201217710 六、發明說明： 【發明所屬之技術領域】 本發明係有關一種蓄熱焚化爐之自淨裝置及方法，尤 指一種將焚化氣流之流向切換週期延長，俾讓蓄熱槽出口 端之溫度達到所設定之自淨焚化切換溫度，而利用高溫將 蓄熱材料底部之附著物質高溫熱脫附或分解去除，恢復其 蓄熱功能之設計者。 【先前技術】 按，生活和生産中廣泛應用的有機溶劑，在室溫下易 揮發成氣體，故又名揮發性有機物（Volatile Organic Compounds ’ VOCs)，而多數的VOCs對人體有一定毒性，必 須加以處理；其中，焚化法為VOCs廢氣處理方式之一種， 在適當條件下之VOCs去除率可達99%以上，燃燒後之產物 通常為水、二氧化碳、氮氧化物、硫氧化物…等，故為一 種可有效處理廢氣中所含之VOCs及臭氣之方法。 次按，VOCs通常會採用蓄熱焚化爐（Regenerative Thermal Oxidizer，RT0)予以焚化，第一圖所示為常見之 雙槽式蓄熱焚化爐，其於内部填充蓄熱材料（11a、lib)之 第一與第二蓄熱槽（l〇a、l〇b)之間連結燃燒室（12)，並將 一焚化氣流控制裝置（20)連結至每一蓄熱槽（10a、10b)， 而該焚化氣流控制裝置（20)之控制器（21)根據所設定之切 換時間控制切斷閥群（22a、22b、22c、22d)之啟閉，進而 切換焚化氣流於該第一與第二蓄熱槽（1 〇a、10b)之流向（一 流入且一流出）；藉此，其操作包含兩步驟：步驟1 :令切 201217710 斷間（22a)開、切斷閥（22b)關、切斷閥（22c)關、切斷閥（22d) 開’而將待焚化廢氣藉由該焚化氣流控制裝置（2〇)導入第 一蓄熱槽（l〇a)預熱至一定溫度，然後通過燃燒室（12)進入 第二蓄熱槽（l〇b) ’亦即燃燒後氣流之高溫會轉移儲存於第 二蓄熱槽（10b)中；步驟2 :待經過所設定之切換時間後， 該焚化氣流控制裝置（2〇)則令切斷閥（22a)關、切斷閥（22b) 開、切斷閥（22c)開、切斷閥（22d)關，而改將待焚化廢氣 導入已蓄熱之第二蓄熱槽（10b)將待焚化廢氣體預熱，再通 過燃燒室（12)進入已冷卻之第一蓄熱槽（1〇a)，燃燒後氣流 之高溫則再轉移儲存於第一蓄熱槽（1〇a)中，而完成一循環 熱交換。 然而’該蓄熱材料（lla、lib)之溫度會隨著深度而逐 漸下降，在焚化爐使用一段時間之後’該蓄熱材料（11&、 lib)底部因溫度不足’而會有高沸點有機物、有機聚合單 體、油霧及焦質（tar)類之附著物質，甚至導致堵塞，致使 該蓄熱材料（11a、lib)逐漸喪失蓄熱功能；其中，前述之 附著物質可於焚化爐系統關閉後以熱水或溶劑予以清除， 但僅能淺層清除並不能徹底清除乾淨；再者，另一種將附 著物質清除之方法，乃使用一外部熱源將逐一導入該第一 與第二蓄熱槽（l〇a、10b)之沖洗氣流加熱，而將該蓄熱材 料（11a、lib)由底部向上熱烘（bake-out)清除附著物質， 但此設計必須多加一組外部熱源與沖洗氣流之管線，增加 了燃料及設備之成本。 此外，雙槽式蓄熱焚化爐在蓄熱槽預熱/蓄熱切換時， 預熱蓄熱槽中之待焚化氣體會因尚未焚化而被排放，因此 201217710 會有未焚化氣體週期性排放之問題。而為解決雙槽式蓄熱 焚化爐之上述問題’亦有如第二圖所示之三（多）槽式蓄熱 焚化爐，其於内部填充蓄熱材料（3ia、31b、31c)之第一、 第二與第三蓄熱槽（30a、30b、30c)之間連結燃燒室（32)， 並將一焚化氣流控制裝置（4〇)連結至每一蓄熱槽（3〇a、 30b、30c)，而每一蓄熱槽（3〇a、3〇b、30c)尚連結一沖洗 " 氣流控制裝置（50) ’該焚化氣流控制裝置（40)之控制器（41) ， 根據所設定之切換時間控制切斷閥群（42a、42b、42c、42d、 42e、42f、51a、51b、51c)之啟閉，進而切換焚化氣流與 ® 沖洗氣流於每一蓄熱槽（30a、. 30b、30c)之流向（一焚化氣 流流入、一焚化氣流流出且一沖洗氣流流入）；藉此，較雙 槽式蓄熱焚化爐增設一蓄熱槽，而在蓄熱及預熱步驟間多 一個通入沖洗氣流之步驟（詳細之操作步驟，非為本案專利 標的，不再贅述），解決雙槽式蓄熱焚化爐會有未焚化氣體 週期性排放之問題，但其仍須藉由一外部熱源將沖洗氣流 加熱，俾將該蓄熱材料（31a、31b、31c)由底部向上熱烘清 除附著物質。 • 【發明内容】 本發明之主要目的，係欲提供一種蓄熱焚化爐之自淨 裝置及方法，而具有無須外部熱源即得以將附著於蓄熱材 料之物質徹底清除乾淨之功效。 為達上述功效，本發明蓄熱焚化爐之自淨裝置之結構 特徵’係於内部填充蓄熱材料之複數蓄熱槽之間連結燃燒 室，並將一焚化氣流控制裴置連結至每一蓄熱槽，且於該 焚化氣流控制裝置之焚化氣流出口端設置一溫度計，該溫 201217710 度計連結至該焚化氣流控制裝置之控制器，而該控制器令 B氣流進行常純式或是自淨模紅模式轉換及流向切 換；然而，該常態模式係根據所設定之常態焚化切換時間 控制切斷閥群之啟閉，進而切換焚化氣流於每—蓄熱槽之 流向，該自淨模式乃根據所設定之自淨焚化切換溫度控制 」 士刀斷閥群之啟閉，進而切換焚化氣流於每一蓄熱槽之流向 者。 山此夕卜進一步於該焚化氣流控制裝置之焚化氣流入口 • $設置第—璧力計且於出口端設置第二壓力計，該第一與 第二壓力計連結至該焚化氣流控制裝置之控制器，而令該 控制器根據所設定之蓄熱槽入口端與出口端之壓力差自動 進行常態模式與自淨模式之轉換。或者，該控制器根據手 動進行常態模式與自淨模式之轉換。 再者，該自淨模式另根據所設定之自淨焚化切換時間 控制切斷閥群之啟閉，進而強制切換焚化氣流於每一蓄熱 槽之流向，俾以做為防止蓄熱槽高溫悶燃之安全機制。另， .豸蓄熱槽為雙槽式或是多槽式。又，該常態焚化切換時間 為60〜18〇秒，該自淨焚化切換溫度為2〇〇〜45〇。匚，該自 淨焚化切換時間為該常態焚化切換時間之2〜6倍。 另者’本發明蓄熱焚化爐之自淨方法，係提供一自淨 模式轉換訊號，而令焚化氣流於每一蓄熱槽之流向切換模 式，由根據常態焚化切換時間控制流向切換之常態模式， 轉換成根據自淨焚化切換溫度控制流向切換之自淨模式 者0 201217710 ' 自净模式轉換訊號為蓄熱槽入口端與出口端 之壓力差或疋人員輸入。又，該自淨模式另根據所設定之 自淨焚化切換時間強制㈣焚化氣流於每—蓄熱槽之流 向俾以做為防止蓄熱槽高溫闊燃之安全機制。另，該常 態焚化切換時間為6〇〜⑽秒，該自淨焚化切換溫度為觸 〜450°c，該自淨焚化切換時間為該常態焚化切換時間之2 J 〜6倍。 【實施方式】 φ 首先，請參閱第三圖所示，本發明蓄熱焚化爐之自淨 裝置第-實施例’係以雙槽式f熱焚化爐為實施對象，其 於内部填充蓄熱材料（lla、llb)之第一與第二蓄熱槽 (l〇a、l〇b)之間連結燃燒室（12)，並將一焚化氣流控制裝 置（20)連結至每一蓄熱槽（1〇a、1〇b)，且於該焚化氣流控 制裝置（20)之焚化氣流出口端設置一溫度計（6〇),該溫度 6十（60)連結至該焚化氣流控制裝置（2〇)之控制器（21 )，而 該控制器（21)令焚化氣流進行常態模式或是自淨模式之模 式轉換及流向切換。 攀 . 然而’該常態模式係根據所設定之常態焚化切換時間 (通常為60〜180秒）控制切斷閥群（22a、22b、22c、22d) 之啟閉’進而切換焚化氣流於每一蓄熱槽（10a、1〇b)之流 向，又’該自淨模式乃根據所設定之自淨焚化切換溫度.控 制切斷閥群（22a、22b、22c、22d)之啟閉，進而切換焚化 氣流於每一蓄熱槽（l〇a、10b)之流向；其中，該常態模式 為一般蓄熱焚化爐之運轉模式，而該自淨模式則為本發明 201217710 所增》又之運轉模式，其乃將焚化氣流之流向切換週期較該 常態模式延長，俾讓該蓄熱槽（10a、10b)出口端之溫度達 到自淨焚化切換溫度（本案設定為200〜45(rc)，遂藉高溫 將該蓄熱材料（lla、llb)底部之附著物質分解去除，恢復 該蓄熱材料（11a、lib)之蓄熱功能。 再者，進一步於該焚化氣流控制裝置（20)之焚化氣流 入口端設置第一壓力計（71)且於出口端設置第二壓力計 (72)，該第一與第二壓力計（71、72)連結至該焚化氣流控 φ 制裝置（20)之控制器（21)，而令該控制器（21)根據所設定 之蓄熱槽壓力差自動進行常態模式與自淨模式之轉換；因 此，當蓄熱槽入口端與出口端之壓力差產生急遽擴大之趨 勢時，即表示該蓄熱材料（lla、llb)已有附著物質形成堵 塞之情事’該控制器（21)乃將焚化爐之運轉模式由常態模 式轉換成自淨模式；又，當蓄熱槽入口端與出口端恢復正 常壓力差時，則表示該蓄熱材料（lla、Ub)之附著物質已 被分解去除，該控制器（21)乃將焚化爐之運轉模式由自淨 φ 模式轉換回常態模式；不過，該控制器（21)除了根據所設 疋之蓄熱槽壓力差自動進行常態模式與自淨模式之轉換， 亦可由人員手動操作常態模式與自淨模式之轉換。 此外’為了預防該溫度計（60)失效而造成危險，該自 淨模式另根據所設定之自淨焚化切換時間（本案設定為該 常態焚化切換時間之2〜6倍）控制切斷閥群（22a、22b、 22c、22d)之啟閉’進而強制切換焚化氣流於每一蓄熱槽 (l〇a、l〇b)之流向，俾以做為防止蓄熱槽高溫悶燃之安全 201217710 機制。 藉此，本發明於雙槽式蓄熱焚化爐第一應用例之運轉 條件如下： 待焚化廢氣含有高沸點單乙醇氨（MEA，沸點171°C)與 二甲基亞颯（DMS0，沸點189°C);常態模式之入口溫度50 °C，焚化溫度850°C，出口平均溫度90°C，焚化氣流切換 週期90秒；自淨模式之入口溫度50°C，焚化溫度850°C， 出口溫度達250°C再切換焚化氣流流向，焚化氣流切換週期 約270秒。 又，本發明於雙槽式蓄熱焚化爐第二應用例之運轉條 件如下： 待焚化廢氣含有高沸點甲基β比咯啶酮（NMP，沸點202 °C);常態模式之入口溫度50°C，焚化溫度850°C，出口平 均溫度90°C，焚化氣流切換週期90秒；自淨模式之入口溫 度入口溫度50°C，焚化溫度850°C，出口溫度達250°C再 切換焚化氣流流向，焚化氣流切換週期約270秒。 另，本發明於雙槽式蓄熱焚化爐第三應用例之運轉條 件如下： 待焚化廢氣含有高沸點二甲基曱醯胺（DMF，沸點153 °C);常態模式之入口溫度5(TC，焚化溫度850°C，出口平 均溫度90°C，焚化氣流切換週期90秒；自淨模式之入口溫 度50°C，焚化溫度850°C，出口溫度達200°C再切換焚化 氣流流向，焚化氣流切換週期約210秒。 另者，請參閱第四圖所示，本發明蓄熱焚化爐之自淨 201217710 裝置第二實施例，係以多槽式蓄熱焚化爐為實施對象，其 於内部填充蓄熱材料（31a、31b、31c)之第一、第二與第三 蓄熱槽（30a、30b、30c)之間連結燃燒室（32)，並將一焚化 氣流控制裝置（40)連結至每一蓄熱槽（30a、30b、30c)，而 每一蓄熱槽（30a、30b、30c)尚連結一沖洗氣流控制裝置 (50)，且於該焚化氣流控制裝置（40)之焚化氣流出口端設 J 置一溫度計（60)，該溫度計（60)連結至該焚化氣流控制裝 ' 置（40)之控制器（41)，而該控制器（41)令焚化氣流進行常 態模式或是自淨模式之模式轉換及流向切換。 然而，該常態模式係根據所設定之常態焚化切換時間 (通常為60〜180秒）控制切斷閥群（42a、42b、42c、42d、 42e、42f、51a、51b、51c)之啟閉，進而切換焚化氣流與 沖洗氣流於每一蓄熱槽（30a、30b、30c)之流向；又，該自 淨模式乃根據所設定之自淨焚化切換溫度控制切斷閥群 (42a、42b、42c、42d、42e、42f、51a、51b、51c)之啟閉， 進而切換焚化氣流與沖洗氣流於每一蓄熱槽（10a、1 Ob)之 流向；其操作步驟乃與第一實施例相同，不再贅述。 9 藉此，本發明於多槽式蓄熱焚化爐第一應用例之運轉 條件如下： 待焚化廢氣含有聚合物笨乙烯（Styrene)與生產透明 - 塑料聚甲基丙烯酸甲酯（PMMA )的單體甲基丙稀酸甲酯 (MMA);常態模式之入口溫度50°C，焚化溫度850°C，出 口平均溫度90°C，焚化氣流切換週期90秒；自淨模式之入 口溫度50°C，焚化溫度850°C，出口溫度達350°C再切換 -10 - 201217710 焚化氣流流向，焚化氣流切換週期約36〇秒。 又，本發明於雙槽式蓄熱焚化爐第二應用例之運轉條 件如下： 待焚化廢氣含有二甲硫醚（DMS)與二曱基亞颯 (廳〇,彿點189。〇;常態模式之入口溫度35t，焚化溫 度825°C，出口平均溫度11(rc，焚化氣流切換週期9〇秒； 自淨模式之入口溫度35。〇，焚化溫度825<t，出口溫度達 250 C再切換焚化氣流流向，焚化氣流切換週期約秒。 φ 基於如是之構成，本發明係讓蓄熱焚化爐之運轉模 式，除了原本之常態模式之外另增設了自淨模式，而該自 淨模式乃當蓄熱槽内部之蓄熱材料有附著物質堵塞時，藉 由將焚化氣流之流向切換週期較該常態模式延長，俾讓蓄 &槽出口端之溫度達到所設定之自淨焚化切換溫度，利用 高溫將蓄熱材料底部之附著物質分解去除，恢復其蓄熱功 能；然而’本發明所增設之自淨模式，並不須藉助外部熱 源’係由焚化爐本身之焚化溫度將蓄熱材料底部之附著物 • 冑高溫熱脫附或分解去除，而具有無須外部熱源即得以將 附著於蓄熱材料之物質徹底清除乾淨之功效。 綜上所述，本發明所揭示之技術手段，確具「新穎性」、 「進步性」及「可供產業利用」等發明專利要件，祈請鈞 • 局惠賜專利，以勵發明，無任德感。 #，上賴揭露之圖式、說明，僅為本發日月之較佳實 施例，大凡熟悉此項技藝人士，依本案精神範缚所作之修 飾或等效變化，仍應包括本案申請專利範圍内。 场· -11 - 201217710 【圖式簡單說明】 第一圖係習知雙槽式蓄熱焚化爐之結構說明圖。 第二圖係習知多槽式蓄熱焚化爐之結構說明圖。 第三圖係本發明實施於雙槽式蓄熱焚化爐之結構說明 圖。 ^ 第四圖係本發明實施於多槽式蓄熱焚化爐之結構說明 圖。 【主要元件符號說明】 籲 （l〇a、10b)蓄熱槽 (11a、lib)蓄熱材料 (12)燃燒室 (20) 焚化氣流控制裝置 (21) 控制器 (22a、22b、22c、22d)切斷閥 (30a、30b、30c)蓄熱槽 (31a、31b、31c)蓄熱材料 • (32)燃燒室 (40) 焚化氣流控制裝置 (41) 控制器 (42a、42b、42c、42d、42e、42f)切斷閥 - (50)沖洗氣流控制裝置 . (51a、51b、51c)切斷閥 (60)溫度計 (71、72)壓力計 -12 -201217710 VI. Description of the Invention: [Technical Field] The present invention relates to a self-cleaning device and method for a heat storage incinerator, and more particularly to extending a flow switching cycle of an incineration gas stream, and letting the temperature at the outlet end of the heat storage tank reach the set The designer who switches the temperature from the net incineration and uses the high temperature to thermally desorb or decompose the attached material at the bottom of the heat storage material to restore its heat storage function. [Prior Art] Organic solvents, widely used in life and production, are easily volatilized into gases at room temperature, so they are also known as Volatile Organic Compounds 'VOCs. Most VOCs are toxic to humans. The incineration method is one of the treatment methods of VOCs waste gas. Under suitable conditions, the removal rate of VOCs can reach more than 99%, and the products after combustion are usually water, carbon dioxide, nitrogen oxides, sulfur oxides, etc. It is a method for effectively treating VOCs and odors contained in exhaust gas. Sub-press, VOCs are usually incinerated using a Regenerative Thermal Oxidizer (RT0). The first figure shows a common two-slot regenerative incinerator, which is filled with the first heat storage material (11a, lib). A combustion chamber (12) is coupled between the second heat storage tanks (10a, lb), and an incineration gas flow control device (20) is coupled to each of the heat storage tanks (10a, 10b), and the incineration gas flow control device (20) The controller (21) controls the opening and closing of the shut-off valve group (22a, 22b, 22c, 22d) according to the set switching time, and further switches the incineration gas flow to the first and second heat storage tanks (1 〇a) , 10b) flow direction (one inflow and first-class out); thereby, its operation consists of two steps: Step 1: make cut 201217710 break (22a) open, shut off valve (22b) off, shut off valve (22c) off The shut-off valve (22d) is opened, and the incineration gas to be incinerated is introduced into the first heat storage tank (l〇a) by the incineration gas flow control device (2〇) to be preheated to a certain temperature, and then enters the first stage through the combustion chamber (12). The second heat storage tank (l〇b) 'that is, the high temperature of the gas stream after combustion will be transferred and stored in the second heat storage tank (10b) Step 2: After the set switching time, the incineration airflow control device (2〇) closes the shut-off valve (22a), shuts off the valve (22b), and closes the shut-off valve (22c). The shut-off valve (22d) is closed, and the waste gas to be incinerated is introduced into the second heat storage tank (10b) that has been recharged to preheat the waste gas to be incinerated, and then enters the cooled first heat storage tank through the combustion chamber (12) (1〇 a) The high temperature of the gas stream after combustion is transferred to the first heat storage tank (1〇a) to complete a cycle of heat exchange. However, the temperature of the heat storage material (lla, lib) will gradually decrease with depth. After using the incinerator for a period of time, the bottom of the heat storage material (11&, lib) will have high boiling organic matter and organic Polymerized monomer, oil mist and tar-like substances, even causing clogging, causing the heat storage material (11a, lib) to gradually lose heat storage function; wherein the aforementioned adhesion substance can be heated after the incinerator system is turned off Water or solvent is removed, but it can only be removed by shallow layer and cannot be completely removed. In addition, another method of removing the adhering substances is to introduce the first and second heat storage tanks one by one using an external heat source (l〇a The flushing airflow of 10b) is heated, and the heat accumulating material (11a, lib) is bake-out from the bottom to remove the adhering substance, but the design must add a set of external heat source and flushing gas pipeline to increase the fuel. And the cost of the equipment. In addition, when the double-tank type thermal storage incinerator is switched between preheating/heat storage in the heat storage tank, the gas to be incinerated in the preheating heat storage tank will be discharged because it has not been incinerated, so there will be a problem of periodic discharge of unburned gas in 201217710. In order to solve the above problems of the two-tank type heat storage incinerator, there is also a three (multi) trough type regenerative incinerator as shown in the second figure, which is internally filled with the first and second heat storage materials (3ia, 31b, 31c). A combustion chamber (32) is coupled to the third heat storage tank (30a, 30b, 30c), and an incineration gas flow control device (4〇) is coupled to each of the heat storage tanks (3〇a, 30b, 30c), and each A heat storage tank (3〇a, 3〇b, 30c) is connected to a flushing " airflow control device (50) 'the controller (41) of the incineration airflow control device (40), according to the set switching time control cut Opening and closing of the shut-off valve group (42a, 42b, 42c, 42d, 42e, 42f, 51a, 51b, 51c), thereby switching the flow of the incineration gas stream and the flushing gas flow in each of the heat storage tanks (30a, 30b, 30c) ( An incineration gas stream flows in, an incineration gas stream flows out and a flushing gas stream flows in; thereby, a heat storage tank is added to the double-tank type heat storage incinerator, and a step of flushing air flow is introduced between the heat storage and preheating steps (detailed The operation steps are not the patent subject of this case, and will not be described again) No problem will incineration incinerator exhaust gases of the periodic, but still by an external heat source to heat the purge stream, to serve the storage material (31a, 31b, 31c) from the bottom upwards hot baking clear adhering substance. SUMMARY OF THE INVENTION The main object of the present invention is to provide a self-cleaning device and method for a heat storage incinerator, which has the effect of completely removing the material adhering to the heat storage material without an external heat source. In order to achieve the above effects, the structural feature of the self-cleaning device of the regenerative incinerator of the present invention is to connect the combustion chamber between the plurality of heat storage tanks filled with the heat storage material, and connect an incineration gas flow control device to each of the heat storage tanks, and The incineration gas flow control device is provided with a thermometer at the outlet end of the incineration gas stream, and the temperature 201217710 is connected to the controller of the incineration gas flow control device, and the controller converts the B gas flow into a constant-purity or self-cleaning mode. Switching; however, the normal mode controls the opening and closing of the shut-off valve group according to the set normal incineration switching time, and further switches the flow direction of the incineration gas flow in each of the heat storage tanks, and the self-cleaning mode is controlled according to the set self-cleaning switching temperature The opening and closing of the knife-breaking valve group, and then switching the flow of the incineration gas flow to each of the heat storage tanks. The mountain further extends the incineration gas flow inlet of the incineration gas flow control device. • The first pressure gauge is installed and a second pressure gauge is disposed at the outlet end, and the first and second pressure gauges are coupled to the control of the incineration gas flow control device. The controller automatically switches between the normal mode and the self-cleaning mode according to the pressure difference between the inlet end and the outlet end of the set heat storage tank. Alternatively, the controller manually switches between the normal mode and the self-clean mode. Furthermore, the self-cleaning mode controls the opening and closing of the shut-off valve group according to the set self-cleaning incineration switching time, thereby forcibly switching the flow direction of the incineration gas flow in each heat storage tank, thereby serving as a safety mechanism for preventing high temperature smoldering of the heat storage tank. . In addition, the enthalpy is a double tank or a multi tank. Further, the normal incineration switching time is 60 to 18 sec., and the self-incineration switching temperature is 2 〇〇 to 45 〇.匚, the self-incineration switching time is 2 to 6 times of the normal incineration switching time. In addition, the self-cleaning method of the regenerative incinerator of the present invention provides a self-cleaning mode switching signal, and the inflowing mode of the incineration gas flow in each of the regenerators is controlled by the normal mode of the flow switching according to the normal incineration switching time. Self-cleaning incineration switching temperature control flow switching mode of self-cleaning mode 0 201217710 ' The self-cleaning mode conversion signal is the pressure difference between the inlet end and the outlet end of the regenerator and the input of the personnel. In addition, the self-cleaning mode is forced to (4) the inflow of the incineration gas flow in each of the heat storage tanks according to the set self-cleaning incineration switching time as a safety mechanism for preventing high-temperature and wide-burning of the heat storage tank. In addition, the normal incineration switching time is 6 〇 to (10) seconds, and the self-cleaning switching temperature is a touch of ~450 ° C, and the self-cleaning switching time is 2 J to 6 times of the normal incineration switching time. [Embodiment] φ First, as shown in the third figure, the self-cleaning device of the present invention is a two-tank f-heat incinerator, which is filled with a heat storage material (lla, Ll)) connecting the combustion chamber (12) between the first and second heat storage tanks (10a, l), and connecting an incineration gas flow control device (20) to each of the heat storage tanks (1〇a, 1) 〇b), and a thermometer (6〇) is disposed at the outlet end of the incineration gas stream of the incineration gas flow control device (20), and the temperature is sixty (60) connected to the controller of the incineration gas flow control device (2〇) (21 And the controller (21) enables the incineration airflow to perform mode switching and flow direction switching in the normal mode or the self-cleaning mode. However, the normal mode controls the opening and closing of the shut-off valve group (22a, 22b, 22c, 22d) according to the set normal incineration switching time (usually 60 to 180 seconds), thereby switching the incineration gas flow to each heat storage. The flow direction of the grooves (10a, 1〇b), and the self-cleaning mode controls the opening and closing of the shut-off valve group (22a, 22b, 22c, 22d) according to the set self-cleaning switching temperature, and then switches the incineration gas flow to each a flow direction of a heat storage tank (l〇a, 10b); wherein the normal mode is an operation mode of a general regenerative incinerator, and the self-cleaning mode is an operation mode of the invention added in 201217710, which is an incineration airflow The flow switching cycle is extended from the normal mode, so that the temperature at the outlet end of the heat storage tank (10a, 10b) reaches the self-cleaning switching temperature (this case is set to 200 to 45 (rc), and the heat storage material (lla, llb) is taken by high temperature. The bottom attached material is decomposed and removed to restore the heat storage function of the heat storage material (11a, lib). Further, a first pressure gauge (71) is further disposed at the inlet end of the incineration gas stream of the incineration gas flow control device (20) and is disposed at the outlet. end a second pressure gauge (72) is coupled to the controller (21) of the incineration airflow control device (20), and the controller (21) is The set pressure difference of the heat storage tank automatically switches between the normal mode and the self-cleaning mode; therefore, when the pressure difference between the inlet end and the outlet end of the heat storage tank increases sharply, the heat storage material (lla, llb) is attached. The substance forms a blockage. 'The controller (21) converts the operation mode of the incinerator from the normal mode to the self-clean mode; and when the inlet end and the outlet end of the heat storage tank return to the normal pressure difference, it indicates the heat storage material (lla) The attached material of Ub) has been decomposed and removed. The controller (21) converts the operation mode of the incinerator from the self-cleaning φ mode back to the normal mode; however, the controller (21) is not only according to the heat storage tank pressure set. The difference automatically switches between the normal mode and the self-clean mode, and can also be manually switched between the normal mode and the self-clean mode by the person. In addition, in order to prevent the thermometer (60) from being dangerous, the self-cleaning mode In addition, according to the set self-cleaning incineration switching time (this case is set to 2 to 6 times of the normal incineration switching time), the shut-off valve group (22a, 22b, 22c, 22d) is controlled to open and close, and then the incineration gas flow is forcibly switched. The flow direction of the heat storage tanks (l〇a, l〇b) is used as a safety mechanism to prevent high temperature smoldering of the heat storage tank. The operating conditions of the first application example of the present invention in the double tank type heat storage incinerator are as follows: The gas to be incinerated contains high boiling point monoethanolamine (MEA, boiling point 171 ° C) and dimethyl hydrazine (DMS0, boiling point 189 ° C); normal mode inlet temperature 50 ° C, incineration temperature 850 ° C, average outlet temperature At 90 °C, the incineration gas flow switching cycle is 90 seconds; the inlet temperature of the self-cleaning mode is 50 °C, the incineration temperature is 850 °C, the outlet temperature is 250 °C, and the incineration gas flow direction is switched, and the incineration gas flow switching cycle is about 270 seconds. Further, the operating conditions of the second application example of the double-tank type thermal storage incinerator of the present invention are as follows: The gas to be incinerated contains a high boiling point methyl β-pyrrolidone (NMP, boiling point 202 ° C); the inlet temperature of the normal mode is 50 ° C The incineration temperature is 850 ° C, the average outlet temperature is 90 ° C, the incineration gas flow switching cycle is 90 seconds; the inlet temperature of the self-cleaning mode is 50 ° C, the incineration temperature is 850 ° C, the outlet temperature is 250 ° C, and the flow of the incineration gas is switched. The incineration gas flow switching cycle is about 270 seconds. In addition, the operating conditions of the third application example of the present invention in the double-tank type thermal storage incinerator are as follows: The waste gas to be incinerated contains high boiling point dimethyl decylamine (DMF, boiling point 153 ° C); the inlet temperature of the normal mode is 5 (TC, The incineration temperature is 850 °C, the average outlet temperature is 90 °C, the incineration gas flow switching period is 90 seconds; the inlet temperature of the self-cleaning mode is 50 °C, the incineration temperature is 850 °C, the outlet temperature is 200 °C, then the incineration gas flow direction is switched, and the incineration gas flow is switched. The cycle is about 210 seconds. In addition, as shown in the fourth figure, the second embodiment of the self-cleaning 201217710 device of the regenerative incinerator of the present invention is a multi-tank regenerative incinerator, which is internally filled with a heat storage material (31a). a combustion chamber (32) connected between the first, second and third heat storage tanks (31a, 30b, 30c) of 31, 31c), and an incineration gas flow control device (40) coupled to each heat storage tank (30a) And 30b, 30c), and each of the heat storage tanks (30a, 30b, 30c) is connected to a flushing airflow control device (50), and a thermometer is arranged at the outlet end of the incineration airflow of the incineration airflow control device (40). 60), the thermometer (60) is linked to the incineration The airflow control device (40) is a controller (41), and the controller (41) causes the incineration airflow to perform a mode switching and a flow direction switching in a normal mode or a self-cleaning mode. However, the normal mode is based on the set normal state. The incineration switching time (usually 60 to 180 seconds) controls the opening and closing of the shut-off valve group (42a, 42b, 42c, 42d, 42e, 42f, 51a, 51b, 51c), thereby switching the incineration gas flow and the flushing gas flow to each heat storage. The flow direction of the grooves (30a, 30b, 30c); further, the self-cleaning mode controls the shut-off valve group (42a, 42b, 42c, 42d, 42e, 42f, 51a, 51b, 51c) according to the set self-cleaning switching temperature Opening and closing, and then switching the flow direction of the incineration gas stream and the flushing gas flow in each of the heat storage tanks (10a, 1 Ob); the operation steps are the same as those in the first embodiment, and will not be described again. 9 Thereby, the present invention is multi-tank type heat storage. The operating conditions of the first application of the incinerator are as follows: The incineration waste gas contains a polymer Styrene and a monomer for producing transparent-plastic polymethyl methacrylate (PMMA) methyl methacrylate (MMA); Normal mode inlet temperature 50 ° C, incineration temperature 850 ° C, the average temperature of the outlet is 90 ° C, the incineration gas flow switching cycle is 90 seconds; the inlet temperature of the self-cleaning mode is 50 ° C, the incineration temperature is 850 ° C, the outlet temperature is 350 ° C and then the switch -10 - 201217710 Incineration gas flow direction, incineration The gas flow switching cycle is about 36 sec. Further, the operating conditions of the second application example of the present invention in the double-tank type thermal storage incinerator are as follows: The waste gas to be incinerated contains dimethyl sulfide (DMS) and diterpenoids (hall, buddha) Point 189.常; normal mode inlet temperature 35t, incineration temperature 825 °C, outlet average temperature 11 (rc, incineration gas flow switching cycle 9 sec; self-cleaning mode inlet temperature 35. 〇, incineration temperature 825 < t, outlet temperature up to 250 C Then, the flow direction of the incineration gas flow is switched, and the switching cycle of the incineration gas flow is about seconds. φ Based on the constitution, the present invention allows the operation mode of the thermal storage incinerator to be added to the self-cleaning mode in addition to the original normal mode, and the self-cleaning mode is to store heat. When the heat storage material inside the tank is blocked by the adhering substance, the flow rate of the incineration gas flow is extended by the normal mode, and the temperature of the outlet end of the storage tank reaches the set self-cleaning switching temperature, and the heat storage material is used at a high temperature. The attached material at the bottom is decomposed and removed to restore its heat storage function; however, the self-cleaning mode added by the present invention does not require an external heat source to remove the deposit at the bottom of the heat storage material from the incineration temperature of the incinerator itself. Attached or decomposed and removed, and the material attached to the heat storage material can be completely removed without an external heat source In summary, the technical means disclosed in the present invention have the invention patents such as "novelty", "progressiveness" and "available for industrial use", and pray for the patent to encourage the invention. There is no sense of morality. #, The drawings and descriptions of the disclosure are only the preferred embodiments of the present day and the month, and those who are familiar with this skill, who have made modifications or equivalent changes according to the spirit of the case, still It should be included in the scope of the patent application of this case. Field · -11 - 201217710 [Simple description of the diagram] The first picture is the structural description of the conventional double-tank type thermal storage incinerator. The second picture is the structure of the conventional multi-tank type thermal storage incinerator The third figure is a structural explanatory diagram of the present invention implemented in a double-tank type heat storage incinerator. The fourth figure is a structural explanatory diagram of the present invention implemented in a multi-tank type heat storage incinerator. L〇a, 10b) heat storage tank (11a, lib) heat storage material (12) combustion chamber (20) incineration gas flow control device (21) controller (22a, 22b, 22c, 22d) shut-off valve (30a, 30b, 30c) Heat storage tank (31a, 31b, 31c) heat storage material • (32) burning Chamber (40) Incineration airflow control device (41) Controller (42a, 42b, 42c, 42d, 42e, 42f) shut-off valve - (50) flushing airflow control device. (51a, 51b, 51c) shut-off valve (60 ) Thermometer (71, 72) pressure gauge -12 -