TWI803060B - A combustion furnace with the mixing device of fume - Google Patents
A combustion furnace with the mixing device of fume Download PDFInfo
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一種燃燒爐,特別是涉及一種具有煙氣混合裝置之燃燒爐。A combustion furnace, in particular to a combustion furnace with a flue gas mixing device.
目前國內汽電共生廠大多以燃煤鍋爐為主,鍋爐會產生硫氧化物、氮氧化物等空氣污染物,氮氧化物可能涉及酸雨、地面臭氧的形成,於現有氮氧化物排放控制技術,有低氮氧化物燃燒器(LNB)、分段燃燒(staged combustion)、再燃燒(reburning)、煙氣迴流法(FGR)、選擇性觸媒還原法(SCR),以及選擇性非觸媒還原法(SNCR)等,可用於減少氮氧化物的排放,因此如何在經濟可行的情況下,選取與組合最有利的控制技術,達到最大可能減少排放量仍是一大挑戰。At present, most domestic steam-electricity co-generation plants mainly use coal-fired boilers. Boilers will produce air pollutants such as sulfur oxides and nitrogen oxides. Nitrogen oxides may be related to the formation of acid rain and ground ozone. Compared with existing nitrogen oxide emission control technologies, There are low NOx burner (LNB), staged combustion, reburning, flue gas recirculation (FGR), selective catalytic reduction (SCR), and selective non-catalytic reduction Therefore, it is still a big challenge to select and combine the most favorable control technologies to achieve the greatest possible reduction in emissions under economically feasible conditions.
一般情況下,當燃燒反應達到化學平衡時,會產生多種主要和次要產物,若助燃物是空氣時,則會形成少量的氮氧化物(NOx),燃燒後的產物所形成的氧化數和溫度有關,例如: 將硫在空氣中燃燒,在溫度超過1540°C時,將會開始產生NOx,更高溫時的NOx更多,且NOx的量也會隨氧過量的比例而變。In general, when the combustion reaction reaches a chemical equilibrium, a variety of primary and secondary products will be produced. If the combustion aid is air, a small amount of nitrogen oxides (NOx) will be formed. The oxidation number and Temperature is related, for example: burning sulfur in air, when the temperature exceeds 1540°C, NOx will start to be produced, and the NOx will be more at higher temperatures, and the amount of NOx will also change with the proportion of excess oxygen.
氮氧化物在大氣中種類有很多,其中以NO與NO2對大氣汙染最有影響,NO的極小部分在爐內會成為NO2,而NO2有很強的毒性,該些總括稱為NOx,有鑒於環保意識的抬頭,政府為了降低其NOx排放值,而將其工業鍋爐之NOx排放標準依附其內,使得許多減少NOx之各種排放控制技術出現。There are many types of nitrogen oxides in the atmosphere. Among them, NO and NO2 have the most impact on air pollution. A very small part of NO will become NO2 in the furnace, and NO2 is very toxic. These are collectively called NOx. In view of With the rising awareness of environmental protection, in order to reduce its NOx emission value, the government has attached the NOx emission standard of its industrial boilers to it, which has led to the emergence of various emission control technologies for reducing NOx.
NOx的形成主要經由兩種途徑,其一為燃料氮氧化物,由燃料中所含之氮成分,在燃燒時與氧化合而形成,另一則為熱式氮氧化物,其為火焰在高溫下,使燃燒氣體中的氮與氧產生反應而形成,尤其於火焰峰溫大於1600℃時,熱式氮氧化物將急遽產生,故習知許多抑制氮氧化物之方法,即為透過其燃燒方法抑制其產生,惟其抑制成效有限。The formation of NOx is mainly through two ways, one is fuel nitrogen oxides, which are formed by combining nitrogen components contained in fuel with oxygen during combustion, and the other is thermal nitrogen oxides, which are formed by flames at high temperatures. It is formed by the reaction of nitrogen and oxygen in the combustion gas. Especially when the peak flame temperature is greater than 1600 ° C, thermal nitrogen oxides will be produced rapidly. Therefore, many methods of suppressing nitrogen oxides are known, that is, through its combustion method Inhibit its production, but its inhibitory effect is limited.
本發明之主要目的,係提供一種具有煙氣混合裝置之燃燒爐,其以煙氣混合裝置之第一煙氣管件輸送第二蓄熱式燃燒器所排放之煙氣至管體,且經第二空氣管件輸送助燃氣體至管體,將部分之煙氣與該助燃氣體混合,形成混合氣體,此混合氣體係為預熱後之氣體,因此輸送至燃燒爐後,可進一步維持燃燒爐之溫度,不僅大幅抑制氮氧化物生成,更可減少二氧化碳的排放等功效。The main purpose of the present invention is to provide a combustion furnace with a flue gas mixing device, which uses the first flue gas pipe of the flue gas mixing device to transport the flue gas discharged from the second regenerative burner to the pipe body, and through the second The air pipe fittings transport the combustion-supporting gas to the pipe body, and mix part of the flue gas with the combustion-supporting gas to form a mixed gas. This mixed gas system is a preheated gas, so after being transported to the combustion furnace, the temperature of the combustion furnace can be further maintained. Not only greatly suppresses the formation of nitrogen oxides, but also reduces carbon dioxide emissions.
為了達到上述之目的,本發明之一實施例係揭示一種具有煙氣混合裝置之燃燒爐,包含:一燃燒爐及一煙氣混合裝置,該燃燒爐包含一爐體,該爐體設置一排氣口及一進氣口,該煙氣混合裝置包含一管體、一第一煙氣管件、一第二煙氣管件、一第一空氣管件及一第二空氣管件,該管體分別連通該第一煙氣管件、該第二煙氣管件、該第一空氣管件及該第二空氣管件,該第一煙氣管件係連通該排氣口,該第一空氣管件係連通該進氣口,該第二煙氣管件係連通一排氣裝置,該第二空氣管件係連通一進氣裝置;In order to achieve the above object, one embodiment of the present invention discloses a combustion furnace with a flue gas mixing device, comprising: a combustion furnace and a flue gas mixing device, the combustion furnace includes a furnace body, and the furnace body is provided with a row Gas port and an air inlet, the flue gas mixing device includes a pipe, a first flue gas pipe, a second flue gas pipe, a first air pipe and a second air pipe, the pipe respectively communicates with the The first flue gas pipe, the second flue gas pipe, the first air pipe and the second air pipe, the first flue gas pipe is connected to the exhaust port, the first air pipe is connected to the air inlet, The second flue gas pipe is connected to an exhaust device, and the second air pipe is connected to an air intake device;
其中,該爐體內燃燒產生一煙氣,該煙氣經該排氣口輸出至該第一煙氣管件,該第一煙氣管件輸送該煙氣至該管體,並經該第二煙氣管件將部分該煙氣輸出至該排氣裝置;Wherein, the combustion in the furnace produces a flue gas, and the flue gas is output to the first flue gas pipe through the exhaust port, and the first flue gas pipe transports the flue gas to the pipe body, and passes through the second flue gas a pipe fitting to output a portion of the flue gas to the exhaust device;
其中,該進氣裝置輸出一助燃氣體經該第二空氣管件輸送至該管體,該助燃氣體於該管體中與部分之該煙氣進行混合,形成一混合氣體,並經該第一空氣管件輸送至該進氣口,使得該爐體內進行燃燒。Wherein, the air intake device outputs a combustion-supporting gas to the pipe body through the second air pipe, and the combustion-supporting gas is mixed with part of the flue gas in the pipe body to form a mixed gas, which is passed through the first air pipe. Pipes are delivered to the air inlet to allow combustion to take place within the furnace body.
於最佳實施例中,該第二空氣管件更包含一噴射管,該噴射管設於該第二空氣管件之一端,並位於該管體中,以傳輸出該助燃氣體至該管體,並捲吸管體內煙氣進入該第一空氣管件。In a preferred embodiment, the second air pipe part further includes an injection pipe, the injection pipe is arranged at one end of the second air pipe part and is located in the pipe body, so as to deliver the combustion-supporting gas to the pipe body, and The smoke inside the suction pipe enters the first air pipe.
於最佳實施例中,該第一空氣管件包括一漸縮部及一本體部,該漸縮部連接該管體且朝該本體部方向漸縮,該噴射管之末端與該本體部之距離為55mm~95mm。In a preferred embodiment, the first air pipe includes a tapering portion and a body portion, the tapering portion is connected to the pipe body and tapers toward the body portion, the distance between the end of the injection pipe and the body portion 55mm~95mm.
於最佳實施例中,更包含一輸送氣體裝置,其連通該第一煙氣管件。In a preferred embodiment, it further includes a gas conveying device, which communicates with the first flue gas pipe.
於最佳實施例中,該煙氣混合裝置設置於該輸送氣體裝置下游處10~12倍水力直徑。In a preferred embodiment, the flue gas mixing device is set at 10-12 times the hydraulic diameter downstream of the gas delivery device.
於最佳實施例中,該煙氣混合裝置設置於該輸送氣體裝置下游處10倍以上之水力直徑。In a preferred embodiment, the flue gas mixing device is arranged at a hydraulic diameter more than 10 times downstream of the gas conveying device.
於最佳實施例中,更包含一第一控制閥、一第二控制閥及一控制單元,該第一控制閥係連通該第一煙氣管件、該第一空氣管件及該第一蓄熱式燃燒器之一第一對外開口,該第二控制閥係連通該第一煙氣管件、該第一進氣管件及該第二蓄熱式燃燒器之一第二對外開口,該控制單元分別與該第一控制閥、該第二控制閥及一運算處理單元訊號連接,該控制單元用以控制該第一控制閥及該第二控制閥進行換向切換。In the preferred embodiment, it further includes a first control valve, a second control valve and a control unit, the first control valve is connected to the first flue gas pipe, the first air pipe and the first regenerative One of the first external openings of the burner, the second control valve communicates with the first flue gas pipe, the first air intake pipe and the second external opening of the second regenerative burner, the control unit is connected with the The first control valve, the second control valve and an operation processing unit are connected in signal, and the control unit is used to control the first control valve and the second control valve to perform reversing switching.
有關本發明之相關申請專利特色與技術內容,在以下配合參考圖式之較佳實施例的詳細說明中,將可清楚的呈現。The features and technical contents of the relevant patent applications of the present invention will be clearly presented in the following detailed description of preferred embodiments with reference to the drawings.
請參閱第一圖及第二A圖,第一圖為本發明之一實施例之裝置示意圖,第二A圖為本發明之一實施例之氣體流動混合示意圖。如圖所示,本發明之具有煙氣混合裝置之燃燒爐,包含燃燒爐1及煙氣混合裝置2,以下詳細說明之。Please refer to the first figure and the second figure A, the first figure is a schematic diagram of the device according to one embodiment of the present invention, and the second figure A is a schematic diagram of the gas flow mixing according to one embodiment of the present invention. As shown in the figure, the combustion furnace with a flue gas mixing device of the present invention includes a
接續上述,燃燒爐1包含爐體11,爐體11設置排氣口101及進氣口102,其中,爐體11內進行燃燒,其燃燒過程將產生煙氣G1,煙氣G1包含氮氧化物、二氧化碳等汙染氣體,而煙氣G1經排氣口101輸出。Continuing from the above, the
再次參閱第一圖及第二A圖,一併參閱第三A圖及第三B圖,第三A圖為本發明之一實施例之煙氣混合裝置等角示意圖,第三B圖為本發明之一實施例之煙氣混合裝置剖面示意圖。如圖所示,煙氣混合裝置2包含管體21、第一煙氣管件22、第二煙氣管件23、第一空氣管件24及第二空氣管件25,管體21分別連通第一煙氣管件22、第二煙氣管件23、第一空氣管件24及第二空氣管件25,其中,管體21可經由法蘭盤FL及螺栓(圖未示)連通管件,第一煙氣管件22係連通爐體11之排氣口101,第二煙氣管件23係連通排氣裝置3,第一空氣管件24係連通爐體11之進氣口102,第二空氣管件25係連通進氣裝置4。Refer to the first figure and the second figure A again, and refer to the third figure A and the third figure B together. The third figure A is an isometric schematic diagram of a flue gas mixing device according to an embodiment of the present invention, and the third figure B is the present invention. A schematic cross-sectional view of a flue gas mixing device according to an embodiment of the invention. As shown in the figure, the flue
承如前述裝置結構,其於燃燒爐1之爐體11可為箱式爐、立式爐、圓筒爐或大型方爐,但不在此限,因此,爐體11係使用燃燒器進行加熱,此一燃燒過程中,爐體11內產生煙氣G1,煙氣G1經由爐體11之排氣口101輸出至煙氣混合裝置2之第一煙氣管件22,煙氣G1將沿著第一煙氣管件22抵達管體21內,此時,部分之煙氣G1經第二煙氣管件23傳輸至排氣裝置3進行廢氣排放。Inheriting the above-mentioned device structure, the
接續上述,於一實施例中,更包含一輸送氣體裝置5,輸送氣體裝置5連通第一煙氣管件22,輸送氣體裝置5用於輸送第一煙氣管件22內之煙氣G1至管體21,於一實施例中,輸送氣體裝置5可為排風機、鼓風機,但不在此限。Continuing the above, in one embodiment, a
接續上述,進氣裝置4將會輸出助燃氣體G2,助燃氣體G2用於幫助燃燒,例如氧氣,但不在此限,進氣裝置4連通第二空氣管件25,於一實施例中,第二空氣管件25更包含噴射管252,噴射管252設於第二空氣管件25之一端,並位於管體21中,以傳輸出助燃氣體G2至管體21,進氣裝置4以第二空氣管件25及噴射管252傳輸助燃氣體G2至管體21,其中,於一實施例中,第一空氣管件24包括一漸縮部242及一本體部244,漸縮部242連接管體21且朝本體部244之方向漸縮,噴射管252末端之位置與本體部244之位置對應,且噴射管252之末端與本體部244之距離為55mm~95mm,以提升煙氣G1受助燃氣體G2帶動並捲吸進入第一空氣管件24中的效率,在煙氣G1之流量為240立方公尺/小時,及助燃氣體G2之流量為220立方公尺/小時的條件下,當噴射管252之末端與本體部244之距離為55mm時,其捲吸煙氣G1之比例可達9.7%,於較佳實施例中,亦可調整排氣壓力,即第一煙氣管件22傳輸煙氣G1之壓力,在同樣流量條件下,其進氣壓力即傳輸助燃氣體G2之壓力為11000帕斯卡,且將排氣壓力調降至1850帕斯卡時,其捲吸煙氣G1之比例更可達15.3%,但不在此限。Continuing the above, the
接續上述,於一實施例中,煙氣混合裝置2設置於輸送氣體裝置5之下游處大於10倍之水力直徑,即係煙氣混合裝置2距離輸送氣體裝置5大於10倍之水力直徑,使噴射管252捲吸煙氣G1之比例得以維持,避免煙氣混合裝置2與輸送氣體裝置5之距離過遠,導致捲吸煙氣G1之比例下降,或煙氣混合裝置2與輸送氣體裝置5之距離過近,致使助燃氣體G2被過強的煙氣G1夾帶至排氣裝置3並排出,於較佳實施例中煙氣混合裝置2設置於輸送氣體裝置5之下游處10~12倍水力直徑,但不在此限。Continuing the above, in one embodiment, the flue
接續上述,當助燃氣體G2行經管體21時,噴射管252快速輸送助燃氣體G2,並捲吸管體21內之煙氣G1,使助燃氣體G2與管體21內之另一部分之煙氣G1進行混合,此一步驟係將助燃氣體G2進行預熱,而形成混合氣體G3,混合氣體G3經第一空氣管件24輸送至爐體11之進氣口102,使得爐體11依據混合氣體G3進行燃燒,如此一來,透過煙氣混合裝置2將燃燒後所產生的氣體進行回收再利用,由於煙氣G1含氧量約8-10%,其含氧量較低,因此使得氮氣與氧氣的結合機率大幅降低,而可抑制氮氧化物的生成。Continuing the above, when the combustion-supporting gas G2 travels through the
請參閱第二B圖及第二C圖,且一併參閱第三A圖及第三B圖,第二B圖至第二C圖為本發明之另一實施例之氣體流動混合示意圖。如圖所示,燃燒爐1更包含第一蓄熱式燃燒器12及第二蓄熱式燃燒器13,第一蓄熱式燃燒器12具有第一對內開口121及第一對外開口122,第一對內開口121及第一對外開口122分別設置於第一蓄熱式燃燒器12之兩側,第二蓄熱式燃燒器13具有第二對內開口131及第二對外開口132,第二對內開口131及第二對外開口132分別設置於第二蓄熱式燃燒器13之兩側,且第一蓄熱式燃燒器12之第一對內開口121連通爐體11之進氣口102,及第二蓄熱式燃燒器13之第二對內開口131連通爐體11之排氣口101,於一實施例中,第一蓄熱式燃燒器12以及第二蓄熱式燃燒器13包含至少一燃料管件FP,用以輸送燃料F至爐體11。Please refer to the second figure B and the second figure C, and also refer to the third figure A and the third figure B. The second figure B to the second figure C are the schematic diagrams of gas flow mixing according to another embodiment of the present invention. As shown in the figure, the
接續上述,如第二B圖所示,第一蓄熱式燃燒器12依據燃料F進行燃燒,經第一蓄熱式燃燒器12之第一對內開口121輸出火焰FI至爐體11內,於一實施例中,於燃燒爐1之爐體11內置放欲加熱之工件A,並對置放於爐體11內之工件A進行加工,工件A放置處與第一蓄熱式燃燒器12之第一對內開口121及第二蓄熱式燃燒器13之第二對內開口131為相對設置,並以第一蓄熱式燃燒器12之第一對內開口121輸出火焰FI而可對工件A進行加熱,此一燃燒過程中,產生煙氣G1,並經由第二蓄熱式燃燒器13之第二對內開口131吸入後,由第二對外開口132輸出至煙氣混合裝置2之第一煙氣管件22,煙氣G1將沿著第一煙氣管件22抵達管體21,部分之煙氣G1經第二煙氣管件23傳輸至排氣裝置3進行廢氣排放。Continuing the above, as shown in the second figure B, the first
接續上述,進氣裝置4輸出助燃氣體G2,助燃氣體G2經噴射管252傳輸至管體21,當助燃氣體G2行經管體21時,與管體21內另一部分之煙氣G1進行混合,將助燃氣體G2預熱,形成混合氣體G3,混合氣體G3再經第一空氣管件24輸送至第一蓄熱式燃燒器12,使得第一蓄熱式燃燒器12依據混合氣體G3與燃料F進行燃燒,藉此可將燃燒後所產生的氣體進行回收再利用,由於煙氣G1含氧量約8-10%,其含氧量較低,因此使得氮氣與氧氣的結合機率大幅降低,而可抑制氮氧化物的生成。Continuing from the above, the
請參閱第二C圖、第三A圖、第三B圖及第四圖,第四圖為本發明之再一實施例之裝置示意圖,如圖所示,更進一步的,於第一煙氣管件22內設置第一控制閥C1、於第一空氣管件24內設置第二控制閥C2及控制單元7,第一控制閥C1係連通第一煙氣管件22、第一空氣管件24及第一蓄熱式燃燒器12之第一對外開口122,第二控制閥C2係連通第一煙氣管件22、第一空氣管件24及第二蓄熱式燃燒器13之第二對外開口132,控制單元7分別與第一控制閥C1、第二控制閥C2及運算處理單元6訊號連接,控制單元7用以控制第一控制閥C1及第二控制閥C2進行開度調整,其中,第一控制閥C1及第二控制閥C2係換向閥,但不在此限。Please refer to the second figure C, the third figure A, the third figure B and the fourth figure. The fourth figure is a schematic diagram of the device of another embodiment of the present invention. As shown in the figure, further, the first smoke The first control valve C1 is set in the pipe fitting 22, and the second control valve C2 and the control unit 7 are set in the first
接續上述,於一實施例中,可透過第一控制閥C1以及第二控制閥C2進行第一蓄熱式燃燒器12及第二蓄熱式燃燒器13之換向輸送氣體,也就是其中一燃燒器從排氣轉換成進氣並對爐體11產生燃燒火焰FI,如第二C圖所示,第一蓄熱式燃燒器12及第二蓄熱式燃燒器13換向後,第一蓄熱式燃燒器12連接之第一空氣管件24轉換為第一煙氣管件22,第一蓄熱式燃燒器12連接之第一煙氣管件22轉換為第一空氣管件24。Continuing the above, in one embodiment, the first
接續上述,如第二C圖所示,第二蓄熱式燃燒器13依據燃料F進行燃燒,經第二蓄熱式燃燒器13之第二對內開口131輸出火焰FI至爐體11內,於燃燒過程中,產生煙氣G1,並經由第一蓄熱式燃燒器12之第一對內開口121吸入後,由第一對外開口122輸出至煙氣混合裝置2之第一煙氣管件22,煙氣G1將沿著第一煙氣管件22抵達管體21,部分之煙氣G1經第二煙氣管件23傳輸至排氣裝置3進行廢氣排放。Continuing the above, as shown in the second figure C, the second
接續上述,進氣裝置4輸出助燃氣體G2,助燃氣體G2經噴射管252傳輸至管體21,當助燃氣體G2行經管體21時,與管體21內另一部分之煙氣G1進行混合,將助燃氣體G2預熱,形成混合氣體G3,混合氣體G3再經第一空氣管件24輸送至第二蓄熱式燃燒器13,使得第二蓄熱式燃燒器13依據混合氣體G3與燃料F進行燃燒,藉此可將燃燒後所產生的氣體進行回收再利用。Continuing from the above, the
再次參閱第四圖,如圖所示,更進一步設置第一流量計F1、第二流量計F2及第一溫度感測器T1,第一流量計F1係設置於第一煙氣管件22上之任一處,但不在此限,可偵測到煙氣G1之第一流量值之處即可,第二流量計F2係設置於第一空氣管件24上之任一處,但不在此限,可偵測到助燃氣體G2之第二流量值之處即可,第一溫度感測器T1係設置於燃燒爐1之爐體11之任一處,但不在此限,可感測到爐體11內之工作溫度即可,其中,第一溫度感測器T1可為熱電偶,但不在此限。Referring to the fourth figure again, as shown in the figure, the first flowmeter F1, the second flowmeter F2 and the first temperature sensor T1 are further provided, and the first flowmeter F1 is arranged on the first
接續上述,第一煙氣管件22上更可設置第二溫度感測器T2,用以感測煙氣G1之第一溫度值,及第一空氣管件24更可設置第三溫度感測器T3,用以感測助燃氣體G2之第二溫度值,並經運算處理單元6與第一流量計F1、第二流量計F2、第一溫度感測器T1、第二溫度感測器T2及第三溫度感測器T3訊號連接,而可接收並依據第一流量值、第二流量值、工作溫度值、第一溫度值及第二溫度值進行運算,而生成運算處理結果,其中,第二溫度感測器T2及第三溫度感測器T3為熱電偶,但不在此限。Continuing the above, the first
綜上所述,本發明之有煙氣混合裝置之燃燒爐,以煙氣混合裝置可進一步將部分之煙氣與助燃氣體混合,即利用回收之煙氣之熱能將助燃氣體預熱,而形成混合氣體,從而達到降低二氧化碳排放量及抑制氮氧化物生成,同時,可節省30-40%之燃料,更將高達90%之廢熱回收再利用,大幅提高燃燒效率,故確實可以達成本發明之目的。To sum up, in the combustion furnace with flue gas mixing device of the present invention, the flue gas mixing device can further mix part of the flue gas with the combustion-supporting gas, that is, use the heat energy of the recovered flue gas to preheat the combustion-supporting gas to form Mixed gas, so as to reduce carbon dioxide emissions and inhibit the generation of nitrogen oxides. At the same time, it can save 30-40% of fuel, and recover and reuse up to 90% of waste heat, greatly improving combustion efficiency, so it can indeed achieve the goal of the present invention. Purpose.
惟以上所述者,僅為本發明之較佳實施例而已,當不能以此限定本發明實施之範圍,即凡依本發明申請專利範圍及發明說明內容所作之簡單的等效變化與修飾,皆仍屬本發明專利涵蓋之範圍內。But the above-mentioned ones are only preferred embodiments of the present invention, and should not limit the implementation scope of the present invention, that is, any simple equivalent changes and modifications made according to the scope of the patent application for the present invention and the contents of the description of the invention, All still belong to the scope covered by the patent of the present invention.
1:燃燒爐 101:排氣口 102:進氣口 11:爐體 12:第一蓄熱式燃燒器 121:第一對內開口 122:第一對外開口 13:第二蓄熱式燃燒器 131:第二對內開口 132:第二對外開口 2:煙氣混合裝置 21:管體 22:第一煙氣管件 23:第二煙氣管件 24:第一空氣管件 242:漸縮部 244:本體部 25:第二空氣管件 252:噴射管 3:排氣裝置 4:進氣裝置 5:輸送氣體裝置 6:運算處理單元 7:控制單元 A:工件 C1:第一控制閥 C2:第二控制閥 F:燃料 F1:第一流量計 F2:第二流量計 FI:火焰 FL:法蘭盤 FP:燃料管件 T1:第一溫度感測器 T2:第二溫度感測器 T3:第三溫度感測器 G1:煙氣 G2:助燃氣體 G3:混合氣體 1: Burning furnace 101: Exhaust port 102: air inlet 11: furnace body 12: The first regenerative burner 121: The first pair of inner openings 122: The first external opening 13: Second regenerative burner 131: The second pair of inner openings 132: Second external opening 2: Flue gas mixing device 21: tube body 22: The first flue gas pipe 23: The second flue gas pipe 24: First air fitting 242: tapered part 244: Body Department 25:Second air pipe fitting 252: Injection pipe 3: exhaust device 4: Air intake device 5: Gas delivery device 6: Operation processing unit 7: Control unit A: Workpiece C1: first control valve C2: Second control valve F: Fuel F1: first flow meter F2: Second flow meter FI: Flame FL: Flange FP: fuel pipe fittings T1: The first temperature sensor T2: Second temperature sensor T3: The third temperature sensor G1: Smoke G2: combustion gas G3: mixed gas
第一圖:其為本發明之一實施例之裝置示意圖; 第二A圖:其為本發明之一實施例之氣體流動混合示意圖; 第二B圖至第二C圖:其為本發明之另一實施例之氣體流動混合示意圖; 第三A圖:其為本發明之一實施例之煙氣混合裝置等角示意圖; 第三B圖:其為本發明之一實施例之煙氣混合裝置剖面示意圖;以及 第四圖:其為本發明之再一實施例之裝置示意圖。 The first figure: it is a device schematic diagram of an embodiment of the present invention; The second figure A: it is a schematic diagram of gas flow mixing in an embodiment of the present invention; The second figure B to the second figure C: it is a schematic diagram of gas flow mixing in another embodiment of the present invention; Figure 3 A: It is an isometric schematic diagram of a flue gas mixing device according to an embodiment of the present invention; Figure 3 B: It is a schematic cross-sectional view of a flue gas mixing device according to an embodiment of the present invention; and Figure 4: It is a schematic diagram of a device according to yet another embodiment of the present invention.
1:燃燒爐 1: Burning furnace
11:爐體 11: furnace body
101:排氣口 101: Exhaust port
102:進氣口 102: air inlet
2:煙氣混合裝置 2: Flue gas mixing device
3:排氣裝置 3: exhaust device
4:進氣裝置 4: Air intake device
5:輸送氣體裝置 5: Gas delivery device
Claims (7)
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Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
TW505763B (en) * | 2000-06-20 | 2002-10-11 | John Zink Co Llc | Fuel dilution methods and apparatus for NOx reduction |
US7104787B2 (en) * | 2004-05-06 | 2006-09-12 | Eclipse, Inc. | Apparatus for radiant tube exhaust gas entrainment |
CN102099624A (en) * | 2008-07-15 | 2011-06-15 | 法孚斯坦因公司 | Device for controlling regenerative burners |
CN209490681U (en) * | 2018-11-17 | 2019-10-15 | 江苏腾天工业炉有限公司 | Using gas flow as the low NOx emission control systems of mathematical model |
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Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
TW505763B (en) * | 2000-06-20 | 2002-10-11 | John Zink Co Llc | Fuel dilution methods and apparatus for NOx reduction |
US7104787B2 (en) * | 2004-05-06 | 2006-09-12 | Eclipse, Inc. | Apparatus for radiant tube exhaust gas entrainment |
CN102099624A (en) * | 2008-07-15 | 2011-06-15 | 法孚斯坦因公司 | Device for controlling regenerative burners |
CN209490681U (en) * | 2018-11-17 | 2019-10-15 | 江苏腾天工业炉有限公司 | Using gas flow as the low NOx emission control systems of mathematical model |
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