal combustion engine by filtering; the catalytic reaction system is provided with a catalyst carrier, and the catalyst required for the reduction reaction is coated on the inner wall.
其中,包括顺次连接且贯通的前箱体、中箱体和后箱体,所述前箱体内设置气态氨生成系统,所述中箱体内设置颗粒物去除系统,所述后箱体内设置催化反应系统。Wherein, it includes a front box body, a middle box body and a rear box body which are connected and connected in sequence, a gaseous ammonia generation system is set in the front box body, a particle removal system is set in the middle box body, and a catalytic reaction system is set in the rear box body. system.
其中,所述气态氨生成系统包括设置在前箱体内的气流式喷头,以及与气流式喷头的接口分别相连的尿素-水溶液管和压缩空气供应管,所述尿素-水溶液管与盛放有尿素-水溶液的尿素-水溶液储罐相连,所述压缩空气供应管与外部压缩空气相连;所述尿素-水溶液管和压缩空气供应管上分别设置有溶液流量控制阀和压缩空气控制阀。Wherein, the gaseous ammonia generation system includes an airflow nozzle arranged in the front box, and a urea-water solution pipe and a compressed air supply pipe respectively connected to the interface of the airflow nozzle, and the urea-water solution pipe is connected with the urea The urea-water solution storage tank of the aqueous solution is connected, and the compressed air supply pipe is connected with external compressed air; the urea-water solution pipe and the compressed air supply pipe are respectively provided with a solution flow control valve and a compressed air control valve.
其中,所述气态氨生成系统包括设置在前箱体内的压喷式喷头,以及与压喷式喷头的接口分别相连的尿素-水溶液管、溶液流量控制阀、高压齿轮泵和盛放有尿素-水溶液的尿素-水溶液储罐。Wherein, the gaseous ammonia generation system includes a pressure spray nozzle arranged in the front box, and a urea-water solution pipe connected to the interface of the pressure spray nozzle, a solution flow control valve, a high-pressure gear pump and a urea-water solution in full bloom. Urea-water storage tank for aqueous solution.
其中,所述中箱体前端连接前箱体,后端连接后箱体,底端连接锥形灰斗,灰斗底部安装锁灰螺帽;所述中箱体后端还连接有喷吹管,所述喷吹管与所述外部压缩空气相连。Wherein, the front end of the middle box is connected to the front box, the rear end is connected to the rear box, the bottom end is connected to a tapered ash hopper, and an ash lock nut is installed at the bottom of the ash hopper; the rear end of the middle box is also connected to a blowing pipe. The blowing pipe is connected with the external compressed air.
其中,所述喷吹管通过压缩空气支路管与压缩空气供应管相连;所述压缩空气支路管上依次设置有喷吹供气阀、压缩空气储罐和电磁脉冲阀,所述电磁脉冲阀通过控制导线与喷吹控制仪相连,喷吹供气阀控制进入压缩空气储罐的压缩空气量,喷吹控制仪通过控制导线向电磁脉冲阀发出通电信号,控制电磁脉冲阀开启以通过喷吹管向中箱体内喷吹气体。Wherein, the blowing pipe is connected to the compressed air supply pipe through the compressed air branch pipe; the compressed air branch pipe is provided with a blowing air supply valve, a compressed air storage tank and an electromagnetic pulse valve in sequence, and the electromagnetic pulse valve The injection air supply valve controls the amount of compressed air entering the compressed air storage tank through the control wire. Blow gas into the middle box.
其中,所述中箱体后端设置有喷吹喷嘴,所述喷吹喷嘴与所述喷吹管相连。Wherein, the rear end of the middle box is provided with a blowing nozzle, and the blowing nozzle is connected with the blowing pipe.
其中,所述中箱体内设置有滤筒花板,所述滤筒花板中心部为圆形孔,外边缘形状与中箱体内腔横截面形状相匹配;所述滤筒花板上安装有滤筒过滤单元,所述滤筒过滤单元包括安装在中箱体前端的滤筒前盲板、安装在中箱体后端的滤筒环板、与滤筒前盲板和滤筒环板形成柱状腔体的不锈钢过滤毡、以及分别设置在不锈钢过滤毡内外壁的滤筒内层保护网和滤筒外层保护网。Wherein, a filter cartridge flower plate is arranged in the middle box, the center of the filter cartridge flower plate is a circular hole, and the shape of the outer edge matches the cross-sectional shape of the inner cavity of the middle box; the filter cartridge flower plate is installed with The filter cartridge filter unit, the filter cartridge filter unit includes a filter cartridge front blind plate installed at the front end of the middle box, a filter cartridge ring plate installed at the rear end of the middle box, forming a columnar shape with the filter cartridge front blind plate and the filter cartridge ring plate The stainless steel filter felt in the cavity, and the filter cartridge inner protection net and filter cartridge outer protection net respectively arranged on the inner and outer walls of the stainless steel filter felt.
其中,所述后箱体中部设置有十字形隔板,将后箱体截面分成四个等尺寸空间,在每个等尺寸空间内设置一个陶瓷催化单元。Wherein, the middle part of the rear box is provided with a cross-shaped partition, which divides the section of the rear box into four equal-sized spaces, and a ceramic catalytic unit is arranged in each equal-sized space.
其中,所述陶瓷催化单元为一沿其纵向开设多个方形通道、且在其方形通道的内壁上涂覆催化剂的陶瓷催化剂载体,每个陶瓷催化单元四周裹附有玻纤防震毡,防止陶瓷催化单元在震动情况下受损。Wherein, the ceramic catalytic unit is a ceramic catalyst carrier with a plurality of square channels opened along its longitudinal direction, and the inner wall of the square channel is coated with catalyst. Each ceramic catalytic unit is surrounded by a glass fiber shockproof felt to prevent ceramic Catalytic unit damaged by vibrations.
其中,所述后箱体后端安装有后挡板,所述后挡板上设置有四个与陶瓷催化单元位置相对应且尺寸小于陶瓷催化单元的孔,以防止陶瓷催化单元窜动。Wherein, a rear baffle is installed at the rear end of the rear box, and four holes corresponding to the positions of the ceramic catalytic unit and smaller in size than the ceramic catalytic unit are arranged on the rear baffle to prevent the ceramic catalytic unit from moving.
(三)有益效果(3) Beneficial effects
上述技术方案所提供的内燃机尾气净化装置,装置结构简单、体积小、重量轻,仅需一套精巧的气流式喷雾系统或压力喷雾系统实现气态氨生成功能,实用性强;从根本上解决了选择性催化还原法的安全性问题;解决了选择性催化还原法的气态氨生成量不稳定的弊病。The internal combustion engine tail gas purification device provided by the above technical solution has a simple structure, small size, and light weight. It only needs a set of exquisite airflow spray system or pressure spray system to realize the function of gaseous ammonia generation, and has strong practicability; it fundamentally solves the problem of The safety problem of the selective catalytic reduction method; the disadvantage of unstable gaseous ammonia production in the selective catalytic reduction method is solved.
附图说明 Description of drawings
图1是本发明实施例1的内燃机尾气净化装置的结构示意图;Fig. 1 is the structural representation of the internal combustion engine tail gas cleaning device of embodiment 1 of the present invention;
图2是图1中的A-A剖面图;Fig. 2 is A-A sectional view among Fig. 1;
图3是图1中的B-B剖面图;Fig. 3 is the B-B sectional view among Fig. 1;
图4是本发明实施例2的内燃机尾气净化装置的结构示意图。Fig. 4 is a schematic structural view of an exhaust gas purification device of an internal combustion engine according to Embodiment 2 of the present invention.
其中,1:锁灰螺帽;2:灰斗;3:前中箱固定螺栓组;4:不锈钢过滤毡;5:滤筒前盲板;6:气流式喷头;7:柴油机尾气排管;8:前箱体;9:尿素--水溶液管;10:溶液流量控制阀;11:尿素--水溶液;12:尿素--水溶液储罐;13:压缩空气控制阀;14:压缩空气供应管;15:压缩空气支路管;16:喷吹供气阀;17:压缩空气储罐;18:喷吹控制仪;19:电磁脉冲阀;20:控制导线;21:中箱体;22:喷吹管;23:滤筒外层保护网;24:滤筒内层保护网;25:喷吹喷嘴;26:后箱体;27:玻纤防震毡;28:陶瓷催化单元;29:十字隔板;30:后挡板;31:终排放口;32:滤筒花板;33:滤筒固定螺栓组;34:中后箱固定螺栓组;35:滤筒环板;36:高压齿轮泵;37:压喷式喷头。Among them, 1: ash lock nut; 2: ash hopper; 3: front middle box fixing bolt group; 4: stainless steel filter felt; 5: front blind plate of filter cartridge; 6: air flow nozzle; 7: diesel engine exhaust pipe; 8: Front box; 9: Urea-water solution pipe; 10: Solution flow control valve; 11: Urea-water solution; 12: Urea-water solution storage tank; 13: Compressed air control valve; 14: Compressed air supply pipe ;15: Compressed air branch pipe; 16: Injection air supply valve; 17: Compressed air storage tank; 18: Injection control instrument; 19: Electromagnetic pulse valve; 20: Control wire; 21: Middle box; 22: Injection pipe; 23: Filter cartridge outer protection net; 24: Filter cartridge inner protection net; 25: Injection nozzle; 26: Rear box; 27: Glass fiber shockproof felt; 28: Ceramic catalytic unit; 29: Cross partition Plate; 30: rear baffle; 31: final discharge port; 32: filter cartridge flower plate; 33: filter cartridge fixing bolt group; 34: middle and rear box fixing bolt group; 35: filter cartridge ring plate; 36: high pressure gear pump ; 37: pressure spray nozzle.
具体实施方式 Detailed ways
下面结合附图和实施例,对本发明的具体实施方式作进一步详细描述。以下实施例用于说明本发明,但不用来限制本发明的范围。The specific implementation manners of the present invention will be further described in detail below in conjunction with the accompanying drawings and embodiments. The following examples are used to illustrate the present invention, but are not intended to limit the scope of the present invention.
本发明提供了一种用于柴油机尾气净化的装置,该装置采用尿素(CON2H4)-水溶液通过管线进入尾气净化装置内部,通过气流喷雾(实施例1)或高压喷雾(实施例2)将尿素-水溶液变为微液滴状态并与高温尾气充分混合,在高温尾气的作用下尿素-水溶液中的尿素迅速被加热至160℃以上分解,产生氨气(NH3)和缩二脲(CONH),其中氨气(NH3)中的一部分作为脱除SO2的反应物,另一部分作为选择性催化还原法的反应物,这种方法不仅氨气发生装置体积小,安全性高,而且通过对液态尿素输入量的控制可实现对氨气发生量的精确控制。The present invention provides a device for purifying exhaust gas from diesel engines. The device uses urea (CON 2 H 4 )-water solution to enter the interior of the exhaust gas purification device through pipelines, and sprays through airflow (Example 1) or high-pressure spray (Example 2). The urea-water solution is changed into a micro-droplet state and fully mixed with high-temperature exhaust gas. Under the action of high-temperature tail gas, the urea in the urea-water solution is rapidly heated to above 160°C and decomposed, producing ammonia (NH 3 ) and biuret ( CONH), wherein part of the ammonia (NH 3 ) is used as the reactant for removing SO 2 , and the other part is used as the reactant for the selective catalytic reduction method. This method not only has a small size of the ammonia gas generating device, but also has high safety and The precise control of the amount of ammonia gas can be realized by controlling the input amount of liquid urea.
实施例1Example 1
如图1所示:用于排量为9升、最高转速为2500r/min的高速柴油机的柴油机尾气净化装置,其基本外形尺寸为:长×宽×高=1300mm×400mm×400mm,该装置的结构如图1所示,图2为图1的A-A剖面图,图3为图1的B-B剖视图,其包括锁灰螺帽1、灰斗2、前中箱固定螺栓组3、不锈钢过滤毡4、滤筒前盲板5、气流式喷头6、柴油机尾气排管7、前箱体8、尿素-水溶液管9、溶液流量控制阀10、尿素-水溶液11、尿素-水溶液储罐12、压缩空气控制阀13、压缩空气供应管14、压缩空气支路管15、喷吹供气阀16、压缩空气储罐17、喷吹控制仪18、电磁脉冲阀19、控制导线20、中箱体21、喷吹管22、滤筒外层保护网23、滤筒内层保护网24、喷吹喷嘴25、后箱体26、玻纤防震毡27、陶瓷催化单元28、十字隔板29、后挡板30、终排放口31、滤筒花板32、滤筒固定螺栓组33、中后箱固定螺栓组34、滤筒环板35。As shown in Figure 1: the diesel engine exhaust purification device for high-speed diesel engines with a displacement of 9 liters and a maximum speed of 2500r/min, its basic dimensions are: length × width × height = 1300mm × 400mm × 400mm, the device’s The structure is shown in Figure 1, Figure 2 is the A-A sectional view of Figure 1, and Figure 3 is the B-B sectional view of Figure 1, which includes the ash locking nut 1, the ash bucket 2, the front middle box fixing bolt group 3, and the stainless steel filter felt 4 , filter cartridge front blind plate 5, air flow nozzle 6, diesel engine exhaust pipe 7, front box 8, urea-water solution pipe 9, solution flow control valve 10, urea-water solution 11, urea-water solution storage tank 12, compressed air Control valve 13, compressed air supply pipe 14, compressed air branch pipe 15, injection air supply valve 16, compressed air storage tank 17, injection control instrument 18, electromagnetic pulse valve 19, control wire 20, middle box 21, Injection pipe 22, filter cartridge outer protection net 23, filter cartridge inner protection net 24, injection nozzle 25, rear box 26, glass fiber shockproof felt 27, ceramic catalytic unit 28, cross partition 29, rear baffle 30 , final discharge port 31, filter cartridge flower plate 32, filter cartridge fixing bolt group 33, middle and rear box fixing bolt group 34, filter cartridge ring plate 35.
本实施例中,由气流式喷头6、前箱体8、尿素-水溶液管9、溶液流量控制阀10、尿素-水溶液储罐12、压缩空气供应管14、压缩空气控制阀13组成气态氨生成系统,其中前箱体8为水平置的钢板制钣金箱体,其前部为圆筒状,中间部分为圆方过度箱体,其后部为方形箱体,其前端与柴油机尾气排管7相连接,其后端通过前中箱固定螺栓组3与中箱体21连接,其前部为圆筒状箱体上部分别插入尿素-水溶液管9和压缩空气供应管14,这两条管线接入位于圆筒状箱体中心的气流式喷头6的相应接口;尿素-水溶液管9的另一端接尿素-水溶液储罐12底部,尿素-水溶液管中间设置溶液流量控制阀10,尿素-水溶液储罐12为一竖置的罐体,压缩空气供应管14中间设置压缩空气控制阀13;In the present embodiment, gaseous ammonia is formed by air flow nozzle 6, front box body 8, urea-water solution pipe 9, solution flow control valve 10, urea-water solution storage tank 12, compressed air supply pipe 14, and compressed air control valve 13. system, wherein the front box body 8 is a horizontally placed steel plate sheet metal box body, its front part is cylindrical, the middle part is a round and square transition box body, its rear part is a square box body, and its front end is connected to the exhaust pipe of the diesel engine. 7, its rear end is connected to the middle box body 21 through the front middle box fixing bolt group 3, and its front part is a cylindrical box body, and the upper part is inserted into the urea-water solution pipe 9 and the compressed air supply pipe 14 respectively. Connect to the corresponding interface of the airflow nozzle 6 located in the center of the cylindrical box body; the other end of the urea-water solution pipe 9 is connected to the bottom of the urea-water solution storage tank 12, and a solution flow control valve 10 is arranged in the middle of the urea-water solution pipe, and the urea-water solution The storage tank 12 is a vertical tank body, and a compressed air control valve 13 is arranged in the middle of the compressed air supply pipe 14;
由锁灰螺帽1、灰斗2、不锈钢过滤毡4、滤筒前盲板5、压缩空气支路管15、喷吹供气阀16、压缩空气储罐17、喷吹控制仪18、电磁脉冲阀19、控制导线20、中箱体21、喷吹管22、滤筒外层保护网23、滤筒内层保护网24、喷吹喷嘴25、滤筒花板32、滤筒固定螺栓组33、滤筒环板35组成颗粒物去除系统。中箱体21为一水平置的前后两端和下端空置的方形钢板制钣金箱体,其底面通过焊接与天方地圆的钢板制灰斗2连接,锁灰螺帽1拧在天方地圆的钢板制灰斗的下部圆筒外侧的螺纹上;中箱体21前端通过前中箱固定螺栓组3与前箱体8连接,其后端通过中后箱体固定螺栓组34与后箱体26连接;在其内腔设置一外方内圆钢板制的滤筒花板32,该滤筒花板32的外方焊接在中箱体21内腔偏后部位;由滤筒前盲板5滤筒环板35、滤筒外层保护网23、滤筒内层保护网24、不锈钢过滤毡4组成滤材为不锈钢过滤毡4的滤筒过滤单元,其中滤筒前盲板5为一钢板制圆盲板,滤筒环板35为一钢制环形钢板,其内圆是供外滤式滤筒的出风通道,不锈钢过滤毡4为一被折叠成手风琴琴箱状并围成筒状的过滤材料,其外层围有滤筒外层保护网23,其内层有网状的滤筒内层保护网24。这个滤筒过滤单元通过滤筒固定螺栓组33连接在滤筒花板32上。从压缩空气供应管14接出一压缩空气支路管15,在该管上设置一喷吹供气阀16向压缩空气储罐17供应压缩空气,当外滤式滤筒的过滤材料上积累的颗粒物量超过一定限值时,喷吹控制仪18通过控制导线20发出一个信号向电磁脉冲阀19通电,电磁脉冲阀19瞬间开启,压缩空气储罐中的压缩空气通过喷吹管22到喷吹喷嘴25向外滤式滤筒内腔喷吹(与尾气过滤方向相反),实现清理附着在过滤层上的积灰,被清理后的积灰落入灰斗中2,待积满后,拧开锁灰螺帽1排出。It consists of ash lock nut 1, ash hopper 2, stainless steel filter felt 4, filter cartridge front blind plate 5, compressed air branch pipe 15, injection air supply valve 16, compressed air storage tank 17, injection control instrument 18, electromagnetic Pulse valve 19, control wire 20, middle box 21, injection pipe 22, filter cartridge outer protection net 23, filter cartridge inner protection net 24, injection nozzle 25, filter cartridge flower plate 32, filter cartridge fixing bolt group 33 1. The filter cartridge ring plate 35 forms a particle removal system. The middle box 21 is a square steel sheet metal box with the front and rear ends and the lower end vacant in a horizontal position. The thread on the outside of the lower cylinder of the steel plate ash hopper; the front end of the middle box 21 is connected to the front box 8 through the front middle box fixing bolt group 3, and its rear end is connected to the rear box through the middle and rear box fixing bolt group 34. 26 connection; a filter cartridge flower plate 32 made of an outer inner circular steel plate is arranged in its inner cavity, and the outer side of the filter cartridge flower plate 32 is welded to the rear part of the inner cavity of the middle box body 21; the front blind plate 5 of the filter cartridge Filter cartridge ring plate 35, filter cartridge outer protective net 23, filter cartridge inner protective net 24, and stainless steel filter felt 4 form a filter cartridge filter unit in which the filter material is stainless steel filter felt 4, and the front blind plate 5 of the filter cartridge is a steel plate Make a round blind plate, the filter cartridge ring plate 35 is a steel annular steel plate, and its inner circle is the air outlet channel for the outer filter cartridge, and the stainless steel filter felt 4 is a folded accordion box shape and surrounded into a cylindrical shape filter material, its outer layer is surrounded by a filter cartridge outer layer protection net 23, and its inner layer has a mesh filter cartridge inner layer protection net 24. This filter cartridge filter unit is connected on the filter cartridge flower plate 32 through the filter cartridge fixing bolt group 33 . A compressed air branch pipe 15 is connected from the compressed air supply pipe 14, and a blowing air supply valve 16 is set on the pipe to supply compressed air to the compressed air storage tank 17. When the amount of particulate matter exceeds a certain limit, the injection controller 18 sends a signal through the control wire 20 to energize the electromagnetic pulse valve 19, and the electromagnetic pulse valve 19 opens instantly, and the compressed air in the compressed air storage tank passes through the injection pipe 22 to the injection nozzle. 25 Blow to the inner cavity of the outer filter cartridge (opposite to the direction of exhaust gas filtration) to clean up the ash accumulated on the filter layer, and the cleaned ash will fall into the ash hopper. Gray nut 1 is discharged.
由后箱体26、玻纤防震毡27、陶瓷催化单元28、十字隔板29、后挡板30、终排放口31组成催化反应系统,后箱体26为一方形箱体和一前方后圆箱体组合而成,其前端通过中后箱体固定螺栓组34与中箱体连接,后端与终排放口31焊接连接。在后箱体26中部设置一十字隔板29,将后箱体26方形截面分成四个等尺寸方形空间,在每个方形空间内置放一个陶瓷催化单元28,陶瓷催化单元28为一沿其纵向开设许多方形通道(截面尺寸为4.3mm×4.3mm)的催化剂载体,在其方形通道的内壁上涂覆催化剂的陶瓷制品,每个陶瓷催化单元28四周采用玻纤防震毡27裹附,以免陶瓷催化单元28在震动情况下受损。后挡板30为一方形钢板,内部均布四个略小于陶瓷催化单元的方孔,起到防止陶瓷催化单元向前窜动的作用。The catalytic reaction system is composed of a rear box 26, a glass fiber shockproof felt 27, a ceramic catalytic unit 28, a cross partition 29, a rear baffle 30, and a final discharge port 31. The rear box 26 is a square box and a front and back circle. The box body is combined, and its front end is connected with the middle box body through the fixing bolt group 34 of the middle and rear box body, and the rear end is welded with the final discharge port 31. A cross partition 29 is set in the middle part of the rear box body 26, and the square section of the rear box body 26 is divided into four square spaces of equal size. A ceramic catalytic unit 28 is built in each square space. The ceramic catalytic unit 28 is a Open the catalyst carrier of many square passages (cross-sectional size is 4.3mm * 4.3mm), on the inner wall of its square passage, coat the ceramic product of catalyst, adopt glass fiber antivibration blanket 27 to wrap around each ceramic catalytic unit 28, prevent ceramic The catalytic unit 28 is damaged in the event of shocks. The rear baffle 30 is a square steel plate, and four square holes slightly smaller than the ceramic catalytic unit are evenly distributed inside, so as to prevent the ceramic catalytic unit from moving forward.
实施例2Example 2
本实施例与实施例1的区别之处在于,将实施例1中由气流式喷头6、前箱体8、供尿素-水溶液管9、溶液流量控制阀10、尿素-水溶液储罐12、压缩空气供应管14、压缩空气控制阀13组成的气态氨生成系统更换为由高压齿轮泵36、前箱体8、压喷式喷头37、溶液流量控制阀10、供尿素-水溶液管9和尿素-水溶液储罐12组成的气态氨生成系统;喷雾方式由气流式喷雾更换为压力式喷雾;其中前箱体8为水平置的钢板制钣金箱体,其前部为圆筒状,中间部分为圆方过度箱体,其后部为方形箱体,其前端与柴油机尾气排管7相连接,其后端通过前中箱固定螺栓组3与中箱体21连接,其前部为圆筒状箱体上部分别插入供尿素-水溶液管9,管线接入位于圆筒状箱体中心的压喷式喷头37的相应接口;供尿素-水溶液管9的另一端接溶液流量控制阀10和高压齿轮泵36,尿素-水溶液储罐12为一竖置的罐体。The difference between this embodiment and Embodiment 1 is that in Embodiment 1, the air flow nozzle 6, the front box body 8, the urea-water solution supply pipe 9, the solution flow control valve 10, the urea-water solution storage tank 12, the compressor The gaseous ammonia generating system formed by the air supply pipe 14 and the compressed air control valve 13 is replaced by a high-pressure gear pump 36, a front casing 8, a pressure spray nozzle 37, a solution flow control valve 10, a urea-water solution pipe 9 and a urea- A gaseous ammonia generating system composed of aqueous solution storage tank 12; the spraying method is replaced by airflow spraying to pressure spraying; wherein the front box 8 is a horizontal steel sheet metal box, the front part is cylindrical, and the middle part is Round and square excessive box, its rear part is a square box, its front end is connected with the exhaust pipe 7 of the diesel engine, its rear end is connected with the middle box body 21 through the front middle box fixing bolt group 3, and its front part is cylindrical The upper part of the box body is inserted into the urea-water solution pipe 9 respectively, and the pipeline is connected to the corresponding interface of the pressure spray nozzle 37 located in the center of the cylindrical box body; the other end of the urea-water solution pipe 9 is connected to the solution flow control valve 10 and the high-pressure gear The pump 36 and the urea-water solution storage tank 12 are a vertical tank body.
上述实施例1和实施例2的用于内燃机尾气净化的装置气的工作原理相同,如下:Above-mentioned embodiment 1 and the working principle of the device gas that is used for internal combustion engine tail gas purification of embodiment 2 are the same, as follows:
在正常工作时,实施例1中尿素-水溶液储罐中12的尿素-水溶液11在重力作用下经供尿素-水溶液管9、溶液流量控制阀10进入气流式喷头6;通过压缩空气供应管14、压缩空气控制阀13的压缩空气也同时进入气流式喷头6,在气流式喷头6中,压缩空气与尿素-水溶液11充分混合,因压缩空气的流速极高,故在压缩空气与尿素-水溶液11的速度差的作用下,尿素-水溶液11的液膜被撕裂,形成极微细尿素-水溶液11液滴被喷出气流式喷头6,形成一片极微细尿素-水溶液11液滴形成的雾区。When working normally, the urea-water solution 11 in the urea-water solution storage tank 12 in the embodiment 1 enters the air flow type nozzle 6 through the urea-water solution pipe 9 and the solution flow control valve 10 under the action of gravity; through the compressed air supply pipe 14 1. The compressed air of the compressed air control valve 13 also enters the airflow nozzle 6 at the same time. In the airflow nozzle 6, the compressed air is fully mixed with the urea-water solution 11. Under the action of the speed difference of 11, the liquid film of urea-water solution 11 is torn, forming very fine urea-water solution 11 droplets, which are sprayed out of the airflow nozzle 6, forming a mist area formed by very fine urea-water solution 11 droplets .
在正常工作时,实施例2中尿素-水溶液储罐中12的尿素-水溶液11在高压齿轮泵36的抽吸作用下经供尿素-水溶液管9、溶液流量控制阀10向压喷式喷头37提供高压尿素-水溶液液流,在高压作用下压喷式喷头37喷出极微细尿素-水溶液11液滴形成的雾区。During normal operation, the urea-water solution 11 in the urea-water solution storage tank 12 in the embodiment 2 is supplied to the pressure spray nozzle 37 through the urea-water solution pipe 9 and the solution flow control valve 10 under the suction of the high-pressure gear pump 36. A high-pressure urea-water solution flow is provided, and the pressure spray nozzle 37 sprays out a mist area formed by extremely fine urea-water solution 11 droplets under the action of high pressure.
柴油机尾气通过柴油机尾气排管7进入前箱体8前部圆筒状箱体,遇到这片极微细尿素-水溶液11液滴形成的雾区后,迅速混合,因柴油机尾气是高温气体(350℃--430℃左右),故极微细尿素-水溶液11液滴迅速被加热,其中的水分迅速蒸发,其中的尿素(CON2H4)会在高温下(160℃以上)发生分解反应(CON2H4)=(NH3)+(CONH),产生氨气(NH3)和缩二脲(CONH),其中的氨气与尾气中的气体混合,混合后一部分氨气立即与尾气中的二氧化硫发生如下化学反应,其反应式为:The diesel engine exhaust enters the front cylindrical box of the front box body 8 through the diesel engine exhaust pipe 7, and after encountering the mist area formed by the extremely fine urea-water solution 11 droplets, it mixes rapidly, because the diesel engine exhaust is a high-temperature gas (350 ℃--430℃), so the extremely fine urea-water solution 11 droplets are heated rapidly, the water in it evaporates rapidly, and the urea (CON 2 H 4 ) in it will decompose at high temperature (above 160℃) (CON 2 H 4 )=(NH 3 )+(CONH), producing ammonia gas (NH 3 ) and biuret (CONH), wherein the ammonia gas is mixed with the gas in the tail gas, and a part of the ammonia gas is immediately mixed with the gas in the tail gas Sulfur dioxide undergoes the following chemical reaction, and its reaction formula is:
SO2+H2O+xNH3=(HN4)xH2-xSO3(1)SO 2 +H 2 O+xNH 3 =(HN 4 )xH 2 −xSO 3 (1)
得到亚硫酸铵中间产品,亚硫酸铵再进行氧化:Obtain ammonium sulfite intermediate product, and ammonium sulfite is further oxidized:
(NH4)XH2-XSO3+1/2O2+(2-x)NH3=(NH4)2SO42(NH 4 )XH 2 -XSO 3 +1/2O 2 +(2-x)NH 3 =(NH 4 )2SO 4 2
实现了完全干法脱硫,脱硫后的终产物硫酸铵(NH4)2SO4和尿素分解后缩二脲(CONH)会形成细小的固态颗粒混入尾气中。Complete dry desulfurization is achieved, and the final products after desulfurization, ammonium sulfate (NH 4 ) 2 SO 4 and biuret (CONH) after urea decomposition, will form fine solid particles and mix into the tail gas.
中箱体21所包含的主要部分是颗粒物去除系统实际上是一个以不锈钢过滤毡4为过滤材料的折叠式滤筒,尾气与脱硫后剩余氨气等的混合气体从前箱体8进入中箱体21前端后首先遇到滤筒前盲板5,其为一钢板制圆盲板,混合气体通不过,只能绕行通过折叠式不锈钢过滤毡4外层,然后穿过折叠式不锈钢过滤毡4进入滤筒内腔,实现过滤。通过过滤,将尾气中的颗粒物(包括尾气中原有的碳化颗粒物等颗粒物和尿素分解后缩二脲(CONH)和脱硫后的硫酸铵(NH4)2SO4细小的固态颗粒)去除。当不锈钢过滤毡4积累了一定量的颗粒物后,会使过滤层阻力加大,影响混合气体通过,此时通过启动喷吹控制仪18,经控制导线20发出一个信号向电磁脉冲阀19通电,电磁脉冲阀19瞬间开启,压缩空气储罐17中的压缩空气通过喷吹管22、22到喷吹喷嘴25,由喷吹喷嘴25向外滤式滤筒内腔喷吹(与尾气过滤方向相反),实现清理附着在不锈钢过滤毡4外层上的积累的颗粒物,被清理后的颗粒物落入灰斗2中,待灰斗2积满颗粒物后,拧开锁灰螺帽1排出。经过滤后去除颗粒物后的尾气与脱硫后剩余氨的混合气体通过滤筒花板32和滤筒环板35中空的通道进入后箱体26中的催化反应系统,在混合气体穿过陶瓷催化单元28的多个内壁上涂覆催化剂方形通道时,在高温和催化条件下,尾气混合气中的气态氨与氮氧化物(包括NO和NO2)发生下列化学反应:The main part contained in the middle box 21 is the particle removal system, which is actually a pleated filter cartridge with stainless steel filter felt 4 as the filter material. The mixed gas of tail gas and residual ammonia after desulfurization enters the middle box from the front box 8 21 After the front end, it first encounters the front blind plate 5 of the filter cartridge, which is a round blind plate made of steel plate, and the mixed gas cannot pass through, so it can only bypass the outer layer of the folded stainless steel filter felt 4, and then pass through the folded stainless steel filter felt 4 Enter the inner cavity of the filter cartridge to achieve filtration. Through filtration, the particulate matter in the exhaust gas (including the original carbonized particulate matter in the exhaust gas and fine solid particles of biuret (CONH) after urea decomposition and ammonium sulfate (NH 4 ) 2 SO 4 after desulfurization) is removed. When the stainless steel filter felt 4 accumulates a certain amount of particles, the resistance of the filter layer will increase, affecting the passage of the mixed gas. At this time, by starting the injection control device 18, a signal is sent through the control wire 20 to energize the electromagnetic pulse valve 19. The electromagnetic pulse valve 19 is opened instantly, the compressed air in the compressed air storage tank 17 passes through the injection pipes 22 and 22 to the injection nozzle 25, and the injection nozzle 25 sprays to the inner cavity of the outer filter cartridge (opposite to the exhaust gas filtration direction) , to realize cleaning the accumulated particles attached to the stainless steel filter felt 4 outer layers, the cleaned particles fall into the ash hopper 2, and after the ash hopper 2 is full of particles, unscrew the ash lock nut 1 to discharge. The mixed gas of the exhaust gas after filtering to remove particulate matter and the residual ammonia after desulfurization enters the catalytic reaction system in the rear box 26 through the hollow channel of the filter cartridge flower plate 32 and the filter cartridge ring plate 35, and the mixed gas passes through the ceramic catalytic unit When the multiple inner walls of 28 are coated with catalyst square channels, under high temperature and catalytic conditions, the gaseous ammonia in the exhaust gas mixture and nitrogen oxides (including NO and NO 2 ) undergo the following chemical reactions:
4NH3+4NO+O2=4N2+6H2O4NH 3 +4NO+O 2 =4N 2 +6H 2 O
8NH3+6NO2=7N2+12H2O28NH 3 +6NO 2 =7N 2 +12H 2 O2
同时在高温和催化条件下,尾气混合气中的一氧化碳与氮氧化物(包括NO和NO2)发生下列化学反应:At the same time, under high temperature and catalytic conditions, carbon monoxide and nitrogen oxides (including NO and NO 2 ) in the exhaust gas mixture undergo the following chemical reactions:
2CO+2NO+O2=2CO2+N2 2CO+2NO+O 2 =2CO 2 +N 2
4CO+2NO2=4CO2+N224CO+2NO 2 =4CO 2 +N 2 2
通过上述化学反应,将柴油机尾气中的一氧化碳与氮氧化物生成对环境无害的氮气、二氧化碳和水。综上,通过以上三级净化,将柴油机排放的主要气态污染物(NOX、SO2、CO)及固态颗粒污染物。实现绝大部分去除。因此,以上结构和过程带来如下有益效果:Through the above chemical reaction, the carbon monoxide and nitrogen oxides in the exhaust gas of the diesel engine are converted into nitrogen, carbon dioxide and water which are harmless to the environment. To sum up, through the above three-stage purification, the main gaseous pollutants (NO X , SO 2 , CO) and solid particle pollutants emitted by diesel engines are eliminated. Achieve the vast majority of removal. Therefore, the above structure and process bring the following beneficial effects:
(1)装置结构简单、体积小、重量轻,仅需一套精巧的气流式喷雾系统实现气态氨生成功能,代替选择性催化还原法中氨气蒸发器、氨气缓冲罐、气体流量阀等庞大的设备组成的气态氨生成系统,这对于大部分为移动污染源柴油机来言,更具备实用性。(1) The device is simple in structure, small in size and light in weight, and only needs a set of exquisite airflow spraying system to realize the function of gaseous ammonia generation, replacing the ammonia evaporator, ammonia buffer tank, gas flow valve, etc. in the selective catalytic reduction method The gaseous ammonia generation system composed of huge equipment is more practical for most diesel engines that are mobile pollution sources.
(2)从根本上解决了选择性催化还原法的安全性问题(2) Fundamentally solve the safety problem of selective catalytic reduction method
因选择性催化还原法是通过在氨气蒸发器中氨水蒸发产生气态氨再经氨气缓冲罐最后将气态氨在混入尾气中,在这个过程中,产生的气态氨的浓度很容易达到爆炸临界区间浓度,存在着很高的安全隐患;而本发明中气态氨产生的方法是将尿素-水溶液直接混入高温尾气之中,通过尿素的分解产生气态氨,这种方法生成气态氨的浓度能够远远偏离氨气的浓度爆炸区间,从而完全消除了选择性催化还原法安全隐患。Because the selective catalytic reduction method is to produce gaseous ammonia by evaporating ammonia water in the ammonia evaporator, and finally mix the gaseous ammonia into the tail gas through the ammonia buffer tank. In this process, the concentration of gaseous ammonia can easily reach the explosion criticality. interval concentration, there is a very high potential safety hazard; and the method for producing gaseous ammonia in the present invention is to directly mix urea-water solution into the high-temperature tail gas, and generate gaseous ammonia through the decomposition of urea, and the concentration of gaseous ammonia generated by this method can be far It is far away from the concentration explosion range of ammonia, thus completely eliminating the safety hazard of the selective catalytic reduction method.
(3)解决了选择性催化还原法的气态氨生成量不稳定的弊病(3) Solve the disadvantages of unstable gaseous ammonia production in the selective catalytic reduction method
由于选择性催化还原法是在氨气蒸发器重产生气态氨,其产生量对温度非常敏感,必须精确控制氨气蒸发器的温度,方能控制发生量,同时还要通过氨气缓冲罐缓冲,再用气体调节阀调整,最终才能实现以合适的氨气量注入尾气中。而本发明因生成气态氨的方法不同,其气态氨在尾气中的注入量完全取决于尿素-水溶液的浓度和注入量,而浓度在配置时极易控制,混入量只要通过一个液体调节阀(比气体调节阀小得多)就能精确控制,而且不会因温度条件的变化而改变。从而实现了精确控制注入尾气气态氨的目的。不会造成因注入气态氨过量而造成氨的污染,也不会因注入气态氨过少造成净化气态污染物中的NOX和CO效率低的问题。Since the selective catalytic reduction method regenerates gaseous ammonia in the ammonia evaporator, its production is very sensitive to temperature, and the temperature of the ammonia evaporator must be precisely controlled to control the production. At the same time, it must be buffered by the ammonia buffer tank. Then use the gas regulating valve to adjust, and finally realize the injection of an appropriate amount of ammonia into the exhaust gas. And the present invention is different because of the method for generating gaseous ammonia, and the injection amount of its gaseous ammonia in tail gas completely depends on the concentration and the injection amount of urea-water solution, and concentration is very easy to control when disposing, as long as the mixing amount passes through a liquid regulating valve ( Much smaller than a gas regulating valve) can be precisely controlled and will not change due to changes in temperature conditions. Therefore, the purpose of precisely controlling the injection of tail gas gaseous ammonia is realized. It will not cause ammonia pollution due to excessive injection of gaseous ammonia, and will not cause low efficiency of purifying NOx and CO in gaseous pollutants due to too little injection of gaseous ammonia.
以上所述仅是本发明的优选实施方式,应当指出,对于本技术领域的普通技术人员来说,在不脱离本发明技术原理的前提下,还可以做出若干改进和替换,这些改进和替换也应视为本发明的保护范围。The above is only a preferred embodiment of the present invention, it should be pointed out that for those of ordinary skill in the art, without departing from the technical principle of the present invention, some improvements and replacements can also be made, these improvements and replacements It should also be regarded as the protection scope of the present invention.
Claims (8)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201210050162.7A CN103291419B (en) | 2012-02-29 | 2012-02-29 | A kind of tail gas purification device of combustion engine |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201210050162.7A CN103291419B (en) | 2012-02-29 | 2012-02-29 | A kind of tail gas purification device of combustion engine |
Publications (2)
Publication Number | Publication Date |
---|---|
CN103291419A CN103291419A (en) | 2013-09-11 |
CN103291419B true CN103291419B (en) | 2015-12-16 |
Family
ID=49092862
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201210050162.7A Expired - Fee Related CN103291419B (en) | 2012-02-29 | 2012-02-29 | A kind of tail gas purification device of combustion engine |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN103291419B (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP6479541B2 (en) * | 2015-04-03 | 2019-03-06 | ヤマシンフィルタ株式会社 | strainer |
CN104771969B (en) * | 2015-04-20 | 2017-01-11 | 北京京能未来燃气热电有限公司 | Refined filtration drum dedusting device and refined filtration drum dedusting method for inlet air filtering system of gas turbine |
CN105240093B (en) * | 2015-09-30 | 2017-12-22 | 暴辰生 | A kind of diesel engine exhaust gas purification device |
DE102016208171A1 (en) * | 2016-05-12 | 2017-11-16 | Robert Bosch Gmbh | Apparatus and method for improving the recirculation of reductant in an exhaust gas reduction system |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2819549A1 (en) * | 2001-01-12 | 2002-07-19 | Renault | EXHAUST GAS TREATMENT SYSTEM FOR A COMBUSTION ENGINE |
CN2572010Y (en) * | 2002-07-31 | 2003-09-10 | 李清华 | Carbon smoke pollution purifier for diesel engine |
CN1629458A (en) * | 2003-12-18 | 2005-06-22 | 丰田哲郎 | Particulate matter reducing apparatus |
CN1935335A (en) * | 2005-09-01 | 2007-03-28 | 通用汽车环球科技运作公司 | Flash injector for nh3-scr nox aftertreatment |
CN101806238A (en) * | 2010-03-13 | 2010-08-18 | 中国第一汽车集团公司 | Air-assisted atomized urea reducing agent spraying controlling system of pump power |
US7937933B2 (en) * | 2006-08-16 | 2011-05-10 | Man Truck & Bus Ag | Exhaust gas post treatment system |
CN202493322U (en) * | 2012-02-29 | 2012-10-17 | 北京市劳动保护科学研究所 | Tail gas purification device of internal combustion engine |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007077957A (en) * | 2005-09-16 | 2007-03-29 | Hino Motors Ltd | Exhaust emission control device |
-
2012
- 2012-02-29 CN CN201210050162.7A patent/CN103291419B/en not_active Expired - Fee Related
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2819549A1 (en) * | 2001-01-12 | 2002-07-19 | Renault | EXHAUST GAS TREATMENT SYSTEM FOR A COMBUSTION ENGINE |
CN2572010Y (en) * | 2002-07-31 | 2003-09-10 | 李清华 | Carbon smoke pollution purifier for diesel engine |
CN1629458A (en) * | 2003-12-18 | 2005-06-22 | 丰田哲郎 | Particulate matter reducing apparatus |
CN1935335A (en) * | 2005-09-01 | 2007-03-28 | 通用汽车环球科技运作公司 | Flash injector for nh3-scr nox aftertreatment |
US7937933B2 (en) * | 2006-08-16 | 2011-05-10 | Man Truck & Bus Ag | Exhaust gas post treatment system |
CN101806238A (en) * | 2010-03-13 | 2010-08-18 | 中国第一汽车集团公司 | Air-assisted atomized urea reducing agent spraying controlling system of pump power |
CN202493322U (en) * | 2012-02-29 | 2012-10-17 | 北京市劳动保护科学研究所 | Tail gas purification device of internal combustion engine |
Also Published As
Publication number | Publication date |
---|---|
CN103291419A (en) | 2013-09-11 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP6403355B2 (en) | Method and system for removing particulate matter soot, ash and heavy metals from engine exhaust gas | |
CN103291419B (en) | A kind of tail gas purification device of combustion engine | |
CN101314105A (en) | Control technique and apparatus for flue gas NOx of cement kiln | |
JP5801472B2 (en) | Exhaust gas purification device | |
CN105240093B (en) | A kind of diesel engine exhaust gas purification device | |
CN106268270A (en) | A kind of grate kiln denitrating system | |
CA2954013A1 (en) | Method and system for the removal of particulate matter and heavy metals from engine exhaust gas | |
CN202493322U (en) | Tail gas purification device of internal combustion engine | |
GB2545751A (en) | Apparatus for gas cleaning | |
KR101122748B1 (en) | Exhaust gas purifier and method of exhaust gas purification | |
KR20230082733A (en) | SCR system equipped with soot blower that prevents dust in the exhaust gas generated during the cement manufacturing process from adhering to the SCR catalyst | |
CN101322902A (en) | Uniset for controlling cement kiln flue gas | |
KR101938910B1 (en) | SCR chamber with mixer | |
CN206853478U (en) | Utilize the ammonia spraying and mixing system of outside filtering type dust catcher gas purifying chamber structure | |
CN214261075U (en) | Novel flue gas treatment system | |
CN212467734U (en) | High-temperature dust removal and denitration integrated device | |
KR101527718B1 (en) | NOx emission purification system using multi nozzle injection of urea powder | |
CN203891982U (en) | SCR denitration system for tail gas of generator set | |
CN108561210A (en) | Marine Diesel Engine Pollutant Emission Treatment System | |
CN203971758U (en) | A kind of denitrating flue gas spraying urea liquid emitter | |
CN208220872U (en) | Marine diesel particulate matter discharges entrapment device | |
CN111841320A (en) | High-temperature dust removal and denitration integrated device | |
US20170165607A1 (en) | Methods and apparatus to treat exhaust streams | |
CN205172696U (en) | Diesel engine exhaust purifying device | |
KR100965136B1 (en) | Hazardous Exhaust Gas Reduction System |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20151216 Termination date: 20190228 |
|
CF01 | Termination of patent right due to non-payment of annual fee |