KR20020055630A - Urea-SCR SYSTEM CONTROLED WITH TEMPERATURE AND RPM - Google Patents
Urea-SCR SYSTEM CONTROLED WITH TEMPERATURE AND RPM Download PDFInfo
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- KR20020055630A KR20020055630A KR1020000084826A KR20000084826A KR20020055630A KR 20020055630 A KR20020055630 A KR 20020055630A KR 1020000084826 A KR1020000084826 A KR 1020000084826A KR 20000084826 A KR20000084826 A KR 20000084826A KR 20020055630 A KR20020055630 A KR 20020055630A
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/08—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
- F01N3/10—Exhaust 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
- F01N3/18—Exhaust 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
- F01N3/20—Exhaust 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
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/12—Improving ICE efficiencies
Abstract
Description
본 발명은 온도 rpm제어형 Urea-SCR 시스템에 관한 것으로, 보다 상세하게는, Pt/Al2O3촉매와 V2O5/TiO2촉매를 직렬로 연결시켜 촉매 활성영역을 확장시키고, 온도, rpm 데이터를 입력신호로 하여 요소 주입량을 조절함으로써 NOx/NH3의 비를 일정하게 조절할 수 있는 온도 rpm제어형 Urea-SCR 시스템에 관한 것이다.The present invention relates to a temperature rpm controlled Urea-SCR system, and more particularly, a Pt / Al2O3 catalyst and a V2O5 / TiO2 catalyst are connected in series to extend the catalytic active region, and the temperature and rpm data are input signals. The present invention relates to a temperature rpm controlled Urea-SCR system capable of constantly adjusting the ratio of NOx / NH3 by adjusting the injection amount.
자동차는 형태에 따라서 승용차나, 버스 및 트럭 등으로 분류하지만, 같은 차종이라도 사용하는 연료에 따라서 가솔린을 연료로 사용하는 가솔린 차량이나 디젤을 연료로 사용하는 디젤 차량 및 LPG(Liquefied Petroleum Gas)를 연료로 사용하는 LPG 차량으로 부르기도 한다.Although automobiles are classified into passenger cars, buses, and trucks according to their type, the same type of fuel is used for gasoline vehicles using gasoline as a fuel, diesel vehicles using diesel as a fuel, and LPG (Liquefied Petroleum Gas) as fuel. Also known as LPG vehicles.
이중에서, 디젤차량은 산소 과잉분위기에서 연소되므로 가솔린 엔진에 비해서 유해물질인 NOx의 발생량이 상당히 많고, 린번 분위기에서 연소되므로 NOx를 제거하기가 힘들다. 따라서, NOx제거기술로서 가장 활발히 개발이 진행되는 것이 Urea(요소)-SCR(Selective Catalytic Reduction)시스템이다. 이 Urea-SCR 시스템은 요소를 수용액 형태로 배기 가스라인에 공급하여 NOx와 NH2-CO-NH2(요소)를 반응시켜 NOx를 N2+O2로 변환시키는 방법이다.Among them, diesel vehicles are burned in an oxygen-exhaust atmosphere, so the generation of NOx, which is a harmful substance, is considerably higher than that of gasoline engines, and it is difficult to remove NOx since it is burned in a lean burn atmosphere. Therefore, the most active development of NOx removal technology is the Urea (urea) -SCR (Selective Catalytic Reduction) system. The Urea-SCR system supplies urea to an exhaust gas line in the form of an aqueous solution to react NOx with NH2-CO-NH2 (urea) to convert NOx to N2 + O2.
이러한 구성을 지닌 종래의 Urea-SCR 시스템에서는 Urea-SCR 촉매의 활성영역(온도)이 너무 좁아서 일정 온도범위에서만 요소의 공급시에 NOx를 제거할 수 있는 점과, NOx값을 실시간으로 읽을 수 있는 NOx 센서가 구비되어 있지 않기 때문에각 엔진마다 속도, rpm, 부하, 온도 등의 데이터를 일일이 맵핑(mapping)하여 데이터로 저장해야 하는 문제가 있다.In the conventional Urea-SCR system having such a configuration, the active area (temperature) of the Urea-SCR catalyst is so narrow that NOx can be removed during urea supply only within a certain temperature range, and the NOx value can be read in real time. Since the NOx sensor is not provided, data such as speed, rpm, load, temperature, and the like must be mapped and stored as data for each engine.
이와 같은 문제점을 해결하기 위한 본 발명은 촉매 활성영역을 확장시키고, 온도, rpm 데이터를 입력신호로 하여 요소 주입량을 조절함으로써 NOx/NH3의 비를 일정하게 조절하여 NOx의 발생을 최대한 억제할 수 있는 온도 rpm제어형 Urea-SCR 시스템을 제공하는데 그 목적이 있다.The present invention for solving this problem is to expand the catalytic active region, and by adjusting the urea injection amount by using the temperature, rpm data as an input signal to constantly adjust the ratio of NOx / NH3 to suppress the generation of NOx The purpose is to provide a temperature rpm controlled Urea-SCR system.
도 1은 본 발명에 따른 Urea-SCR 시스템을 보인 구성도,1 is a block diagram showing a Urea-SCR system according to the present invention,
도 2는 본 발명에 따른 Urea-SCR 시스템에서의 NOx정화율을 나타낸 그래프.Figure 2 is a graph showing the NOx purification rate in the Urea-SCR system according to the present invention.
[도면의 주요부분에 대한 부호의 설명][Explanation of symbols on the main parts of the drawings]
2:엔진 4;배기 다기관2: engine 4; exhaust manifold
10:촉매기 12,14:Pt/Al2O3촉매, V2O5/TiO2촉매10: Catalyst 12, 14: Pt / Al2O3 catalyst, V2O5 / TiO2 catalyst
16:열전대 20:인젝터16: Thermocouple 20: Injector
22:CPU 24:DAS22: CPU 24: DAS
26:증폭회로 30:요소탱크26: amplifier circuit 30: element tank
32:요소공급펌프 34:공기공급포트32: Urea supply pump 34: Air supply port
상술한 목적을 달성하기 위한 본 발명의 온도 rpm제어형 Urea-SCR 시스템은 엔진의 배기 매니폴드로부터 배기파이프를 통해 배출되는 배기가스 중의 유해물질을 정화하기 위한 촉매기와, 상기 배기파이프에 설치되어 에어공급포트를 통해 유입되는 공기에 의해서 요소를 분사하는 인젝터와, 요소탱크내의 요소를 상기 인젝터로 공급하는 요소공급펌프와, 상기 촉매기내의 온도를 측정하는 열전대와, 상기 열전대로부터의 입력신호에 의거하여 증폭회로를 거쳐 상기 인젝터에 요소주입 제어신호를 출력하는 CPU를 포함하는 Urea-SCR 시스템에 있어서, 상기 촉매기내에는 PtAl2O3촉매와 V2O5TiO2촉매를 직렬로 연결된 상태로 배치되어 있으며, 상기 CPU는 상기 열전대로부터 입력되는 온도 데이터와, 엔진 회전수센서로부터 입력되는 엔진의 rpm 데이터에 의거하여 상기 인젝터에 요소주입 제어신호를 출력하는 것을 특징으로 한다.Temperature rpm controlled type Urea-SCR system of the present invention for achieving the above object is a catalytic device for purifying the harmful substances in the exhaust gas exhausted from the exhaust manifold of the engine through the exhaust pipe, the air supply is installed in the exhaust pipe On the basis of the injector for injecting the urea by the air flowing through the port, the urea supply pump for supplying the urea in the urea tank to the injector, the thermocouple for measuring the temperature in the catalyst, and the input signal from the thermocouple In the Urea-SCR system including a CPU for outputting the urea injection control signal to the injector via an amplification circuit, a PtAl 2 O 3 catalyst and a V 2 O 5 TiO 2 catalyst are arranged in series in the catalyst, and the CPU is separated from the thermocouple. Based on the temperature data inputted and the rpm data of the engine inputted from the engine speed sensor, Characterized in that the element injection control signal to the injector.
이하, 첨부한 도면을 참조하여 본 발명의 바람직한 실시예에 따른 온도 rpm제어형 Urea-SCR 시스템에 대하여 상세히 설명한다.Hereinafter, a temperature rpm controlled Urea-SCR system according to a preferred embodiment of the present invention will be described in detail with reference to the accompanying drawings.
도 1은 본 발명에 따른 Urea-SCR 시스템을 보인 구성도이고, 도 2는 본 발명에 따른 Urea-SCR 시스템에서의 NOx정화율을 나타낸 그래프이다.1 is a block diagram showing a Urea-SCR system according to the present invention, Figure 2 is a graph showing the NOx purification rate in the Urea-SCR system according to the present invention.
먼저, 도 1에 도시된 바와 같이, Urea-SCR 시스템의 전체적인 구성을 보면, 엔진(2)의 배기 매니폴드(4)로부터 배기파이프(6)를 통해 배출되는 배기가스 중의 유해물질을 정화하기 위한 촉매기(10)와, 배기파이프(6)에 설치되어 에어공급포트(34)를 통해 유입되는 공기에 의해서 요소를 분사하는 인젝터(20)와, 요소탱크(30)내의 요소를 인젝터(20)로 공급하는 요소공급펌프(32)와, 촉매기(10)내의 온도를 측정하는 열전대(16)와, 열전대(16)로부터의 입력신호에 의거하여 증폭회로(26)를 거쳐 인젝터(20)에 요소주입 제어신호를 출력하는 CPU(22)를 구비하고 있다.First, as shown in FIG. 1, the overall configuration of the Urea-SCR system is used to purify harmful substances in the exhaust gas discharged from the exhaust manifold 4 of the engine 2 through the exhaust pipe 6. The injector 20, which is installed in the catalyst 10, the exhaust pipe 6, and injects urea by air flowing through the air supply port 34, and the urea in the urea tank 30, is injected into the injector 20. To the injector 20 via the urea supply pump 32 to be supplied to the reactor, the thermocouple 16 for measuring the temperature in the catalyst 10, and the amplification circuit 26 based on an input signal from the thermocouple 16. A CPU 22 for outputting an element injection control signal is provided.
여기에서, 촉매기(10)의 열전대(16)에서 감지한 온도값은 DAS(Data Acquisition System)로 입력되며, DAS(24)는 입력된 온도값을 CPU(제어유닛)(22)으로 전달한다. CPU(22)는 입력된 온도값에 의거하여 DAS(24)를 거쳐 증폭회로(26)에 요소주입 제어신호를 출력한다. 증폭회로(26)를 거치면서 증폭된 신호를 인젝터(20)로 공급되어 이를 듀티제어하게 되며, 인젝터(20)는 요소공급펌프(32)를 통해 요소탱크(30)로부터 유입된 요소를 배기파이프(6)로 분사하게 된다. 이렇게 주입된 요소는 NOx와 반응하여 이를 N2와 O2로 변환시키게 되며, 촉매기(10)를 거치면서 정화된 배기가스는 중간 배기파이프(18)를 통해 소음기로 공급된 다음, 엔드 파이프를 통해 대기중으로 배출된다.Here, the temperature value detected by the thermocouple 16 of the catalyst 10 is input to a data acquisition system (DAS), and the DAS 24 transmits the input temperature value to the CPU (control unit) 22. . The CPU 22 outputs the element injection control signal to the amplification circuit 26 via the DAS 24 based on the input temperature value. Through the amplification circuit 26, the amplified signal is supplied to the injector 20 to control the duty. The injector 20 exhausts the urea introduced from the urea tank 30 through the urea supply pump 32. To (6). The injected urea reacts with NOx and converts it into N2 and O2, and the purified exhaust gas passing through the catalyst 10 is supplied to the silencer through the intermediate exhaust pipe 18 and then to the atmosphere through the end pipe. Discharged to the air.
이러한 구성의 Urea-SCR 시스템에 있어서, 촉매 활성영역을 확장시키기 위한 방안으로, 본 발명의 바람직한 실시예에서는 NOx농도 대신에 온도를 읽어서 NOx값을 예측하는 방안을 예시하였다.In the Urea-SCR system having such a configuration, as a method for expanding the catalytic active region, a preferred embodiment of the present invention exemplifies a method of predicting the NOx value by reading the temperature instead of the NOx concentration.
4NO+4NH3+O2→4N2+6H2O4NO + 4NH3 + O2 → 4N2 + 6H2O
6NO+8NH3→7N2+9H2O를 고려하면,Considering 6NO + 8NH3 → 7N2 + 9H2O,
NOx/NH3는 대략 1:1이 적당하고, 엔진 rpm을 고려하면, 총 NOx량을 알 수 있다.Approximately 1: 1 is suitable for NOx / NH3, and considering the engine rpm, the total amount of NOx can be known.
즉, 초당 NOx량(ℓ/sec)은 다음의 수학식 1에 의해 얻을 수 있다.That is, the amount of NOx per second (l / sec) can be obtained by the following equation (1).
여기에서, rpm, 배기량은 운전조건 및 엔진의 사양에 따라 알 수 있는 값이고, NOx농도는 온도에 의해 대치될 수 있다.Here, rpm and displacement are known values depending on the operating conditions and the specifications of the engine, and the NOx concentration can be replaced by temperature.
따라서, 초당 NOx량(ℓ/sec)은 수학식 1에 의해서 계산되고 상기 화학식 1에서 요소와 초당 NOx량(ℓ/sec)을 고려하면, 적량적으로 반응에 참여하는 요소의 양을 계산할 수 있으며, 이를 바탕으로 요소 수용액을 공급할 수 있다.Therefore, the amount of NOx per second (ℓ / sec) is calculated by Equation 1 and considering the amount of urea and NOx per second (ℓ / sec) in the formula 1, it is possible to calculate the amount of urea participating in the reaction appropriately Based on this, an aqueous solution of urea can be supplied.
따라서, NOx농도 대신에, 촉매기(10)에 설치된 열전대(16)에서 온도값을 얻고 엔진 회전수센서로부터 엔진의 rpm값을 얻으면, 그때의 NOx량을 추측할 수 있으며, 이를 바탕으로 DAS에서 측정된 양에 의거하여 요소를 주입시키도록 한다.Therefore, instead of the NOx concentration, if the temperature value is obtained from the thermocouple 16 installed in the catalyst 10 and the rpm value of the engine from the engine speed sensor, the amount of NOx at that time can be estimated, and based on this, Inject urea based on the measured quantity.
이와 같이 주입된 요소 수용액은 촉매기(10)내의 Pt/Al2O3촉매(14)와 V2O5/TiO2촉매(12)를 지나면서 NOx와 반응하게 되어 NOx를 N2와 O2로 분해시킨다.The injected urea aqueous solution reacts with the NOx while passing through the Pt / Al2O3 catalyst 14 and the V2O5 / TiO2 catalyst 12 in the catalyst 10 to decompose NOx into N2 and O2.
이렇게 평가된 NOx 전환율을 도 2의 그래프에 나타내었다. 이 그래프는 엔진 rpm을 1500으로 고정시키고, 촉매 온도를 증가시키면서 얻은 것이다. 이 그래프에서 보면, 150∼400℃까지 넓은 영역에서 활성이 나타났고, 요소량과 NOx량의 조화가 잘 이루어짐으로써 높은 활성이 나타났다.The NOx conversion rate thus evaluated is shown in the graph of FIG. 2. This graph was obtained by fixing the engine rpm to 1500 and increasing the catalyst temperature. In this graph, activity was shown in a wide range from 150 to 400 ° C., and a high activity was shown by a good balance between urea and NOx.
즉, rpm과 촉매의 온도만으로 NOx저감을 위한 Urea-SCR 시스템의 구성이 가능하였으며, 우수한 성능을 나타내었다.That is, it was possible to configure the Urea-SCR system for reducing NOx only by rpm and catalyst temperature, and showed excellent performance.
이상으로 설명한 본 발명에 의하면, Pt/Al2O3촉매와 V2O5/TiO2촉매를 직렬로 연결시켜 촉매 활성영역을 확장시키고, 온도, rpm 데이터를 입력신호로 하여 요소 주입량을 조절함으로써 NOx/NH3의 비를 일정하게 조절하여 NOx의 발생을 최대한 억제할 수 있으며, 유해가스의 저감에 따라 환경오염을 줄일 수 있는 이점이 있다.According to the present invention described above, the Pt / Al2O3 catalyst and the V2O5 / TiO2 catalyst are connected in series to expand the catalyst active region, and the ratio of NOx / NH3 is fixed by adjusting the urea injection amount by using the temperature and rpm data as input signals. It is possible to suppress the generation of NOx as much as possible, and to reduce the environmental pollution according to the reduction of harmful gases.
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KR100999615B1 (en) * | 2007-12-14 | 2010-12-08 | 현대자동차주식회사 | System for control urea injection of selective catalytic reduction system on vehicle exhaust line and method thereof |
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Publication number | Priority date | Publication date | Assignee | Title |
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KR100867799B1 (en) * | 2007-06-07 | 2008-11-10 | 현대자동차주식회사 | Method for controlling engine of urea-scr vehicle |
US8359831B2 (en) | 2008-10-31 | 2013-01-29 | Ti Group Automotive Systems, L.L.C. | Reactant delivery for engine exhaust gas treatment |
US8875493B2 (en) | 2008-10-31 | 2014-11-04 | Ti Group Automotive Systems, L.L.C. | Reactant delivery for engine exhaust gas treatment |
CN109012175A (en) * | 2013-03-22 | 2018-12-18 | 日本碍子株式会社 | Reducing agent injection apparatus, emission-control equipment and waste gas processing method |
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