KR20100042498A - Purification device of exhaust gas - Google Patents

Purification device of exhaust gas Download PDF

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KR20100042498A
KR20100042498A KR1020080101671A KR20080101671A KR20100042498A KR 20100042498 A KR20100042498 A KR 20100042498A KR 1020080101671 A KR1020080101671 A KR 1020080101671A KR 20080101671 A KR20080101671 A KR 20080101671A KR 20100042498 A KR20100042498 A KR 20100042498A
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catalyst
nitrogen oxide
exhaust gas
filter
oxide storage
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KR1020080101671A
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Korean (ko)
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KR100993358B1 (en
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이효경
이상민
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현대자동차주식회사
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    • 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
    • F01N3/24Exhaust 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 constructional aspects of converting apparatus
    • F01N3/36Arrangements for supply of additional fuel
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2255/00Catalysts
    • B01D2255/20Metals or compounds thereof
    • B01D2255/202Alkali metals
    • 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
    • F01N2570/00Exhaust treating apparatus eliminating, absorbing or adsorbing specific elements or compounds
    • F01N2570/04Sulfur or sulfur oxides
    • 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
    • F01N2570/00Exhaust treating apparatus eliminating, absorbing or adsorbing specific elements or compounds
    • F01N2570/14Nitrogen oxides
    • 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
    • F01N2610/00Adding substances to exhaust gases
    • F01N2610/14Arrangements for the supply of substances, e.g. conduits
    • F01N2610/1453Sprayers or atomisers; Arrangement thereof in the exhaust apparatus

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Health & Medical Sciences (AREA)
  • Toxicology (AREA)
  • Exhaust Gas After Treatment (AREA)
  • Processes For Solid Components From Exhaust (AREA)

Abstract

PURPOSE: A purification device of an exhaust gas is provided to prevent the sulfur poisoning of the nitrogen oxide absorbing catalyst arranged in the catalyst filter by allowing catalyst filter to have alkali metal or the alkyl earth metal. CONSTITUTION: An exhaust gas purification device includes a catalyst filter(110) and a nitrogen oxide absorbing catalyst(140). The catalyst filter collects soot or PM included in the exhaust gas. The nitrogen oxide absorbing catalyst is installed at the end of the catalyst filter and intakes the nitrogen oxide. The catalyst filter has at least one of alkali metal or the alkaline earth metal for collecting the Sox.

Description

배기가스 정화장치{PURIFICATION DEVICE OF EXHAUST GAS}Exhaust gas purification device {PURIFICATION DEVICE OF EXHAUST GAS}

본 발명은 배기가스 정화장치에 관한 것으로서, 보다 상세하게는 엔진에서 배기되는 배기가스에 포함된 입자상물질(PM)과 질소화합물(NOx)을 제거하는 배기가스 정화장치에 관한 것이다.The present invention relates to an exhaust gas purification apparatus, and more particularly, to an exhaust gas purification apparatus for removing particulate matter (PM) and nitrogen compounds (NOx) contained in exhaust gas exhausted from an engine.

일반적으로 디젤엔진에는 질소산화물(NOx)과 입자상물질(PM)을 포집하기 위한 질소산화물 흡장촉매(LNT: Lean NOx Trap)와 촉매여과필터(CPF: Catalyst Particulate Filter)가 장착된다.In general, a diesel engine is equipped with a nitrogen oxide storage catalyst (LNT) and a catalyst filtration filter (CPF) to capture nitrogen oxides (NOx) and particulate matter (PM).

한편, 연료 중에 포함되어 있는 황성분이 상기 질소산화물 흡장촉매를 오염시켜, 질소산화물의 흡장효율과 재생효율이 저하되는 문제점이 있다.On the other hand, the sulfur component contained in the fuel contaminates the nitrogen oxide storage catalyst, there is a problem that the storage efficiency and regeneration efficiency of the nitrogen oxide is lowered.

도 4는 일반적인 질소산화물 흡장촉매의 황산화물 피독 상태를 도시한 그래프이다.Figure 4 is a graph showing the sulfur oxide poisoning state of a typical nitrogen oxide storage catalyst.

도 4를 참조하면, 황산화물(SOx)은 촉매의 전단부에 흡착되어 질소산화물의 포집 능력을 저하시켜 배기가스의 정화능력을 감소시킨다.Referring to FIG. 4, sulfur oxide (SOx) is adsorbed at the front end of the catalyst to lower the trapping ability of nitrogen oxides to reduce the purification ability of the exhaust gas.

상기와 같이, 황성분으로 오염된 질소산화물 흡장촉매를 재생하기 위한 별도의 황제거모드가 수행되고, 이 때 질소산화물 흡장촉매는 섭씨 600도 내지 700도로 가열된다. 여기서 고온으로 인하여 상기 질소산화물 흡장촉매가 열화되는 문제점이 있다.As described above, a separate sulfur removal mode for regenerating the nitrogen oxide storage catalyst contaminated with sulfur components is performed, wherein the nitrogen oxide storage catalyst is heated to 600 degrees Celsius to 700 degrees Celsius. Here, there is a problem in that the nitrogen oxide storage catalyst is deteriorated due to high temperature.

또한, 상기 질소산화물 흡장촉매가 황성분으로 오염되는 것을 방지하기 위해서 황성분 포집장치를 별도로 구비하는 경우도 있으나, 비용이 상승하는 문제점이 있고, 별도로 황성분 포집장치에서 황성분을 제거하기 위한 황제거 모드가 더 필요하다.In addition, in order to prevent the nitrogen oxide storage catalyst from being contaminated with sulfur components, a sulfur component collecting device may be separately provided, but there is a problem in that the cost increases, and a sulfur removing mode for removing sulfur components from the sulfur component collecting device is further provided. need.

따라서, 본 발명은 상기한 바와 같은 문제점을 해결하기 위하여 창출된 것으로, 본 발명의 목적은 질소산화물 흡장촉매가 황성분으로 피독되는 것을 방지하는 배기가스 정화장치를 제공하는 것이다. Accordingly, the present invention has been made to solve the above problems, and an object of the present invention is to provide an exhaust gas purification apparatus which prevents the nitrogen oxide storage catalyst from being poisoned with sulfur.

아울러, 포집된 황성분을 제거하기 위해 상기 질소산화물 흡장촉매의 온도를 고온으로 상승시키지 않는 배기가스 정화장치를 제공하는 것이다.In addition, it is to provide an exhaust gas purification apparatus that does not increase the temperature of the nitrogen oxide storage catalyst to a high temperature in order to remove the collected sulfur component.

아울러, 배기가스에 포함된 황성분을 제거하기 위한 별도의 황성분 포집장치를 구비하지 않는 배기가스 정화장치를 제공하는 것이다.In addition, to provide an exhaust gas purification apparatus that does not have a separate sulfur component collecting device for removing the sulfur component contained in the exhaust gas.

이러한 목적을 달성하기 위한 본 발명에 따른 배기가스 정화장치는, 배기가스에 포함된 매연(soot)이나 입자상 물질(PM)을 포집하는 촉매여과필터(CPF) 및 상기 촉매여과필터 후단에 설치되어 질소산화물을 흡장하는 질소산화물 흡장촉매(LNT)를 포함하고, 상기 촉매여과필터에는 황산화물(SOx)를 포집하기 위한 알칼리 금속 또는 알칼리 토금속 중 적어도 하나의 성분이 포함된다.Exhaust gas purifying apparatus according to the present invention for achieving this object, the catalyst filter (CPF) for trapping the soot (soot) or particulate matter (PM) contained in the exhaust gas and nitrogen is installed in the rear end of the catalyst filter filter A nitrogen oxide storage catalyst (LNT) that occludes an oxide, and the catalyst filtration filter includes at least one component of an alkali metal or an alkaline earth metal for trapping sulfur oxides (SOx).

상기 알칼리 금속 또는 알칼리 토금속은 워시코트에 섞여 상기 촉매여과필터에 코팅되어 형성되고, 상기 알칼리 금속 또는 알칼리 토금속에 의해서 상기 촉매여과필터에 포집된 황산화물은, 상기 촉매여과필터 재생시 설정온도 이상에서 분리되어 제거된다.The alkali metal or alkaline earth metal is mixed with a wash coat to form a coating on the catalyst filter, and the sulfur oxides collected in the catalyst filter by the alkali metal or alkaline earth metal are above a predetermined temperature during regeneration of the catalyst filter. It is separated and removed.

상기 설정온도는 섭씨 600도 내지 800도의 범위 내에 포함되고, 상기 촉매여 과필터의 재생은 주행거리 기준으로 500km 내지 1000km 주기로 재생된다.The set temperature is included in the range of 600 degrees Celsius to 800 degrees Celsius, the regeneration of the catalyst filter is regenerated in 500km to 1000km cycle based on the driving distance.

상기 촉매여과필터 재생시 상기 촉매여과필터 후단에 설치된 상기 질소산화물 흡장촉매의 온도는 섭씨 500도 내지 550도의 범위에 포함되어 상기 촉매여과필터에서 분리된 황산화물은 상기 질소산화물 흡장촉매에 흡장되지 않고 통과하여 외기로 배출되어 제거되고, 상기 질소산화물 흡장촉매 전단에 장착되고 후분사된 원료를 이용하여 환원제를 생성시키는 디젤연료 분해촉매(DFC)를 포함하며, 상기 질소산화물 흡장촉매는 상기 환원제를 이용하여 질소산화물을 흡장하는 것이 바람직하다.When the catalyst filtration filter is regenerated, the temperature of the nitrogen oxide storage catalyst installed at the rear end of the catalyst filtration filter is in the range of 500 ° C to 550 ° C so that the sulfur oxide separated from the catalyst filtration filter is not occluded in the nitrogen oxide storage catalyst. It is discharged to the outside to be removed to the outside, and includes a diesel fuel decomposition catalyst (DFC) for producing a reducing agent using a raw material which is mounted in front of the nitrogen oxide storage catalyst and post-injected, the nitrogen oxide storage catalyst using the reducing agent It is preferable to occlude nitrogen oxide.

상기 디젤연료 분해촉매(DFC) 전단에 연료를 후분사하는 포스트 인젝터가 배치될 수 있다.Post injectors for post-injection of fuel may be disposed in front of the diesel fuel decomposition catalyst (DFC).

상술한 바와 같이 본 발명에 따른 배기가스 정화장치에 의하면, 촉매여과필터에 황산화물을 포집하기 위한 알칼리 금속 또는 알칼리 토금속 성분이 포함되어 있으므로 촉매여과필터 후단에 배치된 질소산화물 흡장촉매의 황피독이 미연에 방지될 수 있다.As described above, according to the exhaust gas purifying apparatus according to the present invention, since the catalyst filter contains an alkali metal or alkaline earth metal component for trapping sulfur oxides, sulfur poisoning of the nitrogen oxide storage catalyst disposed at the rear of the catalyst filter is unburned. Can be prevented.

아울러, 질소산화물 흡장촉매의 효율이 향상되고, 별도의 황성분을 포집하기 위한 포집장치가 필요하지 않다.In addition, the efficiency of the nitrogen oxide storage catalyst is improved, and a separate collecting device for collecting a separate sulfur component is not required.

또한, 촉매여과필터의 재생시 황성분이 제거됨으로써 포집된 황성분을 제거하기 위한 별도의 황제거 모드가 필요하지 않다.In addition, since the sulfur component is removed during the regeneration of the catalytic filtration filter, a separate sulfur removal mode for removing the collected sulfur component is not required.

또한, 황성분을 제거하기 위해서 질소산화물 흡장촉매를 고온으로 가열하지 않아도 됨으로써 질소산화물 흡장촉매가 열화되지 않는다.In addition, the nitrogen oxide storage catalyst does not deteriorate because the nitrogen oxide storage catalyst does not have to be heated to a high temperature in order to remove the sulfur component.

이하, 본 발명의 바람직한 실시예를 첨부한 도면에 의거하여 상세하게 설명하면 다음과 같다.Hereinafter, preferred embodiments of the present invention will be described in detail with reference to the accompanying drawings.

도 1은 본 발명의 실시예에 따른 배기가스 정화장치의 전체적인 구성도이다.1 is an overall configuration diagram of an exhaust gas purifying apparatus according to an embodiment of the present invention.

도 1을 참조하면, 배기가스 정화장치는 엔진, 촉매여과필터(110), 포스트 인젝터(120), 디젤연료 분해촉매(130), 질소산화물 흡장촉매(140), 및 머플러(150)를 포함한다.Referring to FIG. 1, the exhaust gas purification apparatus includes an engine, a catalytic filtration filter 110, a post injector 120, a diesel fuel decomposition catalyst 130, a nitrogen oxide storage catalyst 140, and a muffler 150. .

상기 촉매여과필터(110)의 전후단에는 내부에 축적된 입자상물질(PM)의 양을 검출하기 위한 차압센서(미도시)가 배치되고, 상기 질소산화물 흡장촉매(140)의 전단에는 질소산화물의 농도를 검출하는 검출센서(미도시)가 배치된다.A differential pressure sensor (not shown) for detecting the amount of particulate matter (PM) accumulated therein is disposed at the front and rear ends of the catalyst filtration filter 110, and the front of the nitrogen oxide storage catalyst 140 has a A detection sensor (not shown) for detecting the concentration is disposed.

상기 디젤연료 분해촉매(130)는 상기 포스트 인젝터(120)에서 분사된 연료를 분해하여 환원제를 생성하고, 생성된 환원제를 상기 질소산화물 흡장촉매(140)에 공급한다. 상기 질소산화물 흡장촉매(140)는 상기 환원제를 이용하여 질소산화물을 제거한다.The diesel fuel decomposition catalyst 130 decomposes the fuel injected from the post injector 120 to generate a reducing agent, and supplies the generated reducing agent to the nitrogen oxide storage catalyst 140. The nitrogen oxide storage catalyst 140 removes nitrogen oxides using the reducing agent.

상기 촉매여과필터(110)에는 상기 입자상물질(PM)을 포집하기 위한 필터몸체와 이 몸체에 코팅되는 촉매를 포함하고, 상기 촉매는 배기가스 중에 포함된 황산화물(Sox)를 포집하기 위한 알칼리금속 또는 알칼리 토금속이 포함된다.The catalyst filtration filter 110 includes a filter body for collecting the particulate matter (PM) and a catalyst coated on the body, and the catalyst is an alkali metal for collecting sulfur oxides (Sox) contained in the exhaust gas. Or alkaline earth metals.

상기 알칼리금속 또는 상기 알칼리 토금속은 와시코트 내에 섞여 촉매여과필터(110)의 몸체에 코팅되어 형성되는 것이 바람직하다.The alkali metal or the alkaline earth metal is preferably formed by being mixed with the wash coat and coated on the body of the catalyst filtration filter 110.

특히, 배기가스 중에 포함된 황성분이 상기 질소산화물 흡장촉매(140)에 다량 포집되면, 질소산화물의 포집성능과 재생효율이 급격하게 저감되는데, 본 발명의 실시예에서는 상기 황성분이 상기 촉매여과필터(110)에서 미리 포집되어 상기 질소산화물 흡장촉매(140)의 성능이 저하되지 않는다.In particular, when a large amount of sulfur contained in the exhaust gas is collected in the nitrogen oxide storage catalyst 140, the trapping performance and regeneration efficiency of the nitrogen oxide is drastically reduced, in the embodiment of the present invention, the sulfur component is the catalyst filtration filter ( Since it is collected in advance in 110, the performance of the nitrogen oxide storage catalyst 140 is not reduced.

아울러, 상기 촉매여과필터(110) 재생시 상기 촉매여과필터(110)에 포집된 황성분도 제거된다. 따라서, 황성분으로 피독된 상기 질소산화물 흡장촉매(140)에서 황을 제거하기 위한 별도의 탈황모드가 필요하지 않다.In addition, sulfur components collected in the catalyst filtration filter 110 are also removed when the catalyst filtration filter 110 is regenerated. Therefore, a separate desulfurization mode for removing sulfur from the nitrogen oxide storage catalyst 140 poisoned with sulfur is not required.

본 발명의 실시예에서, 상기 질소산화물 흡장촉매(140)에서 황성분을 제거하기 위해 섭씨 700도로 상기 질소산화물 흡장촉매(140)를 가열하는 모드가 적용되지 않으므로 상기 질소산화물 흡장촉매(140)의 열화가 진행되지 않는다.In the embodiment of the present invention, since the mode for heating the nitrogen oxide storage catalyst 140 to 700 degrees Celsius to remove the sulfur component in the nitrogen oxide storage catalyst 140 is not applied, deterioration of the nitrogen oxide storage catalyst 140 Does not proceed.

또한, 상기 질소산화물 흡장촉매(140)에 황성분이 피독되는 것을 방지하기 위해서 별도의 황포집촉매가 배치되지 않으므로, 생산비용이 저감된다.In addition, since a separate sulfur collecting catalyst is not disposed in order to prevent poisoning of sulfur components in the nitrogen oxide storage catalyst 140, the production cost is reduced.

도 2는 본 발명의 실시예에 따른 배기가스 정화장치에서 촉매여과필터에 코팅되는 워시코트에 포함되는 성분을 나타내는 표이다.Figure 2 is a table showing the components included in the washcoat coated on the catalyst filter in the exhaust gas purifying apparatus according to an embodiment of the present invention.

도 2를 참조하면, 상기 촉매여과필터(110)에 코팅되는 워시코트에 포함되는 상기 알칼리금속은 Li, Na, K, Rb, Cs 및 Fr 등이 있고, 상기 알칼리 토금속은 Be, Mg, Ca, Sr, Ba 및 Ra 등이 있다.2, the alkali metals included in the washcoat coated on the catalyst filtration filter 110 include Li, Na, K, Rb, Cs and Fr, and the alkaline earth metals are Be, Mg, Ca, Sr, Ba and Ra and the like.

상기 알칼리금속 또는 상기 알칼리 토금속에 대한 화학적인 특징에 대해서는 상세한 설명을 생략한다.Detailed descriptions of chemical characteristics of the alkali metal or the alkaline earth metal will be omitted.

도 3은 본 발명의 실시예에 따른 배기가스 정화장치의 작동 원리를 도시한 순서도이다.3 is a flow chart showing the operating principle of the exhaust gas purifying apparatus according to the embodiment of the present invention.

도 3을 참조하면, 제1단계(S10)에서 황성분이 포집되고, 제2단계(S20)에서 촉매여과필터(110)가 재생되며, 제3단계(S30)에서 상기 촉매여과필터(110)에 포집된 황성분이 제거된다.Referring to FIG. 3, sulfur components are collected in a first step S10, a catalyst filtration filter 110 is regenerated in a second step S20, and the catalyst filtration filter 110 is regenerated in a third step S30. Collected sulfur is removed.

상기 제1단계(S10)에서, 배기가스에 포함된 황성분은 상기 촉매여과필터(110)에 포집되어 상기 질소산화물 흡장촉매(140)는 황성분으로 피독되지 않는다.In the first step (S10), the sulfur component contained in the exhaust gas is collected in the catalyst filtration filter 110 so that the nitrogen oxide storage catalyst 140 is not poisoned as a sulfur component.

상기 제2단계(S20)는 상기 촉매여과필터(110)에 포집된 입자상물질(PM)과 황성분을 동시에 제거하기 위한 재생모드가 수행되고, 이 때 상기 촉매여과필터(110)의 내부 온도는 약 섭씨 700 내지 800도의 범위 내에 포함되며, 재생주기는 약 500km 내지 1000km의 범위에 포함된다.In the second step (S20), a regeneration mode for simultaneously removing particulate matter (PM) and sulfur components collected in the catalyst filtration filter 110 is performed, and the internal temperature of the catalyst filtration filter 110 is about It is included in the range of 700 to 800 degrees Celsius, and the regeneration period is included in the range of about 500 km to 1000 km.

상기와 같은 온도에서 상기 촉매여과필터(110)에 포집된 입자상물질(PM)과 황성분은 촉매성분과 반응하여 제거되거나 일부는 분리되어 외기로 배출된다.At this temperature, particulate matter (PM) and sulfur components collected in the catalyst filtration filter 110 are removed by reaction with the catalyst component or partly separated and discharged to the outside air.

특히, 상기 촉매여과필터(110)에 포집된 황성분은 재생시 높은 온도로 인하여 분리되고, 상기 질소산화물 흡장촉매(140)에 도달하게 되며, 이때 상기 질소산화물 흡장촉매(140)의 온도가 약 섭씨 500도 내지 550도의 범위에 포함되므로 상기 황성분은 상기 질소산화물 흡장촉매(140)에 흡장되지 않고 통과하게 된다.In particular, the sulfur component collected in the catalyst filtration filter 110 is separated due to the high temperature during regeneration, and reaches the nitrogen oxide storage catalyst 140, wherein the temperature of the nitrogen oxide storage catalyst 140 is about Celsius Since the sulfur component is included in the range of 500 to 550 degrees, the sulfur component passes through the nitrogen oxide storage catalyst 140 without being occluded.

따라서, 상기 질소산화물 흡장촉매(140)는 황성분으로 피독되지 않고, 배기가스에 포함된 질소산화물을 용이하게 포집할 수 있다. Therefore, the nitrogen oxide storage catalyst 140 is not poisoned with sulfur and can easily collect nitrogen oxide contained in exhaust gas.

아울러, 본 발명의 실시예에서, 별도의 황성분을 제거하기 위한 탈황재생모 드가 필요하지 않으며 상기 촉매여과필터(110)를 재생하는 모드만으로 탈황이 수행된다.In addition, in the embodiment of the present invention, a desulfurization regeneration mode for removing a separate sulfur component is not necessary, and desulfurization is performed only by regenerating the catalytic filtration filter 110.

따라서, 상기 질소산화물 흡장촉매(140)를 고온(약 섭씨 700도)로 가열하는 탈황재생모드가 수행되지 않으므로 상기 질소산화물 흡장촉매(140)의 열화를 미연에 방지할 수 있다. Therefore, since the desulfurization regeneration mode for heating the nitrogen oxide storage catalyst 140 to a high temperature (about 700 degrees Celsius) is not performed, deterioration of the nitrogen oxide storage catalyst 140 may be prevented in advance.

여기서, 탈황재생모드 주기보다 상기 촉매여과필터(110)를 재생하는 모드의 주기가 짧기 때문에 상기 촉매여과필터(110)에 포집된 황성분의 양이 작고 이에 따라 제거효율이 늘어날 뿐만 아니라 시간도 단축된다.Here, since the period of the mode for regenerating the catalyst filtration filter 110 is shorter than the desulfurization regeneration mode period, the amount of sulfur components collected in the catalyst filtration filter 110 is small, thereby increasing the removal efficiency and shortening the time. .

이상으로 본 발명에 관한 바람직한 실시예를 설명하였으나, 본 발명은 상기 실시예에 한정되지 아니하며, 본 발명의 실시예로부터 당해 발명이 속하는 기술분야에서 통상의 지식을 가진 자에 의한 용이하게 변경되어 균등하다고 인정되는 범위의 모든 변경을 포함한다. Although the preferred embodiments of the present invention have been described above, the present invention is not limited to the above embodiments, and easily changed and equalized by those skilled in the art from the embodiments of the present invention. It includes all changes to the extent deemed acceptable.

도 1은 본 발명의 실시예에 따른 배기가스 정화장치의 전체적인 구성도이다.1 is an overall configuration diagram of an exhaust gas purifying apparatus according to an embodiment of the present invention.

도 2는 본 발명의 실시예에 따른 배기가스 정화장치에서 촉매여과필터에 코팅되는 워시코트에 포함되는 성분을 나타내는 표이다.Figure 2 is a table showing the components included in the washcoat coated on the catalyst filter in the exhaust gas purifying apparatus according to an embodiment of the present invention.

도 3은 본 발명의 실시예에 따른 배기가스 정화장치의 작동 원리를 도시한 순서도이다.3 is a flow chart showing the operating principle of the exhaust gas purifying apparatus according to the embodiment of the present invention.

도 4는 일반적인 질소산화물 흡장촉매의 황산화물 피독 상태를 도시한 그래프이다.Figure 4 is a graph showing the sulfur oxide poisoning state of a typical nitrogen oxide storage catalyst.

<도면의 주요부분에 대한 부호의 설명><Description of the symbols for the main parts of the drawings>

100: 엔진100: engine

110: 촉매여과필터110: catalytic filtration filter

120: 포스트 인젝터120: post injector

130: 디젤연료 분해촉매130: diesel fuel decomposition catalyst

140: 질소산화물 흡장촉매140: nitrogen oxide storage catalyst

150: 머플러150: muffler

Claims (8)

배기가스에 포함된 매연(soot)이나 입자상 물질(PM)을 포집하는 촉매여과필터(CPF); 및A catalytic filtration filter (CPF) for collecting soot or particulate matter (PM) contained in exhaust gas; And 상기 촉매여과필터 후단에 설치되어 질소산화물을 흡장하는 질소산화물 흡장촉매(LNT)를 포함하고,A nitrogen oxide storage catalyst (LNT) installed at a rear end of the catalyst filtration filter to occlude nitrogen oxides, 상기 촉매여과필터에는 황산화물(SOx)를 포집하기 위한 알칼리 금속 또는 알칼리 토금속 중 적어도 하나의 성분이 포함된 것을 특징으로 하는 배기가스 정화장치.The catalytic filter is an exhaust gas purification device, characterized in that at least one component of the alkali metal or alkaline earth metal for trapping sulfur oxides (SOx). 제1 항에 있어서,According to claim 1, 상기 알칼리 금속 또는 알칼리 토금속은 워시코트에 섞여 상기 촉매여과필터에 코팅되어 형성되는 배기가스 정화장치.And the alkali metal or alkaline earth metal is mixed with a wash coat and coated on the catalyst filtration filter. 제1 항에 있어서,According to claim 1, 상기 알칼리 금속 또는 알칼리 토금속에 의해서 상기 촉매여과필터에 포집된 황산화물은, 상기 촉매여과필터 재생시 설정온도 이상에서 분리되어 제거되는 것을 특징으로 하는 배기가스 정화장치.The sulfur oxide trapped in the catalyst filter by the alkali metal or alkaline earth metal is separated and removed at a temperature higher than a predetermined temperature during regeneration of the catalyst filter. 제3 항에 있어서,The method of claim 3, 상기 설정온도는 섭씨 600도 내지 800도의 범위 내에 포함되는 것을 특징으로 하는 배기가스 정화장치.The set temperature is an exhaust gas purification device, characterized in that included in the range of 600 to 800 degrees Celsius. 제4 항에 있어서,The method of claim 4, wherein 상기 촉매여과필터의 재생은 주행거리 기준으로 500km 내지 1000km 주기로 재생되는 배기가스 정화장치.Regeneration of the catalyst filter is an exhaust gas purification device that is regenerated at a cycle of 500km to 1000km based on the driving distance. 제4 항에 있어서,The method of claim 4, wherein 상기 촉매여과필터 재생시 상기 촉매여과필터 후단에 설치된 상기 질소산화물 흡장촉매의 온도는 섭씨 500도 내지 550도의 범위에 포함되어 상기 촉매여과필터에서 분리된 황산화물은 상기 질소산화물 흡장촉매에 흡장되지 않고 통과하여 외기로 배출되어 제거되는 것을 특징으로 하는 배기가스 정화장치.When the catalyst filtration filter is regenerated, the temperature of the nitrogen oxide storage catalyst installed at the rear end of the catalyst filtration filter is in the range of 500 ° C to 550 ° C so that the sulfur oxide separated from the catalyst filtration filter is not occluded in the nitrogen oxide storage catalyst. Exhaust gas purification apparatus characterized in that the discharge to the outside to pass through. 제1 항에 있어서,According to claim 1, 상기 질소산화물 흡장촉매 전단에 장착되고 후분사된 원료를 이용하여 환원제를 생성시키는 디젤연료 분해촉매(DFC)를 포함하고,It includes a diesel fuel decomposition catalyst (DFC) for producing a reducing agent by using a raw material that is mounted to the front of the nitrogen oxide storage catalyst and post-injected, 상기 질소산화물 흡장촉매는 상기 환원제를 이용하여 질소산화물을 흡장하는 것을 특징으로 하는 배기가스 정화장치.The nitrogen oxide storage catalyst is an exhaust gas purification apparatus, characterized in that for storing the nitrogen oxide using the reducing agent. 제7 항에 있어서,The method of claim 7, wherein 상기 디젤연료 분해촉매(DFC) 전단에 연료를 후분사하는 포스트 인젝터가 배치되는 배기가스 정화장치.And a post injector for post-injecting fuel in front of the diesel fuel decomposition catalyst (DFC).
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