M324171 八、新型說明： 【新型所屬之技術領域】 本創作係有關一種廢氣濃縮焚化奘¥ Θ sa 又化名置’特別是關於—種可提高有機廢氣處 理效率之低污染濃縮蓄熱焚化裝置。 【先前技術】M324171 VIII. New description: [New technical field] This creation is about a kind of low-pollution concentrated heat storage incinerator that can improve the efficiency of organic waste gas treatment. [Prior Art]
半導體製&業和光電業之製程會排放大量含有揮發性有機物質⑽ 0聊icCo聊nds)之廢氣，因此環保空污法規訂定了廢氣慨去除效率標準， __細#峨綱放量大、組 成複雜（高、低彿點之有機物f混合，例如含有lpA，Ace*，腦醜等。） ^放度屬低至巾細⑽〜麵_之㈤，使得着輕之就處理技術相 田困難般在處理大風置低濃度的廢氣時，多會結合兩種以上之處理方式， 例如使㈣石轉輪或流體化床使廢氣吸附濃縮之後，再_燒焚化或冷凝等方 法進行後處理。 如第一圖所示，習知之濃縮蓄熱焚化裝置10包括彿石轉輪12、蓄熱式焚化 爐14第一抽氣風車16、第二抽氣風車18、排放煙囪2〇和閥件組。彿石轉輪 12主要分成二個操作區間，即吸附區12&、脫附區以及冷卻區既，其内部 均填充用來吸附或脫附觀之沸石或活性礙；f熱式焚化爐14係為雙塔式，包 括第一蓄熱室14a、第二蓄熱室14c和加熱室14b，其中第一蓄熱室⑷與第二 蓄…、至14c内部具有用來吸收或者釋放熱能的蓄熱材；閥件組則包括用來控制 ^、氣之第閥件22a和第二閥件22c，以及控制廢氣排氣之第三閥件22b盘 第四閥件22d。 因此’廢氣自沸石轉輪12前端進入後，利用沸石轉輪12後端之第一抽氣 M324171 風車16抽氣，使廢氣經沸石轉輪12之吸附區12a吸附成為乾淨氣體而送至排 放煙囪20排放，當吸附區12a表面吸附VOC至接近飽和時，即將彿石轉輪12 旋轉至脫附區12b位置，讓常溫之空氣、鈍氣或者廢氣流經冷卻區並經過 熱交換器24加熱（一般約加熱至180〜220。〇後通過脫附區12b，故可脫附沸石 轉輪所吸附之VOC而形成而VOC濃度之廢氣，同時使用第二抽氣風車Μ抽 :_氣將高濃度之廢氣送入蓄熱式焚化爐14 ;脫附處理完成之脫附區12b可旋轉至 -冷卻區12c位置降溫以繼續進行吸附處理，故可連續操作而不需停機再生。 • 而當第一閥件22a開啟、第二閥件22b關閉、第三閥件22c關閉以及第四 閥件22d開啟時，高VOC濃度之廢氣經第二抽氣風車18送入蓄熱式焚化爐14 之第一蓄熱室14a，經過加熱室14b加熱到設定溫度(例如為85〇。〇焚化分解後 送至第二蓄熱室14c，燃燒後廢氣之熱能被第二蓄熱室14c内蓄熱材吸收而排放 至排放煙自20，第二蓄熱室14c於吸收足夠熱能後(吸收時間例如是12〇sec)， 可切換閥件組而使第一閥件22a關閉、第二閥件22b開啟、第三閥件22c開啟 以及第四閥件22d關閉，而使廢氣先進入第二蓄熱室14b，經過第二蓄熱室地 _内之蓄熱材預熱後送至加熱室14c焚化分解，最後經過第一蓄熱室14&吸收熱 能而排放至排放煙_ 20，由於第-蓄熱室l4a與第二蓄熱室_内之蓄熱材可 交替儲存燃燒後廢氣之熱能並用以預熱待焚化廢氣，故可減少焚化廢氣耗費之 燃料而節省成本和能源。 祕濃縮蓄熱焚化裝置1〇之沸石轉輪12可將廢氣成分濃縮約7〜15倍，再 配合使用熱回收效率可達80〜之蓄熱式焚化爐14，故不但能有效處理揮發 性廢氣且能源節約效果極佳，雜初設成本高、然而因操作成本低，可在W 年内回收成本，逐漸受到產業重視。 M324171 但上述濃縮蓄熱焚化裝置1〇因需於第一蓄熱室14a與第二蓄熱室ία之間交互 切換蓄熱，第一閥件22a、第二閥件22b、第三閥件22c、第四閥件22d於切換 過程中會有短暫時間之全開，因為廢氣通過第一蓄熱室14a或者第二蓄熱室14b 之阻抗(壓^貝）較大，故於此切換期間，廢氣不會經過第一蓄熱室、第二蓄熱 ,至14c或者是加熱室14b而直接流向排氣煙囪20,導致濃縮蓄熱焚化裝置1〇排 -放廢氣之VOC濃度大幅提高（接近廢氣入口之voc濃度）而產生一濃度突波 -(peak)。假設燃燒V0C的破壞效率為_，則平日排放漢度為人口值的现， ♦但切換閥件組時V0C排放濃度接近入口濃度值⑽％)，也就是排放濃度瞬間變 成平時之5G倍，不㈣致廢氣處理整舰率降低，若濃度監_好伽到突波 出現點’還會造成廢氣V0C濃度量測值過高而可能無法通過環保空污標準而遭 罰款。 因此係有三塔式蓄熱焚化爐或旋轉閥式蓄熱焚化爐之發明以改善上述就 濃度突波之刺，但三塔式t歸化爐錢_式#熱焚化爐之触為造價過 高。 有鐘於此’本創作係針對上述之困擾，提出一種低污染濃縮蓄熱焚化裝置， 以改善上述之缺失。 【新型内容】 本創作之主要目的，係在提供一種低污染濃縮蓄熱焚化裝置，其僅需運用 裝置本身之廢差動力即可有效將高v〇c濃度之廢氣導回廢氣入口進行再處理 無需增加齡動錢耗不影響吸_石轉輪操雜能，_有效降低雙拔 v〇c M324171 本創作之另一目的，係在提供一種低污染濃縮蓄熱焚化裝置，其係具有建 置成本較低之優點。 為達J上述之目的，本創作係提出一種低污染濃縮蓄熱焚化裝置，包括沸 石轉輪、畜熱式焚倾、管路組錢再喊管馳，沸石轉輪侧以進行廢氣 ‘ /農縮I熱式义化爐具有蓄熱室與加熱室以供焚化廢氣含有之VOC，管路組係 連通彿石轉輪、蓄熱式焚化爐與排放煙函，再回收管路組則與管路組相連，因 •此可顧低污染濃_熱焚化裝置本身之壓絲力有效進行廢氣之再回收。 • 底下藉由具體實施例配合所附的圖式詳加說明，當更容易瞭解本創作的目 的、技術内容、特點及其所達成的功效。 【實施方式】 Η為本作< f施例的結構示意圖，如圖所示，低污染濃縮蓄熱焚 化滅置30主要包括彿石轉輪32、蓄熱式焚化爐％、管路組與再回收管路組， 沸石轉輪32具有吸附區32a、脫附區娜與冷卻區版，而蓄熱式焚化爐料具 有第蓄…、至34a加熱至34b與第二蓄熱室32c,管路組包括管件組與閥件組， • ’、中&件、、且包括第-营件伽、第二管件獅、第三管件46c、第四管件偏、 -第五管件46e和第六管件術，閥件組包括第一閥件伽、第二閥件微、第三 間件42c第四閥件42(1與第五閥件426，再回收管路組包括再回收管件48與 再回收閥件50，而閥件組與再回收閥件5〇均為自動闕。 第&件46a之-知連接提供廢氣之第一氣體來源（圖未示），另一端連接 吸附區32a之左側，第二管件働之一端連接吸附區32a之右側，另一端連接 排放煙自4G ’第一官件46b上另設有第一抽氣風車洲；第三管件46c之一端連 接第二氣體來源（圖未示），其可提供空氣或是純氣，另一端連接冷卻區版之 M324171 •左侧⑽管件之-端連接冷卻區32c右側，另一端連接脫附區娜右側， 第e件46d上另成有熱父換器44;第五管件伽之一端連接脫附區娜左側， 端、U蓄熱室34a與第二蓄熱室34c相連，且第五管件伽上設有第 二抽氣風車38 ’其純風量㈣—減風車％的i/iq，第五管件伽上靠近 ‘第-蓄熱室34a與第二蓄熱室34c的位置分別設有第一闊件似與第二闊件 -42b’U件46f之-端與第一蓄熱室3如與該第二蓄熱室撕相連，另一端 -則連接排放煙自40，第六管件46f上靠近第一蓄熱室施與第二蓄熱室地的 籲位置刀別。又有第—閥件42。與第四閥件伽，靠近排放煙固4〇位置則設有第五 闊件42e ;再回收管件48連接第六管件46f與第-管件46a，且再回收管件48 上設有再回收閥件50;另外可以位於第六管件46f與再回收管件48連滅之一 三通閥（圖未示）來取代第五閥件似與再回收閥件5〇。 第三圖為本創作之另-實施例的結構示意圖，其與第二圖之差異在於省略 第三管件46c而以第-管件46a取代之，如圖所示，第一管件偷之一端連接 於第-氣體來源，另-端則連接於吸附區32a與冷卻區32c之左側。 因此’如第二圖和第三圖所示，利用第一抽氣風車36可使第一氣體來源提 t、之廢氣自第《件46a進入沸石轉輪32之吸附區32a，經吸附區32a吸附廢 氣含有之VOC後成為乾淨氣體而經第二管件働送至排放煙_ 4〇排放，當吸附 區32a表面吸附VOC至接近飽和時，讓沸石轉輪％旋轉至脫附區32b位置，使 第二氣體來源所提供之常溫的空氣、鈍麟者第—氣體來源提供之廢氣自第三 管件46c(如第二圖所示）或者第一管件46a(如第三圖所示）進入冷卻區32C，並 經第四管件46d送至熱交換器44加熱，成為高溫（18〇〜220°C)空氣後通過脫附 區32b，可使沸石轉輪32吸附之v〇C脫附出來而形成高v〇C濃度之廢氣，使用 M324171 第二抽氣風車38將其經第五管件46e送入蓄熱式焚化爐34，脫附處理完成之脫 附區32b可旋轉至冷倾32c錄降溫後繼續進行吸附處理，故可連續操作而 不需停機再生。 而當閥件組之第-閥件42a開啟、第二閥件伽關閉、第三閥件攸關閉、 第靖牛42d開啟、第五閥件42e開啟以及再回收閥件5〇關閉時，高v〇c濃度 -廢氣經第二減風車38送人蓄減焚鎌34之第―f齡施，經過加熱室 -34b加熱到設定溫細如為說）焚化分解後送至第二蓄熱室地，燃燒後廢 >氣的熱能被第二蓄熱室34c内之蓄熱材(例如馬鞍形陶究塊或蜂巢狀陶竞塊或平 行通道陶魏)吸收後排放至排放_ 40，於第二蓄熱室34c吸收足夠之熱能後 (時間例如是版c)，切換閥件組使第一閥件似關閉、第二閥件伽開啟、 第三閥件開啟及第四閥件·件關閉，第五閥件42e與再回收間件如則維持分 別轉原本開啟與關閉之狀態，而使廢氣先進入第二蓄熱室34c，經過其内部之 蓄熱材預熱後送至加熱室34b焚化分解，最後經過第—蓄熱室施吸收熱能而 排放至排放煙函40。 > /述之蓄熱式焚化爐54會於第-蓄熱室34a與第二蓄熱室34c之間交互切 換蓄熱’當第-閥件42a、第二閥件42b、第三閥件42c、第四閥件伽因切換 而處於短暫（約1秒)之全開狀態時，此時第五閥件似為關閉狀態而再回收闕 件50則為開啟狀態，使得再回收管件48的進入端（靠近第六管件撕端)壓力 會增高約6-10 inchW.G. ’遠高於再回收管件48的輸出端（靠近第一管件伽 進入滞石轉輪32端)之壓力（負壓），使原本應流向排氣_ 4〇的廢氣自動導流 到再回收管件48與第-管件46a而被吸入沸石轉輪32，無需增加額外動力或轉 動元件即可進行廢氣之再回收處理，可有效降低低污染濃縮蓄熱焚化裝置3〇排 10 M324171 •放廢氣之TO濃度，大幅消除原本會產生的v〇c濃度突波值。 將，由於彿石轉輪32之脫附風量（自第—氣體來源或者第二氣體來源進 入脫附區32b之空氣、鈍氣或者廢氣風量）只有處理風量（自第_氣體來源進入 吸附區32a之廢氣風量）的1/10左右，因此短暫i秒鐘引入高濃度職氣造 .成之沸石轉輪32吸附負荷尚在合理範圍，故不會損害沸石轉輪犯或影㈣操 .-作性能，又假設彿石轉輪32旋轉週期為_秒，則沸石轉輪％每次增加之吸 -收負荷小於原本之1/900，因此影響相當微小。 •以上所述係藉由實施例說明本創作之特點，其目的在使熟習該技術者能瞭 解本創作之内容並據以實施，而非限定太 本創作之專利範圍，故凡其他未脫離太 創作所揭示之精神而完成之等效修料修改，仍應包含在以下所述之中請= 範圍中。 【圖式簡單說明】 第-圖為習知之濃縮蓄熱焚化裝置的結構示意圖。 第二圖為本創作低污染濃縮蓄熱焚鱗置之—實施綱結構示意圖。 鲁第三圖為本創作低污染濃縮賴焚化褒置之另一實施例的結構示意圖。 【主要元件符號說明】 、 10 濃縮蓄熱焚化裝置 12、32沸石轉輪 12a、32a吸附區 12b、32b脫附區 12c、32c冷卻區 14、34蓄熱式焚化爐 11 !r '产_ M324171 ' 14a、34a第一蓄熱室 14b、34b加熱室 14c、34c第二蓄熱室 16、36 第一抽氣風車 18 ^ 38 第二抽氣風車 -20、40 排放煙囪 • 22a、42a第一閥件 φ 22b、42b第二閥件 22c、42c第三閥件 22d、42d第四閥件 24、44 熱交換器 30 低污染濃縮蓄熱焚化裝置 42e 第五閥件 46a 第一管件 46b 第二管件 46c 第三管件 46d 第四管件 46e 第五管件 48 再回收管件 50 再回收閥件 12The semiconductor manufacturing industry and the photovoltaic industry process will emit a large amount of exhaust gas containing volatile organic substances (10), so the environmental air pollution regulations set the exhaust gas removal efficiency standards, __细#峨纲量量The composition is complex (high and low point of the organic matter f mixed, for example, containing lpA, Ace*, brain ugly, etc.) ^The degree of relaxation is as low as the thin (10) ~ face _ (five), making it difficult to handle the technology Generally, in the treatment of high-temperature low-concentration exhaust gas, two or more treatment methods are combined, for example, the (four) stone runner or the fluidized bed is used to adsorb and concentrate the exhaust gas, and then subjected to post-treatment by incineration or condensation. As shown in the first figure, the conventional concentrated heat storage incinerator 10 includes a Fossil runner 12, a regenerative incinerator 14, a first pumping windmill 16, a second pumping windmill 18, a discharge chimney 2, and a valve member group. The Buddha wheel 12 is mainly divided into two operation sections, namely, the adsorption zone 12 & the desorption zone and the cooling zone, both of which are filled with zeolite for adsorbing or desorbing or active; f thermal incinerator 14 The utility model is a double tower type, comprising a first regenerator 14a, a second regenerator 14c and a heating chamber 14b, wherein the first regenerator (4) and the second accumulating chambers, 14c have internal heat storage materials for absorbing or releasing thermal energy; The group includes a valve member 22a and a second valve member 22c for controlling the gas, and a third valve member 22d for controlling the exhaust gas to be exhausted. Therefore, after the exhaust gas enters from the front end of the zeolite runner 12, the first exhaust gas M324171 windmill 16 at the rear end of the zeolite runner 12 is pumped, so that the exhaust gas is adsorbed into the clean gas through the adsorption zone 12a of the zeolite runner 12 and sent to the discharge chimney. 20 discharge, when the surface of the adsorption zone 12a adsorbs VOC to near saturation, the Buddha wheel 12 is rotated to the position of the desorption zone 12b, and the ambient air, the blunt gas or the exhaust gas flows through the cooling zone and is heated by the heat exchanger 24 ( Generally, it is heated to about 180~220. After passing through the desorption zone 12b, the VOC adsorbed by the zeolite runner can be desorbed to form the VOC concentration exhaust gas, and the second exhaust gas turbine is used for pumping: _ gas will be high concentration The exhaust gas is sent to the regenerative incinerator 14; the desorption zone 12b after the desorption process is completed can be rotated to - the cooling zone 12c is cooled to continue the adsorption process, so that the continuous operation can be performed without stopping the regeneration. When the piece 22a is opened, the second valve member 22b is closed, the third valve member 22c is closed, and the fourth valve member 22d is opened, the exhaust gas having a high VOC concentration is sent to the first regenerator of the regenerative incinerator 14 via the second extraction windmill 18. 14a, after heating chamber 14b It is set to a temperature (for example, 85 〇. After being incinerated and decomposed, it is sent to the second regenerator 14c, and the heat energy of the exhaust gas after being burned is absorbed by the heat storage material in the second regenerator 14c to be discharged to the exhaust fumes 20, and the second regenerator 14c is After absorbing sufficient thermal energy (absorption time is, for example, 12 sec), the valve member group can be switched to close the first valve member 22a, the second valve member 22b is opened, the third valve member 22c is opened, and the fourth valve member 22d is closed. The exhaust gas is first introduced into the second regenerator 14b, preheated through the heat storage material in the second regenerator, sent to the heating chamber 14c for incineration, and finally discharged to the exhaust fumes through the first regenerator 14& Since the heat storage materials in the first regenerators l4a and the second regenerators can alternately store the heat energy of the exhaust gas after combustion and preheat the waste gas to be incinerated, the fuel consumed by the incineration exhaust gas can be reduced to save cost and energy. The zeolite wheel 12 of the device can concentrate the exhaust gas component by about 7 to 15 times, and is combined with the regenerative incinerator 14 having a heat recovery efficiency of 80 to be used, so that the volatile waste gas can be effectively treated and the energy saving effect is excellent. ,miscellaneous Due to the high cost, the cost can be recovered in the year of W, and it is gradually paid attention to by the industry. M324171 However, the above-mentioned concentrated heat storage incinerator 1 exchanges heat storage between the first regenerator 14a and the second regenerator ία. The first valve member 22a, the second valve member 22b, the third valve member 22c, and the fourth valve member 22d may be fully opened during the switching process because the exhaust gas passes through the first regenerator 14a or the second regenerator 14b. The impedance (pressure) is large. Therefore, during the switching, the exhaust gas does not pass through the first regenerator, the second heat storage, to 14c or the heating chamber 14b, and directly flows to the exhaust stack 20, resulting in a concentrated heat storage incinerator. The VOC concentration of the exhaust-discharge gas is greatly increased (close to the vocal concentration of the exhaust gas inlet) to generate a concentration surge. Assume that the destruction efficiency of combustion V0C is _, then the daily emission is the population value, ♦ but the V0C emission concentration is close to the inlet concentration value (10)% when switching the valve group, that is, the emission concentration instantly becomes 5G times of normal, no (4) The rate of exhaust gas treatment for the whole ship is reduced. If the concentration monitoring _ good gamma to the point where the spurt occurs, the V0C concentration of the exhaust gas will be too high and may not be fined by the environmental pollution standard. Therefore, the invention of the three-column regenerative incinerator or the rotary valve type regenerative incinerator is used to improve the above-mentioned thorns on the concentration surge, but the three-tower t-refining furnace has a high cost. In view of the above problems, this creation proposes a low-pollution concentrated heat storage incineration device to improve the above-mentioned deficiency. [New content] The main purpose of this creation is to provide a low-pollution concentrated heat storage incineration device, which can effectively return the exhaust gas with high v〇c concentration back to the exhaust gas inlet for reprocessing without using the waste power of the device itself. The increase in the amount of money does not affect the suction _ stone runners, _ effectively reduce the double pull v 〇 c M324171 Another purpose of this creation is to provide a low pollution concentrated heat storage incinerator, which has a lower construction cost The advantage of low. In order to achieve the above purpose, the author proposes a low-pollution concentrated heat storage incineration device, including zeolite runner, animal-heating incineration, pipeline group money, and shouting, and the zeolite runner side to carry out the exhaust gas. The I thermal furnace has a regenerator and a heating chamber for incinerating the VOC contained in the exhaust gas, the pipeline group is connected with the Fossil runner, the regenerative incinerator and the exhaust fumes, and the recirculating pipeline group is connected to the pipeline group. Because of this, the low-contamination concentration _ heat incineration device itself can be used to effectively recover the exhaust gas. • The detailed description of the specific examples and the accompanying drawings will be used to make it easier to understand the purpose, technical content, characteristics and effects of the creation. [Embodiment] The structure of the present embodiment is as shown in the figure. As shown in the figure, the low-pollution concentrated heat storage incineration and extinguishing unit 30 mainly includes the Fossil runner 32, the regenerative incinerator, the pipeline group and the recycling. The pipeline group, the zeolite runner 32 has an adsorption zone 32a, a desorption zone and a cooling zone plate, and the regenerative incinerator material has a first storage, 34a heating to 34b and a second regenerator 32c, and the pipeline group includes a pipe group With the valve member set, • ', medium & parts, and including the first - camp gamma, the second pipe lion, the third pipe 46c, the fourth pipe bias, the - fifth pipe 46e and the sixth pipe, valve The group includes a first valve member gamma, a second valve member micro, a third member 42c, a fourth valve member 42 (1 and a fifth valve member 426, and the recirculation line set includes a re-recovery tube member 48 and a re-recovery valve member 50, The valve member group and the re-recovery valve member 5〇 are both automatically 阙. The first connection of the first & member 46a provides a source of exhaust gas (not shown), the other end is connected to the left side of the adsorption zone 32a, and the second pipe member One end of the crucible is connected to the right side of the adsorption zone 32a, and the other end is connected to the exhaust smoke from the 4G 'the first official part 46b is additionally provided with the first pumping Windmill continent; one end of the third pipe member 46c is connected to a second gas source (not shown), which can supply air or pure gas, and the other end is connected to the cooling zone version of M324171. • The left side (10) pipe end is connected to the right side of the cooling zone 32c. The other end is connected to the right side of the detachment area, and the e-member 46d is further provided with a hot-replacer 44; one end of the fifth tube is connected to the left side of the detachment area, and the end, U regenerator 34a is connected to the second regenerator 34c. And the fifth pipe member is provided with a second exhaust windmill 38', its pure air volume (four) - i/iq of the reduced windmill %, and the fifth pipe member is converge near the position of the first - regenerator 34a and the second regenerator 34c, respectively The first wide member is similar to the second wide member - 42b' U member 46f - the end is disconnected from the first regenerator 3 as the second regenerator, and the other end is connected to the exhaust smoke from 40, the sixth tubular member 46f is adjacent to the first regenerator to apply the position of the second regenerator chamber. There is a first valve member 42. The fourth valve member is adjacent to the exhaust gas, and the fifth wide member 42e is disposed adjacent to the exhaust gas. The re-recovery pipe member 48 is connected to the sixth pipe member 46f and the first pipe member 46a, and the re-recycling pipe member 48 is provided with a re-recovery valve member 50; A three-way valve (not shown) is disposed between the sixth pipe member 46f and the re-recycling pipe member 48 to replace the fifth valve member and the re-recovery valve member 5. The third figure is the structure of another embodiment of the creation. The schematic diagram differs from the second figure in that the third tubular member 46c is omitted and replaced by the first tubular member 46a. As shown, one end of the first tubular member is connected to the first gas source, and the other end is connected to the adsorption region. 32a and the left side of the cooling zone 32c. Therefore, as shown in the second and third figures, the first exhaust gas source 36 can be used to draw the exhaust gas from the first gas source into the zeolite runner 32 from the piece 46a. The adsorption zone 32a adsorbs the VOC contained in the exhaust gas through the adsorption zone 32a and becomes a clean gas and is sent to the exhaust smoke through the second pipe. When the surface of the adsorption zone 32a adsorbs VOC to near saturation, the zeolite wheel rotates by %. Up to the location of the detachment zone 32b, such that the ambient air supplied by the second gas source, the exhaust gas provided by the blister source of the gas source is from the third pipe member 46c (as shown in the second figure) or the first pipe member 46a (such as The three figures enter the cooling zone 32C and are sent to the fourth pipe 46d to The exchanger 44 is heated to a high temperature (18 〇 220 220 ° C) air and then passed through the desorption zone 32b to desorb the v 〇 C adsorbed by the zeolite runner 32 to form a high v 〇 C concentration of exhaust gas, using M324171 The second pumping windmill 38 sends it to the regenerative incinerator 34 via the fifth pipe member 46e, and the desorption zone 32b after the desorption process is completed can be rotated to the cold dipping 32c to record the temperature and continue the adsorption process, so that the continuous operation can be performed without Stop regeneration. When the first valve member 42a of the valve member group is opened, the second valve member is closed, the third valve member is closed, the second valve member 42d is opened, the fifth valve member 42e is opened, and the recirculating valve member 5 is closed, the height is high. V〇c concentration-exhaust gas is sent to the second regenerator by the second reduction windmill 38 to save the first-firteen-year-old application of the incineration 34, heated to a set temperature by the heating chamber-34b, and then incinerated and sent to the second regenerator The heat energy after combustion is absorbed by the heat storage material in the second regenerator 34c (for example, a saddle-shaped ceramic block or a honeycomb-shaped pottery block or a parallel channel Tao Wei), and is discharged to the discharge _ 40 for the second heat storage. After the chamber 34c absorbs sufficient heat energy (time is, for example, the plate c), the valve member group is switched such that the first valve member is closed, the second valve member is opened, the third valve member is opened, and the fourth valve member is closed. The valve member 42e and the re-recovery member are maintained in the state of being turned on and off, respectively, so that the exhaust gas first enters the second regenerator 34c, is preheated through the heat storage material inside, and is sent to the heating chamber 34b for incineration and decomposition, and finally passes through. The first heat storage chamber absorbs heat energy and discharges to the emission cigarette 40. > / The regenerative incinerator 54 will alternate between the first regenerator 34a and the second regenerator 34c to store heat storage 'When the first valve member 42a, the second valve member 42b, the third valve member 42c, and the fourth When the valve member is switched to be in a fully open state (about 1 second), the fifth valve member seems to be in a closed state and the reclaimed member 50 is in an open state, so that the inlet end of the pipe member 48 is reclaimed (near the first The pressure of the six pipe fittings tearing end will increase by about 6-10 inchW.G. 'The pressure (negative pressure) far higher than the output end of the re-recycling pipe 48 (near the first pipe gamma entering the end of the stagnation wheel 32) makes the original The exhaust gas flowing to the exhaust gas _ 4 自动 is automatically diverted to the re-recycling pipe member 48 and the first pipe member 46a and sucked into the zeolite runner 32, and the exhaust gas can be reprocessed without additional power or rotating components, thereby effectively reducing the low Contaminated concentrated heat storage incinerator 3〇10 M324171 • The TO concentration of the exhaust gas is used to substantially eliminate the v〇c concentration surge value originally generated. The amount of air to be depleted (from the first gas source or the source of the second gas into the desorption zone 32b, the air, the air, or the exhaust gas volume) is only the treated air volume (from the first gas source into the adsorption zone 32a) The exhaust gas volume is about 1/10, so a short-term i seconds introduces a high concentration of gas. The adsorption load of the zeolite wheel 32 is still in a reasonable range, so it will not damage the zeolite runner or shadow (4). The performance, assuming that the rotation period of the Buddha wheel 32 is _ second, the suction-receiving load of the zeolite wheel % is increased by less than 1/900 of the original, so the influence is rather small. The above description is based on the embodiments to illustrate the characteristics of the present invention. The purpose of the present invention is to enable the skilled person to understand the contents of the present invention and implement it according to the definition, instead of limiting the patent scope of the original creation, so that the others are not separated too much. The equivalent modification of the material completed by the spirit revealed by the creation should still be included in the scope of the following description. [Simple description of the drawings] The first figure is a schematic structural view of a conventional concentrated heat storage incinerator. The second picture is a schematic diagram of the implementation of the low-concentration concentrated heat storage and combustion scale. The third figure of Lu is a schematic structural view of another embodiment of the creation of a low pollution concentrated incineration device. [Main component symbol description], 10 concentrated heat storage incinerator 12, 32 zeolite runner 12a, 32a adsorption zone 12b, 32b desorption zone 12c, 32c cooling zone 14, 34 regenerative incinerator 11 !r 'production _ M324171 ' 14a 34a first regenerators 14b, 34b heating chambers 14c, 34c second regenerators 16, 36 first exhausting windmills 18^38 second pumping windmills-20, 40 exhaust chimneys 22a, 42a first valve members φ 22b 42b second valve member 22c, 42c third valve member 22d, 42d fourth valve member 24, 44 heat exchanger 30 low pollution concentrated heat storage incinerator 42e fifth valve member 46a first tube member 46b second tube member 46c third tube member 46d fourth pipe member 46e fifth pipe member 48 reclaimed pipe member 50 reclaimed valve member 12