[go: up one dir, main page]

CN103821598A - Marine diesel engine exhaust selective catalytic reduction denitrification system - Google Patents

Marine diesel engine exhaust selective catalytic reduction denitrification system Download PDF

Info

Publication number
CN103821598A
CN103821598A CN201410109713.1A CN201410109713A CN103821598A CN 103821598 A CN103821598 A CN 103821598A CN 201410109713 A CN201410109713 A CN 201410109713A CN 103821598 A CN103821598 A CN 103821598A
Authority
CN
China
Prior art keywords
catalytic reduction
selective catalytic
diesel engine
cone
marine diesel
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.)
Pending
Application number
CN201410109713.1A
Other languages
Chinese (zh)
Inventor
张洪朋
刘后祥
张银东
孙玉清
陈海泉
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Dalian Maritime University
Original Assignee
Dalian Maritime University
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Dalian Maritime University filed Critical Dalian Maritime University
Priority to CN201410109713.1A priority Critical patent/CN103821598A/en
Publication of CN103821598A publication Critical patent/CN103821598A/en
Pending legal-status Critical Current

Links

Images

Landscapes

  • Exhaust Gas After Treatment (AREA)

Abstract

Marine diesel engine tail gas selective catalytic reduction deNOx systems, including arranging selective catalytic reduction in marine diesel engine exhaust-gas discharge pipe in and removing nitration catalyst ware, atomizer and helical blade blender, the atomizer includes atomizing nozzle, atomizing body and nozzle cap, establishes compressed air room, mixing hole and liquid hole in the atomizing nozzle, and the helical blade blender comprises the helical blade who fixes on the drum inside wall, and the helical blade does not reach drum central part, makes drum central part form through hole. The invention has the advantages that the ammonia water or the urea water is atomized and fully mixed with the tail gas, and meanwhile, the required oxygen is provided for the denitration reaction, and the denitration efficiency is improved.

Description

船舶柴油机尾气选择性催化还原脱硝系统Marine diesel engine exhaust selective catalytic reduction denitrification system

技术领域technical field

本发明属于船用柴油机技术领域,尤其涉及使用选择性催化还原脱硝系统处理船用柴油机尾气中的氮氧化物的装置。The invention belongs to the technical field of marine diesel engines, and in particular relates to a device for treating nitrogen oxides in exhaust gas of marine diesel engines by using a selective catalytic reduction denitrification system.

背景技术Background technique

船舶柴油机排放的尾气中含有大量的氮氧化物,现有船舶柴油机尾气是无脱硝处理的排放,因此,对环境造成一定污染。应该进行处理再排放。现有技术中,有研究提出对船舶柴油机尾气进行选择性催化还原(简称SCR)脱硝处理。但尚未见有实际应用。对船舶柴油机尾气进行选择性催化还原反应中需要氧气参与,但船舶柴油机尾气中的含氧量较低,直接进行选择性催化还原脱硝反应,由于氧气不足,会导致反应不够完全。The tail gas emitted by marine diesel engines contains a large amount of nitrogen oxides. Existing marine diesel engine tail gas is discharged without denitrification treatment, so it causes certain pollution to the environment. Should be treated before discharge. In the prior art, some studies have proposed to perform selective catalytic reduction (SCR for short) denitrification treatment on the tail gas of marine diesel engines. But no practical application has been seen yet. The selective catalytic reduction reaction of marine diesel engine exhaust requires oxygen to participate, but the oxygen content in marine diesel engine exhaust is low, and the selective catalytic reduction and denitrification reaction is directly carried out. Due to insufficient oxygen, the reaction will not be complete.

发明内容Contents of the invention

本发明的目的是提供船舶柴油机尾气选择性催化还原脱硝系统,使船舶柴油机尾气在进行脱硝反应前充分与雾化的氨水或尿素水混合,同时提高混合气体的含氧量。The purpose of the present invention is to provide a selective catalytic reduction denitrification system for marine diesel engine tail gas, so that the marine diesel engine tail gas can be fully mixed with atomized ammonia or urea water before the denitrification reaction, and at the same time, the oxygen content of the mixed gas can be increased.

本发明的技术方案是:船舶柴油机尾气选择性催化还原脱硝系统,包括置于船舶柴油机尾气排放管内的选择性催化还原脱硝催化器,其特征在于:所述船舶柴油机尾气选择性催化还原脱硝系统还包括在尾气排放管内置于选择性催化还原脱硝催化器和尾气入口之间的雾化器和螺旋叶片混合器,所述雾化器包括雾化喷嘴、雾化本体和喷头帽,所述雾化本体是具有内管和外管组成的双层管套,所述雾化喷嘴为圆锥体喷嘴,圆锥体内设与圆锥体底面连通的压缩空气室,圆锥体前部侧壁上设有混合孔,混合孔内端与压缩空气室连通,外端开口,圆锥体侧壁内设有液体孔,液体孔后端与圆锥体底面连通,前端与混合孔连通,雾化喷嘴底面和雾化本体前面通过喷头帽密封连接,其中,圆锥体压缩空气室与雾化本体内管前端连通,圆锥体侧壁内液体孔与雾化本体外管前端连通,雾化本体的内管和外管之间密封,雾化本体的内管后端与压缩空气源相连,雾化本体的外管后端与还原剂源连通;所述螺旋叶片混合器置于选择性催化还原脱硝催化器与雾化器之间,螺旋叶片混合器由固定在圆筒内侧壁上的螺旋叶片构成,螺旋叶片不到达圆筒中心部位,使圆筒中心部位形成直通孔。The technical solution of the present invention is: a marine diesel engine tail gas selective catalytic reduction denitrification system, including a selective catalytic reduction denitrification catalyst placed in the marine diesel engine tail gas exhaust pipe, characterized in that: the marine diesel engine tail gas selective catalytic reduction denitrification system is also It includes an atomizer and a spiral blade mixer built between the selective catalytic reduction denitrification catalyst and the exhaust gas inlet in the exhaust gas discharge pipe, the atomizer includes an atomization nozzle, an atomization body and a nozzle cap, and the atomization The main body is a double-layer sleeve composed of an inner tube and an outer tube. The atomizing nozzle is a cone nozzle, and a compressed air chamber connected to the bottom surface of the cone is provided inside the cone. A mixing hole is provided on the front side wall of the cone. The inner end of the mixing hole communicates with the compressed air chamber, the outer end is open, and there is a liquid hole in the side wall of the cone. The rear end of the liquid hole is connected with the bottom surface of the cone, and the front end is connected with the mixing hole. The nozzle cap is sealed and connected, wherein the compressed air chamber of the cone is connected to the front end of the inner tube of the atomizing body, the liquid hole in the side wall of the cone is connected to the front end of the outer tube of the atomizing body, and the inner tube and the outer tube of the atomizing body are sealed. The rear end of the inner tube of the atomization body is connected to the compressed air source, and the rear end of the outer tube of the atomization body is connected to the reducing agent source; the spiral blade mixer is placed between the selective catalytic reduction denitration catalyst and the atomizer, The helical blade mixer is composed of helical blades fixed on the inner wall of the cylinder. The helical blades do not reach the center of the cylinder, so that the center of the cylinder forms a through hole.

本发明所述船舶柴油机尾气选择性催化还原脱硝系统,其特征在于:所述雾化喷嘴的混合孔有4~10的偶数个,沿圆锥体前部对称分布,两个对称混合孔之间的夹角为120°,液体孔有4~10的偶数个,沿圆锥体对称分布,两个对称液体孔之间的夹角为30°。The marine diesel engine tail gas selective catalytic reduction denitrification system of the present invention is characterized in that: the mixing holes of the atomizing nozzle have an even number of 4 to 10, which are symmetrically distributed along the front part of the cone, and the mixing holes between the two symmetrical mixing holes The included angle is 120°, and the liquid holes have an even number of 4 to 10, which are symmetrically distributed along the cone, and the included angle between two symmetrical liquid holes is 30°.

本发明所述船舶柴油机尾气选择性催化还原脱硝系统,其特征在于:所述雾化喷嘴的混合孔的孔径为1~5mm,液体孔的孔径为0.6~2mm。The marine diesel engine tail gas selective catalytic reduction denitrification system of the present invention is characterized in that: the diameter of the mixing hole of the atomizing nozzle is 1-5mm, and the diameter of the liquid hole is 0.6-2mm.

本发明所述船舶柴油机尾气选择性催化还原脱硝系统,其特征在于:所述混合器的螺旋叶片的螺旋角为45度~60度之间。The marine diesel engine tail gas selective catalytic reduction denitrification system of the present invention is characterized in that: the helical angle of the helical blade of the mixer is between 45 degrees and 60 degrees.

本发明所述船舶柴油机尾气选择性催化还原脱硝系统,其特征在于:所述还原剂为氨水或尿素水。The marine diesel engine tail gas selective catalytic reduction denitrification system of the present invention is characterized in that: the reducing agent is ammonia water or urea water.

本发明的原理是:选择性催化还原脱硝系统中,氨水或尿素水与尾气混合的程度是脱硝效率的决定性因素,氨水或尿素水雾化程度越高,与尾气混合的程度就越高,脱硝效率会越高;同时,选择性催化还原脱硝反应中需要氧气参与。本发明的雾化器利用压缩空气将还原剂(氨水或尿素水)雾化,使还原剂与尾气进行了第一次混合,同时,压缩空气也增加了尾气中的氧含量,有效的提高了脱硝效率,螺旋叶片混合器对尾气和还原剂的混合气体进行第二次混合,使混合更加充分。The principle of the present invention is: in the selective catalytic reduction denitrification system, the mixing degree of ammonia water or urea water and tail gas is the decisive factor of denitrification efficiency. The higher the degree of atomization of ammonia water or urea water is, the higher the degree of mixing with tail gas is. The efficiency will be higher; at the same time, the selective catalytic reduction denitrification reaction requires oxygen to participate. The atomizer of the present invention uses compressed air to atomize the reducing agent (ammonia water or urea water), so that the reducing agent and the tail gas are mixed for the first time. At the same time, the compressed air also increases the oxygen content in the tail gas, effectively improving the Denitrification efficiency, the spiral blade mixer performs a second mixing of the mixed gas of the exhaust gas and the reducing agent to make the mixing more thorough.

本发明的有益效果是,使氨水或尿素水雾化,并与尾气充分混合,同时,为脱硝反应提供所需的氧气,提高脱硝效率。The beneficial effect of the invention is that the ammonia water or urea water is atomized and fully mixed with the tail gas, at the same time, the required oxygen is provided for the denitrification reaction, and the denitrification efficiency is improved.

附图说明Description of drawings

图1是船舶柴油机尾气选择性催化还原脱硝系统组成示意图;Figure 1 is a schematic diagram of the composition of the marine diesel engine tail gas selective catalytic reduction denitrification system;

图2是雾化器结构示意图;Figure 2 is a schematic diagram of the structure of the atomizer;

图3是螺旋叶片混合器结构示意图Figure 3 is a schematic diagram of the structure of the helical blade mixer

图4是螺旋叶片混合器俯视示意图Figure 4 is a schematic diagram of a top view of a helical blade mixer

图中,1-雾化器;2-螺旋叶片混合器;3-选择性催化还原脱硝催化器;4-雾化喷嘴;5-内管;;6-外管;7-喷头帽;8-密封垫圈;9-压缩空气室;10-混合孔;11-液体孔;12-液管;13压缩空气管。In the figure, 1-atomizer; 2-spiral blade mixer; 3-selective catalytic reduction denitration catalyst; 4-atomizing nozzle; 5-inner tube; 6-outer tube; 7-nozzle cap; 8- Sealing gasket; 9-compressed air chamber; 10-mixing hole; 11-liquid hole; 12-liquid pipe; 13 compressed air pipe.

具体实施方式Detailed ways

以下结合附图和实施例对本发明作进一步说明。The present invention will be further described below in conjunction with drawings and embodiments.

实施例是雾化喷头具有六个混合孔和六个液体孔的具体实施例。选择性催化还原脱硝催化器3置于尾气排放管内,尾气排放管内在选择性催化还原脱硝催化器3和尾气入口之间还设有雾化器1和螺旋叶片混合器2,雾化器1包括雾化喷嘴4、雾化本体和喷头帽7,雾化本体是具有内管5和外管6组成的双层管套,雾化喷嘴4为圆锥体喷嘴,圆锥体内设与圆锥体底面连通的压缩空气室9,圆锥体前部侧壁上设有六个混合孔10,混合孔10内端与压缩空气室9连通,外端开口,混合孔10沿圆锥体前部对称分布,两个对称混合孔10之间的夹角为120°,混合孔10的孔径为1~5mm,圆锥体侧壁内设有六个液体孔11,液体孔11后端与圆锥体底面连通,前端与混合孔10连通,液体孔11沿圆锥体对称分布,两个对称液体孔11之间的夹角为30°,液体孔11的孔径为0.6~2mm,雾化喷嘴4底面和雾化本体前面用喷头帽7通过螺纹密封连接,其中,圆锥体压缩空气室9与雾化本体内管5前端连通,圆锥体侧壁内液体孔11与雾化本体外管6前端连通,雾化本体的内管5和外管6之间密封,雾化本体的内管5后端通过压缩空气管13与压缩空气源相连,雾化本体的外管6后端通过液管12与还原剂源连通,还原剂为氨水或尿素水;螺旋叶片混合器2置于选择性催化还原脱硝催化器3与雾化器1之间,螺旋叶片混合器2由固定在圆筒内侧壁上的螺旋叶片构成,螺旋叶片不到达圆筒中心部位,使圆筒中心部位形成直通孔,螺旋叶片的螺旋角为45度~60度之间。An embodiment is a specific embodiment in which the atomizing nozzle has six mixing holes and six liquid holes. The selective catalytic reduction denitrification catalyst 3 is placed in the exhaust gas discharge pipe, and an atomizer 1 and a spiral blade mixer 2 are also arranged in the exhaust gas discharge pipe between the selective catalytic reduction denitrification catalytic converter 3 and the exhaust gas inlet. The atomizer 1 includes Atomizing nozzle 4, atomizing body and nozzle cap 7, the atomizing body is a double-layer pipe sleeve composed of inner tube 5 and outer tube 6, atomizing nozzle 4 is a cone nozzle, and the inside of the cone is connected to the bottom surface of the cone The compressed air chamber 9 is provided with six mixing holes 10 on the front side wall of the cone. The inner ends of the mixing holes 10 communicate with the compressed air chamber 9 and the outer ends are open. The included angle between the mixing holes 10 is 120°, the diameter of the mixing holes 10 is 1-5 mm, six liquid holes 11 are arranged in the side wall of the cone, the rear ends of the liquid holes 11 communicate with the bottom surface of the cone, and the front ends communicate with the mixing holes. 10 connected, the liquid holes 11 are distributed symmetrically along the cone, the angle between the two symmetrical liquid holes 11 is 30°, the diameter of the liquid holes 11 is 0.6-2mm, the bottom surface of the atomizing nozzle 4 and the front of the atomizing body are provided with nozzle caps 7 is connected by thread sealing, wherein the cone compressed air chamber 9 communicates with the front end of the inner tube 5 of the atomizing body, the liquid hole 11 in the side wall of the cone communicates with the front end of the outer tube 6 of the atomizing body, and the inner tube 5 of the atomizing body communicates with the front end of the atomizing body outer tube 6 The outer tubes 6 are sealed, the rear end of the inner tube 5 of the atomizing body is connected to the compressed air source through the compressed air tube 13, and the rear end of the outer tube 6 of the atomizing body is connected to the reducing agent source through the liquid tube 12, and the reducing agent is ammonia water or urea water; the helical blade mixer 2 is placed between the selective catalytic reduction denitrification catalyst 3 and the atomizer 1, and the helical blade mixer 2 is composed of a helical blade fixed on the inner wall of the cylinder, and the helical blade does not reach the circle The central part of the cylinder forms a through hole in the central part of the cylinder, and the helix angle of the helical blade is between 45 degrees and 60 degrees.

柴油机尾气进入排放管,经过雾化器1时与氨水或尿素水第一次混合,然后经过螺旋叶片混合器2,通过改变气体流向,达到充分混合的目的,之后经过选择性催化还原脱硝催化器3进行脱硝反应。Diesel engine exhaust gas enters the exhaust pipe and is first mixed with ammonia water or urea water when passing through the atomizer 1, then passes through the spiral blade mixer 2, and achieves the purpose of sufficient mixing by changing the gas flow direction, and then passes through the selective catalytic reduction denitrification catalyst 3 for denitrification reaction.

还原剂氨水或尿素水由液管12进入雾化器,压缩空气由压缩空气管13进入雾化器,最后到达雾化喷嘴4,在混合孔10中,来自压缩空气室9的压缩空气与来自液体孔11的氨水或尿素水混合雾化。由于两个对称混合孔10之间成120°角,使喷出的氨水或尿素水能与每个部位的尾气混合,两个对称液体管11之间成30°夹角,这样可以使氨水或尿素水顺利流入混合孔10。雾化喷嘴4通过螺旋与内管6固定,通过喷头帽7将雾化喷嘴4与外管6固定,并利用密封垫圈8密封。The reducing agent ammonia water or urea water enters the atomizer through the liquid pipe 12, and the compressed air enters the atomizer through the compressed air pipe 13, and finally reaches the atomizing nozzle 4. In the mixing hole 10, the compressed air from the compressed air chamber 9 and the compressed air from the The ammonia water or urea water in the liquid hole 11 is mixed and atomized. Because the angle of 120° is formed between the two symmetrical mixing holes 10, the sprayed ammonia or urea water can be mixed with the tail gas of each part, and the angle of 30° is formed between the two symmetrical liquid pipes 11, so that the ammonia or urea water can be mixed with each other. The urea water flows into the mixing hole 10 smoothly. The atomizing nozzle 4 is fixed to the inner tube 6 by a spiral, and the atomizing nozzle 4 and the outer tube 6 are fixed by a nozzle cap 7 and sealed by a sealing gasket 8 .

螺旋叶片固定在排放管内壁,中心为直通孔,便于气体流动,减小叶片对尾气的阻力。The helical blade is fixed on the inner wall of the exhaust pipe, and the center is a through hole, which facilitates the flow of gas and reduces the resistance of the blade to the exhaust gas.

Claims (5)

1.船舶柴油机尾气选择性催化还原脱硝系统,包括置于船舶柴油机尾气排放管内的选择性催化还原脱硝催化器(3),其特征在于:所述船舶柴油机尾气选择性催化还原脱硝系统还包括在尾气排放管内置于选择性催化还原脱硝催化器(3)和尾气入口之间的雾化器(1)和螺旋叶片混合器(2),所述雾化器(1)包括雾化喷嘴(4)、雾化本体和喷头帽(7),所述雾化本体是具有内管(5)和外管(6)组成的双层管套;所述雾化喷嘴(4)为圆锥体喷嘴,圆锥体内设与圆锥体底面连通的压缩空气室(9),圆锥体前部侧壁上设有混合孔(10),混合孔(10)内端与压缩空气室(9)连通,外端开口,圆锥体侧壁内设有液体孔(11),液体孔(11)后端与圆锥体底面连通,前端与混合孔(10)连通,雾化喷嘴(4)底面和雾化本体前面通过喷头帽(7)密封连接,其中,圆锥体压缩空气室(9)与雾化本体内管(5)前端连通,圆锥体侧壁内液体孔(11)与雾化本体外管(6)前端连通,雾化本体的内管(5)和外管(6)之间密封,雾化本体的内管(5)后端与压缩空气源相连,雾化本体的外管(6)后端与还原剂源连通;所述螺旋叶片混合器(2)置于选择性催化还原脱硝催化器(3)与雾化器(1)之间,螺旋叶片混合器(2)由固定在圆筒内侧壁上的螺旋叶片构成,螺旋叶片不到达圆筒中心部位,使圆筒中心部位形成直通孔。1. The selective catalytic reduction denitrification system for marine diesel engine exhaust, including a selective catalytic reduction denitrification catalyst (3) placed in the exhaust pipe of marine diesel engine, characterized in that: the selective catalytic reduction denitrification system for marine diesel engine exhaust is also included in the The exhaust pipe is built in the atomizer (1) and the spiral blade mixer (2) between the selective catalytic reduction denitrification catalyst (3) and the exhaust gas inlet, and the atomizer (1) includes the atomization nozzle (4 ), an atomizing body and a nozzle cap (7), the atomizing body is a double-layer sleeve composed of an inner tube (5) and an outer tube (6); the atomizing nozzle (4) is a cone nozzle, There is a compressed air chamber (9) connected to the bottom surface of the cone inside the cone, and a mixing hole (10) is provided on the front side wall of the cone. The inner end of the mixing hole (10) communicates with the compressed air chamber (9), and the outer end is open. , there is a liquid hole (11) in the side wall of the cone, the rear end of the liquid hole (11) communicates with the bottom surface of the cone, the front end communicates with the mixing hole (10), the bottom surface of the atomizing nozzle (4) and the front of the atomizing body pass through the nozzle The cap (7) is sealed and connected, wherein the conical compressed air chamber (9) communicates with the front end of the inner tube (5) of the atomizing body, and the liquid hole (11) in the side wall of the cone communicates with the front end of the outer tube (6) of the atomizing body , the inner tube (5) of the atomizing body and the outer tube (6) are sealed, the rear end of the inner tube (5) of the atomizing body is connected to the compressed air source, and the rear end of the outer tube (6) of the atomizing body is connected to the reduction The agent source is connected; the spiral blade mixer (2) is placed between the selective catalytic reduction denitrification catalyst (3) and the atomizer (1), and the spiral blade mixer (2) is fixed on the inner wall of the cylinder The helical blade is composed of the helical blade, and the helical blade does not reach the center of the cylinder, so that the center of the cylinder forms a through hole. 2.根据权利要求1所述船舶柴油机尾气选择性催化还原脱硝系统,其特征在于:所述雾化喷嘴的混合孔(10)有4~10的偶数个,沿圆锥体前部对称分布,两个对称混合孔(10)之间的夹角为120°,液体孔(11)有4~10的偶数个,沿圆锥体对称分布,两个对称液体孔(11)之间的夹角为30°。2. The marine diesel engine tail gas selective catalytic reduction denitrification system according to claim 1, characterized in that: the mixing holes (10) of the atomizing nozzle have an even number of 4 to 10, symmetrically distributed along the front of the cone, two The included angle between the symmetrical mixing holes (10) is 120°, the liquid holes (11) have an even number of 4 to 10, and are symmetrically distributed along the cone, and the included angle between the two symmetrical liquid holes (11) is 30° °. 3.根据权利要求3所述船舶柴油机尾气选择性催化还原脱硝系统,其特征在于:所述雾化喷嘴的混合孔(10)的孔径为1~5mm,液体孔(11)的孔径为0.6~2mm。3. The marine diesel engine tail gas selective catalytic reduction denitrification system according to claim 3, characterized in that: the diameter of the mixing hole (10) of the atomizing nozzle is 1-5mm, and the diameter of the liquid hole (11) is 0.6- 2mm. 4.根据权利要求1所述船舶柴油机尾气选择性催化还原脱硝系统,其特征在于:所述螺旋叶片混合器(2)的螺旋叶片的螺旋角为45度~60度之间。4. The marine diesel engine tail gas selective catalytic reduction denitrification system according to claim 1, characterized in that: the helical angle of the helical blade of the helical blade mixer (2) is between 45 degrees and 60 degrees. 5.根据权利要求1所述船舶柴油机尾气选择性催化还原脱硝系统,其特征在于:所述还原剂为氨水或尿素水。5. The marine diesel engine tail gas selective catalytic reduction denitrification system according to claim 1, characterized in that: the reducing agent is ammonia water or urea water.
CN201410109713.1A 2014-03-21 2014-03-21 Marine diesel engine exhaust selective catalytic reduction denitrification system Pending CN103821598A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201410109713.1A CN103821598A (en) 2014-03-21 2014-03-21 Marine diesel engine exhaust selective catalytic reduction denitrification system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201410109713.1A CN103821598A (en) 2014-03-21 2014-03-21 Marine diesel engine exhaust selective catalytic reduction denitrification system

Publications (1)

Publication Number Publication Date
CN103821598A true CN103821598A (en) 2014-05-28

Family

ID=50756855

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201410109713.1A Pending CN103821598A (en) 2014-03-21 2014-03-21 Marine diesel engine exhaust selective catalytic reduction denitrification system

Country Status (1)

Country Link
CN (1) CN103821598A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101498181B1 (en) * 2014-11-25 2015-03-04 세종공업 주식회사 Urea mixing apparatus having double injection nozzle
CN104594990A (en) * 2015-02-27 2015-05-06 天纳克(苏州)排放系统有限公司 Hybrid tube and exhaust gas treatment device
CN105386830A (en) * 2014-08-21 2016-03-09 通用汽车环球科技运作有限责任公司 Mixer for short mixing lengths
CN105464764A (en) * 2015-12-11 2016-04-06 潍柴动力股份有限公司 Mixer used for exhaust facility and SCR system
CN106837492A (en) * 2015-12-03 2017-06-13 通用汽车环球科技运作有限责任公司 For the exhaust mixer of close-coupled system
CN106824588A (en) * 2017-03-20 2017-06-13 厦门大学嘉庚学院 A kind of cyclone type spiral water-cooling atomizer and its method of work
CN107649303A (en) * 2017-10-27 2018-02-02 山东佩森环保科技股份有限公司 A kind of high efficiency nozzle of ship desulphurization system

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN87103318A (en) * 1986-05-07 1987-12-02 株式会社日立制作所 Atomizer and the coal-water slurry fired boiler of use atomizer
WO1999005401A1 (en) * 1997-07-24 1999-02-04 Siemens Aktiengesellschaft Exhaust cleaning arrangement for a diesel motor
JP2008180202A (en) * 2007-01-26 2008-08-07 Nissan Diesel Motor Co Ltd Exhaust emission control device
CN101378838A (en) * 2006-02-08 2009-03-04 Stt伊姆特克公司 Injection device
WO2011034270A1 (en) * 2009-09-18 2011-03-24 광성(주) Scr system for a ship or an overland plant
CN201972767U (en) * 2010-11-26 2011-09-14 杭州银轮科技有限公司 Mixer for diesel engine urea-SCR system
CN103230848A (en) * 2013-05-17 2013-08-07 南京凯盛国际工程有限公司 Two-fluid X-shaped nozzle
CN203822427U (en) * 2014-03-21 2014-09-10 大连海事大学 Marine diesel engine exhaust selective catalytic reduction denitrification system

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN87103318A (en) * 1986-05-07 1987-12-02 株式会社日立制作所 Atomizer and the coal-water slurry fired boiler of use atomizer
WO1999005401A1 (en) * 1997-07-24 1999-02-04 Siemens Aktiengesellschaft Exhaust cleaning arrangement for a diesel motor
CN101378838A (en) * 2006-02-08 2009-03-04 Stt伊姆特克公司 Injection device
JP2008180202A (en) * 2007-01-26 2008-08-07 Nissan Diesel Motor Co Ltd Exhaust emission control device
WO2011034270A1 (en) * 2009-09-18 2011-03-24 광성(주) Scr system for a ship or an overland plant
CN201972767U (en) * 2010-11-26 2011-09-14 杭州银轮科技有限公司 Mixer for diesel engine urea-SCR system
CN103230848A (en) * 2013-05-17 2013-08-07 南京凯盛国际工程有限公司 Two-fluid X-shaped nozzle
CN203822427U (en) * 2014-03-21 2014-09-10 大连海事大学 Marine diesel engine exhaust selective catalytic reduction denitrification system

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105386830A (en) * 2014-08-21 2016-03-09 通用汽车环球科技运作有限责任公司 Mixer for short mixing lengths
CN105386830B (en) * 2014-08-21 2018-02-09 通用汽车环球科技运作有限责任公司 Blender for short mixing length
KR101498181B1 (en) * 2014-11-25 2015-03-04 세종공업 주식회사 Urea mixing apparatus having double injection nozzle
CN104594990A (en) * 2015-02-27 2015-05-06 天纳克(苏州)排放系统有限公司 Hybrid tube and exhaust gas treatment device
CN106837492A (en) * 2015-12-03 2017-06-13 通用汽车环球科技运作有限责任公司 For the exhaust mixer of close-coupled system
CN106837492B (en) * 2015-12-03 2019-07-12 通用汽车环球科技运作有限责任公司 Exhaust mixer for close-coupled system
CN105464764A (en) * 2015-12-11 2016-04-06 潍柴动力股份有限公司 Mixer used for exhaust facility and SCR system
CN105464764B (en) * 2015-12-11 2018-04-03 潍柴动力股份有限公司 Blender and SCR system for exhaust facility
CN106824588A (en) * 2017-03-20 2017-06-13 厦门大学嘉庚学院 A kind of cyclone type spiral water-cooling atomizer and its method of work
CN106824588B (en) * 2017-03-20 2022-11-15 厦门大学嘉庚学院 Cyclone spiral water-cooling atomizer and working method thereof
CN107649303A (en) * 2017-10-27 2018-02-02 山东佩森环保科技股份有限公司 A kind of high efficiency nozzle of ship desulphurization system

Similar Documents

Publication Publication Date Title
CN103821598A (en) Marine diesel engine exhaust selective catalytic reduction denitrification system
CN104136727B (en) Waste gas purification apparatus
CN206483347U (en) A kind of empty blender of SCR denitration system spiral-flow type ammonia
CN105289301A (en) Double-rotation SCR denitration method and apparatus thereof
CN203822427U (en) Marine diesel engine exhaust selective catalytic reduction denitrification system
CN207686807U (en) Vent gas treatment urea mixing device
CN204961035U (en) SCR system and blender thereof
CN201871432U (en) Atomizing spray nozzle structure used for spraying liquid reducing agents in SCR (selective catalytic reduction) system
CN105065093B (en) A kind of SCR system and its blender
CN102631849B (en) Pre-heating spray-hole type static mixer
CN207686808U (en) Side post-processes urea mixing device into nozzle integrated form SCR
CN103883379B (en) Ship machine SCR system
CN207093187U (en) SCR urea injection pipe
CN107939488A (en) Vehicle tail gas processing urea mixing device
CN204877612U (en) SCR system and catalytic reaction unit thereof
CN201760232U (en) A spray gun type double-flow nozzle for flue gas denitrification
CN207686806U (en) Vehicle tail gas processing urea mixing device
CN108150255A (en) Vehicle tail gas processing treatment fluid mixing arrangement
CN207905902U (en) Vehicle tail gas processing treatment fluid mixing arrangement
CN207478320U (en) A controllable boiler tail gas denitrification device
CN116255229B (en) Commercial car high-power diesel engine tail gas treatment device
CN216157747U (en) Exhaust purification device of marine diesel engine
CN111810278A (en) A radial jet tight coupling type mixing device for mixing reducing agent fluid
CN205714363U (en) Automotive exhaust catalysis processor
CN210993663U (en) A desulphurization unit for exhaust-gas treatment

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication

Application publication date: 20140528

RJ01 Rejection of invention patent application after publication