CN205700083U - A kind of boat diesel engine tail gas desulfurization denitration combined apparatus - Google Patents
A kind of boat diesel engine tail gas desulfurization denitration combined apparatus Download PDFInfo
- Publication number
- CN205700083U CN205700083U CN201620407268.1U CN201620407268U CN205700083U CN 205700083 U CN205700083 U CN 205700083U CN 201620407268 U CN201620407268 U CN 201620407268U CN 205700083 U CN205700083 U CN 205700083U
- Authority
- CN
- China
- Prior art keywords
- turbine
- outlet
- pipeline
- diesel engine
- exhaust gas
- 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
- 238000006477 desulfuration reaction Methods 0.000 title claims abstract description 27
- 230000023556 desulfurization Effects 0.000 title claims abstract description 27
- 239000007789 gas Substances 0.000 claims abstract description 65
- 239000002918 waste heat Substances 0.000 claims abstract description 21
- 239000002912 waste gas Substances 0.000 claims abstract description 20
- 238000005201 scrubbing Methods 0.000 claims abstract description 15
- 230000002000 scavenging effect Effects 0.000 claims abstract description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 15
- 238000007254 oxidation reaction Methods 0.000 claims description 13
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims description 12
- 230000003197 catalytic effect Effects 0.000 claims description 12
- 230000003647 oxidation Effects 0.000 claims description 10
- HEMHJVSKTPXQMS-UHFFFAOYSA-M sodium hydroxide Inorganic materials [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 15
- 238000005406 washing Methods 0.000 description 15
- 238000000034 method Methods 0.000 description 10
- 229910052717 sulfur Inorganic materials 0.000 description 8
- 239000011593 sulfur Substances 0.000 description 8
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 6
- 239000000295 fuel oil Substances 0.000 description 6
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 6
- 238000005516 engineering process Methods 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000003546 flue gas Substances 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 230000037361 pathway Effects 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 238000006722 reduction reaction Methods 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 239000007832 Na2SO4 Substances 0.000 description 1
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000010531 catalytic reduction reaction Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000003009 desulfurizing effect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- XLYOFNOQVPJJNP-ZSJDYOACSA-N heavy water Substances [2H]O[2H] XLYOFNOQVPJJNP-ZSJDYOACSA-N 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000008520 organization Effects 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000003134 recirculating effect Effects 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 229910052938 sodium sulfate Inorganic materials 0.000 description 1
- 235000011152 sodium sulphate Nutrition 0.000 description 1
- 235000011149 sulphuric acid Nutrition 0.000 description 1
- 238000010792 warming Methods 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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
-
- 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
- Y02T70/00—Maritime or waterways transport
- Y02T70/50—Measures to reduce greenhouse gas emissions related to the propulsion system
Landscapes
- Exhaust Gas After Treatment (AREA)
Abstract
本实用新型的目的在于提供一种船舶柴油机尾气脱硫脱硝联合处理装置,包括柴油机、涡轮增压器、余热锅炉、尾气洗涤塔,柴油机分别连接排气歧管和扫气箱,排气歧管通过涡轮进口管路连接涡轮进口,涡轮出口通过涡轮出口管路连接余热锅炉的进口,涡轮出口管路与涡轮进口管路通过废气旁通通路相通,压气机出口通过压气机出口管路连接扫气箱,压气机出口管路与排气歧管通过压缩空气旁通通路相通,余热锅炉的出口连接余热锅炉出口管路,余热锅炉出口管路与废气洗涤脱硫通路、排放管路通过三通方式相连,废气洗涤脱硫通路连接尾气洗涤塔的进口,尾气洗涤塔的出口与排放管路连通后连通大气。本实用新型能够满足IMO法规对船舶柴油机NOX和SOX排要求。
The purpose of this utility model is to provide a marine diesel engine tail gas desulfurization and denitrification combined treatment device, including a diesel engine, a turbocharger, a waste heat boiler, and an exhaust scrubber. The diesel engine is connected to an exhaust manifold and a scavenging box respectively, and the exhaust manifold passes The turbine inlet pipeline is connected to the turbine inlet, the turbine outlet is connected to the inlet of the waste heat boiler through the turbine outlet pipeline, the turbine outlet pipeline is connected to the turbine inlet pipeline through the waste gas bypass passage, and the compressor outlet is connected to the scavenging box through the compressor outlet pipeline , the outlet pipeline of the compressor is connected with the exhaust manifold through the compressed air bypass passage, the outlet of the waste heat boiler is connected with the outlet pipeline of the waste heat boiler, and the outlet pipeline of the waste heat boiler is connected with the exhaust gas scrubbing and desulfurization passage and the discharge pipeline through a three-way way. The waste gas scrubbing and desulfurization channel is connected to the inlet of the tail gas scrubber, and the outlet of the tail gas scrubber is connected to the discharge pipeline and then connected to the atmosphere. The utility model can meet the NOX and SOX discharge requirements of marine diesel engines in IMO regulations.
Description
技术领域technical field
本实用新型涉及的是一种柴油机尾气处理装置,具体地说是船舶柴油机尾气处理装置。The utility model relates to a diesel engine tail gas treatment device, in particular to a marine diesel engine tail gas treatment device.
背景技术Background technique
随着船舶航运业的迅速发展,船舶废气排放量日益增多,对环境的危害日益严重。根据国家环境保护部监控中心的数据,2013年在中国港口靠泊的船舶共排放二氧化硫58.8万吨,约占全国排放总量的8.4%;港口船舶氮氧化物排放量27.8万吨,约占全国排放总量的11.3%。国际海事组织IMO制定了一系列防污染公约,对船舶废气中有害成分排放进行了严格限制。2016年1月1日起在排放控制区内的船舶排放要求达到Tier III排放标准。With the rapid development of the shipping industry, the emission of ship exhaust gas is increasing day by day, and the harm to the environment is becoming more and more serious. According to the data from the Monitoring Center of the Ministry of Environmental Protection, in 2013, ships berthing at Chinese ports emitted a total of 588,000 tons of sulfur dioxide, accounting for about 8.4% of the country's total emissions; port ships emitted 278,000 tons of nitrogen oxides, accounting for about 8.4% of the country's total emissions. 11.3% of total emissions. The International Maritime Organization (IMO) has formulated a series of anti-pollution conventions, which strictly limit the emission of harmful components in ship exhaust. From January 1, 2016, the emission requirements of ships in the emission control area shall meet the Tier III emission standard.
船舶柴油机减排技术,主要包括采用低硫燃油和废气洗涤技术两种。相对而言,采用低硫燃油比较方便,对船舶改动较小,可以满足IMO对船舶燃油硫含量的要求,但船用高低硫燃油之间差价巨大,使用低硫燃油成本太高,同时现有发动机使用低硫燃油存在粘度过低、润滑性差、容易磨损等问题,对发动机有一定的损害,且低硫燃油在炼制过程中会产生大量的CO2,加剧全球温室效应。Marine diesel engine emission reduction technologies mainly include the use of low-sulfur fuel oil and exhaust gas washing technology. Relatively speaking, it is more convenient to use low-sulfur fuel oil, and the changes to the ship are small, and it can meet the IMO requirements for the sulfur content of ship fuel oil. The use of low-sulfur fuel has problems such as low viscosity, poor lubricity, and easy wear, which will cause certain damage to the engine, and low-sulfur fuel will produce a large amount of CO2 during the refining process, which will intensify the global warming effect.
NOX的脱除主要用选择性催化还原法(SCR),用NH3将NO还原为N2。由于脱硫后的气体温度较低,SCR反应需要较高的温度,需将气体二次加热才能脱硝。The removal of NOX mainly uses Selective Catalytic Reduction (SCR), using NH3 to reduce NO to N2. Due to the low temperature of the gas after desulfurization, the SCR reaction requires a higher temperature, and the gas needs to be heated twice to denitrify.
作为IMO认可的一种除去船舶废气脱硫(FGD)的有效方法,废气洗涤技术通过对燃用低质高硫重油产生的废气进行清洗,除去其中的SOX,满足IMO有关燃油硫含量的要求。湿法FGD具有很高的脱硫效率,但却难以同时脱硝,这是因为船舶柴油机实际尾气中的NOX中90%以上都是NO,NO除了生成络合物以外,几乎不被水或碱液吸收。As an effective method approved by IMO to remove ship exhaust gas desulfurization (FGD), exhaust gas scrubbing technology cleans the exhaust gas produced by burning low-quality high-sulfur heavy oil, removes SOX, and meets IMO's requirements for fuel oil sulfur content. Wet FGD has high desulfurization efficiency, but it is difficult to denitrify at the same time, because more than 90% of NOX in the actual exhaust gas of marine diesel engines is NO, and NO is hardly absorbed by water or lye except for the formation of complexes .
目前,对船舶废气NOX和SOX的研究和处理,都是分开单独进行,即使用两套不同设备,分别对NOX和SOX进行处理。这种废气串联处理方法,设备体积巨大,背压高,对发动机正常工作影响较大,设备投资和运行费用都很高。At present, the research and treatment of ship exhaust NOX and SOX are carried out separately, that is, two sets of different equipment are used to treat NOX and SOX respectively. This exhaust gas series treatment method has huge equipment volume and high back pressure, which has a great impact on the normal operation of the engine, and the equipment investment and operation costs are very high.
发明内容Contents of the invention
本实用新型的目的在于提供能够满足IMO法规对船舶柴油机NOX和SOX排要求的一种船舶柴油机尾气脱硫脱硝联合处理装置。The purpose of the utility model is to provide a ship diesel engine tail gas desulfurization and denitrification combined treatment device that can meet the requirements of IMO regulations on NOX and SOX emissions of ship diesel engines.
本实用新型的目的是这样实现的:The purpose of this utility model is achieved in that:
本实用新型一种船舶柴油机尾气脱硫脱硝联合处理装置,其特征是:包括柴油机、涡轮增压器、余热锅炉、尾气洗涤塔,涡轮增压器包括涡轮和压气机,柴油机分别连接排气歧管和扫气箱,排气歧管通过涡轮进口管路连接涡轮进口,涡轮出口通过涡轮出口管路连接余热锅炉的进口,涡轮出口管路与涡轮进口管路通过废气旁通通路相通,废气旁通通路上安装第一单向截止阀,压气机出口通过压气机出口管路连接扫气箱,压气机出口管路上安装空冷器、水滴捕集器,压气机出口管路与排气歧管通过压缩空气旁通通路相通,压缩空气旁通通路上安装第二单向截止阀,余热锅炉的出口连接余热锅炉出口管路,余热锅炉出口管路与废气洗涤脱硫通路、排放管路通过三通方式相连,废气洗涤脱硫通路连接尾气洗涤塔的进口,尾气洗涤塔的出口与排放管路连通后连通大气,废气洗涤脱硫通路上安装催化氧化装置,催化氧化装置连接臭氧发生器,尾气洗涤塔连接水处理单元。The utility model discloses a marine diesel engine tail gas desulfurization and denitrification combined treatment device, which is characterized in that it includes a diesel engine, a turbocharger, a waste heat boiler, and a tail gas scrubber, the turbocharger includes a turbine and a compressor, and the diesel engine is connected to an exhaust manifold respectively. and the scavenging box, the exhaust manifold is connected to the turbine inlet through the turbine inlet pipe, the turbine outlet is connected to the inlet of the waste heat boiler through the turbine outlet pipe, the turbine outlet pipe is connected to the turbine inlet pipe through the waste gas bypass passage, and the waste gas bypass passage The first one-way stop valve is installed on the road. The compressor outlet is connected to the scavenging box through the compressor outlet pipeline. The bypass passage is connected, and the second one-way stop valve is installed on the compressed air bypass passage. The outlet of the waste heat boiler is connected to the outlet pipeline of the waste heat boiler. The scrubbing and desulfurization pathway is connected to the inlet of the exhaust gas scrubber, the outlet of the exhaust gas scrubber is connected to the discharge pipeline and then connected to the atmosphere, the exhaust gas scrubbing and desulfurization pathway is equipped with a catalytic oxidation device, the catalytic oxidation device is connected to the ozone generator, and the exhaust gas scrubber is connected to the water treatment unit.
本实用新型的优势在于:The utility model has the advantages of:
1、本实用新型采用的一种船舶柴油机尾气脱硫脱硝联合处理系统满足IMO有关船舶废气排放标准。1. A marine diesel engine exhaust desulfurization and denitrification combined treatment system adopted in the utility model meets the relevant IMO emission standards for ships.
2、本实用新型采用臭氧催化氧化法,将不易被碱液吸收的NO转化为易被碱液吸收的NO2,大幅提高了碱液对NOX的洗涤脱硝效率。2. The utility model adopts the ozone catalytic oxidation method to convert NO which is difficult to be absorbed by lye into NO2 which is easily absorbed by lye, which greatly improves the washing and denitrification efficiency of lye on NOX.
3、由于使用一套装置同时脱除发动机废气中的NOX和SOX,本实用新型装置的体积和重量要明显小于分别进行脱硫和脱硝的装置的体积和重量之和,设备紧凑,可节省船舶有效空间,投资成本和运行费用低,对发动机影响小。3. Since a set of equipment is used to simultaneously remove NOX and SOX in the exhaust gas of the engine, the volume and weight of the device of the utility model are significantly smaller than the sum of the volume and weight of the devices for desulfurization and denitrification respectively. The equipment is compact and can save ships and effectively The space, investment cost and operation cost are low, and the impact on the engine is small.
4、采用废气旁通技术,保证了废气洗涤脱硫脱硝装置运行的安全性。4. The exhaust gas bypass technology is adopted to ensure the safety of the operation of the exhaust gas scrubbing, desulfurization and denitrification device.
5、在对船舶柴油机尾气脱硫脱硝联合处理的同时,还可以降低颗粒物的排放。5. While desulfurizing and denitrifying the tail gas of marine diesel engines, it can also reduce the emission of particulate matter.
附图说明Description of drawings
图1为本实用新型的结构示意图。Fig. 1 is the structural representation of the utility model.
具体实施方式detailed description
下面结合附图举例对本实用新型做更详细地描述:The utility model is described in more detail below in conjunction with accompanying drawing example:
结合图1,本实用新型的船舶柴油机尾气脱硫脱硝联合处理系统适合于船舶动力装置,该动力装置具有柴油机1,通过排气管2连接到柴油机上的排气歧管3,设置在进气通路上的空气中间冷却器6和水滴捕集器7,连通到排气歧管的涡轮10,以及设置在进气通路上的压气机4;进气通路连通压气机4出口和扫气箱8,包含空气中间冷却器6和水滴捕集器7;含有单向截止阀11的涡轮废气旁通通路直接连接涡轮入口10和余热锅炉12入口;包含单向截止阀5的压缩空气旁通通路直接连接压气机4出口和涡轮10入口;由三通阀13控制的废气洗涤脱硫通路和废气旁通通路。With reference to Fig. 1, the marine diesel engine tail gas desulfurization and denitrification joint treatment system of the present utility model is suitable for a marine power plant. The air intercooler 6 and the water droplet catcher 7 on the top, the turbine 10 connected to the exhaust manifold, and the compressor 4 arranged on the intake passage; the intake passage communicates with the outlet of the compressor 4 and the scavenging box 8, Contains air intercooler 6 and water droplet collector 7; turbine waste gas bypass passage containing one-way stop valve 11 is directly connected to turbine inlet 10 and waste heat boiler 12 inlet; compressed air bypass passage including one-way stop valve 5 is directly connected to The outlet of the compressor 4 and the inlet of the turbine 10; the exhaust gas scrubbing and desulfurization passage and the waste gas bypass passage controlled by the three-way valve 13.
船舶在排放控制区运行时,柴油机的废气通过排气歧管3全部通入涡轮,在涡轮10中膨胀做功,驱动压气机4工作,压气机4压缩新鲜空气,压缩空气经过空气中间冷却器6降温,进入水滴捕集器7,去除其中所含水滴,进入扫气箱8,再通过进气管9,进入柴油机1,参与燃烧;当发动机中低负荷工作时,压缩空气旁通通路中单向截止阀11关闭,在发动机高负荷工作时,柴油机废气量过剩,开启涡轮废气旁通通路中单向截止阀11,旁通多余废气,提高发动机效率。When the ship is running in the emission control area, all the exhaust gas from the diesel engine is passed into the turbine through the exhaust manifold 3, expands in the turbine 10 to perform work, and drives the compressor 4 to work. The compressor 4 compresses fresh air, and the compressed air passes through the air intercooler 6 Cool down, enter the water droplet catcher 7, remove the water droplets contained in it, enter the scavenging air box 8, and then pass through the intake pipe 9, enter the diesel engine 1, and participate in combustion; The shut-off valve 11 is closed, and when the engine is working under high load, the exhaust gas of the diesel engine is excessive, and the one-way shut-off valve 11 in the turbine waste gas bypass passage is opened to bypass excess exhaust gas and improve engine efficiency.
按废气洗涤装置16是否投入运行,船舶柴油机系统分为两种运行模式,非洗涤模式和洗涤模式。Depending on whether the exhaust gas washing device 16 is put into operation, the marine diesel engine system is divided into two operating modes, a non-washing mode and a washing mode.
非洗涤模式:当船舶在非排放控制区和非港口区域航行时,废气经过余热锅炉12回收能量后,经三通阀13,由废气旁通通路直接排入环境大气。Non-scrubbing mode: When the ship is sailing in a non-emission control area and a non-port area, the exhaust gas passes through the waste heat boiler 12 to recover energy, passes through the three-way valve 13, and is directly discharged into the ambient atmosphere through the waste gas bypass passage.
洗涤模式:当船舶在硫排放控制区或港口区域航行时,废气经过余热锅炉12回收能量后,经三通阀13,由废气洗涤脱硫通路流入催化氧化装置15,与臭氧发生器14产生的臭氧发生氧化反应;氧化后的废气进入废气洗涤装置16,用碱液洗涤脱去其中的NOX,SOX和颗粒,经洗涤装置顶部除雾器去除水滴后,排入环境大气,洗涤后的废水进入水处理单元17处理。Scrubbing mode: when the ship is navigating in the sulfur emission control area or port area, the exhaust gas passes through the waste heat boiler 12 to recover energy, passes through the three-way valve 13, flows into the catalytic oxidation device 15 through the exhaust gas scrubbing and desulfurization passage, and the ozone generated by the ozone generator 14 Oxidation reaction occurs; the oxidized waste gas enters the waste gas washing device 16, and is washed with lye to remove NOX, SOX and particles. The processing unit 17 processes.
当船舶废气洗涤装置维修或出现故障时,废气经三通阀13,由废气旁通通路直接排入大气环境。When the marine waste gas washing device is repaired or fails, the waste gas passes through the three-way valve 13 and is directly discharged into the atmosphere through the waste gas bypass passage.
本实用新型装置包括在与柴油机的排气管相连的排气歧管和与油机的进气管相连的扫气箱之间连接的进气系统,所述进气系统包括连通到排气歧管的涡轮、由涡轮驱动的压气机、连接于压气机出口与扫气箱之间的空气中间冷却器。所述进气系统还包括连接于压气机出口和排气歧管之间的包含第一单向截止阀的压缩空气旁通通路,在涡轮进出口之间设置废气旁通管路,废气旁通管路上设置第四单向截止阀,废气旁通管路连接余热锅炉,余热锅炉后通过三通阀连接废气洗涤装置或直接连通大气。在空气中间冷却器与扫气箱之间设置空气水滴捕集器。在尾气洗涤器前有臭氧发生装置和催化氧化器。洗涤器采用一级或多级喷淋塔结构,或采用填料塔结构。本实用新型的船舶柴油机NOX和SOX排放控制装置包含柴油机系统和臭氧氧化装置及废气洗涤装置。在所述柴油机系统中,在空气中间冷却器后增设水滴捕集器。在所述柴油机系统中,增设涡轮废气旁通通路,连通涡轮进出口。增设压缩空气旁通通路,连通压气机出口和涡轮入口。The device of the utility model comprises an air intake system connected between an exhaust manifold connected with the exhaust pipe of the diesel engine and a scavenging box connected with the intake pipe of the diesel engine, and the air intake system includes The turbine, the compressor driven by the turbine, and the air intercooler connected between the compressor outlet and the scavenging box. The air intake system also includes a compressed air bypass passage including a first one-way stop valve connected between the compressor outlet and the exhaust manifold, and a waste gas bypass pipeline is arranged between the turbine inlet and outlet, and the waste gas bypass A fourth one-way stop valve is arranged on the pipeline, the waste gas bypass pipeline is connected to the waste heat boiler, and the waste heat boiler is connected to the waste gas scrubbing device through a three-way valve or directly connected to the atmosphere. An air droplet catcher is installed between the air intercooler and the scavenging air box. Before the tail gas scrubber, there is an ozone generator and a catalytic oxidizer. The scrubber adopts a one-stage or multi-stage spray tower structure, or a packed tower structure. The NOX and SOX emission control device of the marine diesel engine of the utility model comprises a diesel engine system, an ozone oxidation device and an exhaust gas washing device. In the diesel engine system, a water drop catcher is added after the air intercooler. In the diesel engine system, a turbine waste gas bypass passage is added to communicate with the turbine inlet and outlet. A compressed air bypass passage is added to connect the compressor outlet and the turbine inlet.
在所述柴油机系统中,非再循环的废气,经余热锅炉后,通过三通阀,或去废气洗涤装置洗涤或直接排入大气。In the diesel engine system, the non-recirculating exhaust gas passes through the waste heat boiler, then passes through the three-way valve, or goes to the exhaust gas cleaning device for washing or is directly discharged into the atmosphere.
在所述联合减排装置中,所述废气预洗装置、洗涤器和废气洗涤装置采用一级或多级喷淋塔结构,或采用填料塔结构。In the combined emission reduction device, the exhaust gas prewashing device, scrubber and exhaust gas scrubbing device adopt a one-stage or multi-stage spray tower structure, or adopt a packed tower structure.
本实用新型的船舶柴油机尾气脱硫脱硝联合处理方法的主要特点为:The main features of the combined desulfurization and denitrification treatment method for marine diesel engine tail gas of the utility model are:
船舶在氮氧化物排放控制区航行时,柴油机的废气通过排气歧管全部通入涡轮,做功驱动压气机工作,压缩新鲜空气,压缩空气经过空气中间冷却器降温,进入水滴捕集器,去除其中所含水滴,进入扫气箱,再由进气管,进入柴油机参与燃烧;压缩空气旁通通路中单向截止阀关闭,当发动机高负荷工作时,开启涡轮废气旁通通路中单向截止阀,旁通多余废气。When the ship is navigating in the nitrogen oxide emission control area, the exhaust gas of the diesel engine is completely fed into the turbine through the exhaust manifold, and works to drive the compressor to work, compress fresh air, and the compressed air passes through the air intercooler to cool down, enters the water droplet collector, and removes The water droplets contained in it enter the scavenging air box, and then enter the diesel engine through the intake pipe to participate in combustion; the one-way stop valve in the compressed air bypass passage is closed, and when the engine is working under high load, open the one-way stop valve in the turbine waste gas bypass passage , Bypass excess exhaust gas.
废气经过余热锅炉回收能量后,经三通阀由废气洗涤脱硫通路流入催化氧化装置,与臭氧发生器产生的臭氧发生催化氧化反应;氧化后的废气进入废气洗涤装置,用碱液洗涤脱去其中的NOX,SOX和颗粒,经洗涤装置顶部除雾器去除水滴后,排入环境大气,洗涤后的废水进入水处理单元处理。After the exhaust gas recovers energy through the waste heat boiler, it flows into the catalytic oxidation device from the exhaust gas washing and desulfurization passage through the three-way valve, and undergoes a catalytic oxidation reaction with the ozone generated by the ozone generator; the oxidized exhaust gas enters the exhaust gas washing device, and is washed with lye to remove it. The NOX, SOX and particles are discharged into the ambient atmosphere after the demister at the top of the washing device removes the water droplets, and the washed wastewater enters the water treatment unit for treatment.
船舶柴油机尾气中的主要有害气体成分中NO和SO2占主体,所以本实用新型主要处理烟气中的SO2和NO。钠碱法洗涤对SOX的脱除效率很高,但对NO脱除效果不理想;通过臭氧催化氧化法,将NO转化为易被碱液吸收的NO2,同时实现联合脱硫脱硝。The main harmful gas components in marine diesel engine tail gas are NO and SO2, so the utility model mainly treats SO2 and NO in flue gas. Sodium-alkali washing has a high removal efficiency for SOX, but the removal effect for NO is not ideal; through the ozone catalytic oxidation method, NO is converted into NO2, which is easily absorbed by alkali solution, and combined desulfurization and denitrification are realized at the same time.
本实用新型的化学反应过程如下:The chemical reaction process of the present utility model is as follows:
1、尾气脱硫过程1. Tail gas desulfurization process
O3+SO2→SO3+O2 O 3 +SO 2 →SO 3 +O 2
2NaOH+SO3→Na2SO4+H2O2NaOH+SO 3 →Na 2 SO 4 +H 2 O
SO3+H2O→H2SO4 SO 3 +H 2 O→H 2 SO 4
2NaOH+H2SO4→Na2SO4+2H2O2NaOH + H2SO4 → Na2SO4 + 2H2O
2、尾气脱硝过程2. Tail gas denitrification process
O3+NO→NO2+O2 O 3 +NO→NO 2 +O 2
O3+NO2→NO3+O2 O 3 +NO 2 →NO 3 +O 2
NO3+NO2→2N2O5 NO 3 +NO 2 →2N 2 O 5
N2O5+H2O→2HNO3 N 2 O 5 +H 2 O→2HNO 3
2NaOH+2NO2→NaNO3+NaNO2+H2O2NaOH+2NO 2 →NaNO 3 +NaNO 2 +H 2 O
NaOH+HNO3→NaNO3+H2ONaOH+HNO 3 →NaNO 3 +H 2 O
本实用新型公开了一种船舶柴油机尾气脱硫脱硝联合处理的装置。船舶柴油机在使用重油时所排放的烟气,主要成分为SOX和NOX等。在排放控制区内废气经过余热锅炉回收能量后,经三通阀由废气洗涤脱硫通路流入催化氧化装置,与臭氧发生器产生的臭氧发生催化氧化反应;氧化后的废气进入废气洗涤装置,用碱液洗涤脱去其中的NOX,SOX和颗粒,经洗涤装置顶部除雾器去除水滴后,排入环境大气,洗涤后的废水进入水处理单元处理。本实用新型采用脱硫脱硝联合处理系统,节省了设备投资,减小了占地面积。在提高船舶柴油机能量利用率的同时高效脱除尾气中的SOX和NOX,满足IMO排放法规的标准。The utility model discloses a combined treatment device for desulfurization and denitrification of marine diesel engine tail gas. The main components of the flue gas emitted by marine diesel engines when using heavy oil are SOX and NOX. In the emission control area, after the exhaust gas passes through the waste heat boiler to recover energy, it flows into the catalytic oxidation device through the exhaust gas scrubbing and desulfurization passage through the three-way valve, and undergoes a catalytic oxidation reaction with the ozone generated by the ozone generator; the oxidized exhaust gas enters the exhaust gas scrubbing device and The NOX, SOX and particles are removed by liquid washing, and the water droplets are removed by the demister at the top of the washing device, and then discharged into the ambient atmosphere, and the washed wastewater enters the water treatment unit for treatment. The utility model adopts a desulfurization and denitrification combined treatment system, which saves equipment investment and reduces the occupied area. While improving the energy utilization rate of marine diesel engines, it can efficiently remove SOX and NOX in the exhaust gas, meeting the standards of IMO emission regulations.
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620407268.1U CN205700083U (en) | 2016-05-06 | 2016-05-06 | A kind of boat diesel engine tail gas desulfurization denitration combined apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620407268.1U CN205700083U (en) | 2016-05-06 | 2016-05-06 | A kind of boat diesel engine tail gas desulfurization denitration combined apparatus |
Publications (1)
Publication Number | Publication Date |
---|---|
CN205700083U true CN205700083U (en) | 2016-11-23 |
Family
ID=57304490
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201620407268.1U Expired - Fee Related CN205700083U (en) | 2016-05-06 | 2016-05-06 | A kind of boat diesel engine tail gas desulfurization denitration combined apparatus |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN205700083U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105797553A (en) * | 2016-05-06 | 2016-07-27 | 哈尔滨工程大学 | Desulfurization and denitration combined treatment device of tail gas of marine diesel engine |
-
2016
- 2016-05-06 CN CN201620407268.1U patent/CN205700083U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105797553A (en) * | 2016-05-06 | 2016-07-27 | 哈尔滨工程大学 | Desulfurization and denitration combined treatment device of tail gas of marine diesel engine |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN104358627B (en) | Boat diesel engine NOx and SOx associating emission reduction device and control method | |
CN105797553A (en) | Desulfurization and denitration combined treatment device of tail gas of marine diesel engine | |
CN204253221U (en) | Boat diesel engine NOx and SOx combines emission reduction device | |
CN105289241A (en) | Combined desulphurization and denitration device and method of marine diesel engine | |
CN106984161B (en) | A comprehensive treatment method and device for ship exhaust gas pollutants and ballast water | |
JP6207498B2 (en) | Method for reducing nitrogen oxides and sulfur oxides in exhaust gas from an internal combustion engine | |
CN105771649A (en) | Composite device for aftertreatment of ship low-speed diesel engine end gas | |
CN104437084A (en) | Method for desulfurization and denitration of tail gas of internal combustion engine of ship | |
EP2853718B1 (en) | Method of exhaust gas treatment for a gas turbine system and exhaust gas treatment assembly | |
KR20190065489A (en) | Ship | |
CN109395575A (en) | A kind of ship tail gas desulfurization and denitrification integral processing method and processing device | |
CN107754607B (en) | Comprehensive treatment method and device for exhaust gas of marine diesel engine | |
CN103007691A (en) | Method and equipment of integrally desulfurizing and denitrifying flue gas for marine gas turbine | |
CN108970349A (en) | Boat diesel engine tail gas desulfurization denitrification integrated device and method | |
CN108704466A (en) | A kind of ammonia process ship tail gas denitration integrated device and method | |
CN112058086B (en) | A marine reciprocating desulfurization and denitrification tail gas treatment device | |
CN107875855A (en) | A comprehensive treatment method and device for marine diesel engine exhaust pollutants | |
CN205700083U (en) | A kind of boat diesel engine tail gas desulfurization denitration combined apparatus | |
CN206463755U (en) | A kind of gas pollutant integrated treatment unit | |
CN104121072B (en) | Waste gas pollutant combined removal device for two-stroke diesel engine | |
CN116291809B (en) | Control system and method for removing pollutants in tail gas by combining ammonia gas | |
JP5889229B2 (en) | Recirculation exhaust gas purification device and recirculation exhaust gas purification method | |
CN204412068U (en) | A kind of marine internal combustion engine tail gas desulfurization denitrification apparatus | |
Li et al. | Research Progress of Ship Exhaust Gas Treatment Technology | |
CN209115177U (en) | A kind of motor-vehicle tail-gas after-treatment system micro-bubble water washing device |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20161123 |