• M323583 八、新型說明： 【新型所屬之技術領域】 高效能 本創作係有關於-種蓄熱式焚化爐，尤指具有 蓄熱式廢氣焚化爐。 【先前技術】• M323583 VIII. New Description: [New Technology Area] High Performance This creation is about a type of regenerative incinerator, especially a regenerative exhaust gas incinerator. [Prior Art]
逆木，國内外對於裱保議題日益重視，對於工 排放標準日趨嚴格，揮發性有機物（v〇Cs) 二二= 污染防治重點之一。 則工氣 焚化法為處理VOCs廢氣之一種，在適當焚化條件 VOCs之去除率可達99%以上，燃燒產物依進料氣體 所不同，通常之產物為水、二氧化碳、氮氧化物、硫氧化 物等。焚化法一般可有效改善廢氣中所含之v〇Cs及臭氣 問題，然而，其相當耗費燃料。因此，燃燒器之設計應= V〇Cs與惡臭物質直接通過火焰，並有足夠之燃燒溫度二佟 留時間及適當氣流強度，以提高去除率。 τ 如美國專利案弟5,837,205號中所揭示，一般蓄熱式冲未 化爐（Regenerative Thermal Oxidizer ; RTO)至少包括一 個蓄熱床、進氣控制設備、加熱及溫度控制設備，蓄熱床 内填充石質或陶究蓄熱材料。雙蓄熱床式焚化爐之操作包 含2步驟： 步驟1 :將欲處理氣體先進入一蓄熱床（A床）預熱 至一定溫度，然後通過火焰燃燒後再進入另一蓄熱床（B 床），此時，燃燒後之高溫氣流會將B床加熱，即將高溫氣 5 M323583 流轉移儲存於B床之蓄熱材料中。 已蓄待—設料間經過後，改將欲處理氣體導入 已畜”、、之B床職，再賴燒錢人 氣流可再將熱儲存於A床，而完成-猶環=床- 然雙蓄熱床式焚罐在賴床預熱/㈣切換時， 預,、、、之蓄熱床中的欲處理氣體會因、Counter-wood, domestic and international attention to environmental protection issues, the increasingly strict standards for industrial emissions, volatile organic compounds (v〇Cs) 22 = one of pollution prevention and control. The gas incineration method is a kind of exhaust gas for treating VOCs. The removal rate of VOCs under appropriate incineration conditions can reach more than 99%, and the combustion products are different depending on the feed gas. The usual products are water, carbon dioxide, nitrogen oxides, sulfur oxides. Wait. The incineration method generally improves the v〇Cs and odors contained in the exhaust gas, however, it is quite expensive. Therefore, the design of the burner should = V〇Cs and the odorous material pass directly through the flame, and have sufficient combustion temperature retention time and appropriate gas flow intensity to increase the removal rate. τ As disclosed in U.S. Patent No. 5,837,205, a Regenerative Thermal Oxidizer (RTO) includes at least one regenerator bed, intake control device, heating and temperature control equipment, and a regenerative bed filled with stone or Pottery heat storage material. The operation of the double regenerative bed incinerator comprises two steps: Step 1: The gas to be treated is firstly heated into a regenerator bed (A bed) to be preheated to a certain temperature, and then burned by the flame before entering another regenerator bed (B bed). At this point, the high temperature gas stream after combustion will heat the B bed, that is, the high temperature gas 5 M323583 stream is transferred and stored in the heat storage material of the B bed. It has been reserved - after the passage of the material, the gas will be introduced into the livestock, and the B bed will be stored in the A bed, and then the heat will be stored in the A bed, and the completion - Yuhuan = bed - When the double regenerative bed type incinerator is used for preheating/(4) switching, the gas to be treated in the preheating bed of pre, , and
蟪〇弟-A圖所示，蓄熱式焚化爐出口濃度度於每次闕 件切換時’會有未處理氣體交差污染排放及洩漏（尖峰 處）。相對而言，未處理氣體之燃燒破壞去除效率也會有週 期性的低落，如第一 B圖。As shown in Figure A, the regenerative incinerator outlet concentration will have untreated gas cross-contamination emissions and leakage (peaks) at each switch. In contrast, the efficiency of combustion damage removal of untreated gas is also periodically degraded, as shown in Figure B.
提升閥（poppet valve)之基本構造如第二圖所示，當 驅動元件303將控制閥碟片（disc ) 3〇2下壓，則氣流可由 進氣孔304進入而由出氣孔3〇5流出；反之，若驅動元件 303將控制閥碟片（disc) 3〇2上提，則氣流可由進氣孔3〇4 進入而由出氣孔306流出。因此，提升閥可快速輕易改變 官線上氣流流向，而用來代替傳統之碟閥（buttof^ valve)。美國專利案第6,〇39,927號揭示一種配備提升閥之 二蓄熱床焚化爐，其目的在於改良提升閥之結構，以便使 熱交換時氣流變換更加順暢，同時增加提升閥之耐用度。 然而，其並未解決上述二蓄熱床焚化爐預熱/蓄熱切換時有 未處理之氣體洩漏的問題。 為解決上述雙蓄熱床焚化爐之缺點，亦有提出三蓄熱 床焚化爐，即有三蓄熱床（A、B及C床），且每一蓄熱床 6 ^ M323583 除進氣及出氣端外，尚包含一沖洗端(purge)。具體而言， ^ 其操作方式包含6步驟： 步驟1 :當Α床導入廢氣預熱時，Β床通入沖洗氣流 (purge gas)將上一循環中該床未處理之廢氣沖入廢氣流 中，經燃燒後通入C床導出並將熱儲存； • 步驟2 : A床導入廢氣預熱，B床停止沖洗而導出氣流 _ 並將熱儲存，C床停止導出廢氣而通入沖洗氣流； 步驟3 : A床停止導入廢氣預熱而通入沖洗氣流，B床 * 導出氣流並將熱儲存，C床停止沖洗而導入廢氣預熱； 步驟4 : A床停止沖洗而導出氣流並將熱儲存，B床停 止導出廢氣而通入沖洗氣流，C床導入廢氣預熱； ‘ 步驟5 : A床導出氣流並將熱儲存，B床停止沖洗而導 ▲ 入廢氣預熱，C停止床導入廢氣預熱而通入沖洗氣流；及 步驟6 : A床停止導出廢氣而通入沖洗氣流，B床導入 廢氣預熱，C停止沖洗而導出氣流並將熱储存，而完成一 φ_ 循環。 簡而言之，三蓄熱床焚化爐因在蓄熱及預熱步驟間多 一個通入沖洗氣流之步驟，故需多一個蓄熱床。然而，三 蓄熱床焚化爐雖然解決二蓄熱床焚化爐預熱/蓄熱切換時 有未處理之氣體交差污染排放及洩漏等低效率及惡臭的問 _ 題的問題，但其裝置成本較高，且因結構繁複，控制閥動 件繁多，操作可靠度低，維修亦屬不易。 因此，三蓄熱床焚化爐並不是一種最佳之解決方法， 如何提供一種裝置成本低、結構簡易、易於控制、操作可 7 M323583 靠度高及維修之蓄熱式焚化爐係為相關業者所急迫有待尋 求解決之方案以及改進之處。 【新型内容】The basic configuration of the poppet valve is as shown in the second figure. When the driving member 303 presses the control valve disc 3〇2, the air flow can enter through the air inlet hole 304 and flow out through the air outlet hole 3〇5. On the other hand, if the driving member 303 lifts the control valve disc 3〇2, the airflow can enter through the air inlet hole 3〇4 and flow out through the air outlet hole 306. Therefore, the poppet valve can quickly and easily change the flow direction of the official line, and is used to replace the traditional buttof valve. U.S. Patent No. 6, 39,927 discloses a two-storage bed incinerator equipped with a poppet valve, the purpose of which is to improve the structure of the poppet valve to make the air flow change more smoothly during heat exchange and to increase the durability of the poppet valve. However, it does not solve the problem of untreated gas leakage during the preheating/heat storage switching of the above two regenerator bed incinerators. In order to solve the shortcomings of the above-mentioned double regenerative bed incinerator, there are also three regenerative bed incinerators, namely three regenerator beds (A, B and C beds), and each regenerator bed 6 ^ M323583 except for the intake and outlet ends, Contains a rinse. Specifically, ^ the operation mode comprises 6 steps: Step 1: When the boring machine is introduced into the exhaust gas for preheating, the boring machine is passed into a purge gas to flush the untreated exhaust gas from the bed into the exhaust gas stream in the previous cycle. After combustion, it is introduced into the C bed and is stored and stored in heat; • Step 2: The A bed is introduced into the exhaust gas to preheat, the B bed is stopped to be flushed and the air flow is taken out _ and the heat is stored, and the C bed is stopped to be exhausted and the flushing air flow is passed; 3: The A bed stops introducing the exhaust gas to preheat and enters the flushing airflow. The B bed* exports the airflow and stores the heat. The C bed stops flushing and introduces the exhaust gas to warm up. Step 4: The A bed stops flushing and the airflow is exhausted and stored. The B bed stops the exhaust gas and enters the flushing air flow, and the C bed introduces the exhaust gas to preheat; 'Step 5: The A bed leads out the air flow and stores the heat, the B bed stops flushing and the ▲ exhaust gas preheats, and the C stop bed introduces the exhaust gas preheating And the flushing airflow is introduced; and step 6: the A bed stops the exhaust gas and passes into the flushing airflow, the B bed introduces the exhaust gas to preheat, C stops the flushing to extract the airflow and stores the heat, and completes a φ_cycle. In short, the three-storage bed incinerator requires one more regenerator bed because of the additional step of flushing the airflow between the heat storage and preheating steps. However, although the three-storage bed incinerator solves the problem of low efficiency and odor such as untreated gas cross-contamination discharge and leakage during the preheating/heat storage switching of the two-storage bed incinerator, the installation cost is high, and Due to the complicated structure, the control valve has many moving parts, the operation reliability is low, and the maintenance is not easy. Therefore, the three-storage bed incinerator is not the best solution. How to provide a device with low cost, simple structure, easy control, and operation. 7 M323583 High-reliability and maintenance of the regenerative incinerator system is urgent for the relevant industry. Seek solutions and improvements. [New content]
為了改善上述習知技術所面臨的問題，本創作設計出 一種高效能蓄熱式廢氣焚化爐，可提昇有機廢氣處理之處 理效率，並減少裝設、增加穩定度、可靠度及維修成本。 本創作之高效能蓄熱式廢氣焚化爐包含： 一第一熱交換單元； 第一進/出氣控制單元，其與該第一熱交換單元連 接， 苐二熱交換單元； 接 第二進/出氣控制單元，其與該第二熱交換單元連 =焚料元，其設置於該第-與第二熱交換單元之間； 下游端(poppetvalve)單元，設置於焚化爐之 個密料片及-驅動單元；及 制閥碟片、複數 一缓衝槽，其與該提升閥單元相連接。 熱交能蓄熱式廢氣焚化爐中，該第-盘第-陶是畜熱材料較佳。 」限制，以石質或 奴而言，常以碟閥來控制管路友 ，、官路内徑形狀相同之薄板作為間，並:=通’其具 』精由電子控制 8 M323583 =控=閥轉_«開敬或關閉 間早、成本較低且維修容易。 〇 ㈣门稱化 閥也必須相對增大’開啟或關；二：内時， 關閉，因此若管路構造較條管路之開啟或 閥，且控制該碟閥的電子控二=要相當數量的碟 外平本到作之同效此畜熱式廢氣焚化爐中， 弟—進/出氣控制單元可視情況進-步分別為I提升門ϊ 兀’以控制該該第-與第二熱交換單元之進/出=早 以—提升閥單元取代二個以上之 *亦P， 減少架設及維修成本，同時易於精化管路結構’ 本創作之高效能蓄熱式廢氣焚化爐中，在該 兀與緩衝槽之下游端可再串聯連二早 其之切換可將管路制於同—排放口或通道。 猎由 本=之南效能#熱式廢氣焚化爐中，該緩衝槽之體 未声於第—與第二熱交換單元預熱/#熱切換時之 U乳體之體積’且該缓衝槽截取未處理氣體後，可細 :,導引至該焚化爐之上游端’再次導入本系統處理： :枯疋可、工由B路導引至例如濟石吸附轉輪濃縮器、廢 =化爐、活性碳吸附床、沸石吸附床、濕式洗務塔 凌态等其他任何形式之廢氣淨化設備處理。 " 此外，本創作另關於—種用於截取蓄熱式廢氣化 週期轉換時所交差污染㈣漏的未燃燒廢氣之緩衝^ 置，其包含·· M323583 至少一提升閥單元，其包含複數個進/出氣端、一控制 閥碟片、複數個密封墊片及一驅動單元；及 一緩衝槽，其與該提升閥單元相連接。 本創作之緩衝截取裝置中，該缓衝槽在截取未處理氣 體後，可經由管路導引至例如沸石吸附轉輪濃縮器、廢氣 焚化爐、活性碳吸附床、沸石吸附床、濕式洗滌塔、冷凝 器等其他任何形式之廢氣淨化設備處理。In order to improve the problems faced by the above-mentioned conventional technologies, the present design has designed a high-efficiency regenerative exhaust gas incinerator which can improve the efficiency of organic waste gas treatment, and reduce installation, increase stability, reliability and maintenance cost. The high-performance regenerative exhaust gas incinerator of the present invention comprises: a first heat exchange unit; a first inlet/outlet control unit connected to the first heat exchange unit, a second heat exchange unit; and a second inlet/outlet control a unit connected to the second heat exchange unit = a fuel element disposed between the first and second heat exchange units; a downstream end (poppetvalve) unit disposed in a dense chip and a drive of the incinerator And a valve disc, a plurality of buffer tanks connected to the poppet valve unit. In the heat exchange energy storage type exhaust gas incinerator, the first plate-ceramic is preferably a livestock heat material. "Restriction, in the case of stone or slaves, the discs are often used to control the pipeline friends, and the thin plates with the same inner diameter of the official road are used as the room, and: = pass 'its' fine electronic control 8 M323583 = control = The valve turns _«open or close the room early, the cost is low and the maintenance is easy. 〇(4) The door weigh valve must also be relatively 'open or closed'; 2: inside, close, so if the pipe structure is more open than the pipe or the valve, and the electronic control of the disc valve is controlled = a considerable amount In the case of the same type of waste heat incinerator, the brother-inlet/outlet control unit can take the step of increasing the threshold to control the first and second heat exchanges. The unit's entry/exit = as early as - the poppet valve unit replaces more than two * also P, which reduces the cost of erection and maintenance, and at the same time facilitates the refinement of the pipeline structure. In this high-performance regenerative exhaust gas incinerator, The downstream end of the buffer tank can be connected in series two times to switch the pipeline to the same discharge port or passage. In the thermal exhaust gas incinerator, the body of the buffer tank is not in the volume of the U-emulsion when the first and the second heat exchange unit are preheated/#hot-switched and the buffer tank is intercepted. After untreated gas, it can be fine: it is guided to the upstream end of the incinerator and re-introduced into the system for treatment:: dry, can be guided by road B to, for example, Ji Shi adsorption wheel concentrator, waste = furnace , such as activated carbon adsorption bed, zeolite adsorption bed, wet scrubbing tower, etc., and other forms of exhaust gas purification equipment. " In addition, this creation is also related to a type of buffer for unburned exhaust gas used to intercept the leakage (4) leakage of the regenerative waste gas cycle, including: · M323583 at least one poppet unit, which includes a plurality of a gas outlet end, a control valve disc, a plurality of gaskets and a driving unit; and a buffer tank connected to the poppet valve unit. In the buffer intercepting device of the present invention, after the intercepting of the untreated gas, the buffer tank can be guided via a pipeline to, for example, a zeolite adsorption runner concentrator, an exhaust gas incinerator, an activated carbon adsorption bed, a zeolite adsorption bed, and a wet scrubbing. Other types of exhaust gas purification equipment such as towers, condensers, etc. are treated.
【實施方式】 為使充分瞭解本創作之目的、特徵及功效，兹藉由下 述具體之實施例，並配合所附之圖式，對本創作做一詳細 說明，說明如後。 ^ 實施例1 第三圖為本創作之高效能蓄熱式廢氣焚化爐的示i 圖。如圖所*，該淨化裝置包含：一第_熱交換單元Μ :第一進/出氣控制單元24; —第二熱交換單元22; 一 出氣，制單元25;-资化單元23，其設置於該第 、弟一熱父換單元之間；一提升閥單元3〇，1包三 ’出氣端3〇4、3〇5及306、一控制閥碟片3〇2、密刪3 及一驅動單元303 ;及一緩衝槽40。 開啟2啟動風車1〇’將第一進/出氣控制單元24之閥2 閉閥242,且第二進/出氣控制單元25之闕况 自閉閥251 ’將廢氣導入第—熱交換單元21，高溫 M323583 熱材料進行空氣預熱熱回收熱交換，再經由焚化單元2 廢氣焚化處理後進人第二熱交換單元22，此雜焚化處理 =高溫氣流可將第二熱交換單元22内壁之蓄熱材料加 、，經所設定之時間後，-方面，同時將閥242及251開 啟亚關閉閥241及閥252，將廢氣導入第二⑼換單元^ 預辞以提祕氣氣流溫度’經由焚化單元23將廢氣焚化處 =後進入弟-熱交換單元21，此時經焚化處理後之高溫氣 又可將第-熱交換單元21内壁之蓄熱材料加熱。另一方 ^ ’在上述閥242及251開啟並關閉闕241及閥况之同 時’以驅動單幻〇3將控制_片地上提至盘密封塾片 3〇7接觸，待第一熱交換單元21中未處理之廢氣經由進氣 端304及出氣端306進入緩衝槽4〇後’驅動單元3〇3可將 控制閥碟片302下壓至與密封墊片斯接觸，此時，氣流 又可經由進氣端3〇4及出氣端3〇5至排放單元％排放。而 缓衝槽40中未經焚化處理之廢氣因風車1〇所造成之負 壓，會再次被導入焚化爐2〇處理。 實施例2 第四圖為本創作搭配雙提升閥單元之高效能蓄熱式廢 氣焚化爐的示意圖。如圖所示，除在該提升閥單元3〇與緩 衝槽40之下游端可再串聯連接另一提升閥單元31之外， 其於與實施例1相同，藉由其之切換可將管路共甩於同一 排放口或通道。 11 M323583 實施例3 〆第五圖為本創作搭配多組提升閥單元之高效能 廢氣焚化爐的示意圖。如圖所示，除第一及第二進/出氣杵 制單元24及25各為提升閥單元26及27之外，其於與二 施例1相同。當提升閥單元26之驅動單元263將控制閱^ 片=下壓至與密封塾片267接觸，且提升闊單力U之驅 動單兀273將控制閥碟片272上提至與密封墊片277接觸 後，廢氣氣流可進人第—熱交換單元21，而由第二熱交換 單元22β排出。反之，當控制閥碟片262上提而控制閥碟片 272下壓時，廢氣氣流可進入第二熱交換單元22，而由第 熱又換單元21排出。其餘步驟如實施例丨中所述。亦即， 以二提升閥單元26及27取代第三圖中241、242、251、 252四個閥’可簡化管路結構，減少架設及維修成本，同 時易於精準控制。 實施例4 、第/、圖為搭配沸石轉輪吸附系統之本創作高效能蓄熱 式苽氣火化爐的示意圖。如圖所示，緩衝槽4〇之出氣端 4〇1可連接至Α點，而將緩衝槽40所截取之第一與第二熱 又換單元21及22切換時未處理之廢氣導引至沸石轉輪吸 附系統60之入口端再次處理。或連接至B點，而將未處理 之廢乳導引至蓄熱式廢氣焚化爐之入口端再次處理。 如上所述’本創作完全符合專利三要件：新穎性、進 步丨生和產業上的可利用性。以新穎性和進步性而言，本創 12 M323583 作係藉著設置至少一提升閥單元，以解決習知技術在二蓄 熱床式焚化爐預熱/蓄熱切換時有未處理之氣體交差污染 排放及洩漏等低效率及惡臭的問題。進而可改善二床式蓄 熱焚化爐之排放效率，同時降低惡臭的問題；就產業上的 可利用性而言，利用本創作所衍生的產品，當可充分滿足 目前市場的需求。 本創作在上文中已以較佳實施例揭露，然熟習本項技 術者應理解的是，該實施例僅用於描繪本創作，而不應解 讀為限制本創作之範圍。應注意的是，舉凡與該實施例等 效之變化與置換，均應設為涵蓋於本創作之範疇内。因此 ，本創作之保護範圍當以下文之申請專利範圍所界定者為 準〇 【圖式簡單說明】 第一 A圖為蓄熱式焚化爐出口濃度與閥件切換時間之 φ 關係圖。 第一 B圖為蓄熱式焚化爐廢氣破壞去除效率與閥件切 換時間之關係圖。 第二圖為提升閥之基本構造圖。 第三圖為本創作之高效能蓄熱式廢氣焚化爐的示意 圖。 第四圖為本創作搭配雙提升閥單元之高效能蓄熱式廢 氣焚化爐的示意圖。 第五圖為本創作搭配多組提升閥單元之高效能蓄熱式 13 • M323583 廢氣焚化爐的示意圖。 第六圖為搭配沸石轉輪吸附系統之本創作高效能蓄熱 式廢氣焚化爐的示意圖。[Embodiment] In order to fully understand the purpose, features and effects of the present invention, the present invention will be described in detail by way of the following specific embodiments and with the accompanying drawings. ^ Embodiment 1 The third figure is a diagram of the high-performance regenerative exhaust gas incinerator of the present invention. As shown in the figure, the purification device comprises: a first heat exchange unit Μ: a first inlet/outlet control unit 24; a second heat exchange unit 22; an outlet, a unit 25; and a chemistry unit 23, which are arranged Between the unit and the younger father, the unit is replaced by a unit; a poppet valve unit 3〇, 1 pack of three 'exhaust ends 3〇4, 3〇5 and 306, a control valve disc 3〇2, a secret deletion 3 and a a driving unit 303; and a buffer tank 40. Turning on the 2 start windmill 1〇', the valve 2 of the first inlet/outlet control unit 24 is closed 242, and the shut-off valve 251' of the second inlet/outlet control unit 25 introduces the exhaust gas into the first heat exchange unit 21, The high temperature M323583 hot material is subjected to air preheating heat recovery heat exchange, and then incinerated by the incineration unit 2 to enter the second heat exchange unit 22, and the miscellaneous incineration treatment=high temperature gas flow can add the heat storage material on the inner wall of the second heat exchange unit 22 After the set time, on the other hand, the valves 242 and 251 are simultaneously opened to the sub-close valve 241 and the valve 252, and the exhaust gas is introduced into the second (9) unit to predict the gas flow temperature 'via the incineration unit 23 The exhaust gas incineration station = after entering the heat exchange unit 21, and the high temperature gas after the incineration treatment can heat the heat storage material on the inner wall of the first heat exchange unit 21. The other side ^' while the above-mentioned valves 242 and 251 open and close the crucible 241 and the valve condition 'to drive the single illusion 3 to lift the control _ sheet to the disc sealing cymbal 3 〇 7 contact, to be the first heat exchange unit 21 The untreated exhaust gas enters the buffer tank 4 via the intake end 304 and the outlet end 306, and the drive unit 3〇3 can press the control valve disc 302 into contact with the gasket. At this time, the airflow can be passed through The intake end 3〇4 and the outlet end 3〇5 are discharged to the discharge unit%. The unburned exhaust gas in the buffer tank 40 is again introduced into the incinerator 2 by the negative pressure caused by the windmill. Embodiment 2 The fourth figure is a schematic diagram of a high-efficiency regenerative waste gas incinerator with a double poppet unit. As shown in the figure, except that the other poppet valve unit 31 can be connected in series at the downstream end of the poppet valve unit 3 and the buffer tank 40, it is the same as in the first embodiment, and the pipeline can be switched by the switch. Coexist in the same discharge or passage. 11 M323583 Example 3 〆 Figure 5 is a schematic diagram of a high-performance exhaust gas incinerator with multiple sets of poppet valve units. As shown in the figure, except that the first and second intake/exhaust gas suppression units 24 and 25 are each of the poppet valve units 26 and 27, they are the same as in the second embodiment. When the driving unit 263 of the poppet valve unit 26 presses the control sheet = down to contact with the sealing jaw 267, and the driving unit 273 that lifts the wide single force U, the control valve disc 272 is lifted up to the sealing gasket 277. After the contact, the exhaust gas stream can enter the first heat exchange unit 21 and be discharged by the second heat exchange unit 22β. Conversely, when the control valve disc 262 is lifted and the control valve disc 272 is depressed, the exhaust gas stream can enter the second heat exchange unit 22 and be discharged by the first heat exchange unit 21. The remaining steps are as described in the embodiment. That is, replacing the four valves 241, 242, 251, and 252 in the third figure with the two poppet valve units 26 and 27 simplifies the piping structure, reduces the cost of erection and maintenance, and is easy to accurately control. Example 4, Figure /, is a schematic diagram of a high-efficiency heat storage helium gas cremation furnace with a zeolite wheel adsorption system. As shown in the figure, the outlet end 4〇1 of the buffer tank 4〇 can be connected to the defect point, and the untreated exhaust gas when the first and second heat-replacement units 21 and 22 intercepted by the buffer tank 40 are switched is guided to The inlet end of the zeolite wheel adsorption system 60 is again treated. Or connect to point B and direct the untreated waste milk to the inlet end of the regenerative exhaust gas incinerator for further treatment. As mentioned above, this creation is fully in line with the three requirements of patents: novelty, progressive hygiene and industrial availability. In terms of novelty and advancement, the Ben 12 M323583 is based on the provision of at least one poppet valve unit to solve the problem of untreated gas cross-contamination emissions during the preheating/heat storage switching of the two regenerative bed incinerators. And low efficiency and bad smells such as leaks. Further, the discharge efficiency of the two-bed heat storage incinerator can be improved, and the problem of malodor can be reduced; in terms of industrial availability, the products derived from the creation can fully satisfy the needs of the current market. The present invention has been disclosed in the above preferred embodiments, and it should be understood by those skilled in the art that the present invention is only intended to depict the present invention and should not be construed as limiting the scope of the present invention. It should be noted that variations and permutations that are equivalent to the embodiment are intended to be within the scope of the present invention. Therefore, the scope of protection of this creation is as defined in the following patent application scope [Simplified illustration] The first A is a plot of the relationship between the outlet concentration of the regenerative incinerator and the switching time of the valve. The first B is a graph showing the relationship between the exhaust gas destruction removal efficiency of the regenerative incinerator and the valve cutting time. The second picture shows the basic structure of the poppet valve. The third picture is a schematic diagram of the high-performance regenerative exhaust gas incinerator of the creation. The fourth picture is a schematic diagram of a high-efficiency regenerative waste gas incinerator with a double poppet unit. The fifth picture is a schematic diagram of the high-efficiency regenerative 13 • M323583 exhaust gas incinerator with multiple sets of poppet valve units. The sixth figure is a schematic diagram of the high-performance regenerative waste gas incinerator with the zeolite runner adsorption system.
【主要元件符號說明】 10 20 21 22 23 24 25 241、242、251、252 26、27 262 > 272 263 > 273 267 ^ 277 30、31 301 、 311 302 、 312 303 、 313 304 、 305 、 306 307 、 317 314 、 315 、 316 第一風機 焚化爐 第一熱交換單元 第二熱交換單元 焚化單元 第一進/出氣控制單元 第二進/出氣控制單元 閥 提升閥單元 控制閥碟片 驅動單元 密封墊片 提升閥單元 管路切換盒 控制閥碟片 驅動單元 進/出氣端 密封墊片 進/出氣端 14 • M323583 40 缓衝槽 401 出氣端 41、42 閥 50 排放單元 60 沸石轉輪吸附系統 61 熱交換器 15[Description of main component symbols] 10 20 21 22 23 24 25 241, 242, 251, 252 26, 27 262 > 272 263 > 273 267 ^ 277 30, 31 301 , 311 302 , 312 303 , 313 304 , 305 , 306 307 , 317 314 , 315 , 316 First Fan Incinerator First Heat Exchange Unit Second Heat Exchange Unit Incineration Unit First Inlet / Outlet Control Unit Second Inlet / Outlet Control Unit Valve Poppet Unit Control Valve Disc Drive Unit Gasket Poppet Unit Line Switch Box Control Valve Disc Drive Unit Inlet/Outlet End Seal Inlet/Outlet End 14 • M323583 40 Buffer Tank 401 Outlet End 41, 42 Valve 50 Discharge Unit 60 Zeolite Runner Adsorption System 61 heat exchanger 15