、發明說明： 【發明所屬之技術領域】 本發明係有關一種減除切換峰值之蓄熱焚化爐，係有關一種蓄熱 焚化爐（Regenerative Thermal Oxidizer，RTO)，藉由設有一蓄 熱焚化爐、一廢氣主要管路、一廢氣進口閥組、一通向控制閥組、— 乾淨氣送風管路、一氣體控制閥組及一第一風車，可將蓄熱燃燒爐 氣流流動方向在切換蓄熱床時一方面使切換氣流方向時的洩漏污 染去除，另一作用其一蓄熱床的未燃燒廢氣不致有外洩，而產生 運轉之/于染峰值，達到穩定利用之功能，適用於產生有機廢氣需 要減除之行業如某些特定工業之生產領域，如半導體業、光電產業， 化工業等。 【先前技術】 揮發性有機物質（Volatile Organic Compound，V0C)在產業界廣 泛被使用’亦隨製程而排放至大氣環境，例如，隨半導體與光電業製 程排放之有機廢氣’ IPA(Isopropyl Alcohol，GIU))、丙酮、環己鋼 等’易造成環境污染《各國對於揮發性有機物質皆有嚴格的空污管制 標準，以維護環保以及民眾的健康；以中華民國為例，環保署已公告 實施半導體製造業空氣污染管制及排放標準；對於揮發性有機廢氣強 制要求之削減率，以半導體業為例，至少應大於90%。 有機廢氣的處理方法很多，熱焚化是重要的方法之一，而 蓄熱焚化爐是其中一種，特色是熱回效率可以高達以上。 其中蓄熱焚化爐（RT0)可為雙塔式而配置有二個蓄熱床 (Regenerative beds),蓄熱床内充填蓄熱材，使揮發性有機 廢氣流經蓄熱床預熱（此時蓄熱材釋出熱能），而後揮發性有機 廢氣進入燃燒室，此時，由於燃燒爐燃料喷嘴產生輔助熱能可 提供熱量及VOCs成分氧化分解產生的熱量，使燃燒室保持— 定的溫度（例如850。〇,在設計的停留時間中有機廢氣所含 的VOCs成份幾乎被完全氧化成H20及C02。 第1圖係為-般傳統蓄熱焚化爐（RT〇)之結構示意圖，為雙 塔式蓄熱焚化爐；其中之蓄熱焚化爐i 〇 a主要含有兩組蓄熱 床，第一蓄熱床12 a和第二蓄熱床11a、燃燒室13 a及其相連 之廢氣進出管線和流向調節閥等；其中風機2 8 a自廢氣來源端抽排 有機廢氣（VOCs Laden Air)至蓄熱焚化爐1 〇 a入口後，可有兩 種模式進入燃燒室13 a中反應。第一種模式：有機廢氣藉由一風機 2 8 a入口進入管線，分別經由第一流向調節閥21a進入第一蓄熱 床12 a (此時的第二流向調節閥2 2 a和第三流向調節閥2 3 a為 〇FF[關閉]狀態）；預熱後進的有機廢氣進入燃燒室中進行反 應；有機廢氣在燃燒室13 a中由燃料喷嘴14 a提供一燃燒用火焰 I 5 a ’其燃燒室1 3 a内部之燃燒溫度可達攝氏溫度8〇〇〜95〇β(：，將 有機廢氣經氧化反應形成HA及C〇2;有機廢氣流經由第二蓄熱床 II a、第四流向調節閥2 4 a，前方由煙囪3 51 a排出至大氣中， 在通過第二蓄熱床1 1 a後，第二蓄熱床1 1a被自燃燒室的高溫氣 流加熱。第二種模式：有機廢氣由風機2 8 a前段進入管線，分別經 1329728 由第三流向調節閥2 3 a (此時的第-流向調節閥2 i a和第四流向 調節閥2 4 a為OFF狀態）進入第二蓄熱床i工a •在通過第二蓄熱 床1 1 a預熱後’有機廢氣在燃燒室i 3 a中由燃燒喷嘴i 4 a提供 -燃燒用火焰1 5 a將有機廢氣氧化成恥及c〇2，然後通過第一蓄 熱床12a，及第二流向調節閥22a排放，第_f熱床被自燃 燒室的高溫氣流加熱。 其上述之第-種和第二種模式定時#環做氣流流動方向 切換保持第-蓄熱床12a及第二蓄熱床…可維持高溫 用以預熱有機廢氣；其中蓄熱材多為陶料料所組成。習用之 蓄熱焚化爐i Q a，運作·巾於雙塔式焚化爐進出閥門做切 換蓄熱床時’會產生-個相當於人口濃度的排放峰值到煙自 (排放吟由純化爐對有機廢氣的破壞效率可達卿以上， 而入口氣流在切換時會直接排到煙自，以此猶破壞效率預 估’可知此濃度是經焚化爐處裡過排氣的5〇倍高，此一直造 成產業界的_;習用蓄熱焚化爐的缺點在於閥之氣流流動方 向切換時會產P汙染之切換峰值’其汗染之缺失使得其於實 用場合有其不便。 有鐘於此’本發明期能提供一種減除切換峰值之蓄熱焚化爐，藉 由設有乾淨氣賴管路、氣魅制及[財之組合設 計’即可減除習用蓄熱焚化爐裝置因閥組切換氣流流動方向時之汗 染峰值的目的’以极防止有機錢料械，並可提餘關於半導 8 體業或光電產業之設備需求使用，乃潛心研思1計組製，為本發明 所欲研創之動機者。 【發明内容】 本發明之主要目的’在提供—種減除切換峰值之蓄熱焚化爐，藉 由設有一蓄熱焚化爐、—廢氣主要管路、—廢氣進口_、—通向控 綱組、-乾淨氣賴管路、—氣綱組及—第_風車之組合設 計，使有機廢氣在高靜壓除淨之效應作用下，運作週期中其—蓄熱2 位處理廢氣汙染自動送進燃燒室中燃燒，防止切換峰值之汗染者。 本發明之次-目的，在提供—種減除切鱗值之蓄熱焚化爐具 減除汗染魏度，對傳統蓄熱焚化爐之配合裝置，藉由-蓄熱焚化爐、' -廢亂主要管路、-廢氣進口閥組、—通向控糊組、—乾淨氣送風 管路、-氣體控綱組及—第-風車之組合設計，來_姆管路， 使雙塔式之蓄熱焚聽於運作聊巾氣流流動方向切換時不致有切 換峰值產生之〉于染物㈣’以供半導體設備、光電設備或其他需去除 設備產生汙染物之環境使用者。 本發明主要係包含有-蓄熱焚化爐、—廢氣主要管路、一廢氣進 口閥組、-通向控侧組、—乾淨氣賴管路一氣體控侧組及— 第-風車；該廢氣主要管路倾蓄熱焚化爐之通氣f路連接，而廢氣 管路上設有廢氣進口閥組及通向控制閥組來控制切換管路，以控制管 路中之廢氣之流向，並使切換氣流方向時，來源有機廢氣不會直 接排放；而該乾淨氣送風管路之一端係與廢氣主要管路相連接，以供 送入氣體進入廢氣主要管路中，而乾淨氣送風管路上設有氣體控制閥 1329728 組及第一風車，以使氣體能快速進入廢氣主要管路中，提供蓄孰焚化 爐切換氣流流動方向時，乾淨氣送風管路中之氣體可藉由廢氣主要管 路快速抵達至蓄鍵化爐之通錄路裡，將未燃燒之有機廢氣以該 塵力源將其送進雜室’防止未處理麵廢氣直接排出，達到 去除廢氣汙染者。 本發明之其他特點及具體實施例可於以下配合附圖之詳細說明 中’進一步瞭解。 【實施方式】 請參考第2圖所示’係為本發明減除切換峰值之蓄哉焚化爐之社 構示意圖，係包含有-蓄熱焚化爐1〇 '—廢氣主要管路2 〇、一廢 氣進口閥組3 ◦、-通向控制閥組4 〇、一乾淨氣送風管路㈧、一 氣體控侧組6 0及-第-風車7 !;該蓄熱焚化爐i _第一蓄 熱床U、第二蓄熱床12及_燃燒室13，鞠燒室⑶系位與第 -蓄熱床！ i及第二蓄熱床i 2之頂部相通之空間，而該第一蓄熱床 1 1及第二蓄熱床i 2各設有至少—通氣管^ 4(第1氣管路1 4 1、第=通氣管路χ 4 2) ’以供氣體之進出，其中該第—蓄熱床工 1及第二蓄熱床1 2係有蓄熱材填入，該f熱材係、由喊、金屬、金 屬氧化物或以上之組合所组成，另難燒室丄3其結_式 化燃燒式、觸雜燒式、電熱氧化式、電缝化式、絲反應式其 中之-種所組成，而其燃燒室！3中包含有—燃料噴嘴以供燃燒^ 3之熱能’另亦可改用電熱器或電毀產生器等來提供該燃燒室^之 熱能。而該廢氣主要管路2 0係、與蓄熱焚化爐丄Q之第—蓄熱床工工 10 1329728 及第二蓄熱床1 2的通氣管路1 4(第一通氣管路1 4 i、第二通氣管 路1 4 2)連接以供廢氣進入燃燒室13產生熱氧化，並將處理後之氣 體排出大氣中’而於廢氣主要管路2 0上設有廢氣進口閱組3 〇及通 向控制閥組4 0 ’其中本實施例的廢氣進口閥組3 〇係採用一個三通 閥31結構組成，通向控制閥組4 0係採用一個四通閥4 1結構，而該 廢氣進口閥組3 0係設於廢氣主要管路2 0之進氣端，以控制廢氣進 出，其中廢氣進口閥組3 0連設有一廢氣管路21通往燃燒室13 中，藉由廢氣進口閥組3 0來控制切換管路，而該廢氣管路2 i上進 一步連設有一熱交換器8 0，以供預先加熱用，其中該熱交換器8〇 之熱源係採電熱器、燃燒熱源、電漿產生器或廢熱回收其中一種提供 者，該熱交換器8 0可包含有殼管式之熱交換管路通道和一供有 機廢氣廢氣進出之結構體（圖未示）；熱交換管路通道中填充 有流動的熱傳導介質，以進行熱交換動作；而可加入之熱傳導介質包 括有：空氣、航、水及鱗油."等任何形態之越（而熱傳導介質 經由加熱後所形成之熱氣、高溫航、熱水及熱媒油，可經由不同的 方法加以利用；熱傳導介質可隨工廠内機台要求而作變更）。另 通向控制閥組4 0係設於廢氣主要管路2 〇靠近蓄熱焚化i 〇處， 以控制廢氣之進出於第-蓄熱床i i及第二蓄熱床i 2中及燃燒後之 氣體排放’藉由通向控綱組4 Q㈣換管路而該廢氣主要管路2 0路之末端係連設有—翻82，以供將氣體減出大氣中 ，另於廢 乳主要管路2 G上進-步設有第二風車7 2，該第二風車7 2係設於 廢氣進^組3 0之前端，以供形成風壓來拉抽管財之氣體者。 另又有乾淨氣送風管路5◦，該乾淨氣送風管路5 0之-端係 。廢氣路2 〇相連接，以供送入氣趙進入廢氣主要管路2 〇 中，而該乾淨氣送風管路5 0上設有氣體控制閥組6 0及第-風車7 、t本實施例的氣體控制閥組6⑽、採用—個三通閥6丄結構， 該氣體控觸㈣G係設於乾錢賴管路5 Q上，雜㈣氣體進 出，該氣__6 Q物—嶋路5 i，簡放用，藉由 氣體控制閥組6 〇來控制切換管路，而第-風車71係設於乾淨氣送 風管路5 Q之ϋ供將缝拉抽送人純主要管路2 0中，其中 該第一風車7 1’其送風壓力規格值對第—f熱床“'第二蓄熱床 1 2之壓知具有克服之值，藉此，提供蓄熱焚化爐工〇之雙塔氣流切 換時’以乾淨統風管路5 〇送人氣體，防止未進職线理有機廢 氣直接排出，達到去除廢氣汙染者。 請參考第3、4圖所示，係為採用不同之閥組結構之示意圖，其 中該廢氣進口間組3 0、通向控制閥組4 〇及氣趙控制閥組6 〇係採 用三通閥結構設計來控_換管路，而簡向控糊組4⑽採用二 個三通閥4 2、4 3結構組成一種減除切換峰值之蓄熱焚化爐，係 包含有-蓄熱焚化爐10、-廢氣主要管路2 〇、—廢氣進口間組3 ◦、一通向控綱組4 0、-乾淨氣送風管路5 〇、一氣體控綱組 6 2及-第-風車7 i ;該蓄熱焚化爐2 〇設有第一蓄熱床工丄、第 二蓄熱床12及-燃燒室13，該燃燒η 3係位與第—f熱床工工 12 ^^728 及第-蓄熱床1 2之卿相通之㈣’而該第__蓄熱床丨！及第二蓄 熱床1 2各設有至少一通氣管路1 4(第-通氣管路1 4 3、第二通氣 s路14 4、第二通氣管路i 4 5、第四通氣管路i 4 6)，而通氣管 路14係設計成二進二出之狀態，以供氣體之進出^而該廢氣主要管 路2 0係與蓄熱焚化爐i Q之第—f熱床i丄及第二f熱床^ 2的通 氣管路1 4(第-通氣管路丄4 3、第三通氣管路i 4 5)連接以供廢 氣進入燃燒室1 3轉，並將麟後之氣體經軌管路(第二通氣管路 1 4 4、第四軌管路1 4 6)輸往廢氣主要管路2 Q再排出大氣中， 而於廢氣主要管路2 Q上設有廢氣進α閥組3 〇及通向控制閥組4 〇，其中本實施例的廢氣進口閥組3 0係採用一個三通閥3 結構組 成，通向控制閥組4 〇係採用二個三通閥4 2、4 3結構，該第一= 通閥4 2係設於第-通氣管路丨4 3及第三通氣管路i 4 5相接於廢 氣主要管路2 〇上的地方，以控制廢氣之行進方向，另該第二三通閥 4 3係設於第二通氣管路！ 4 4及第四通氣4 6相接於廢氣主 要管路2 0上的地方’以控峰氣之行進方向，而該廢氣進口間組3 0係設於廢氣主要管路2 〇之進氣端，亦採用三通閥3 i之結構以控 制廢氣進出，其中廢氣進口_3 0連設有-廢氣管路2 m往燃燒 室1 3中’藉由廢氣進口_3 〇來控制切換管路，而該廢氣管路2 1上進-步連設有-熱交換器8 0 ’以供預先加熱用，其中該熱交換 器8 0之熱源係採電熱器、燃燒熱源、電漿產生器或廢熱回收其中一 種提供者，另通向控制閥組4 〇係設於廢氣主要管路2 〇靠近蓄熱焚 13 1329728. 化爐10處’以控制廢氣之進出於第—蓄熱床i丄及第二蓄熱床^ 2 中及燃燒後之氣體排放，藉由通向控制閥組4◦來切換管路，而該廢 氣主要管路2 0之末端係連設有-煙iu8 2，以供將氣體排放出大氣[Technical Field] The present invention relates to a regenerative incinerator for reducing peak switching, relating to a Regenerative Thermal Oxidizer (RTO), which is provided with a regenerative incinerator and an exhaust gas. The pipeline, an exhaust gas inlet valve group, a control valve group, a clean air supply air line, a gas control valve group and a first windmill can switch the flow direction of the regenerative combustion furnace on the one hand when switching the regenerator bed Leakage pollution in the direction of airflow is removed, and the unburned exhaust gas acting on one of the regenerator beds is not leaked, and the operating/staining peak is generated to achieve stable utilization, and is suitable for industries that need to reduce organic waste gas. Production areas of certain industries, such as semiconductor industry, optoelectronic industry, chemical industry, etc. [Prior Art] Volatile Organic Compound (V0C) is widely used in the industry and is also discharged to the atmosphere with process, for example, organic waste gas discharged with semiconductor and photovoltaic industry processes. IPA (Isopropyl Alcohol, GIU) )), acetone, cyclohexyl steel, etc. 'Easy to cause environmental pollution'. Countries have strict air pollution control standards for volatile organic substances to protect the environment and the health of the people. In the case of the Republic of China, the EPA has announced the implementation of semiconductors. Manufacturing air pollution control and emission standards; for the mandatory reduction rate of volatile organic waste gas, the semiconductor industry, for example, should be at least 90%. There are many ways to treat organic waste gas. Thermal incineration is one of the important methods, and a thermal storage incinerator is one of them. The characteristic is that the heat recovery efficiency can be as high as above. The regenerative incinerator (RT0) can be a two-tower type with two regenerative beds, and the regenerative bed is filled with a heat accumulating material, so that the volatile organic waste gas flows through the regenerator bed to preheat (at this time, the heat storage material releases heat energy) Then, the volatile organic waste gas enters the combustion chamber. At this time, the auxiliary heat energy generated by the fuel nozzle of the burner can provide heat and the heat generated by the oxidative decomposition of the VOCs component, so that the combustion chamber maintains a constant temperature (for example, 850. The VOCs contained in the organic waste gas are almost completely oxidized into H20 and C02 during the residence time. The first figure is a schematic diagram of a conventional conventional regenerative incinerator (RT〇), which is a double-tower regenerative incinerator; The incinerator i 〇a mainly comprises two sets of regenerator beds, a first regenerator bed 12 a and a second regenerator bed 11 a , a combustion chamber 13 a and its associated exhaust gas inlet and outlet lines and flow direction regulating valves, etc.; wherein the fan 28 8 a is from the exhaust gas source After exhausting the organic exhaust gas (VOCs Laden Air) to the inlet of the thermal storage incinerator 1 〇a, there are two modes of reaction into the combustion chamber 13 a. The first mode: organic exhaust gas is passed through a fan 2 8 a Entering the pipeline, respectively entering the first regenerator bed 12a via the first flow regulating valve 21a (the second flow regulating valve 2 a and the third flow regulating valve 23 a at this time are in the 〇 FF [closed] state); preheating The backward organic exhaust gas enters the combustion chamber for reaction; the organic exhaust gas provides a combustion flame I 5 a 'in the combustion chamber 13 a from the fuel nozzle 14 a. The combustion temperature inside the combustion chamber 13 3 can reach 8 ° C. 〜95〇β(:, the organic waste gas is oxidized to form HA and C〇2; the organic waste gas stream is discharged to the atmosphere through the second regenerator bed II a, the fourth flow direction regulating valve 24 a, and the front side is exhausted by the chimney 3 51 a After passing through the second regenerator bed 1 1 a, the second regenerator bed 11a is heated by the high temperature airflow from the combustion chamber. The second mode: the organic exhaust gas enters the pipeline from the front section of the fan 28 8 a, through the third flow direction through 1329728 The regulating valve 2 3 a (the first flow regulating valve 2 ia and the fourth flow regulating valve 24 a at this time is in an OFF state) enters the second regenerator bed i • after preheating through the second regenerator bed 1 1 a 'Organic exhaust gas is supplied from the combustion nozzle i 4 a in the combustion chamber i 3 a - the flame for combustion 1 5 a oxidizing the organic waste gas into shame and c 〇 2, and then discharging through the first regenerator bed 12a and the second flow regulating valve 22a, the _f hot bed being heated by the high temperature air flow from the combustion chamber. The second mode timing #ring is used to switch the flow direction of the airflow to maintain the first heat storage bed 12a and the second heat storage bed. The temperature can be maintained to preheat the organic waste gas; wherein the heat storage material is mostly composed of ceramic materials. The conventional heat storage incinerator i Q a, operation and towel in the double-tower incinerator when entering and exiting the valve to switch the regenerator bed will generate - a peak corresponding to the concentration of the population to the smoke from the discharge (the efficiency of the destruction of the organic waste gas by the purification furnace can reach Above, and the inlet airflow will be directly discharged to the smoke when switching, so as to destroy the efficiency estimate, it is known that this concentration is 5 times higher than that in the incinerator, which has always caused the industry _; The disadvantage of the regenerative incinerator is that the switching peak of the P pollution is generated when the flow direction of the valve is switched. The lack of sweating makes it inconvenient for practical use. There is a clock in this section. In the invention period, a regenerative incinerator capable of reducing the switching peak value can be provided, and the conventional regenerative incinerator device can be reduced by providing a clean gas line, a gas system and a combination design The purpose of the valve group to switch the peak of the sweat flow when the flow direction of the airflow is to prevent the organic money from being used, and to use the equipment for the semi-conductor industry or the optoelectronic industry, it is a research and development system. The motivator of the invention is intended to be developed. SUMMARY OF THE INVENTION The main object of the present invention is to provide a regenerative incinerator that reduces switching peaks by providing a regenerative incinerator, a main exhaust gas line, an exhaust gas inlet, and a control group. The clean gas pipeline, the gas group and the -the windmill are combined to make the organic waste gas in the combustion cycle under the effect of high static pressure removal. Burns to prevent switching of peak sweats. The second-purpose object of the present invention is to provide a regenerative incineration furnace for reducing the scale value and to reduce the sweating and dyeing degree, and to cooperate with a conventional regenerative incinerator, by means of a heat storage incinerator, and a - waste main pipe Road, - exhaust gas inlet valve group, - to the control paste group, - clean air supply line, - gas control group and - the first - windmill combination design, to the _ m pipeline, so that the double tower type of heat storage When switching the flow direction of the airflow, the switch does not cause the peak value of the "stains (4)" for semiconductor devices, optoelectronic devices or other environmental users who need to remove the equipment to produce pollutants. The invention mainly comprises a heat storage incinerator, an exhaust gas main pipeline, an exhaust gas inlet valve group, a control side group, a clean gas pipeline, a gas control side group, and a first windmill; The pipeline is stored in the heat storage incinerator, and the exhaust gas pipeline is provided with an exhaust gas inlet valve group and a control valve group to control the switching pipeline to control the flow direction of the exhaust gas in the pipeline and to change the direction of the airflow. The source organic waste gas is not directly discharged; and one end of the clean air supply line is connected with the main exhaust gas line for feeding the gas into the main exhaust line, and the clean air supply line is provided with a gas control valve. 1329728 group and the first windmill, so that the gas can quickly enter the main pipeline of the exhaust gas, and when the accumulator incinerator switches the flow direction of the airflow, the gas in the clean air supply pipeline can be quickly reached to the storage key by the main pipeline of the exhaust gas. In the pass of the furnace, the unburned organic waste gas is sent to the chamber by the dust source source to prevent the untreated surface exhaust gas from being directly discharged, so as to remove the exhaust gas polluter. Other features and embodiments of the invention will be apparent from the following detailed description of the drawings. [Embodiment] Please refer to Fig. 2 for a schematic diagram of the structure of the accumulator incinerator for reducing the peak value of the present invention. The system includes a regenerative incinerator 1〇'--the main pipeline of the exhaust gas 2 〇, an exhaust gas The inlet valve group 3 ◦, the control valve group 4 〇, the clean air supply line (8), the gas control side group 60 and the - windmill 7 !; the thermal storage incinerator i _ the first regenerator bed U, The second regenerator bed 12 and the _combustion chamber 13, the calcining chamber (3) and the first-reservoir bed! i and the space at the top of the second regenerator bed i 2, and the first regenerator bed 1 1 and the second regenerator bed i 2 are each provided with at least a vent pipe 4 (the first gas line 1 4 1 , the second pass) The gas line χ 4 2) 'for the gas in and out, wherein the first heat storage bed 1 and the second heat storage bed 12 are filled with a heat storage material, which is shouted, metal, metal oxide or The combination of the above, the other difficult to burn chamber 丄 3 its combination of _ type combustion type, touch miscellaneous type, electrothermal oxidation type, electro-sewn type, silk reaction type, and its combustion chamber! 3 includes a fuel nozzle for the thermal energy of the combustion unit. Alternatively, an electric heater or an electric generator or the like may be used to provide the heat energy of the combustion chamber. And the exhaust gas main pipeline 20 system, and the first of the heat storage incinerator 丄Q-heat storage bed worker 10 1329728 and the second regenerator bed 12 (the first ventilation line 1 4 i, the second The vent line 1 4 2) is connected for the exhaust gas to enter the combustion chamber 13 to generate thermal oxidation, and the treated gas is discharged into the atmosphere', and the exhaust gas main pipeline 20 is provided with an exhaust gas inlet group 3 〇 and the control is provided The valve group 40' is in which the exhaust gas inlet valve group 3 of the present embodiment is composed of a three-way valve 31, and the control valve group 40 is a four-way valve 41 structure, and the exhaust gas inlet valve group 3 The 0 is disposed at the intake end of the main exhaust line 20 of the exhaust gas to control the ingress and egress of the exhaust gas, wherein the exhaust gas inlet valve block 30 is connected with an exhaust gas line 21 to the combustion chamber 13 through the exhaust gas inlet valve group 30. Controlling the switching line, and further connecting a heat exchanger 80 to the exhaust gas line 2 i for preheating, wherein the heat source of the heat exchanger 8 is a heating electric heater, a combustion heat source, and a plasma generator. Or one of the providers of waste heat recovery, the heat exchanger 80 may comprise a shell-and-tube heat exchange tube a passageway and a structure for feeding in and out of the organic exhaust gas (not shown); the heat exchange pipeline is filled with a flow of heat transfer medium for heat exchange operation; and the heat transfer medium that can be added includes: air, air, Water and scale oil."The more the shape (the heat transfer medium formed by heating, hot water, hot water and heat medium oil can be used by different methods; the heat transfer medium can be used with the factory machine Change as required). Further, the control valve group 40 is disposed in the main exhaust gas line 2 〇 near the heat storage incineration unit , to control the gas emission into and out of the first heat storage bed ii and the second heat storage bed i 2 ' By switching to the control group 4 Q (four) for the pipeline, the end of the main pipeline of the exhaust gas is connected with a turn 82 to reduce the gas out of the atmosphere, and on the main pipeline 2 G of the waste milk. The second windmill 7 2 is provided in the step-by-step manner, and the second wind turbine 7 2 is disposed at the front end of the exhaust gas inlet group 30 for forming a wind pressure to draw the gas of the gas. In addition, there is a clean air supply line 5 ◦, the clean air supply line 50-end system. The exhaust gas path 2 is connected to the gas to enter the main gas line 2 of the exhaust gas, and the clean air supply line 50 is provided with a gas control valve group 60 and a windmill 7 , t. The gas control valve group 6 (10) adopts a three-way valve 6丄 structure, and the gas control touch (four) G system is arranged on the dry money Lai pipeline 5 Q, and the miscellaneous (four) gas enters and exits, the gas __6 Q material - the road 5 i For ease of use, the gas control valve group 6 〇 is used to control the switching line, and the first windmill 71 is disposed at the clean air supply line 5 Q for sewing and pumping the pure main pipeline 20, Wherein the first windmill 7 1 ′ has a value of the air supply pressure specification value for the first f-heat bed “ 2 second regenerator bed 1 2 , thereby providing a double-column flow switching when the regenerative incinerator process is provided. 'The gas is sent to the clean air line 5 to prevent the direct discharge of the organic waste gas from the incoming line, so as to remove the waste gas. Please refer to the figures in Figures 3 and 4 for the different valve block structure. , wherein the exhaust gas inlet group 30, the control valve group 4 〇, and the gas control valve group 6 are designed by using a three-way valve structure Control _ change the pipeline, and the simple control paste group 4 (10) uses two three-way valves 4 2, 4 3 structure to form a regenerative incinerator that reduces the switching peak, including the -heat storage incinerator 10, - the main pipeline of the exhaust gas 2 〇, - exhaust gas inlet group 3 ◦, one to the control group 40, - clean air supply line 5 〇, a gas control group 6 2 and - the first windmill 7 i; the thermal storage incinerator 2 The first regenerator bed, the second regenerator bed 12, and the combustion chamber 13, the combustion η 3 system is in communication with the first-file bed worker 12^^728 and the first-heat storage bed 12 (') The first __ regenerator bed 及 and the second regenerator bed 12 are each provided with at least one vent line 14 (the first vent line 143, the second vent 144, and the second vent line i 4 5 The fourth vent line i 4 6), and the vent line 14 is designed to be in two-in and two-out states for the gas to enter and exit the gas and the main line of the exhaust gas 20 and the first of the heat storage incinerators i Q - f The hot bed i 丄 and the second f hot bed ^ 2 vent line 14 (the first vent line 丄 43, the third vent line i 4 5) are connected for the exhaust gas to enter the combustion chamber 13 3 turn, and The gas pipeline of Lin Hou (second pass) The pipeline 1 4 4, the fourth rail pipeline 1 4 6) is sent to the exhaust gas main pipeline 2 Q and then discharged into the atmosphere, and the exhaust gas into the main pipeline 2 Q is provided with the exhaust gas into the α-valve 3 〇 and the control The valve block 4 〇, wherein the exhaust gas inlet valve block 30 of the embodiment is composed of a three-way valve 3 structure, and the control valve group 4 is connected to the control valve group 4, and two three-way valves 4, 4 3 are adopted, the first = The valve 4 2 is arranged in the first vent line 丨 4 3 and the third vent line i 4 5 is connected to the main line 2 of the exhaust gas to control the direction of travel of the exhaust gas, and the second third The valve 4 3 is provided in the second ventilation line! 4 4 and the fourth ventilation 4 6 is connected to the main exhaust line 20 of the exhaust gas to control the direction of travel of the peak gas, and the exhaust gas inlet group 30 is disposed at the intake end of the main exhaust line 2 废气. The structure of the three-way valve 3 i is also used to control the ingress and egress of the exhaust gas, wherein the exhaust gas inlet _30 is connected with the exhaust gas line 2 m to the combustion chamber 13 by 'exhaust gas inlet _3 〇 to control the switching line, and The exhaust gas line 2 1 is further connected with a heat exchanger 80 0 for preheating, wherein the heat source of the heat exchanger 80 is an electric heating device, a combustion heat source, a plasma generator or waste heat recovery. One of the providers, the other is connected to the control valve group 4 〇 is set in the main exhaust line 2 〇 near the regenerative combustion 13 1329728. The furnace 10 is controlled to control the exhaust gas into the first heat storage bed i and the second regenerator bed ^ 2 In the middle and after the combustion of the gas, the pipeline is switched by the control valve group 4◦, and the end of the main pipeline 20 of the exhaust gas is connected with the smoke iu8 2 for discharging the gas out of the atmosphere.
中’另於廢氣進氣管路2 〇上進-步設有第二風車7 2，該第二風車 7 2係設鱗氣ita陳3 0之純’以卿錢縣姉管路中之 氣體，另該第二風車7 2亦可設於廢氣主要管路2◦之末端與煙自8 2之間（如第4®所示）’以供形姐縣姉#路巾之氣體者。 另設有-乾淨氣送風管路5 〇，該乾淨氣送風管路5 〇之一端係 與廢氣主要管路2 Q相連接，赌送人氣體進人廢氣主要管路2 〇 中，而該乾淨氣送風管路5 〇上設有氣體控制閥組6 〇及第一風車7 1，其中本實施例的氣體控制閥組6 〇係採用一個三通間6丄結構， 該氣體控糊組6⑽設於乾賴送風管路5 〇上，以供控制氣體進 出，該氣體控糊組6 〇連設有一氣體管路5 i，以供排放用，藉由In the middle of the exhaust gas intake pipe 2, the second windmill 7 2 is provided, and the second windmill 7 2 is equipped with a gas of the genus ita Chen 3 0 pure In addition, the second windmill 72 may be disposed between the end of the main exhaust line 2◦ and the smoke from 8 (as shown in the 4th) for the gas of the Xie County 姊# road towel. There is also a clean air supply line 5 〇, one end of the clean air supply line 5 连接 is connected with the main exhaust line 2 Q, and the gambling gas is sent into the main line 2 of the exhaust gas, and the clean The gas supply air line 5 is provided with a gas control valve group 6 〇 and a first windmill 7 1 , wherein the gas control valve group 6 of the present embodiment adopts a three-way 6 丄 structure, and the gas control paste group 6 (10) is provided. a gas line 5 , is connected to the air supply line 5 , to control the gas in and out, and the gas control group 6 is connected with a gas line 5 i for discharge.
氣體控制閥組6 0來控制切換管路，而第—風車7 i係設於乾淨氣送 風管路5 0之-端，以供將氣體拉抽送人廢氣進氣管似q中，其中 該第-風車7 1，其麼力規格值對第—f_ i、第二蓄熱床工2 之壓損具有克服之值’藉此’提供f熱焚化爐i Q之雙塔氣流切換時， 以乾淨氣賴管路5 〇送人_ ’防止未織錢廢氣直接排出，達 到去除廢氣汙染者。 請參考第5圖所示’係另一採用不同之閥組結構之示意圖，其中 該廢氣進口閥組3 〇、通向控制間組4 〇及氣體控制閥組6 〇係採用 14 1329728. 二通閥結構設計來控制切換管路，而該通向控綱組4 Q係採用四個 二通閥44、45、46、47結構組成。一種減除切換峰值之蓄熱 焚化爐，係包含有一蓄熱焚化爐i 〇、一廢氣主要管路2 〇、一廢氣 進口閥組3 0、一通向控制閥組4 〇、一乾淨氣送風管路5 〇、一氣 體控綱組6 0及-第-風車7 Q ;該蓄熱焚化爐丨〇設有第一蓄熱 床1 1、第二蓄熱床12及-燃燒室13，該燃燒室13係位與第一 蓄熱床11及第二蓄熱床12之頂部相通之空間，而該第一蓄熱床1 1及第二蓄熱床1 2各設有至少一通氣管路1 4(第一通氣管路1 4 3、第二通氣管路14 4'第三通氣管路14 5、第四通氣管路14 6)，而通氣管路14係設計成二進二出之狀態，以供氣體之進出。而 該廢氣主要管路2 0係與蓄熱焚化爐1〇之第一蓄熱床丄丄及第二蓄 熱床1 2的通氣管路1 4(第一通氣管路1 4 3、第三通氣管路1 4 5) 連接以供廢氣進入燃燒室13熱氧化，並將處理後之氣體經通氣管路 1 4 (第一通氣管路1 4 4、第四通氣管路1 4 6 )輸往廢氣主要管路 2 0再排出大氣中，而於廢氣主要管路2 〇上設有廢氣進口閥組3 〇 及通向控制閥組4 0，其中本實施例的廢氣進口閥組係採用二個二通 閥3 2、3 3結構組成，通向控制閥組4 0係採用四個二通閥4 4、 4 5、4 6、4 7結構，該第一個及第二個二通閥4 4、4 5係設於 第一通氣管路14 3及第三通氣管路14 5上，以控制廢氣之行進方 向，另該第三個及第四個二通閥46、47係設於第二通氣管路14 4及第四通氣管路14 6上的地方，以控制廢氣之行進方向，而該廢 15 1329728. 氣進口閥組3 0係設於廢氣主要管路2 0之進氣端，亦採用二個二通 閥32、33之結構以控制廢氣進出，其中廢氣進口閥組3〇連設有 一廢氣管路21通往燃燒室13中，藉由廢氣進口閥組3 〇來控制切 換管路，而該廢氣管路21上進一步連設有一熱交換器8 〇，以供預 先加熱用，其中該熱交換器8 0之熱源係採電熱器、燃燒熱源、電漿 產生器或廢熱回收其中一種提供者，另通向控制閥組4 〇係設於廢氣 主要管路2 0靠近蓄熱焚化爐1〇處，以控制廢氣之進出於第一蓄熱 床11及第二蓄熱床12中及燃燒後之氣體排放，藉由通向控制閥組 來切換管路，而該廢氣主要管路2〇之末端係連設有一煙囪82，以 供將氣體排放出大氣中，另於廢氣主要管路2〇上進一步設有第二風 車7 2，該第二風車72係設於廢氣進口閥組3〇之前端，以供形成 風壓來拉齡針之氣體，純帛二風車7 2亦可辦純主要管路 2 0之末端與煙囪之間（圖未示），以供形成風壓來拉抽管路中之氣體 者。 、 另設有一乾淨氣送風管路5 〇，該乾淨氣送風管路5 〇之一端係 與廢氣主要管路2 〇相連接，以供送人氣體進人廢氣主要管路2 〇 中’而該乾淨氣送風管路5◦上設有氣體控制閥組6 〇及第一風車了 1，其中本實施例的氣體控制閥組6 0係採用二個二通閥6 2、6 3 結構，該氣體蝴敝6 〇係設於乾淨氣送風管路5 Q上以供㈣ 氣體進出，該氣體控制閥組6 0連設有-氣艘管路5!，以供排放用， 藉由氣體控_組⑽來控伽換管路，而第-風車7 1係設於乾淨 1329728. ”、/1*目路5 〇之一端，以供將氣體拉抽送入廢氣主要管路2 〇中， 其中該第-風車7 i，其壓力規格值對第一蓄熱幻丄、第二蓄熱床 1 2之壓損具有克服之值，麻’提供f熱焚化爐丨q之雙塔氣流切 換時’以乾淨氣送風管路5 〇送入氣體’防止未燃燒有機廢氣直接排 出，達到去除廢氣汙染者。 由乂上可知’本發明之裝置係具有如下實用優點： 1、藉由乾淨氣送風管路與廢氣主要管路連接，而廢氣主要管路係與 蓄熱焚化爐之第-蓄熱床及第二蓄熱床的通氣管路連接，以供蓄 熱焚化爐之雙塔氣流_時，送人壓力較高之氣體將通氣管路形 成壓力源將其一蓄熱床空間内未處理之氣體進入燃燒 至’防止未燃燒有機廢氣直接排出，達到去除廢氣汙染者。 2藉Φ廢氣管路、通氣管路及纽賴管路上設有控綱組，以控 制管中之氣體流向’以避免雙塔氣流運作週期中切換時，產生切 換汗染峰值’防止切換峰值之汗染，以提升空氣品質者。 X上所述者，僅為本發明之較佳實施例而已，舉凡依本發明申請 專利範圍賴之均等設計變化，均應為本案之技術所涵蓋。 综上所述’本發明揭示一種可有效節省能源、並達到排放之標準 及效率之減除切換污料值之#熱焚化爐，具有_性以及產業上 之利用價值，爰依法提出發明專利申請。 17 【圖式簡單說明】 第1圖係為傳統蓄熱焚化爐之結構示意圖。 第2圖係為本發明第一實施例中減除切換峰值之蓄熱焚化爐實施例之 結構示意圖。 第3圖係為本發明第二實施例中減除切換峰值之蓄熱焚化爐實施例之 結構示意圖。 第4圖係為本發明第三實施例中減除切換峰值之蓄熱焚化爐實施例之 結構不意圖。 第5圖係為本發明第四實施例中減除切換峰值之蓄熱焚化爐實施例之 結構不意圖。 【主要元件符號說明】 10、 蓄熱焚化爐 11、 第一蓄熱床 12、 第二蓄熱床 13、 燃燒室 14、 通氣管路 141、第一通氣管路 14 2、第二通氣管路 1 4 3、第一通氣管路 14 4、第二通氣管路 14 5、第三通氣管路 1329728 14 6、第四通氣管路 2 0、廢氣主要管路 21、廢氣管路 3 0、廢氣進口閥組 31、三通閥 3 2、二通閥 3 3、二通閥 4 0、通向控制閥組 41、四通閥 4 2、三通閥 4 3、三通閥 4 4、二通閥 4 5、二通閥 4 6、二通閥 4 7、二通閥 5 0、乾淨氣送風管路 51、氣體管路 6 0、氣體控制閥組 61、三通閥 6 2、二通閥 6 3、二通閥 19 1329728 71、第一風車 7 2、第二風車 8 0、熱交換器 8 2、煙囪 1 0 a、蓄熱焚化爐 1 1 a、第二蓄熱床 12 a、第一蓄熱床 13 a、燃燒室 14 a、燃料喷嘴 15 a、火焰 21 a、第一流向調節閥 2 2 a、第二流向調節閥 2 3 a、第三流向調節閥 2 4 a、第四流向調節閥 2 8 a、風機 3 5 1 a、煙囪 20The gas control valve group 60 controls the switching line, and the first windmill 7 i is disposed at the end of the clean air supply line 50 for pulling the gas to the human exhaust gas inlet pipe, wherein the first - Windmill 7 1, the force specification value for the first -f_i, the second heat storage bed 2 pressure loss has the value of overcoming 'by this' to provide f heat incinerator i Q double tower airflow switching, to clean gas Lai pipeline 5 〇送人 _ 'Prevent the undistributed waste gas directly discharged, to achieve the removal of waste gas polluting. Please refer to Figure 5 for a diagram showing another structure of a different valve block. The exhaust gas inlet valve block 3 〇, the control group 4 〇 and the gas control valve group 6 are 14 1329728. The two-way valve The structure is designed to control the switching line, and the access control group 4 Q is composed of four two-way valves 44, 45, 46, 47. The invention relates to a regenerative incinerator for reducing the peak value of switching, comprising a regenerative incinerator i 〇, an exhaust gas main pipeline 2 〇, an exhaust gas inlet valve group 30, a control valve group 4 〇, and a clean air supply duct 5 〇, a gas control group 60 and a - windmill 7 Q; the regenerative incinerator is provided with a first regenerator bed 1 1 , a second regenerator bed 12 and a combustion chamber 13 , the combustion chamber 13 The first regenerator bed 11 and the second regenerator bed 12 are connected to each other, and the first regenerator bed 1 1 and the second regenerator bed 12 are each provided with at least one vent line 14 (the first vent line 1 4 3 The second vent line 14 4' is a third vent line 14 5 and a fourth vent line 14 6), and the vent line 14 is designed to be in two-in and two-out states for gas in and out. The exhaust gas main pipeline 20 is connected to the first regenerator bed of the regenerative incinerator 1 and the vent line 14 of the second regenerator bed 12 (the first ventilation line 14 3 , the third ventilation line) 1 4 5) connected for the thermal oxidation of the exhaust gas into the combustion chamber 13, and the treated gas is sent to the exhaust gas through the vent line 14 (the first vent line 14 4 and the fourth vent line 146) The pipeline 20 is discharged into the atmosphere, and the exhaust gas inlet valve group 3 〇 and the control valve group 40 are disposed on the main exhaust pipe 2 〇, wherein the exhaust gas inlet valve group of the embodiment adopts two two-way The valve 3, 3 3 is composed of a structure, and the control valve group 40 is connected to four two-way valves 4 4, 4 5, 4 6 and 4 7 , and the first and second two-way valves 4 4 4 5 is disposed on the first ventilation line 14 3 and the third ventilation line 14 5 to control the traveling direction of the exhaust gas, and the third and fourth two-way valves 46, 47 are disposed in the second passage The gas line 14 4 and the fourth vent line 14 6 are placed to control the direction of travel of the exhaust gas, and the waste 15 1329728. The gas inlet valve block 30 is disposed at the intake end of the main exhaust line 20 of the exhaust gas. Adopt two The two-way valves 32, 33 are configured to control the ingress and egress of the exhaust gas, wherein the exhaust gas inlet valve group 3 is connected with an exhaust gas line 21 to the combustion chamber 13, and the exhaust gas inlet valve group 3 is used to control the switching pipeline. Further, a heat exchanger 8 is further disposed on the exhaust gas line 21 for preheating, wherein the heat source of the heat exchanger 80 is a supplier of electric heating, combustion heat source, plasma generator or waste heat recovery. Further, the control valve group 4 is disposed at the exhaust gas main pipe 20 near the heat storage incinerator 1 to control the gas emission into and out of the first regenerator bed 11 and the second regenerator bed 12, The pipeline is switched by the control valve group, and a chimney 82 is connected to the end of the main pipeline 2 of the exhaust gas for discharging the gas out of the atmosphere, and further disposed on the main pipeline 2 of the exhaust gas. The second windmill 72 is disposed at the front end of the exhaust gas inlet valve group 3〇 for the gas to form the wind pressure to pull the amp, and the pure windmill 7 2 can also be used for the pure main pipeline 2 0 Between the end and the chimney (not shown) for the formation of wind pressure By pumping the gas in the conduit. There is also a clean air supply line 5 〇, one end of the clean air supply line 5 与 is connected with the main exhaust line 2 ,, for the supply of human gas into the main line of the exhaust gas 2 而A gas control valve group 6 〇 and a first windmill 1 are disposed on the clean air supply line 5, wherein the gas control valve group 60 of the embodiment adopts two two-way valves 6 2, 6 3 structure, the gas The butterfly 〇6 设 is installed on the clean air supply line 5 Q for (4) gas in and out, the gas control valve group 60 is connected with the gas pipeline 5! for discharge, by gas control _ group (10) to control the gamma exchange line, and the first windmill 7 1 is set at one end of the clean 1329728. ”, /1* 目路5 ,, for drawing the gas into the main pipeline 2 of the exhaust gas, wherein the first - Windmill 7 i, the pressure specification value has the value of overcoming the pressure loss of the first heat storage illusion and the second heat storage bed 12, and the air flow of the double tower flow when the heat supply of the heat incinerator is provided Pipeline 5 〇 Feeding gas 'Prevents unburned organic waste gas from being directly discharged to remove exhaust gas pollutants. As can be seen from the above description The utility model has the following practical advantages: 1. The clean air supply pipeline is connected with the main pipeline of the exhaust gas, and the main pipeline of the exhaust gas is connected with the first heat storage bed of the heat storage incinerator and the ventilation pipeline of the second heat storage bed for When the double-column airflow of the thermal storage incinerator is _, the gas with higher pressure is used to form a pressure source to ventilate the untreated gas in a regenerator bed space to prevent the unburned organic exhaust gas from being directly discharged to remove the exhaust gas. Polluters. 2 By means of the Φ exhaust line, the vent line and the Nilai line, there is a control group to control the flow of gas in the tube to avoid switching peaks during the switching of the operation of the two towers. Switching to the peak of the sweating to improve the air quality. The above is only the preferred embodiment of the present invention, and the uniform design changes according to the scope of the patent application of the present invention should be covered by the technology of the present invention. In summary, the present invention discloses a heat incinerator capable of effectively saving energy and achieving emission standards and efficiency, and having the value of switching pollutants, having _ sex and industrial benefits. Value, 提出Proposed invention patent application according to law. 17 [Simple description of the diagram] Figure 1 is a schematic diagram of the structure of a conventional regenerative incinerator. Fig. 2 is a diagram of the implementation of the regenerative incinerator in which the switching peak is subtracted in the first embodiment of the present invention. 3 is a schematic structural view of an embodiment of a regenerative incinerator in which a switching peak is subtracted in a second embodiment of the present invention. FIG. 4 is a regenerative incineration in which a switching peak is subtracted in a third embodiment of the present invention. The structure of the furnace embodiment is not intended. Fig. 5 is a schematic view showing the structure of the embodiment of the regenerative incinerator for reducing the peak switching in the fourth embodiment of the present invention. [Description of main components] 10. The regenerative incinerator 11, first The regenerator bed 12, the second regenerator bed 13, the combustion chamber 14, the vent line 141, the first vent line 14, the second vent line 143, the first vent line 144, and the second vent line 14 5. The third ventilation line 1329728 14 6. The fourth ventilation line 20, the exhaust main line 21, the exhaust line 30, the exhaust inlet valve group 31, the three-way valve 3, the two-way valve 3 3, two Through valve 40, leading to control valve group 4 1. Four-way valve 4, three-way valve 4 3, three-way valve 4 4, two-way valve 4 5, two-way valve 4 6 , two-way valve 47, two-way valve 50, clean air supply line 51 , gas line 60, gas control valve group 61, three-way valve 6, 2, two-way valve 63, two-way valve 19 1329728 71, first windmill 7.2, second windmill 80, heat exchanger 8 Chimney 10 a, regenerative incinerator 1 1 a, second regenerator bed 12 a, first regenerator bed 13 a, combustion chamber 14 a, fuel nozzle 15 a, flame 21 a, first flow regulating valve 2 2 a, Second flow regulating valve 2 3 a, third flow regulating valve 2 4 a, fourth flow regulating valve 2 8 a, fan 3 5 1 a, chimney 20