KR20120010352A - Exhaust gas purifying device utilize electrolysis hydrogen for SCR reduction - Google Patents

Exhaust gas purifying device utilize electrolysis hydrogen for SCR reduction Download PDF

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KR20120010352A
KR20120010352A KR1020100071818A KR20100071818A KR20120010352A KR 20120010352 A KR20120010352 A KR 20120010352A KR 1020100071818 A KR1020100071818 A KR 1020100071818A KR 20100071818 A KR20100071818 A KR 20100071818A KR 20120010352 A KR20120010352 A KR 20120010352A
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hydrogen
exhaust gas
oxygen
storage battery
tank
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Korean (ko)
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조연근
박광수
전효준
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에스케이이노베이션 주식회사
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/92Chemical or biological purification of waste gases of engine exhaust gases
    • B01D53/94Chemical or biological purification of waste gases of engine exhaust gases by catalytic processes
    • B01D53/9404Removing only nitrogen compounds
    • B01D53/9409Nitrogen oxides
    • B01D53/9431Processes characterised by a specific device
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/92Chemical or biological purification of waste gases of engine exhaust gases
    • B01D53/94Chemical or biological purification of waste gases of engine exhaust gases by catalytic processes
    • B01D53/9404Removing only nitrogen compounds
    • B01D53/9409Nitrogen oxides
    • B01D53/9413Processes characterised by a specific catalyst
    • B01D53/9418Processes characterised by a specific catalyst for removing nitrogen oxides by selective catalytic reduction [SCR] using a reducing agent in a lean exhaust gas
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B1/00Electrolytic production of inorganic compounds or non-metals
    • C25B1/01Products
    • C25B1/02Hydrogen or oxygen
    • C25B1/04Hydrogen or oxygen by electrolysis of water
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N3/00Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
    • F01N3/02Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust
    • F01N3/021Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters
    • F01N3/033Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters in combination with other devices
    • F01N3/035Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters in combination with other devices with catalytic reactors, e.g. catalysed diesel particulate filters
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N3/00Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
    • F01N3/08Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
    • F01N3/10Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust
    • F01N3/18Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by methods of operation; Control
    • F01N3/20Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by methods of operation; Control specially adapted for catalytic conversion ; Methods of operation or control of catalytic converters
    • F01N3/2066Selective catalytic reduction [SCR]
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/36Hydrogen production from non-carbon containing sources, e.g. by water electrolysis

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Combustion & Propulsion (AREA)
  • Health & Medical Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • Biomedical Technology (AREA)
  • General Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Toxicology (AREA)
  • Electrochemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Exhaust Gas After Treatment (AREA)

Abstract

PURPOSE: An exhaust purifying apparatus using electrolyzed hydrogen as the reducing agent of a selective catalyst reduction reaction is provided to charge power in a storage battery and use the stored electric energy from the storage battery by including a thermoelectric element. CONSTITUTION: An exhaust purifying apparatus includes a nitrogen oxide reducing catalyst part(1) and a particle eliminating filter part(2). The nitrogen oxide reducing catalyst part and the particle eliminating filter part are successively arranged from the upstream of exhaust gas flow. The nitrogen oxide reducing catalyst part and the particle eliminating filter part are inserted into the exhaust pipe of a diesel engine(3). The apparatus includes a first storage battery(7) and an electrolyzing unit(4). The first storage battery charges or supplies power generated from the drive of the diesel engine. The electrolyzing unit is in connection with the first storage battery and is driven based on the power of the first storage battery. The electrolyzing unit generates hydrogen and oxygen based on the electrolysis of water. The hydrogen is supplied to the front part of the nitrogen oxide reducing catalyst part to be used as a reducing agent.

Description

전기분해 수소를 선택적 촉매 환원반응의 환원제로 활용하는 배기가스 정화장치{Exhaust gas purifying device utilize electrolysis hydrogen for SCR reduction} Exhaust gas purifying device utilizes electrolysis hydrogen for SCR reduction

본 발명은 전기분해반응에 의해 발생된 수소를 선택적 촉매 환원반응(Selective catalytic reduction;SCR) 환원제로서 활용하는 배기가스 정화장치에 관한 것으로, 더욱 상세하게는 질소산화물저감촉매(LNC) 및 입자제거필터(DPF; Diesel particulate filter)를 포함하는 배기가스정화장치에 있어서, 축전지(battery)의 잉여전력을 활용하거나 배기온도에 따른 열전소자를 열원으로 이용하여 물을 전기분해하여 수소를 얻고, 이를 배기가스 정화장치의 환원제로 활용하는 장치에 관한 것이다.The present invention relates to an exhaust gas purification apparatus utilizing hydrogen generated by an electrolysis reaction as a selective catalytic reduction (SCR) reducing agent, and more particularly, a nitrogen oxide reduction catalyst (LNC) and a particle removal filter. In an exhaust gas purifying apparatus including a diesel particulate filter (DPF), hydrogen is obtained by electrolyzing water by using surplus power of a battery or by using a thermoelectric element according to the exhaust temperature as a heat source, and exhaust gas thereof. It relates to a device utilized as a reducing agent of the purification device.

디젤엔진은 연비 효율이 좋고, 우수한 신뢰성을 바탕으로 자동차, 선박뿐만 아니라 산업 전반에서 다양하게 사용되고 있으며, 고출력 및 고부하 운전이 가능하여 수요가 계속 증가하고 있다. 이와 같은 저연비의 디젤엔진 차량의 증가가 예상되고 있는 반면, 디젤엔진은 배출되는 질소산화물(NOx)과 입자상 물질(PM;Particulate matter)이 필연적으로 배출되는 문제점을 가지고 있다. 이에 대하여 디젤엔진에서 배출되는 질소산화물과 입자상 물질을 저감시키기 위하여 고압 연료 분사 시스템, 신연소 개념 및 배기가스 재순환(EGR) 등과 같은 다양한 엔진관련 기술들이 개발되어 적용되어 왔으나, 배기 규제가 강화됨에 따라 이러한 기술만으로 규제를 만족하기에는 한계가 있어 배기 후처리 기술의 적용이 불가피해졌다.Diesel engines are used in various industries as well as automobiles and ships based on good fuel efficiency and excellent reliability, and the demand is continuously increasing due to high power and high load operation. While an increase in such low fuel consumption diesel engine vehicles is expected, diesel engines have a problem of inevitably emitting NOx and particulate matter (PM). Various engine related technologies such as high pressure fuel injection system, new combustion concept, and exhaust gas recirculation (EGR) have been developed and applied to reduce nitrogen oxides and particulate matters emitted from diesel engines. The application of exhaust aftertreatment technology is inevitable due to limitations in satisfying regulations with these technologies alone.

따라서 산화촉매나 DPF(Diesel particulate filter)의 개발과 각종 질소산화물 저감용 촉매 개발이나 배기후처리 장치에 대한 연구가 진행되고 있다. Therefore, research on the development of oxidation catalysts or diesel particulate filters (DPF), catalysts for reducing nitrogen oxides, and exhaust post-treatment devices has been conducted.

질소산화물 저감 방법(SCR)은 촉매를 모듈화하여 배출가스가 흐르는 중간에 설치하고, 환원제를 분사하여 촉매층에서 환원반응을 통하여 유해한 질소산화물을 무해한 질소와 수증기로 분해하여 배출 질소산화물을 저감시키는 방법으로 공정 및 반응조건에 따라 NO가 분해되는 반응은 다양하나 주반응은 하기 식과 같은 반응을 통해 분해된다.
Nitrogen oxide reduction method (SCR) is a method of modularizing the catalyst and installing it in the middle of the flow of exhaust gas, and spraying a reducing agent to decompose harmful nitrogen oxide into harmless nitrogen and water vapor through reduction reaction in the catalyst layer to reduce the emission nitrogen oxide. The reaction in which NO is decomposed varies depending on the process and reaction conditions, but the main reaction is decomposed through a reaction such as the following formula.

6NO + 4NH3 → 5N2 + 6H2O 6NO + 4NH 3 → 5N 2 + 6H 2 O

4NO + 4NH3 + O2 → 4N2 + 6H2O4NO + 4NH 3 + O 2 → 4N 2 + 6H 2 O

2NO + 2H2 → N2 + 2H2O2NO + 2H 2 → N 2 + 2H 2 O

2NO + 2CO → N2 + 2CO2
2NO + 2CO → N 2 + 2CO 2

이때 상기 선택적 촉매 환원 반응에 사용되는 환원제로는 암모니아, 우레아, 탄화수소를 사용할 수 있으나, 상기 암모니아(NH3) 및 우레아 등은 별도로 공급이 가능한 인프라가 필요한 단점이 있어 탄화수소가 선호되고 있으며, 그 유형으로는 경유, 등유, 프로필렌, 프로판, 에틸렌, 부틸렌, 메탄 등이 있다. 하지만, 탄화수소의 경우 디젤연료를 사용함에 따라 연비의 악화를 초래하는 문제점이 있다. In this case, as the reducing agent used in the selective catalytic reduction reaction, ammonia, urea, or hydrocarbons may be used, but ammonia (NH 3 ) and urea, etc., have a disadvantage in that an infrastructure that can be supplied separately is preferred, and hydrocarbons are preferred. Examples include light oil, kerosene, propylene, propane, ethylene, butylene, and methane. However, in the case of hydrocarbons, there is a problem that causes deterioration of fuel economy by using diesel fuel.

또한, 입자상 물질의 저감 방법으로 디젤 입자 필터(DPF) 방식이 널리 사용되고 있으며, 필터에 포집된 PM을 연속적으로 재생하는 방법에 따라 연속재생식, 강제재생식으로 나눌 수 있다. 연속재생식 방법은 DPF 전단에 설치된 산화촉매에 의해 NO를 NO2로 전환하여 PM을 재생하는 방식으로 강제적으로 필터의 온도를 높일 수 있는 보조기구를 사용하는 강제재생식보다 실제 자동차 배기가스 온도인 250~600℃에서 질소산화물 저감 성능 및 입자상 물질의 제거효율이 보다 향상시킬 수 있다.In addition, a diesel particulate filter (DPF) method is widely used as a method of reducing particulate matter, and may be classified into a continuous regeneration type or a forced regeneration type according to a method of continuously regenerating PM collected in the filter. The continuous regeneration method converts NO into NO 2 by the oxidation catalyst installed in the front of the DPF, and regenerates PM. Nitrogen oxide reduction performance and the removal efficiency of particulate matter at 250 ~ 600 ℃ can be improved more.

따라서, 본 발명은 상기 종래 기술의 문제점을 해결하기 위한 것으로서 디젤엔진의 구동으로 전력을 충전 또는 공급할 수 있는 축전지의 잉여전력으로 구동되는 전기분해장치를 구비하여, 상기 전기분해장치에서 수소 및 산소를 발생시키며, 상기 발생된 수소를 질소 저감 촉매 환원반응의 환원제로 활용함으로써 별도의 부가 장비가 필요없이 환원제를 균일 및 안정적으로 자체 공급할 수 있을 뿐만 아니라, 다른 환원제에 비해 질소 저감 효율을 높이는 것에 그 목적이 있다.Accordingly, the present invention is to solve the problems of the prior art and has an electrolysis device which is driven by the surplus power of the battery which can be charged or supplied by the driving of the diesel engine, the hydrogen and oxygen in the electrolysis device By using the generated hydrogen as a reducing agent of the nitrogen reduction catalytic reduction reaction, it is possible to supply the reducing agent uniformly and stably without additional equipment, and to increase the nitrogen reduction efficiency in comparison with other reducing agents. There is this.

또한, 본 발명은 배기관을 통과하는 배기가스의 폐열을 발전용 열전소자를 사용하여 축전지의 충전 및 기타 전원으로 활용할 수 있다.  In addition, the present invention can utilize the waste heat of the exhaust gas passing through the exhaust pipe as a charging of the battery and other power source using the thermoelectric element for power generation.

또한 본 발명에 의해 발생된 수소는 연료전지의 원료로 이용이 가능하며, 산소는 디젤엔진에 흡입되어 엔진 효율을 높일 수 있도록 할 수 있다.In addition, hydrogen generated by the present invention can be used as a raw material of the fuel cell, oxygen can be sucked into the diesel engine to increase the engine efficiency.

본 발명은 상기와 같은 과제를 해결하기 위하여, 디젤 엔진의 배기관에 삽입되는 질소산화물 저감 촉매부와 입자 제거 필터부를 배기가스의 흐름에 대해 상류로부터 순차적으로 구비하는 배기가스 정화장치에 있어서, 전기분해장치를 구비하여 상기 전기분해장치에서 물을 전기분해반응하여 수소 및 산소를 발생시키며, 발생된 수소를 질소산화물 저감 촉매부의 전단에 공급하는 배기가스 정화장치를 제공한다.
SUMMARY OF THE INVENTION In order to solve the above problems, the present invention provides an electrolytic gas purification apparatus including a nitrogen oxide reduction catalyst portion and a particle removal filter portion inserted into an exhaust pipe of a diesel engine sequentially from upstream with respect to the flow of exhaust gas. The present invention provides an exhaust gas purifying apparatus including an apparatus to generate hydrogen and oxygen by electrolyzing water in the electrolytic apparatus, and supplying the generated hydrogen to the front end of the nitrogen oxide reducing catalyst unit.

이하 본 발명을 보다 상세히 설명한다.Hereinafter, the present invention will be described in more detail.

본 발명에 따른 디젤 엔진의 배기가스 정화장치는 배기가스 흐름에 순차적으로 질소산화물 저감 촉매부와 입자 제거 필터부(이하 'DPF'라 함)를 구비한다. 상기 질소산화물 저감 촉매부는 디젤을 분사하여 질소산화물을 저감시키는 선택적 환원 촉매반응(이하 'SCR'라 함)인 것으로, 산소에 의한 반응속도가 빠르고, 이차 오염물질이 발생하지 않는 장점이 있다. 상기 저감된 질소산화물은 질소 저감 촉매에 의해서만 제거되는 것이 아니라 250~350℃의 중온 대역에서 DPF 촉매에 의해 추가적으로 제거되므로 질소산화물을 보다 효과적으로 제거할 수 있으며, 입자 제거 필터부에서는 축적된 입자상 물질이 제거하고, 동시에 일산화탄소 및 탄화수소가 제거된다.The exhaust gas purification apparatus of the diesel engine according to the present invention includes a nitrogen oxide reduction catalyst portion and a particle removal filter portion (hereinafter referred to as 'DPF') sequentially in the exhaust gas flow. The nitrogen oxide reduction catalyst unit is a selective reduction catalytic reaction (hereinafter referred to as 'SCR') to reduce nitrogen oxides by injecting diesel, and has an advantage in that the reaction rate by oxygen is fast and secondary pollutants are not generated. The reduced nitrogen oxides are not only removed by the nitrogen reduction catalyst but additionally removed by the DPF catalyst in the mid-temperature zone of 250 to 350 ° C., thereby effectively removing the nitrogen oxides. Removal and at the same time carbon monoxide and hydrocarbons are removed.

상기 SCR에 있어서, 본 발명은 전기분해장치를 구비하여 질소산화물 저감 촉매부의 환원제로 수소를 사용할 수 있게 된다. 이는 암모니아와 같은 환원제를 사용함에 따른 별도의 부가 장비가 필요없이 선택적 촉매 반응의 환원제를 균일 및 안정적으로 자체 공급할 수 있을 뿐만 아니라, 다른 환원제에 비해 질소 저감 효과가 뛰어나다. In the SCR, the present invention is equipped with an electrolysis device, it is possible to use hydrogen as a reducing agent of the nitrogen oxide reduction catalyst portion. It is possible to supply the reducing agent of the selective catalytic reaction uniformly and stably without the need for additional equipment by using a reducing agent such as ammonia, and has an excellent effect of reducing nitrogen compared to other reducing agents.

상기 전기분해장치는 물을 저장하는 물탱크와 상기 물탱크에 설치되어 전기분해반응을 통해 물에서 수소 및 산소로 분리시키는 전극봉을 포함한다. 상기 전극봉은 양극, 음극으로 각각 설치되어 전원이 인가되면 물을 전기분해하게 된다. 이때 양극에는 산소가스가, 음극에는 수소가스가 발생한다.The electrolysis device includes a water tank for storing water and an electrode rod installed in the water tank to separate hydrogen and oxygen from water through an electrolysis reaction. The electrodes are respectively installed as a positive electrode and a negative electrode to electrolyze water when power is applied. At this time, oxygen gas is generated at the anode and hydrogen gas is generated at the cathode.

이때, 발생된 수소와 산소는 각각 수소탱크와 산소탱크에 저장된다. 상기 수소탱크에 저장된 수소는 라인을 통하여 SCR의 환원제로 사용되기 위하여 질소 저감촉매부의 전단에 공급된다. 이렇게 함으로써 환원제의 별도 공급장치가 필요없이 시스템 안에서 자체적으로 수소를 안정적으로 균일하게 공급할 수 있게 되는 것이다. 또한, 상기 산소탱크에 저장된 산소는 디젤엔진의 전단부의 산소를 흡입할 수 있는 흡입밸브에서 흡입됨으로써 엔진효율을 높일 수 있게 된다. At this time, the generated hydrogen and oxygen are stored in the hydrogen tank and oxygen tank, respectively. Hydrogen stored in the hydrogen tank is supplied to the front end of the nitrogen reducing catalyst portion to be used as a reducing agent of the SCR through the line. By doing so, it is possible to stably and uniformly supply hydrogen in the system without the need for a separate supply of reducing agent. In addition, the oxygen stored in the oxygen tank is sucked in the intake valve that can suck the oxygen in the front end portion of the diesel engine can increase the engine efficiency.

상기 전기분해장치는 디젤엔진의 구동으로부터 생성되는 전력을 충전 또는 공급할 수 있는 제1축전지에서 전원을 공급받는다. 이때 제1축전지에서 공급받는 전원은 여분의 전력을 사용하기 때문에 별도의 전력공급 장치를 추가적으로 구비할 필요가 없다.The electrolysis device receives power from a first storage battery capable of charging or supplying power generated from driving of a diesel engine. At this time, since the power supplied from the first storage battery uses extra power, there is no need to additionally provide a separate power supply device.

본 발명은 상기 전기분해장치에 전원을 공급하는 방식에 있어서, 배기관에 배기가스의 온도를 감지하는 온도센서로 제1온도센서 및 제2온도센서를 구비하여, 상기 온도센서들과 연결된 열전소자가 제1온도센서와 제2온도센서의 온도차로 인해 전력을 발전할 수 있도록 한다. 이렇게 발전된 전력을 추가 구비된 제2축전지에 충전하고, 이렇게 충전된 전력을 공급받을 수 있도록 한다. 이렇게 함으로써 폐열을 회수하여 전력을 발생시키고 이를 전기분해장치의 전원으로 이용하는 에너지 순환 구조를 갖게 됨으로써 경제적인 시스템을 구축할 수 있게 된다. The present invention provides a power supply to the electrolysis device, comprising a first temperature sensor and a second temperature sensor as a temperature sensor for sensing the temperature of the exhaust gas in the exhaust pipe, the thermoelectric element connected to the temperature sensors It is possible to generate power due to the temperature difference between the first temperature sensor and the second temperature sensor. The generated power is charged into the additional storage battery, and thus the charged power can be supplied. By doing so, it is possible to construct an economic system by recovering waste heat to generate electric power and having an energy circulation structure using the same as a power source of an electrolysis device.

상기 열전소자는 폐열 회수 발전을 위한 것으로 열전소자의 제베크(SEEBECK)효과를 통해 발전을 이루는 장치이다. 재베크 효과는 두 종류의 금속을 고리 모양으로 연결하여 한쪽 접점을 고온, 다른 쪽을 저온으로 했을 때 그 회로에 전류가 생기는 현상을 말하는 것으로 본 발명에서는 이러한 것을 이용하여 어떠한 부가적인 기계적 구동 부분 없이 단지 양단간의 온도차를 이용하여 기전력을 발생시킬 수 있는 것이다. 또한, 상기 열전소자는 시스템에 열이 잔존하는 한 지속적으로 발전을 일으킬 수 있고 일정한 온도가 아니더라도 기전력이 발생할 수 있어 디젤 엔진의 배기가스의 온도차를 이용하여 에너지를 재활용할 수 있는 장점이 있다.The thermoelectric device is for waste heat recovery power generation and is a device for generating power through the SEEBECK effect of the thermoelectric device. The rebecking effect refers to a phenomenon in which a current is generated in a circuit when two kinds of metals are connected in a ring shape and one contact is made high temperature and the other is made low temperature. Only the temperature difference between the two ends can generate electromotive force. In addition, the thermoelectric element may generate power continuously as long as heat remains in the system, and electromotive force may be generated even if the temperature is not constant, so that energy may be recycled by using a temperature difference of exhaust gas of a diesel engine.

전기분해장치는 제1축전지의 여분의 전력 또는 배기가스의 폐열을 발전용 열전소자를 이용하여 충전된 제2축전지의 전력을 전원으로 공급받음으로써 물을 전기분해하여 수소 및 산소를 발생시킨다. 상기 발생된 수소 및 산소는 각각 수소탱크 및 산소탱크에 저장되며, 수소는 선택적 촉매 환원반응(SCR)의 환원제로 사용하기 위해 질소 저감 촉매부의 전단에 수소탱크에서 일정하게 공급된다. 또한, 산소는 디젤엔진의 전단에 구비된 흡입밸브에서 흡입되도록 유도함으로써 엔진효율을 향상시키는 데 사용할 수 있다.The electrolysis device generates hydrogen and oxygen by electrolyzing water by receiving the extra power of the first storage battery or the waste heat of the exhaust gas from the second storage battery charged with the thermoelectric element for power generation as a power source. The generated hydrogen and oxygen are stored in a hydrogen tank and an oxygen tank, respectively, and hydrogen is constantly supplied from the hydrogen tank at the front end of the nitrogen reduction catalyst part for use as a reducing agent of the selective catalytic reduction reaction (SCR). In addition, the oxygen can be used to improve the engine efficiency by inducing the suction in the intake valve provided in the front end of the diesel engine.

또한, 본 발명은 자체생산한 수소를 SCR의 환원제로 사용할 뿐만 아니라, 연료전지를 더 구비하여 남는 수소가 있을 경우 수소를 공급하여 연료전지에서 전력을 발생시킬 수 있다. 이러한 전력은 상기 축전지들에 다시 충전되거나 다른 양태로 전기동력장치에 공급함으로써 다른 에너지로 구동될 수 있다. 이는 본 발명에 따른 전기분해장치를 구비한 배기가스 정화장치가 하이브리드 구동엔진을 구비할 수 있게 해줌으로써 보다 복합적인 효과를 나타낼 수 있다. 상기 복합적인 효과라는 것은 엔진의 구동 환경에 따라 저효율, 고출력이 필요한 상황에서는 디젤엔진을 구동하고, 저소음, 저출력이 필요한 상황에서는 연료전지를 이용한 전기구동엔진을 구동시킬 수 있는 것을 말한다.In addition, the present invention not only uses hydrogen produced by itself as a reducing agent of the SCR, but also includes a fuel cell to supply hydrogen when there is remaining hydrogen, thereby generating power in the fuel cell. This power can be driven with other energy by recharging the batteries or by supplying the electric power device in another embodiment. This can exhibit a more complex effect by allowing the exhaust gas purification apparatus having the electrolysis device according to the present invention to have a hybrid driving engine. The complex effect means that the diesel engine can be driven in a situation where low efficiency and high power are required according to the driving environment of the engine, and the electric drive engine using a fuel cell can be driven in a situation where low noise and low power are required.

상기와 같이 전기분해장치에서 생성된 수소는 SCR의 환원제로 사용하여 질소저감 효율을 향상시킬 수 있을 뿐만 아니라, 자체 공급하는 시스템을 갖춤으로써 경제적이며 안정적으로 질소산화물을 저감시킬 수 있다. 이는 탄화수소를 환원제로 사용 시 질소산화물 저감 성능을 위해 450℃의 높은 온도가 요구되는 것에 비해, 수소를 환원제로 사용하게 되면 상기와 같은 높은 온도가 요구되지 않아 150℃에서 질소산화물의 저감이 나타나게 됨으로써 실제 차량의 운행조건에 적합하며 보다 효과적이다. 특히, 종래 탄화수소를 환원제로 사용하는 장치에 수소를 추가로 환원제로 사용할 경우 질소산화물 저감시키는 온도 범위가 넓어짐에 따라 저감율도 크게 향상될 수 있다.As described above, the hydrogen generated in the electrolysis device can be used as a reducing agent of the SCR to not only improve the efficiency of nitrogen reduction, but also reduce the nitrogen oxide economically and stably by having a system to supply itself. This is because when the hydrocarbon is used as a reducing agent, a high temperature of 450 ° C. is required for the performance of reducing nitrogen oxides. However, when hydrogen is used as a reducing agent, the nitrogen oxides are reduced at 150 ° C. because the high temperature is not required. It is suitable for the actual driving conditions and more effective. In particular, when hydrogen is further used as a reducing agent in a device using a conventional hydrocarbon as a reducing agent, the reduction rate may be greatly improved as the temperature range for reducing nitrogen oxide is widened.

이상에서 설명한 바와 같이, 질소 저감 촉매부의 환원제로 암모니아(NH3), 탄화수소를 주로 사용함에 있어서, 상기 암모니아(NH3)의 경우 별도의 장치를 구비하여 암모니아(NH3)의 충전을 필요로 하고, 상기 탄화수소의 경우 디젤연료를 사용함에 따라 연비의 악화를 초래하는데 반해, 본 발명에 따른 배기가스 정화장치는 축전지의 잉여전력을 활용하여 물을 전기분해반응하여 발생하는 수소를 상기 환원제로 활용함으로써 환원제를 균일 및 안정적으로 자체 공급할 수 있어 경제적일 뿐만 아니라, 다른 환원제에 비해 질소 저감 효과가 현저히 뛰어나다.As described above, in the case of mainly using ammonia (NH 3 ) and a hydrocarbon as a reducing agent of the nitrogen reduction catalyst unit, the ammonia (NH 3 ) is equipped with a separate device and requires the filling of ammonia (NH 3 ), In the case of the hydrocarbon, the fuel efficiency is deteriorated by using diesel fuel, whereas the exhaust gas purifying apparatus according to the present invention utilizes hydrogen generated by electrolysis of water as a reducing agent by utilizing surplus power of a battery. It can supply itself uniformly and stably, and it is economical, and the nitrogen reduction effect is remarkably superior to other reducing agents.

또한, 본 발명은 디젤 엔진 배기관에서 나오는 배기가스의 폐열을 이용하여 상기 배기가스의 온도차에 의한 발전할 수 있는 열전소자를 포함함으로써 축전지에 전력을 충전할 수 있을 뿐만 아니라, 더 나아가 충전된 전기에너지를 활용할 수 있는 장점이 있다.In addition, the present invention includes a thermoelectric element capable of generating power by the temperature difference of the exhaust gas by using the waste heat of the exhaust gas emitted from the diesel engine exhaust pipe, thereby not only charging electric power to the storage battery, but also charging electric energy. There is an advantage to utilize.

도 1은 본 발명에 따른 배기가스 정화장치의 일양태
도 2는 본 발명에 따른 배기가스 정화장치의 다른 양태
1 is an aspect of an exhaust gas purifying apparatus according to the present invention
2 is another aspect of the exhaust gas purifying apparatus according to the present invention.

본 발명의 일양태로서 디젤엔진의 배기관(11)에 삽입되는 전기분해장치를 구비한 배기가스 정화장치를 도 1에 나타내었다. 도 1에 따르면 본 발명은 배기가스의 흐름에 따라 상류측으로부터 선택적 환원 촉매반응을 수행하는 질소 저감 촉매부(1)가 구비되고 이에 직렬로 입자 제거 필터부(2)가 구비되며, 디젤엔진의 구동으로부터 발생하는 전력을 충전 또는 공급할 수 있는 제1축전지(7)와 상기 제1축전지(7)와 연결되어 제1축전지(7)의 전력으로 구동되는 전기분해장치(4)를 구비한다. As an aspect of the present invention, an exhaust gas purification apparatus having an electrolysis device inserted into an exhaust pipe 11 of a diesel engine is shown in FIG. According to FIG. 1, the present invention includes a nitrogen reduction catalyst unit 1 for performing a selective reduction catalytic reaction from an upstream side according to the flow of exhaust gas, and a particle removal filter unit 2 is provided in series thereof. A first storage battery 7 capable of charging or supplying power generated from driving and an electrolysis device 4 connected to the first storage battery 7 and driven by the power of the first storage battery 7 are provided.

상기 전기분해장치(4)는 물의 전기분해반응으로 수소 및 산소를 발생시키며, 상기 수소를 질소산화물 저감 촉매부(1)의 전단에 공급함으로써 선택적 환원 촉매반응의 환원제로 활용한다.The electrolysis device 4 generates hydrogen and oxygen by electrolysis of water, and uses the hydrogen as a reducing agent of a selective reduction catalytic reaction by supplying the hydrogen to the front end of the nitrogen oxide reduction catalyst unit 1.

상기 전기분해장치(4)는 물을 저장하는 물탱크(5)와 상기 물탱크(5)에 설치되어 전기분해반응을 통해 물에서 수소 및 산소로 분리시키는 적극봉(6)을 포함하고, 상기 전기분해장치(4)에서 분리된 수소 및 산소는 수소탱크(8) 및 산소탱크(9)에 각각 저장되도록 한다.The electrolysis device 4 includes a water tank 5 for storing water and an electrode rod 6 installed at the water tank 5 to separate hydrogen and oxygen from water through an electrolysis reaction. Hydrogen and oxygen separated in the electrolysis device 4 are to be stored in the hydrogen tank 8 and the oxygen tank 9, respectively.

본 발명의 다른 양태로 디젤엔진의 배기관(11)에 배기가스의 폐열을 회수하여 전력을 발전하여 충전할 수 있는 배기가스 정화장치를 도 2에 나타내었다. 도 2에 따르면 본 발명의 다른 양태는 배기관(11)에 배기가스의 온도를 감지하는 제1온도센서(12) 및 제2온도센서(13)가 더 구비되며, 상기 온도센서들과 연결된 열전소자(14), 상기 열전소자(14)에 연결되어 제1온도센서(12)와 제2온도센서(13)의 온도차로 인해 발전한 전력을 충전할 수 있는 제2축전지(15)를 더 포함하여 제2축전지(15)의 전력을 전기분해장치(4)로 공급하여 수소 및 산소를 발생시키며 상기 수소 및 산소는 수소탱크(8) 및 산소탱크(9)에 각각 저장되도록 한다.In another embodiment of the present invention, an exhaust gas purifying apparatus capable of generating and charging electric power by recovering waste heat of exhaust gas in an exhaust pipe 11 of a diesel engine is shown in FIG. 2. According to FIG. 2, another embodiment of the present invention further includes a first temperature sensor 12 and a second temperature sensor 13 for sensing a temperature of exhaust gas in the exhaust pipe 11, and a thermoelectric element connected to the temperature sensors. 14, a second storage battery 15 connected to the thermoelectric element 14 to charge electric power generated by the temperature difference between the first temperature sensor 12 and the second temperature sensor 13 is further included. Power of the biaxial battery 15 is supplied to the electrolysis device 4 to generate hydrogen and oxygen, and the hydrogen and oxygen are stored in the hydrogen tank 8 and the oxygen tank 9, respectively.

상기와 같이 전기분해반응으로 생성된 수소 및 산소는 각각 저장된 수소탱크(8) 및 산소탱크(9)에서 일정한 압력으로 공급이 가능하도록 압력조절기를 포함할 수 있으며, 인젝션을 통해 소정의 양을 공급하게 된다.Hydrogen and oxygen generated by the electrolysis reaction as described above may include a pressure regulator to be supplied at a constant pressure in the stored hydrogen tank (8) and oxygen tank (9), respectively, and supply a predetermined amount through injection Done.

상기 수소는 수소를 연료로 구동되는 연료전지를 더 포함할 수 있다. 상기 연료전지는 전기구동엔진의 전기를 공급할 수 있다.The hydrogen may further include a fuel cell driven by hydrogen as fuel. The fuel cell may supply electricity of an electric drive engine.

상기 산소는 디젤엔진의 전단에 구비되는 흡입밸브에 의해 흡입되어 엔진효율을 향상시킨다.
The oxygen is sucked by the intake valve provided at the front end of the diesel engine to improve the engine efficiency.

본 발명을 실시예에 의해 상세히 설명한다.The present invention will be described in detail by way of examples.

단, 하기 실시예는 본 발명을 예시하는 것일 뿐, 본 발명의 내용이 하기 실시예에 의해 한정되는 것은 아니다.
However, the following examples are merely to illustrate the invention, but the content of the present invention is not limited by the following examples.

(제조예 1)(Production Example 1)

질소산화물 저감 촉매는 다음과 같이 제조하였다. 감마 알루미나 파우더와 초산 및 증류수를 혼합하여 습식 볼밀을 24시간 분쇄하여 균일한 알루미나 슬러리를 제조한 다음, 직경 11.25인치, 길이 3인치의 400cpi의 코디어라이트 허니컴을 워시코팅(washcoating)하여 알루미나의 담지량이 3g/in3이 되도록 코팅한 다음, 120℃에서 건조한 후, 120~550℃에서 소성하였다. 상기 소성된 알루미나 담지 코디어라이트 건조체를 질산은과 백금 전구체로 염화백금산을 용해하여 제조한 용액에 함침하여 은이 알루미나 중량대비 2.0, 백금촉매성분이 0.001중량% 함침되도록 상기 알루미나 워시코팅과 같은 방법으로 소성하였다.
The nitrogen oxide reduction catalyst was prepared as follows. Gamma alumina powder was mixed with acetic acid and distilled water to grind a wet ball mill for 24 hours to produce a uniform alumina slurry, and then washcoating a 400cpi cordierite honeycomb of 11.25 inches in diameter and 3 inches in length to carry alumina. After coating to 3g / in 3 , and dried at 120 ℃, it was baked at 120 ~ 550 ℃. The calcined alumina-supported cordierite dried body was impregnated into a solution prepared by dissolving platinum chloride with silver nitrate and a platinum precursor, and calcined by the same method as the alumina wash coating such that silver was impregnated with 2.0 to the weight of alumina and 0.001 wt% of a platinum catalyst component. It was.

(제조예 2)(Manufacture example 2)

입자제거 필터는 다음과 같이 제조하였다. 2L 플라스크에 폴리비닐피롤리돈(알드리치 케미컬사, 평균분자량 10,000) 252g을 증류수 1L에 녹여 균일용액을 만든다. 여기에 염화백금산 30.4 g을 넣고 메탄올 1L를 넣고 교반한다. 이 용액을 80℃에서 6시간동안 환류시키고 여과하여 백금함량 0.62 중량%의 암갈색 백금 콜로이드 용액 2,070 g을 얻는다. 암모늄몰리브데이트 15.4g, 수산화칼륨 10g을 각각 증류수 250 mL에 넣고 교반하여 몰리브데늄(Mo) 수용액, 칼륨(K) 수용액을 제조한다.The particle removal filter was prepared as follows. In a 2 L flask, 252 g of polyvinylpyrrolidone (Aldrich Chemical, average molecular weight 10,000) is dissolved in 1 L of distilled water to make a homogeneous solution. 30.4 g of chloroplatinic acid was added thereto, and 1 L of methanol was added thereto, followed by stirring. The solution was refluxed at 80 ° C. for 6 hours and filtered to obtain 2,070 g of a dark brown platinum colloidal solution with a platinum content of 0.62% by weight. 15.4 g of ammonium molybdate and 10 g of potassium hydroxide were added to 250 mL of distilled water, followed by stirring to prepare an aqueous molybdenum (Mo) solution and an aqueous potassium (K) solution.

상기에서 제조된 백금 콜로이드 용액, 몰리브데늄(Mo) 수용액, 칼륨(K) 수용액을 동일 중량비로 혼합하여 촉매화된 필터용 금속염 콜로이드 용액을 얻는다. 코닝사의 직경 11.25˝ 길이 14인치, 셀밀도 200 cpsi인 월플루우 형태의 세라믹 필터를 촉매화된 필터의 지지체로 사용한다. Platinum colloidal solution prepared above, molybdenum (Mo) aqueous solution and potassium (K) aqueous solution are mixed in the same weight ratio to obtain a catalyzed metal salt colloidal solution for the filter. Corning's 11.25 ˝ diameter 14 inch long, cell density 200 cpsi wall filter type ceramic filter is used as a support for the catalyzed filter.

상기 하니컴 모노리스에 7중량%의 티타니아와 실리카 혼합 워시코트액을 침착시킨 후 건조 소성한다. 워시코팅한 지지체에 상기한 촉매화된 필터용 콜로이드 혼합액을 담지시켜 담체에 대해 백금 함량이 0.27중량%, 몰리브데늄 함량이 0.16중량%, 칼륨 함량이 0.077중량%가 되도록 하였다. 120℃에서 3시간 동안 건조한 후, 550℃의 온도에서 4~6시간 동안 소성하여 입자상물질 제거용 필터를 제조하였다.
The honeycomb monolith was deposited with 7% by weight of titania and silica mixed washcoat solution and then calcined dry. The colloidal solution for catalyzed filters described above was supported on the wash-coated support so that the platinum content was 0.27% by weight, the molybdenum content was 0.16% by weight, and the potassium content was 0.077% by weight. After drying for 3 hours at 120 ℃, it was baked for 4-6 hours at a temperature of 550 ℃ to prepare a filter for removing particulate matter.

(실시예)(Example)

제조예 1 에서 제조한 질소산화물 저감 촉매와 제조예 2에서 제조한 입자제거 촉매를 연속적으로 연결한 다음, 스테인레스 스틸로 제작된 캐닝에 위치하였으며, 평가시험에 사용한 엔진은 배기량 11리터의 과급기 및 중간냉각기가 적용된 대우엔진을 사용하였다. 전기분해장치와 상기 전기분해장치에서 발생한 수소 및 산소를 저장하는 수소탱크 및 산소탱크를 구비하고, 상기 수소탱크의 압력조절기를 조절하여 일정압력으로 수소와 탄화수소(디젤)를 질소 저감 촉매부의 전단의 인젠셕을 통해 주입하여 질소 저감 시험 성능을 측정하였다.
The nitrogen oxide reduction catalyst prepared in Preparation Example 1 and the particle removal catalyst prepared in Preparation Example 2 were successively connected, and then placed in a canning made of stainless steel. A Daewoo engine with a cooler was used. It is equipped with an electrolysis device and a hydrogen tank and an oxygen tank for storing hydrogen and oxygen generated in the electrolysis device, by adjusting the pressure regulator of the hydrogen tank to the hydrogen and hydrocarbon (diesel) at a constant pressure of the front end of the nitrogen reduction catalyst portion The nitrogen reduction test performance was measured by injecting through an index.

표 1. 본 발명의 실시예에 따른 배기가스 질소산화물 및 입자상 물질 저감 시험Table 1. Exhaust gas nitrogen oxide and particulate matter reduction test according to an embodiment of the present invention

Figure pat00001

Figure pat00001

상기 실시예에 따른 질소산화물 및 입자상 물질 저감 성능 시험에서 질소산화물 저감 환원제로 탄화수소를 사용한 경우 고온부에서 질소산화물의 저감성능이 나타났으며, 수소를 환원제로 사용할 경우는 저온부에서 질소산화물의 저감이 나타난 것을 확인할 수 있었다. 상기 표1에서 보는 바와 같이, 디젤 환원제와 수소환원제의 질소산화물 저감율은 비슷하게 나오지만, 디젤 환원제의 경우 차량의 연료인 디젤을 환원제로 사용함에 따라, 환원제로 사용한 양으로 인한 연비가 떨어지게 되는 반면 수소의 경우 디젤 환원제 수준의 질소산화물 저감성능을 가질 뿐만 아니라, 연비와는 전기분해장치에서 생산됨에 따라 연비 측면에서는 수소환원제가 더 우수하다고 할 수 있다. 그리고 디젤과 수소를 환원제로 동시 사용할 경우 배기가스가 비교적 낮을 때는 수소환원제에 의해 질소산화물이 저감되고, 비교적 높은 부분에서는 디젤 환원제에서 질소산화물이 저감됨에 따라 77%수준의 우수한 질소산화물 저감을 얻을 수 있다. 다시 말해 기존 탄화수소를 환원제로 사용하는 장치에 수소를 추가로 환원제로 사용할 경우 질산화물 저감시키는 온도 범위가 넓어짐에 따라 저감율도 크게 향상된다는 것을 확인할 수 있다. In the nitrogen oxide and particulate matter reduction performance test according to the above embodiment, when the hydrocarbon was used as the reducing agent for reducing the nitrogen oxides, the reduction performance of the nitrogen oxides was shown at the high temperature portion, and when the hydrogen was used as the reducing agent, the reduction of the nitrogen oxides was shown at the low temperature portion. I could confirm that. As shown in Table 1, the reduction rate of nitrogen oxides of the diesel reducing agent and the hydrogen reducing agent is similar, but in the case of the diesel reducing agent, as the fuel of the vehicle is used as the reducing agent, the fuel consumption due to the amount used as the reducing agent is reduced while hydrogen In this case, as well as nitrogen oxide reduction performance of the diesel reducing agent level, as the fuel economy and the fuel economy is produced in the electrolysis device, it can be said that the hydrogen reduction agent in terms of fuel efficiency. In the case of using diesel and hydrogen as reducing agents, nitrogen oxides are reduced by hydrogen reducing agent when the exhaust gas is relatively low, and nitrogen oxides are reduced by diesel reducing agent in the relatively high part. have. In other words, when hydrogen is used as a reducing agent in a device using an existing hydrocarbon as a reducing agent, the reduction rate is also greatly improved as the temperature range for reducing nitric oxide is widened.

이상과 같이 본 발명에서는 구체적인 장치도와 같이 특정된 사항들과 한정된 실시예 및 도면에 의해 설명되었으나 이는 본 발명의 보다 전반적인 이해를 돕기 위해서 제공된 것일 뿐, 본 발명은 상기의 실시예에 한정되는 것은 아니며, 본 발명이 속하는 분야에서 통상의 지식을 가진 자라면 이러한 기재로부터 다양한 수정 및 변형이 가능하다. In the present invention as described above has been described by the specific matters and the specific embodiments and drawings as shown in the specific device diagram, which is provided only to help a more general understanding of the present invention, the present invention is not limited to the above embodiment. For those skilled in the art, various modifications and variations are possible from such description.

따라서, 본 발명의 사상은 설명된 실시예에 국한되어 정해져서는 아니되며, 후술하는 특허청구범위뿐 아니라 이 특허청구범위와 균등하거나 등가적 변형이 있는 모든 것들은 본 발명 사상의 범주에 속한다고 할 것이다.Therefore, the spirit of the present invention should not be limited to the described embodiments, and all of the equivalents or equivalents of the claims as well as the claims to be described later will belong to the scope of the present invention. .

1 : 질소 저감 촉매부 2 : 입자 제거 필터부
3 : 디젤엔진(Diesel engine) 4 : 전기분해장치
5 : 물탱크 6 : 전극봉
7 : 제1축전지
8 : 수소탱크 9 : 산소탱크
10 : 교류발전기
11 : 배관재
12 : 제1온도센서 13 : 제2온도센서
14 : 열전소자 15 : 제2축전지
1 nitrogen reduction catalyst part 2 particle removal filter part
3: diesel engine 4: electrolysis device
5: water tank 6: electrode
7: first storage battery
8: hydrogen tank 9: oxygen tank
10: alternator
11: piping material
12: first temperature sensor 13: second temperature sensor
14 thermoelectric element 15 secondary battery

Claims (5)

디젤 엔진(3)의 배기관(11)에 삽입되는 질소산화물 저감 촉매(DeNOx 촉매)부(1)와 입자 제거 필터(Diesel Particulate Filter;DPF)부(2)를 배기가스의 흐름에 대해 상류로부터 순차적으로 구비하는 배기가스 정화장치에 있어서,
디젤 엔진의 구동으로부터 생성되는 전력을 충전 또는 공급할 수 있는 제1축전지(7)와; 상기 제1축전지(7)와 연결되어 제1축전지의 전력으로 구동되는 전기분해장치(4);를 구비하며, 상기 전기분해장치(4)는 물의 전기분해반응으로 수소 및 산소를 발생시키며, 상기 수소를 질소산화물 저감 촉매부(1)의 전단에 공급함으로써 촉매의 환원제로 활용하는 것을 특징으로 하는 배기가스 정화장치.
The nitrogen oxide reduction catalyst (DeNOx catalyst) part 1 and the diesel particulate filter (DPF) part 2 inserted into the exhaust pipe 11 of the diesel engine 3 are sequentially disposed from the upstream with respect to the flow of the exhaust gas. In the exhaust gas purification device provided with,
A first storage battery 7 capable of charging or supplying electric power generated from driving of the diesel engine; An electrolysis device 4 connected to the first storage battery 7 and driven by electric power of the first storage battery 7, wherein the electrolysis device 4 generates hydrogen and oxygen through an electrolysis reaction of water. An exhaust gas purification device characterized by utilizing hydrogen as a reducing agent of a catalyst by supplying hydrogen to the front end of the nitrogen oxide reduction catalyst part (1).
제1항에 있어서,
상기 전기분해장치(4)는 물을 저장하는 물탱크(5)와, 상기 물탱크에 설치되어 전기분해반응을 통해 물에서 수소 및 산소로 분리시키는 전극봉(6)을 포함하고, 상기 전기분해장치(4)에서 분리된 수소 및 산소는 수소탱크(8) 및 산소탱크(9)에 각각 저장되는 것을 특징으로 하는 배기가스 정화장치.
The method of claim 1,
The electrolysis device 4 includes a water tank 5 for storing water, and an electrode rod 6 installed at the water tank to separate hydrogen and oxygen from water through an electrolysis reaction. Hydrogen and oxygen separated in (4) are stored in the hydrogen tank (8) and oxygen tank (9), respectively, characterized in that the exhaust gas purification device.
제1항에 있어서,
상기 배기관(11)은 배기가스의 온도를 감지하는 제1온도센서(12) 및 제2온도센서(13)가 구비되며, 상기 온도센서들과 연결된 열전소자(14), 상기 열전소자(14)에 연결되어 제1온도센서(12)와 제2온도센서(13)의 온도차로 인해 발전한 전력을 충전하는 제2축전지(15);를 더 포함하여 제2축전지의 전력을 전기분해장치(4)로 공급하여 수소 및 산소를 발생시키며; 상기 수소 및 산소는 수소탱크(8) 및 산소탱크(9)에 각각 저장되는 것을 특징으로 하는 배기가스 정화장치.
The method of claim 1,
The exhaust pipe 11 is provided with a first temperature sensor 12 and a second temperature sensor 13 for detecting the temperature of the exhaust gas, and the thermoelectric element 14 and the thermoelectric element 14 connected to the temperature sensors. It is connected to the second storage battery 15 for charging the power generated by the temperature difference between the first temperature sensor 12 and the second temperature sensor 13; further comprising the electrolysis device of the power of the second storage battery (4) To generate hydrogen and oxygen; The hydrogen and oxygen are exhaust gas purification device, characterized in that stored in the hydrogen tank (8) and oxygen tank (9), respectively.
제2항 또는 제3항에 있어서,
상기 배기가스 정화장치는 수소탱크(8)에 저장된 수소를 연료로 사용할 있는 연료전지가 더 포함되는 것을 특징으로 하는 배기가스 정화장치.
The method according to claim 2 or 3,
The exhaust gas purification device further comprises a fuel cell capable of using hydrogen stored in the hydrogen tank (8) as fuel.
제2항 또는 제3항에 있어서,
상기 배기가스 정화장치는 산소탱크(9)에 저장된 산소를 흡입할 수 있는 흡입밸브가 디젤엔진(3)의 전단에 더 포함되는 것을 특징으로 하는 배기가스 정화장치.
The method according to claim 2 or 3,
The exhaust gas purification device further comprises an inlet valve for sucking oxygen stored in the oxygen tank (9) at the front end of the diesel engine (3).
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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102015120344A1 (en) * 2015-11-24 2017-05-24 Hans Seidl Device for the reduction of nitrogen oxides
CN108217853A (en) * 2018-01-16 2018-06-29 南京农业大学 A kind of device for handling tube furnace high temperature cabonization tail gas
KR20210066439A (en) 2019-11-28 2021-06-07 한국전력공사 Apparatus and method for purifying exhaust gas using digel reformed hydrogen
CN113153474A (en) * 2021-05-17 2021-07-23 南通理工学院 Marine diesel engine exhaust gas waste heat recycling system and recycling method thereof
KR102353880B1 (en) * 2020-07-17 2022-01-21 주식회사 더 오포 Pollutant treating Apparatus treating pollutant by selective catalytic reduction method

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102015120344A1 (en) * 2015-11-24 2017-05-24 Hans Seidl Device for the reduction of nitrogen oxides
CN108217853A (en) * 2018-01-16 2018-06-29 南京农业大学 A kind of device for handling tube furnace high temperature cabonization tail gas
KR20210066439A (en) 2019-11-28 2021-06-07 한국전력공사 Apparatus and method for purifying exhaust gas using digel reformed hydrogen
KR102353880B1 (en) * 2020-07-17 2022-01-21 주식회사 더 오포 Pollutant treating Apparatus treating pollutant by selective catalytic reduction method
CN113153474A (en) * 2021-05-17 2021-07-23 南通理工学院 Marine diesel engine exhaust gas waste heat recycling system and recycling method thereof
CN113153474B (en) * 2021-05-17 2022-04-01 南通理工学院 Marine diesel engine exhaust gas waste heat recycling system and recycling method thereof

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