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TWI237089B - Method of cleaning NOx for catalysts in a exhaust pipe of the motorcycle - Google Patents

Method of cleaning NOx for catalysts in a exhaust pipe of the motorcycle Download PDF

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Publication number
TWI237089B
TWI237089B TW93103170A TW93103170A TWI237089B TW I237089 B TWI237089 B TW I237089B TW 93103170 A TW93103170 A TW 93103170A TW 93103170 A TW93103170 A TW 93103170A TW I237089 B TWI237089 B TW I237089B
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Taiwan
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air
exhaust gas
exhaust
exhaust pipe
catalyst
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TW93103170A
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Chinese (zh)
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TW200526866A (en
Inventor
Wen-Shing Chang
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Sentec E & E Co Ltd
Sanyang Industry Co Ltd
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Priority to TW93103170A priority Critical patent/TWI237089B/en
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Publication of TW200526866A publication Critical patent/TW200526866A/en

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Abstract

A method of cleaning NOx for catalysts in an exhaust pipe of the motorcycle comprises a fore reduction catalyst is installed in the exhaust pipe near an engine, a re-sued air is conducted into the exhaust pipe at a rear end of the fore reduction catalyst, and a hind oxidation catalyst is installed in the exhaust pipe at a rear end of the re-used air guide position. Thereby, the waste gas with less oxygen containing in the exhausting end of the engine passes through the reduction catalyst with an air to fuel ratio smaller than or equal to 14.7 so as to increase the ability that the reduction catalyst to convert the NOx in the waste gas to a harmless N2 or O2. Then, O2 is guided into by the re-used air so that air to fuel ratio of the waste gas passing through the Oxidized catalyst is larger than 14.7. Thereby, the CO and HC in the waste gas can be converted into harmful CO2 and N2O so as to purify the waste gas exhausting from the motor engine.

Description

1237089 修正 _案號 93103170 五、發明說明(1) 【技術領域】 本發明在機車排氣管道内提昇觸媒淨化氮氧化物的方 法,特別是涉及一還原型觸媒、氧化型觸媒以及指定二次 空氣導入位置的配置技術,同時也包含運用此配置來約制 廢氣空燃比的技術應用。 【先前技術】 在本發明中所稱廢氣的空燃比(A / F ),即是指廢氣中 所含空氣(A i r ) 與燃油(F u e 1 )的混合比例。一般引擎 運作環境中最為理想的空燃比(A/F) 是控制在14. 7前後既 定範圍内(如圖一斜線區域所示),此表示引擎的運轉效率 愈佳,愈不易發生燃燒不完全現象,且利於引擎排氣管道 内的觸媒愈容易與廢氣中的有害物質進行氧化(Oxidation ) 及還原(Reduction) 反應。 坊間的機車,除了配置有引擎控制單元(£11忌丨116(]〇-ntrol Unit, ECU)及含氧感知器(02 Sensor)的引擎作 業環境,較能穩定的控制排放廢氣中的空燃比之外,並無 其他更有效的方法。且知,坊間較小排氣量的機車引擎基 於成本的考量,並沒有裝配含氧感知器的設計。這些未設 含氧感知器的機車引擎,較無法精確的控制並取得趨近於 1 4 · 7的廢氣空燃比值,以至於引擎運轉效率較為低落,燃 燒不完全生成有害廢氣的現象較為嚴重。 影響機車引擎淨化廢氣效率的原因,尚包括觸媒的裝 設技術與二次空氣導入位置等技術。坊間現階段的作法, 是將一只或一只以上披覆有鉑(Pt)、鈀(Pd)及铑(Rh)等貴1237089 Amendment_Case No. 93103170 V. Description of the Invention (1) [Technical Field] The present invention relates to a method for upgrading a catalyst to purify nitrogen oxides in an exhaust pipe of a locomotive, and particularly relates to a reduction catalyst, an oxidation catalyst, and a designation. The configuration technology of the secondary air introduction position also includes the technical application of using this configuration to control the air-fuel ratio of the exhaust gas. [Prior art] The air-fuel ratio (A / F) of the exhaust gas referred to in the present invention refers to the mixing ratio of the air (A i r) contained in the exhaust gas and the fuel (F u e 1). The most ideal air-fuel ratio (A / F) in the general engine operating environment is controlled within a predetermined range around 14.7 (as shown by the slanted area in Figure 1), which indicates that the better the engine's operating efficiency, the less likely it is that combustion will be incomplete. Phenomenon, and the catalyst in the exhaust pipe of the engine is more likely to react with harmful substances in the exhaust gas (Oxidation) and reduction (Reduction) reactions. The locomotive in the field, except for the engine operating environment equipped with an engine control unit (£ 11, 116 (] 〇-ntrol Unit, ECU) and an oxygen sensor (02 Sensor), can more stably control the air-fuel ratio in the exhaust gas. In addition, there is no other more effective method. Also, it is known that locomotive engines with smaller displacements based on cost considerations are not equipped with oxygen sensors. These locomotive engines without oxygen sensors are relatively The exhaust air-fuel ratio approaching 1 4 · 7 cannot be accurately controlled, so that the engine operating efficiency is relatively low, and the phenomenon of incomplete combustion generating harmful exhaust gas is more serious. The reasons affecting the efficiency of locomotive engine purification exhaust gas include Media installation technology and secondary air introduction position, etc. The current practice in the workshop is to coat one or more of the precious metals such as platinum (Pt), palladium (Pd), and rhodium (Rh).

第5頁 1237089 ^ . __案號 93103170 年 (^月6曰 修正_ 五、發明說明(2) 金屬的金屬載體組設於排氣管道内,並在該觸媒載體之前 的機車引擎排氣管道内導入二次空氣。其中二次空氣可藉 機車引擎運轉時產生的間歇性負壓,將外界的新鮮空氣導 入排氣管道内,藉以補足廢氣中定量的氧氣(〇2),使廢氣 的空燃比大於1 4 . 7,藉以促進上述觸媒氧化一氧化碳(C 0 ) 與碳氫化合物(HC)的轉化效率。惟,由於廢氣中已增加了 氧氣(〇2)含量,迫使通過觸媒載體的廢氣空燃比無法小於 或等於14.7,同時因氧化反應時會生成高溫,如此一來, 將導致觸媒還原氮氧化物(NOx) 的轉化效率更為低落,以 至於排放至大氣中的氮氧化物(NOx) 含量只增不減,是造 成酸雨及破壞臭氧層的主因,影響自然環境甚鉅。 【内容】 本發明提昇觸媒淨化氮氧化物的方法,旨在維持原有 氧化型觸媒(Oxidation catalyst)淨化廢氣中一氧化碳( C0 )及碳氫化合物(HC )等有害物質的既有效力情況下, 再加提昇還原型觸媒(Reduction catalyst)淨化氮氧化物 .(NOx) 有害物質的能力為目的者。 為能達到上述目的,本發明的技術包括有下列步驟: 1 .利用引擎排氣端排出的有害廢氣中含氧量較少的特 性,而將至少一只還原型觸媒設置於引擎的前段排氣管道 内,接觸引擎排氣端導入含氧量不足的前段廢氣〔空燃比 (A/F)S14.7〕,以利於將氮氧化物(NOx) 還原成無害的 氮氣(N2)及氧(02);Page 5 1237089 ^. __Case No. 93103170 (^ January 6 amendment_ V. Description of the invention (2) The metal metal carrier is set in the exhaust pipe, and the locomotive engine exhaust before the catalyst carrier The secondary air is introduced into the pipeline. The secondary air can introduce the fresh air from the outside into the exhaust pipe by the intermittent negative pressure generated when the locomotive engine is running, so as to make up for a certain amount of oxygen in the exhaust gas (〇2), and The air-fuel ratio is greater than 14.7, which promotes the conversion efficiency of the above catalysts to oxidize carbon monoxide (C 0) and hydrocarbons (HC). However, since the oxygen (〇2) content has been increased in the exhaust gas, it is forced to pass through the catalyst carrier The air-fuel ratio of the exhaust gas cannot be less than or equal to 14.7. At the same time, high temperatures are generated during the oxidation reaction. As a result, the conversion efficiency of the catalyst to reduce nitrogen oxides (NOx) is even lower, so that the nitrogen oxides emitted into the atmosphere are oxidized. The content of NOx is only increasing, which is the main cause of acid rain and damage to the ozone layer, which has a great impact on the natural environment. [Content] The method for improving the catalyst for purifying nitrogen oxides aims to maintain the original oxygen Oxidation catalyst is used to purify harmful substances such as carbon monoxide (C0) and hydrocarbons (HC) in the exhaust gas, and then a reduction catalyst is used to purify nitrogen oxides. (NOx To achieve the above purpose, the technology of the present invention includes the following steps: 1. Utilize the characteristic of less oxygen content in the harmful exhaust gas exhausted from the exhaust end of the engine, and reduce at least one Type catalyst is installed in the front exhaust pipe of the engine, and the front exhaust gas with insufficient oxygen content [air-fuel ratio (A / F) S14.7] is introduced into the exhaust end of the engine to facilitate the reduction of nitrogen oxides (NOx) to Harmless nitrogen (N2) and oxygen (02);

第6頁 1237089 __案號 93103170 五、發明說明(3) 修正 2 ·利用引擎負壓或電動果作為動力源,將二次空氣導 入上述還原型觸媒後方的排氣管道内,供給定量的氧氣, 使後段廢氣的空燃比(A/F)>14.7 ; 3 ·將至少一只氧化型觸媒設置於上述二次空氣導入位 置後方的排氣管道内,接觸空燃比(A / F )> 1 4 . 7的後段廢氣 ,以利於將一氧化碳(CO)與碳氫化合物(HC)氧化成無害的 二氧化碳(C02) 及水(H20) ’並排放至外界。 然而,為能再加詳述本發明,玆配合圖式詳細說明如 后: 【實施方法】 首觀圖二所示,係揭示出將本發明實施於一機車排氣 管上的配置示意圖,包括有下列架構内容: 在一鄰近引擎排氣端1的排氣管道1 〇内設置至少一只前段 的還原型觸媒(Reduction catalyst)2 。此還原型觸媒2 在實施上是利用一金屬或陶瓷載體内彼覆至少含有鍵金( Rh)成份的貴金屬所製成,用以轉化來自引擎排氣端1載 入還原型觸媒2内的前段廢氣1 2。此外,該還原型觸媒2 的貴金屬成份,在實施上亦可是由姥(Rh)、始(Pt)及把 (Pd)等組成的三元觸媒(Three—way catalyst)。 在上述設置還原塑觸媒2後方的排氣管道11内開設出 一個二次空氣導入口 14 ’用以導入二次空氣。當還原型 觸媒2為設置一只以上時’該二次空氣導入口 1 4的位置位 在最末一只還原型觸媒2的後方° 並在二次空氣導入口 14位置後方的排氣管道11内設置Page 6 1237089 __Case No. 93103170 V. Description of the invention (3) Amendment 2 · Use the negative pressure of the engine or electric fruit as the power source to introduce the secondary air into the exhaust pipe behind the reduction catalyst and supply a fixed amount of Oxygen to make the air-fuel ratio (A / F) of the exhaust gas at the rear stage> 14.7; 3 · At least one oxidation catalyst is set in the exhaust pipe behind the above-mentioned secondary air introduction position and contacts the air-fuel ratio (A / F) > The rear exhaust gas of 14.7 is beneficial to oxidize carbon monoxide (CO) and hydrocarbons (HC) into harmless carbon dioxide (C02) and water (H20) 'and discharge them to the outside world. However, in order to further elaborate the present invention, the detailed description is given below in conjunction with the drawings: [Implementation method] Firstly, as shown in FIG. 2, it is a schematic diagram of a configuration for implementing the present invention on an exhaust pipe of a locomotive, including The following structural contents are provided: At least one front-stage reduction catalyst (Reduction catalyst) 2 is provided in an exhaust pipe 10 adjacent to the exhaust end 1 of the engine. This reduction type catalyst 2 is implemented by using a metal or ceramic carrier covered with a precious metal containing at least a bond gold (Rh) component, which is used to convert the exhaust catalyst 1 from the engine into the reduction type catalyst 2 The front exhaust 1 2. In addition, the precious metal component of the reduced catalyst 2 can also be implemented as a three-way catalyst consisting of thorium (Rh), starting (Pt), and (Pd). A secondary air introduction port 14 'is provided in the exhaust duct 11 behind the above-mentioned reduction plastic catalyst 2 for introducing secondary air. When more than one reduction type catalyst 2 is provided, the position of the secondary air introduction port 14 is located behind the last reduction type catalyst 2 and exhausted behind the secondary air introduction port 14 Set in pipeline 11

第7頁 1237089 Γ_案號93103Π0 年月/日 修正_ 五、發明說明(4) 後段的至少一只的氧化型觸媒(Oxidation catalyst)3 。 此氧化型觸媒3在實施上是利用一金屬或陶瓷載體内披覆 至少含有始(Pt)及Is(Pd)成份的貴金屬所製成,用以轉化 流通過還原型觸媒2的後段廢氣1 3。此外,氧化型觸媒3 的貴金屬成份,亦可是由铑(Rh)、鉑(Pt)及鈀(Pd)等組成 的三元觸媒(Three-way catalyst)。 在本發明上述架構中,自引擎排氣端1排入排氣管道 10内的前段廢氣12中含有多量的一氧化碳(C0)、碳氫化 合物(HC)、氮氧化物(NOx)等有害物質,以及因引擎内 未完全燃燒所殘留的氧氣(〇 2 ),所以前段廢氣1 2中的空燃 比是處於(A/F)S14.7的情況,也因此有利於依據排氣管 道1 〇内的廢氣流向,而規劃出實施本發明之下列步驟及方 法,包括: (1 )·進行還原反應;利用前段的還原型觸媒2淨化來 自引擎排氣端1排入排氣管道1 0内的前段廢氣1 2,使空燃 比(A/F)‘14.7之前段廢氣12中的氮氧化物(NOx)還原成 •無害的氮氣(N2) 及氧氣(02)。 上述步驟中,含有一氧化碳(co )、碳氫化合物(HC )'氮氧化物(NOx)等有害物質的前段廢氣12,在通過還 原型觸媒2中至少包含有主要成份的铑金(Rh)的轉化之後 ’因空燃比(A / F ) S 1 4 · 7 ,故僅剩下一氧化碳(C 0 )及碳 氫化合物(HC)等有害物質尚未被完全淨化,且因氮氧化 物(NOx)被還原時生成氧(〇2),為數雖然不多,但仍有助 於後段廢氣1 3進行氧化反應時的需求。Page 7 1237089 Γ_Case No. 93103Π0 Month / Day Amendment_ V. Description of the invention (4) At least one oxidation catalyst (3) in the latter stage. This oxidizing catalyst 3 is implemented by coating a metal or ceramic carrier with a precious metal containing at least the initial (Pt) and Is (Pd) components, and used to convert the exhaust gas flowing through the rear stage of the reducing catalyst 2 1 3. In addition, the precious metal component of the oxidation catalyst 3 may be a three-way catalyst consisting of rhodium (Rh), platinum (Pt), and palladium (Pd). In the above structure of the present invention, the front exhaust gas 12 discharged from the exhaust end 1 of the engine into the exhaust pipe 10 contains a large amount of harmful substances such as carbon monoxide (C0), hydrocarbons (HC), nitrogen oxides (NOx), And because the residual oxygen (0 2) is not completely combusted in the engine, the air-fuel ratio in the front stage exhaust gas 12 is at (A / F) S14.7, which is also conducive to the The exhaust gas flows, and the following steps and methods for implementing the present invention are planned, including: (1) · Performing a reduction reaction; using a reduction catalyst 2 at the front stage to purify the front stage discharged from the exhaust end 1 of the engine into the exhaust pipe 10 The exhaust gas 12 reduces nitrogen oxides (NOx) in the exhaust gas 12 before the air-fuel ratio (A / F) '14 .7 to harmless nitrogen (N2) and oxygen (02). In the above steps, the front-stage exhaust gas 12 containing harmful substances such as carbon monoxide (co), hydrocarbons (HC) 'nitrogen oxides (NOx), etc., contains at least a rhodium gold (Rh) as a main component in the reduction catalyst 2 After the conversion of 'due to the air-fuel ratio (A / F) S 1 4 · 7, only carbon monoxide (C 0) and hydrocarbons (HC) and other harmful substances have not been completely purified, and due to nitrogen oxides (NOx) Oxygen (〇2) is generated when it is reduced. Although not many, it still contributes to the demand for the oxidation reaction of the exhaust gas 13 in the subsequent stage.

第8頁 1237089Page 8 1237089

(2)·導入一次空氣;自外 原型觸媒2 後方的排氣管道j j 給氧氣(02)進入後段廢氣13中 比至(A/F)>14· 7 狀態。 上述步驟中,控制二次空 可採用引擎負壓作為動力源, 閥,並將該閥體裝設於引擎或 性的負壓吸力所作動,進而將 導入還原型觸媒2後方的排氣 次空氣導入量隨著引擎運轉速 可使得二次空氣導入量與排氣 高還原型觸媒2後方之排氣管 後段廢氣1 3的空燃比(A / F ) > 1 4 二次空氣的方式,亦可採用一 排氣管道1 1内。 界導入二次空氣15於上述還 内,以便隨引擎轉速定量供 ’以提高後段廢氣1 3的空燃 氣導入的方式,在實施上係 包括利用一只二次空氣控制 化油1§的負壓端’接受間歇 外界新鮮空氣(即二次空氣^ 管道11内。這種方式易使二 率的南低而增減,換言之, 置成正比關係’將有助於提 道10内廢氣的含氧量,即使 • 7(如圖三所示)。此外導入 電動果強制哪氣進入後方的 (3 )·進行氧化反應;利用後段的氧化型觸媒3淨化 自上述的後段廢氣13,使空燃比為(A/F)>14· 7之後段廢 13中殘留的一氧化石反(C0)及碳氫化合物(jjc)儘速氧4匕 成無害的二氧化碳(C02)及水(H20)。 上述步驟中,後段的氧化型觸媒3中至少含有主要成 份的始(P t)及把(P d )等貴金屬,能夠在後段廢氣丨3空燃比 (A / F )> 1 4 · 7的情況下發揮既有理想的轉化率。 上述(1 )至(3 )步驟的作法,將可有效提昇前段的還原 型觸媒2淨化氮氧化物(N 0 X )時的轉化率,同時也一併(2) Introduce the air once; from the exhaust pipe j j behind the external prototype catalyst 2, oxygen (02) is introduced into the exhaust gas 13 in the rear stage to the ratio (A / F) > 14.7. In the above steps, the secondary air can be controlled by using the negative pressure of the engine as the power source and the valve, and the valve body is installed in the engine or the negative pressure suction force is actuated, and then the exhaust gas behind the reduction catalyst 2 is introduced. The amount of air introduced with the speed of the engine can make the amount of secondary air introduced and the air-fuel ratio of the exhaust gas at the rear of the exhaust pipe 1 behind the high-reduction catalyst 2 (A / F) > 1 4 the method of secondary air It is also possible to use an exhaust pipe 11 inside. The secondary air 15 is introduced in the above-mentioned range so that the method of increasing the air-fuel introduction of the exhaust gas in the rear stage 13 with the engine speed is quantitatively implemented. The implementation includes the use of a secondary air to control the negative pressure of 1 § The pressure end 'receives intermittent fresh air outside (ie, secondary air ^ in the pipe 11. This method is easy to increase and decrease the second rate of the south, in other words, put in a proportional relationship' will help raise the content of exhaust gas in the channel 10. The amount of oxygen is even • 7 (as shown in Figure 3). In addition, the electric fruit is introduced to force which gas enters the rear (3). The oxidation reaction is carried out; the oxidation catalyst 3 at the rear stage is used to purify the exhaust gas 13 from the above stage to make the air The fuel ratio is (A / F) > The residual monoxide reverse (C0) and hydrocarbons (jjc) in the waste 13 after the stage 14 · 7 are quickly converted into harmless carbon dioxide (C02) and water (H20). In the above steps, the oxidation catalyst 3 in the latter stage contains at least the noble metals (P t) and (P d), which are the main components, and can be used in the exhaust gas in the latter stage. 3 Air-fuel ratio (A / F) > 1 4 · In the case of 7, the existing ideal conversion rate is exerted. The steps of (1) to (3) above will be It can effectively improve the conversion rate of the reduction catalyst 2 in the previous stage when purifying nitrogen oxides (N 0 X).

第9頁 1237089 y :_案號93103170 年(fi月β 修正_ 五、發明說明(6) 維持了後段之氧化型觸媒3 淨化一氧化碳(C 0 )與碳氫化 合物(H C )時的轉化率(如圖三所示),因此,確實足以達 提昇機車引擎的廢氣排放品質。 再者,本發明上述例舉的圖二實施方式,其中所指銜 接自引擎排氣端1 排放廢氣用的排氣管道10及11,也包含 於導引廢氣排放的消音室4 ;換言之,只要是將上述前段 的還原型觸媒2 、導入二次空氣1 5的位置以及後段的氧化 型觸媒3 ,依序設置在排氣管道1 0、1 1或消音室4 的隔板 4 1上(如圖二所示),即屬廢氣的排放流道之内,藉以進行 上述的還原及氧化反應者,均屬本發明所思及之應用,併 予陳明。 綜合上述實施例之說明,相信已詳加揭示本發明的技 術内容及其可供實施的高度利用性,但本發明之技術並不 局限於此,舉凡依據上述以及后述申請專利範圍等内容而 作出簡略修飾的等效技術均應隸屬於本發明之應用範疇, 並予陳明。Page 1237089 y: _Case No. 93103170 (Fi month β amendment_) V. Description of the invention (6) Maintained the oxidation catalyst in the latter stage 3 Conversion rate when purifying carbon monoxide (C 0) and hydrocarbons (HC) (As shown in Figure 3), therefore, it is indeed sufficient to improve the exhaust gas exhaust quality of the locomotive engine. Furthermore, the above-exemplified embodiment of FIG. 2 of the present invention, in which the exhaust gas connected to the exhaust end 1 of the engine is used for exhaust gas exhaustion. The gas ducts 10 and 11 are also included in the muffler chamber 4 that guides exhaust emission; in other words, as long as the above-mentioned reduction catalyst 2 at the previous stage, the position where the secondary air 15 is introduced, and the oxidation catalyst 3 at the rear stage, according to Sequentially arranged on the exhaust pipe 10, 11 or the baffle 41 of the anechoic chamber 4 (as shown in Figure 2), which is within the exhaust flow channel, and those who perform the above reduction and oxidation reactions are all It belongs to the application considered by the present invention, and it will be presented. Based on the description of the above embodiments, it is believed that the technical content of the present invention and the high usability that can be implemented are disclosed in detail, but the technology of the present invention is not limited to Therefore, based on the above and after Patents make brief contents scope of equivalents should be modified under the application scope of the present invention, and to Chen.

第10頁 1237089 修正 _案號 93103170 圖式簡單說明 【圖式簡單說明】 圖一:揭示一理想的轉化率與空燃比間的線形圖,說 明空燃比驅近於1 4. 7時可得到NOx 及CO與HC的最佳轉化率 圖 一 · 揭 示 出 本 發 明 在一排氣 管 道 内 的配 置 示 意 圖 1 說 明 具 有一 前 段 廢 氣 還 原型觸媒 導 入 二次 空 氣 位 置 後 段 廢 氣及 氧 化 型 觸 媒 之 間的運作 流 程 0 圖 三 · 揭 示 出 本 發 明 的轉化率 與 空 辦 比之 間 的 線 形 圖 說 明 當在 轉 化N Ox 時 前 段廢氣的 空 燃 比 ^14 • 7 以 及 在 轉 化C0 與HC 時 後 段 廢 氣 的 空燃比> 1 4 . 7的關連( 3 [ 圖 式 之元 件 代 表 符 號 ] 1- 引擎排氣 端 10 ^ 1 1 排氣管道 12 前段廢氣 13 後段廢氣 14 二次空氣 導 入 V 15 導入二次 空 氣 2- 還原型觸 媒 3- 氧化型觸 媒 4- 消音室 41 隔板Page 10 1237089 Amendment_Case No. 93103170 Simple illustration of the diagram [Simplified illustration of the diagram] Figure 1: Reveal a line chart between the ideal conversion rate and air-fuel ratio, showing that NOx can be obtained when the air-fuel ratio is close to 14.7. And the optimal conversion rates of CO and HC. Figure 1 · Reveals the layout diagram of an exhaust pipe of the present invention. 1 Explains that there is a front stage exhaust gas reduction catalyst introduced into the secondary air. Operation Process 0 Figure III. Reveals a line graph between the conversion rate and air-to-air ratio of the present invention illustrating the air-fuel ratio of the front exhaust gas when converting NOx ^ 14 • 7 and the air-fuel ratio of the rear exhaust gas when converting C0 and HC > 1 4. Reduced contact media 2- 3- 4- Oxidized contact media separator muffling chamber 41

第11頁Page 11

Claims (1)

1237089 案號 93103170 曰 修正 六、申請專利範圍 1. 一種在機車排氣管道内提昇觸媒淨化氮氧化物的方 法,係在引擎排氣端所銜接的排氣管道内配置有至少一只 前段的還原型觸媒及至少一只後段的氧化型觸媒,並將二 次空氣導入於排氣管道内,藉以進行下列步驟: (1 )·進行還原反應:利用至少披覆有铑金(Rh )之前段 的還原型觸媒淨化來自引擎排氣端排入排氣管道内的前段 廢氣,將空燃比(A/F) S 14. 7之前段廢氣中的氮氧化物(NO x)還原成無害的氮氣(N2)及氧氣(02); (2) .導入二次空氣:自外界導入二次空氣於上述還原 型觸媒後方的排氣管道内,供給足量氧氣(02)進入後段廢 氣中,以提高後段廢氣的空燃比至(A / F ) > 1 4 . 7 ; (3) .進行氧化反應:利用至少披覆有鉑(Pt)及鈀(Pd) 之後段的氧化型觸媒淨化來自上述的後段廢氣,將空燃比 為(A/F)>14. 7之後段廢氣中殘留的一氧化碳(C0 )及碳氫 化合物(HC )氧化成無害的二氧化碳(C02)及水(H20),並 排放上述廢氣至外界。 2. 如申請專利範圍第1 觸媒淨化氮氧化物的方法, 氣。 3. 如申請專利範圍第1 觸媒淨化氮氧化物的方法, 空氣。 4. 如申請專利範圍第1 觸媒淨化氮氧化物的方法, 項所述在機車排氣管道内提昇 其中係以引擎負壓導入二次空 項所述在機車排氣管道内提昇 其中係以電動泵強制導入二次 項所述在機車排氣管道内提昇 其中該排氣管道包含導引廢氣1237089 Case No. 93103170 Amendment VI. Application for Patent Scope 1. A method for upgrading catalysts to purify nitrogen oxides in the exhaust pipe of a locomotive. At least one front section of the exhaust pipe connected to the exhaust end of the engine is arranged. The reduction catalyst and at least one oxidation catalyst at the rear stage, and the secondary air is introduced into the exhaust pipe, so as to perform the following steps: (1) · reduction reaction: using at least rhodium gold (Rh) coating The reduction catalyst at the previous stage purifies the front stage exhaust gas discharged from the exhaust end of the engine into the exhaust duct, and reduces the nitrogen oxides (NO x) in the front stage exhaust gas of the air-fuel ratio (A / F) S 14. 7 to harmless Nitrogen (N2) and Oxygen (02); (2). Introduce secondary air: Introduce secondary air from the outside into the exhaust duct behind the reduction catalyst, and supply a sufficient amount of oxygen (02) into the rear exhaust gas. In order to increase the air-fuel ratio of the exhaust gas in the rear stage to (A / F) > 1 4. 7; Purify the exhaust gas from the above-mentioned rear stage and set the air-fuel ratio to (A / F) > 14.7 Residual carbon monoxide (C0) and hydrocarbons (HC) in the exhaust gas in the later stage are oxidized to harmless carbon dioxide (C02) and water (H20), and the above exhaust gas is discharged to the outside. 2. For example, the method for purifying nitrogen oxides in the first scope of the patent application, gas. 3. For the method of purifying nitrogen oxides in the scope of patent application No. 1 catalyst, air. 4. According to the method for purifying nitrogen oxides in the first catalyst range of the patent application, lifting in the exhaust pipe of the locomotive as described in the item is to introduce the secondary air with the negative pressure of the engine. The electric pump is forcibly introduced into the locomotive exhaust pipe as described in the second item, wherein the exhaust pipe contains the guided exhaust gas. 第12頁 '1237089 修正 ;_案號 93103170 六、申請專利範圍 排放的消音室。 inmPage 12 '1237089 Amendment; _ Case No. 93103170 Sixth, the scope of the patent application emissions anechoic chamber. inm
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