TWI504843B - Apparatus and method for treating exhaust gas from vehicle - Google Patents
Apparatus and method for treating exhaust gas from vehicle Download PDFInfo
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Description
本發明是有關於一種廢氣處理裝置及廢氣處理方法,且特別是有關於一種載具廢氣處理裝置及其處理方法。The present invention relates to an exhaust gas treatment device and an exhaust gas treatment method, and more particularly to a carrier exhaust gas treatment device and a treatment method therefor.
引擎運轉所排放的氣體中,造成空氣污染的主要成分例如是微粒物質、氮氧化物、碳氫化合物、一氧化碳等等。其中,氮氧化物在大氣中會氧化形成屬於有毒氣體的二氧化氮,不但影響視線,還會誘發呼吸方面的疾病並對肺部造成傷害。因此,世界各國對於廢氣中氮氧化物的含量愈來愈重視,而相關的排放標準也愈趨嚴格。Among the gases emitted by the operation of the engine, the main components causing air pollution are, for example, particulate matter, nitrogen oxides, hydrocarbons, carbon monoxide, and the like. Among them, nitrogen oxides will oxidize in the atmosphere to form nitrogen dioxide, which is a toxic gas, which not only affects the line of sight, but also induces respiratory diseases and causes damage to the lungs. Therefore, countries around the world are paying more and more attention to the content of nitrogen oxides in exhaust gas, and the relevant emission standards are becoming stricter.
目前用以控制氮氧化物的方式有很多種,例如廢氣再循環系統、選擇性還原觸媒系統、噴水降溫等,而其中又以選擇性還原觸媒系統最具成效。典型的選擇性還原觸媒系統,主要是利用氨氣或尿素水與氮氧化物進行化學反應,藉以使氮氧化物還原成無毒的氮氣及水。而相較於具有毒性的純氨氣,尿素水不但無毒又具有較高的穩定性,且容易儲存及運送。是以,選擇性還原觸媒系統一般多採用尿素水作為反應物。At present, there are many ways to control nitrogen oxides, such as exhaust gas recirculation system, selective reduction catalyst system, water spray cooling, etc., and the selective reduction catalyst system is most effective. A typical selective reduction catalyst system mainly uses ammonia or urea water to chemically react with nitrogen oxides to reduce nitrogen oxides to non-toxic nitrogen and water. Compared with toxic pure ammonia, urea water is not only non-toxic but also highly stable, and easy to store and transport. Therefore, urea selective water is generally used as a reactant in the selective reduction catalyst system.
只是,過去採用尿素水的選擇性還原觸媒系統僅以壓縮空氣輔助尿素水霧化,而這樣的方式不但需耗費額外的能量,也增加空壓機的負擔,更甚者還會連帶地影響煞車與離合器系統的作動。其次,壓縮空氣會降低系統的工作溫度,不但可能誘使預期外的反應發生,進而生成二次污染的產物,也會大大地降低氮氧化物的轉化效率。再者,系統中殘留在噴霧器噴孔及周邊上的尿素水,往往會因為高溫而瞬間蒸發形成結晶,同樣會影響氮氧化物的轉化效率。However, in the past, the selective reduction catalyst system using urea water only assisted the urea water atomization with compressed air, and this method not only requires additional energy, but also increases the burden of the air compressor, and even more affects it. Brake and clutch system actuation. Secondly, compressed air will lower the operating temperature of the system, which may not only induce the expected reaction, but also produce secondary pollution products, which will greatly reduce the conversion efficiency of nitrogen oxides. Furthermore, the urea water remaining in the spray nozzle hole and the periphery of the system tends to evaporate instantaneously due to high temperature to form crystals, which also affects the conversion efficiency of nitrogen oxides.
因此,本發明之一態樣是在提供一種載具廢氣處理裝置,藉由引流管將廢氣通道內的局部廢氣引入混合腔內,可有效預熱還原劑並提升混合效果,進而提高氮氧化物的轉化效率。Therefore, in one aspect of the present invention, a carrier exhaust gas treatment device is provided, wherein a local exhaust gas in an exhaust passage is introduced into a mixing chamber by a drain pipe, thereby effectively preheating the reducing agent and improving the mixing effect, thereby increasing nitrogen oxides. Conversion efficiency.
其次,本發明之另一態樣是在提供一種載具廢氣處理方法,藉由將廢氣通道內的廢氣局部引入混合腔內,同時感測廢氣通道內的廢氣溫度以適時啟動冷卻單元,一方面可有效預熱還原劑並提升混合效果,進而提高氮氧化物的轉化效率,另一方面亦可防止還原劑結晶的沉積物產生,且能適時降低混合腔與噴嘴溫度並減少傳統的空氣使用量,進而達成主動式的熱管理。Secondly, another aspect of the present invention provides a method for treating an exhaust gas of a vehicle by locally introducing the exhaust gas in the exhaust passage into the mixing chamber while sensing the temperature of the exhaust gas in the exhaust passage to start the cooling unit in a timely manner. It can effectively preheat the reducing agent and enhance the mixing effect, thereby improving the conversion efficiency of nitrogen oxides. On the other hand, it can prevent the precipitation of crystals of the reducing agent, and can reduce the mixing chamber and nozzle temperature and reduce the traditional air usage. In order to achieve active thermal management.
依據本發明結構態樣之一實施方式,提出一種載具廢氣處理裝置,包含一廢氣通道、一混合腔、一噴嘴以及一還原劑儲槽。廢氣通道包含一引流管,且引流管具有一第一端與一第二端。混合腔連通廢氣通道,而噴嘴設置在混合腔的一端部,還原劑儲槽則連接噴嘴。其中,引流管的第一端 連接廢氣通道,而引流管的第二端連接混合腔的端部,且第一端的口徑大於第二端的口徑。According to an embodiment of the structural aspect of the present invention, a carrier exhaust gas treatment device is provided, comprising an exhaust gas passage, a mixing chamber, a nozzle and a reducing agent storage tank. The exhaust passage includes a drainage tube, and the drainage tube has a first end and a second end. The mixing chamber communicates with the exhaust passage, and the nozzle is disposed at one end of the mixing chamber, and the reducing agent reservoir is connected to the nozzle. Wherein the first end of the drainage tube The exhaust passage is connected, and the second end of the drain pipe is connected to the end of the mixing chamber, and the diameter of the first end is larger than the diameter of the second end.
依據本發明結構態樣之一實施例,第一端的口徑與第二端的口徑的比值可為1.5至3。引流管與混合腔間可具有一夾角,且夾角可為110度至135度。第二端可設置在混合腔的側壁上而連接混合腔的端部,且第二端可與混合腔的內壁相切。噴嘴可與混合腔正交,且噴嘴可具有一表面抗水鍍層。According to an embodiment of the structural aspect of the present invention, the ratio of the diameter of the first end to the diameter of the second end may be 1.5 to 3. The drainage tube and the mixing chamber may have an angle, and the angle may be 110 to 135 degrees. The second end may be disposed on the side wall of the mixing chamber to connect the end of the mixing chamber, and the second end may be tangent to the inner wall of the mixing chamber. The nozzle can be orthogonal to the mixing chamber and the nozzle can have a surface water resistant coating.
依據本發明結構態樣之另一實施方式,提出一種載具廢氣處理裝置,包含一廢氣通道、一混合腔、一溫度感測器、一噴嘴、一冷卻單元以及一還原劑儲槽。廢氣通道包含一引流管,且引流管具有一第一端與一第二端。混合腔連通廢氣通道,溫度感測器則感測廢氣通道內之溫度。冷卻單元連設於混合腔上,噴嘴設置在混合腔的一端部,而還原劑儲槽則連接噴嘴。其中,引流管的第一端連接廢氣通道,而引流管的第二端連接混合腔的端部,且冷卻單元受控於溫度感測器。藉此,載具廢氣處理裝置尚能在廢氣溫度高於還原劑結晶溫度時,適時通入冷空氣、水霧或進行熱交換,除能有效防止還原劑結晶的沉積物產生,還可降低混合腔與噴嘴溫度並減少傳統的空氣使用量。According to another embodiment of the structural aspect of the present invention, a carrier exhaust gas treatment device is provided, comprising an exhaust gas passage, a mixing chamber, a temperature sensor, a nozzle, a cooling unit, and a reducing agent storage tank. The exhaust passage includes a drainage tube, and the drainage tube has a first end and a second end. The mixing chamber communicates with the exhaust passage and the temperature sensor senses the temperature within the exhaust passage. The cooling unit is connected to the mixing chamber, the nozzle is disposed at one end of the mixing chamber, and the reducing agent reservoir is connected to the nozzle. Wherein, the first end of the drainage tube is connected to the exhaust passage, and the second end of the drainage tube is connected to the end of the mixing chamber, and the cooling unit is controlled by the temperature sensor. Thereby, the vehicle exhaust gas treatment device can also pass cold air, water mist or heat exchange when the exhaust gas temperature is higher than the reductant crystallization temperature, in addition to effectively preventing the deposition of the reductant crystallized deposit, and also reducing the mixing. Cavity and nozzle temperatures and reduce traditional air usage.
依據本發明結構態樣之另一實施例,第一端的口徑可大於第二端的口徑,且第一端的口徑與第二端的口徑的比值可為1.5至3。引流管與混合腔間可具有一夾角,且夾角可為110度至135度。第二端可設置在混合腔的側壁上而連接混合腔的端部,且第二端可與混合腔的內壁相切。噴嘴可與混合腔正交,且噴嘴可具有一表面抗水鍍層。According to another embodiment of the structural aspect of the present invention, the diameter of the first end may be larger than the diameter of the second end, and the ratio of the diameter of the first end to the diameter of the second end may be 1.5 to 3. The drainage tube and the mixing chamber may have an angle, and the angle may be 110 to 135 degrees. The second end may be disposed on the side wall of the mixing chamber to connect the end of the mixing chamber, and the second end may be tangent to the inner wall of the mixing chamber. The nozzle can be orthogonal to the mixing chamber and the nozzle can have a surface water resistant coating.
依據本發明方法態樣之一實施方式,提出一種載具廢氣處理方法,包含將一廢氣通道內的一廢氣藉一引流管局部引入一混合腔內,其中廢氣通道、引流管與混合腔形成一通路。將一還原劑注入混合腔內。感測廢氣通道內之廢氣的溫度,且當廢氣通道內之廢氣的溫度高於還原劑的結晶溫度時,啟動一冷卻單元使混合腔降溫。According to an embodiment of the method aspect of the present invention, a method for treating an exhaust gas of a vehicle is provided, which comprises introducing an exhaust gas in an exhaust gas passage into a mixing chamber by a drainage pipe, wherein the exhaust gas passage, the drainage pipe and the mixing chamber form a path. A reducing agent is injected into the mixing chamber. The temperature of the exhaust gas in the exhaust passage is sensed, and when the temperature of the exhaust gas in the exhaust passage is higher than the crystallization temperature of the reducing agent, a cooling unit is activated to cool the mixing chamber.
依據本發明方法態樣之一實施例,引流管可具有一第一端與一第二端,引流管的第一端可連接廢氣通道,引流管的第二端可連接混合腔,而第一端的口徑大於第二端的口徑,且第一端的口徑與第二端的口徑的比值可為1.5至3。引流管與混合腔間可具有一夾角,且夾角可為110度至135度。還原劑可以係以一噴嘴注入混合腔內,且噴嘴可具有一表面抗水鍍層。According to an embodiment of the method aspect of the present invention, the drainage tube may have a first end and a second end, the first end of the drainage tube may be connected to the exhaust passage, and the second end of the drainage tube may be connected to the mixing chamber, and the first The diameter of the end is larger than the diameter of the second end, and the ratio of the diameter of the first end to the diameter of the second end may be 1.5 to 3. The drainage tube and the mixing chamber may have an angle, and the angle may be 110 to 135 degrees. The reducing agent can be injected into the mixing chamber with a nozzle, and the nozzle can have a surface water resistant coating.
100‧‧‧載具廢氣處理裝置100‧‧‧ Vehicle exhaust gas treatment device
110‧‧‧廢氣通道110‧‧‧Exhaust passage
111‧‧‧引流管111‧‧‧Drainage tube
111a‧‧‧第一端111a‧‧‧ first end
111b‧‧‧第二端111b‧‧‧second end
120‧‧‧混合腔120‧‧‧Mixed cavity
120a‧‧‧端部120a‧‧‧End
130‧‧‧噴嘴130‧‧‧Nozzles
131‧‧‧表面抗水鍍層131‧‧‧Surface water resistant coating
140‧‧‧還原劑儲槽140‧‧‧Reducing agent storage tank
150‧‧‧溫度感測器150‧‧‧temperature sensor
160‧‧‧冷卻單元160‧‧‧Cooling unit
510、520、530‧‧‧步驟510, 520, 530‧ ‧ steps
Da 、Db ‧‧‧口徑D a , D b ‧‧‧ caliber
α ‧‧‧夾角 α ‧‧‧ angle
Q1 、Q2 ‧‧‧流量Q 1 , Q 2 ‧‧‧ flow
第1圖係繪示依照本發明一實施方式的一種載具廢氣處理裝置的示意圖。1 is a schematic view showing a vehicle exhaust gas treatment device according to an embodiment of the present invention.
第2圖係繪示第1圖之載具廢氣處理裝置的局部俯視示意圖。Fig. 2 is a partial plan view showing the vehicle exhaust gas treatment device of Fig. 1.
第3圖係繪示第1圖之載具廢氣處理裝置之噴嘴的示意圖。Fig. 3 is a schematic view showing the nozzle of the vehicle exhaust gas treating device of Fig. 1.
第4圖係繪示依照本發明另一實施方式的一種載具廢氣處理裝置的示意圖。4 is a schematic view showing a carrier exhaust gas treatment device according to another embodiment of the present invention.
第5圖係繪示依照本發明一實施方式的一種載具廢氣處理方法的流程圖。FIG. 5 is a flow chart showing a method for treating an exhaust gas of a vehicle according to an embodiment of the present invention.
請參照第1圖,其繪示依照本發明一實施方式的一種載具廢氣處理裝置100的示意圖。請一併參照第2及3圖,其分別繪示第1圖之載具廢氣處理裝置100的局部俯視示意圖以及噴嘴130的示意圖。如圖所示,載具廢氣處理裝置100包含一廢氣通道110、一混合腔120、一噴嘴130、一還原劑儲槽140、一溫度感測器150以及一冷卻單元160。廢氣通道110包含一引流管111,且引流管111具有一第一端111a與一第二端111b。Please refer to FIG. 1 , which illustrates a schematic diagram of a vehicle exhaust gas treatment device 100 in accordance with an embodiment of the present invention. Referring to FIGS. 2 and 3 together, a partial plan view of the vehicle exhaust gas treatment device 100 of FIG. 1 and a schematic view of the nozzle 130 are respectively shown. As shown, the vehicle exhaust gas treatment device 100 includes an exhaust gas passage 110, a mixing chamber 120, a nozzle 130, a reducing agent reservoir 140, a temperature sensor 150, and a cooling unit 160. The exhaust passage 110 includes a drain tube 111, and the drain tube 111 has a first end 111a and a second end 111b.
引流管111的第一端111a連接廢氣通道110,而引流管111的第二端111b設置在混合腔120的側壁上而連接混合腔120的一端部120a,且引流管111與混合腔120之間具有一夾角α。更具體而言,引流管111的第二端111b與混合腔120的內壁相切(如第2圖所示),且夾角α可為110度至135度。The first end 111a of the drainage tube 111 is connected to the exhaust gas passage 110, and the second end 111b of the drainage tube 111 is disposed on the side wall of the mixing chamber 120 to connect the one end portion 120a of the mixing chamber 120, and between the drainage tube 111 and the mixing chamber 120. It has an angle α. More specifically, the second end 111b of the draft tube 111 is tangent to the inner wall of the mixing chamber 120 (as shown in FIG. 2), and the angle α may be 110 degrees to 135 degrees.
另一方面,混合腔120的底部與廢氣通道110連通,且溫度感測器150用以感測廢氣通道110內的溫度。冷卻單元160連設於混合腔120上,噴嘴130以正交於混合腔120的形式設置在混合腔120的端部120a,還原劑儲槽140則連接噴嘴130。更具體而言,溫度感測器150所設置的位置不限,只要能感測廢氣通道110內的溫度並能直接或間接控制冷卻單元160的啟閉即可,所謂間接控制例如是藉由一中央控制器。冷卻單元160可以是空氣泵、水霧器、風扇或熱交換器等,而所謂冷卻單元160連設於混合腔120上,舉例而言,當冷卻單元160為空氣泵或水霧器時,其可直接設置在混合腔120上或間接經噴嘴130而與混合腔120連接,只 要能將冷空氣注入混合腔120而使混合腔120降溫即可。當冷卻單元160為風扇或熱交換器時,其可直接設置在混合腔120的腔體上,只要能將混合腔120的熱能排出而使混合腔120降溫即可。此外,引流管111的第一端111a的口徑Da 大於第二端111b的口徑Db ,且噴嘴130具有一表面抗水鍍層131(如第3圖所示)。更具體而言,口徑Da 與口徑Db 的比值可為1.5至3。On the other hand, the bottom of the mixing chamber 120 is in communication with the exhaust passage 110, and the temperature sensor 150 is used to sense the temperature within the exhaust passage 110. The cooling unit 160 is connected to the mixing chamber 120. The nozzle 130 is disposed at the end 120a of the mixing chamber 120 in a form orthogonal to the mixing chamber 120, and the reducing agent reservoir 140 is connected to the nozzle 130. More specifically, the position of the temperature sensor 150 is not limited, as long as the temperature in the exhaust gas passage 110 can be sensed and the opening and closing of the cooling unit 160 can be directly or indirectly controlled, for example, the indirect control is performed by Central controller. The cooling unit 160 may be an air pump, a water mister, a fan or a heat exchanger, etc., and the so-called cooling unit 160 is connected to the mixing chamber 120, for example, when the cooling unit 160 is an air pump or a water mister, It can be directly disposed on the mixing chamber 120 or indirectly connected to the mixing chamber 120 via the nozzle 130, as long as the cold air can be injected into the mixing chamber 120 to cool the mixing chamber 120. When the cooling unit 160 is a fan or a heat exchanger, it can be directly disposed on the cavity of the mixing chamber 120, as long as the heat energy of the mixing chamber 120 can be discharged to cool the mixing chamber 120. Further, the diameter D a of the first end 111 a of the draft tube 111 is larger than the diameter D b of the second end 111 b , and the nozzle 130 has a surface water-resistant plating layer 131 (as shown in FIG. 3 ). More specifically, the ratio of the diameter D a to the diameter D b may be 1.5 to 3.
由於引流管111分別連接廢氣通道110與混合腔120,因此廢氣通道110內的廢氣可透過引流管111局部引入混合腔120內,進而能有效地預熱經噴嘴130噴入混合腔120內而霧化的還原劑,降低還原劑因未達工作溫度而導致轉化效率不佳的風險。其次,由於引流管111的第二端111b與混合腔120的內壁相切,因此廢氣經引流管111引入混合腔120時可形成一渦旋氣流,進而能有效地帶動經霧化的還原劑使其分布均勻。再者,由於混合腔120的底部與廢氣通道110連通,故廢氣通道110、引流管111與混合腔120三者可形成一通路,且因連接於廢氣通道110與混合腔120之間的引流管111自廢氣通道110朝混合腔120呈漸縮狀,因此流場強度與流場速度可因此獲得提升。Since the drainage tube 111 is connected to the exhaust passage 110 and the mixing chamber 120 respectively, the exhaust gas in the exhaust passage 110 can be partially introduced into the mixing chamber 120 through the drainage tube 111, thereby effectively preheating the mist sprayed into the mixing chamber 120 through the nozzle 130. The reducing agent reduces the risk of poor conversion efficiency of the reducing agent due to failure to reach operating temperature. Secondly, since the second end 111b of the draft tube 111 is tangent to the inner wall of the mixing chamber 120, the exhaust gas can be introduced into the mixing chamber 120 through the draft tube 111 to form a vortex flow, thereby effectively driving the atomized reducing agent. Make it evenly distributed. Moreover, since the bottom of the mixing chamber 120 is in communication with the exhaust passage 110, the exhaust passage 110, the draft tube 111 and the mixing chamber 120 can form a passage, and the drainage tube connected between the exhaust passage 110 and the mixing chamber 120 The 111 is tapered from the exhaust passage 110 toward the mixing chamber 120, so that the flow field strength and the flow field velocity can be improved.
另一方面,由於噴嘴130具有一表面抗水鍍層131,且引流管111與混合腔120間具有可形成渦旋氣流的配置,因此殘留於噴嘴130噴孔或噴孔周圍的還原劑液滴可被有效帶走,進而大大地減少殘留還原劑因高溫而瞬間蒸發所形成的結晶沉積物。此外,由於廢氣通道110內的溫度可透過溫度感測器150進行感測,且溫度感測器150能夠直接或間接控制冷卻單元160的啟閉,因此載具廢氣處理裝置100可 在廢氣溫度高於還原劑結晶溫度時,適時通入冷空氣、水霧或進行熱交換,不但能有效防止還原劑結晶的沉積物產生,還可降低噴嘴130溫度並減少傳統的空氣使用量。On the other hand, since the nozzle 130 has a surface water-resistant plating layer 131, and the draft tube 111 and the mixing chamber 120 have a configuration capable of forming a swirling airflow, the reducing agent droplet remaining around the nozzle hole or the nozzle hole of the nozzle 130 can be It is effectively carried away, thereby greatly reducing the crystal deposit formed by the instantaneous evaporation of the residual reducing agent due to high temperature. In addition, since the temperature in the exhaust passage 110 can be sensed by the temperature sensor 150, and the temperature sensor 150 can directly or indirectly control the opening and closing of the cooling unit 160, the carrier exhaust treatment device 100 can When the temperature of the exhaust gas is higher than the crystallization temperature of the reducing agent, timely introduction of cold air, water mist or heat exchange can not only effectively prevent the deposit of crystals of the reducing agent, but also reduce the temperature of the nozzle 130 and reduce the conventional air usage.
載具廢氣處理裝置100運作時,引流管111內具有一流量Q1 ,而在廢氣通道110、引流管111與混合腔120三者所形成的通路中,廢氣通道110內具有一流量Q2 。而本發明各實施例之引流管111的口徑Da 、口徑Db 、夾角α以及流量Q1 和流量Q2 的比分別如下表一所示。When the vehicle exhaust gas treatment device 100 is in operation, the flow conduit 111 has a flow rate Q 1 therein, and in the passage formed by the exhaust passage 110, the draft tube 111 and the mixing chamber 120, the exhaust passage 110 has a flow rate Q 2 therein. The ratios of the diameter D a , the diameter D b , the angle α , and the flow rate Q 1 and the flow rate Q 2 of the draft tube 111 according to each embodiment of the present invention are shown in Table 1 below.
請參照第4圖,其繪示依照本發明另一實施方式的一種載具廢氣處理裝置100的示意圖。如圖所示,載具廢氣處理裝置100包含一廢氣通道110、一混合腔120、一噴嘴130、一還原劑儲槽140、一溫度感測器150以及一冷卻單元160。廢氣通道110包含一引流管111,且引流管111具有一第一端111a與一第二端111b。載具廢氣處理裝置100除了引流管111的形狀與引流管111所設置的相對位置以外,其餘皆與前述實施方式相同。更具體而言,引流管111設置在廢氣通道110與混合腔120的內部,且引流管111以 第一端111a連接廢氣通道110,並以第二端111b連接混合腔120。據此,引流管111不會曝露於外,可減緩外在環境因素所造成的影響。Referring to FIG. 4, a schematic diagram of a vehicle exhaust gas treatment device 100 in accordance with another embodiment of the present invention is shown. As shown, the vehicle exhaust gas treatment device 100 includes an exhaust gas passage 110, a mixing chamber 120, a nozzle 130, a reducing agent reservoir 140, a temperature sensor 150, and a cooling unit 160. The exhaust passage 110 includes a drain tube 111, and the drain tube 111 has a first end 111a and a second end 111b. The carrier exhaust gas treatment device 100 is the same as the above-described embodiment except that the shape of the draft tube 111 and the relative position of the draft tube 111 are provided. More specifically, the draft tube 111 is disposed inside the exhaust passage 110 and the mixing chamber 120, and the drain tube 111 is The first end 111a is connected to the exhaust passage 110 and connected to the mixing chamber 120 at the second end 111b. Accordingly, the drainage tube 111 is not exposed, and the effects of external environmental factors can be mitigated.
請參照第5圖,其繪示依照本發明一實施方式的一種載具廢氣處理方法的流程圖。請一併參照第1圖。如圖所示,首先如步驟510,將一廢氣通道內的一廢氣藉一引流管局部引入一混合腔內,其中廢氣通道、引流管與混合腔形成一通路。接著如步驟520,將一還原劑注入混合腔內。之後如步驟530,感測廢氣通道內之廢氣的溫度,且當廢氣通道內之廢氣的溫度高於還原劑的結晶溫度時,啟動一冷卻單元使混合腔降溫。藉此,注入混合腔內的還原劑可有效地預熱,且混合腔內的混合效果可有效提升。除此之外,尚能防止還原劑結晶的沉積物產生,並降低噴嘴溫度以及減少傳統的空氣使用量。Referring to FIG. 5, a flow chart of a method for treating an exhaust gas of a vehicle according to an embodiment of the present invention is shown. Please refer to Figure 1 together. As shown in the figure, first, in step 510, an exhaust gas in an exhaust gas passage is partially introduced into a mixing chamber by a drain pipe, wherein the exhaust gas passage and the draft pipe form a passage with the mixing chamber. Next, as in step 520, a reducing agent is injected into the mixing chamber. Then, as step 530, the temperature of the exhaust gas in the exhaust passage is sensed, and when the temperature of the exhaust gas in the exhaust passage is higher than the crystallization temperature of the reducing agent, a cooling unit is activated to cool the mixing chamber. Thereby, the reducing agent injected into the mixing chamber can be effectively preheated, and the mixing effect in the mixing chamber can be effectively improved. In addition to this, it is possible to prevent deposits of crystals of the reducing agent, reduce the nozzle temperature and reduce the conventional air usage.
雖然本發明已以實施方式揭露如上,然其並非用以限定本發明,任何熟習此技藝者,在不脫離本發明之精神和範圍內,當可作各種之更動與潤飾,因此本發明之保護範圍當視後附之申請專利範圍所界定者為準。Although the present invention has been disclosed in the above embodiments, it is not intended to limit the present invention, and the present invention can be modified and modified without departing from the spirit and scope of the present invention. The scope is subject to the definition of the scope of the patent application attached.
100‧‧‧載具廢氣處理裝置100‧‧‧ Vehicle exhaust gas treatment device
110‧‧‧廢氣通道110‧‧‧Exhaust passage
111‧‧‧引流管111‧‧‧Drainage tube
111a‧‧‧第一端111a‧‧‧ first end
111b‧‧‧第二端111b‧‧‧second end
120‧‧‧混合腔120‧‧‧Mixed cavity
120a‧‧‧端部120a‧‧‧End
130‧‧‧噴嘴130‧‧‧Nozzles
140‧‧‧還原劑儲槽140‧‧‧Reducing agent storage tank
150‧‧‧溫度感測器150‧‧‧temperature sensor
160‧‧‧冷卻單元160‧‧‧Cooling unit
Da 、Db ‧‧‧口徑D a , D b ‧‧‧ caliber
α ‧‧‧夾角 α ‧‧‧ angle
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TW200804673A (en) * | 2006-05-16 | 2008-01-16 | Emitec Emissionstechnologie | Method and device for treating the exhaust gas of an internal combustion engine |
CN202289834U (en) * | 2011-10-28 | 2012-07-04 | 中能东讯新能源科技(大连)有限公司 | High-efficiency denitration device for circulating fluidized bed boiler |
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TW200804673A (en) * | 2006-05-16 | 2008-01-16 | Emitec Emissionstechnologie | Method and device for treating the exhaust gas of an internal combustion engine |
CN202289834U (en) * | 2011-10-28 | 2012-07-04 | 中能东讯新能源科技(大连)有限公司 | High-efficiency denitration device for circulating fluidized bed boiler |
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