//
發明領域： 經濟部智慧財產局員工消費合作社印製 本發明係有關於—種廢氣吸附處理系統之再生裝置及方 法’特別疋指-種以乾淨空氣為紐的二階段式清洗之廢氣 吸附處理系統之再生裝置及方法。 發明背景： 一般產業上廣泛性使用吸附方法去處理廢氣，而運用吸 附劑之多孔性質去將產業排放之廢氣中所含之有機氣體、臭 味或毒性物質產生物理或化學之吸附，使其吸陳該吸附劑 之孔隙内，以達到將產業排放廢氣加以淨化之目的。然而該 吸附劑於吸附飽和後，必須經由一再生程序將充填於吸附劑 内之被吸附物質（例如揮發性有機分子、高沸點化學物質… 等）去除，才可重複使用。 目前工業上最常採用的方法可分為線上再生或線外再生 兩種方法，線上再生通常是利用蒸汽或加高溫的惰性氣體將 吸附於孔隙内之有機分子驅出，例如日本公開昭63-232823 所揭示以蒸汽(110〜175。〇脫吸附的方法，將吸附於活性碳 内有機分子以蒸汽置換的方法脫出。又如英國專利 Britl，546,437及德國專利Ger. Offen2,419,827號所揭示以高 溫(120〜300°〇惰性氣體，將吸附於活性碳内的被吸附質吹 除；曰本公開昭63-310636則教導以加熱空氣將吸附於沸石 轉輪内之有機物去除的方法。線上再生的好處是可連續操 作，且可避免繁雜的吸附劑裝卸過程。唯此種再生方式對於 高沸點的化學物質則往往無法有效的移除，造成其殘留於吸 本紙張尺度適用中國國家標準（CNS)A4規格（210 X 297公釐） --------^------ (请先閱讀•背面之注意事項再填寫本頁) 505537 經濟部智慧財產局員工消費合作社印製 A7 B7 五、發明說明（>) 附劑的孔隙内或分解或聚合成寡聚物而影響吸附劑再吸附的 能力；此外如有易分解之化學品如四甲基二矽銨(HMDS)，三 甲基石夕烧(Trimethylsilanol)等遇水汽則分解為氫氧化矽的固 體或是如乙醇胺（MEA)等在某一溫度下則產生聚合，殘留 於吸附劑的表面而造成吸附劑的吸附能力逐漸下降而無法將 產業排氣有效處理至環保法規規定之排放標準之内，此時唯 有更換吸附劑，或將吸附劑由吸附槽内退出，採線外以更高 溫（通常為300〜l〇〇(TC)直接加熱或以高溫含氧氣體（例 如蒸汽、一氧化碳或氧......等）處理，將滯留於吸附劑孔隙 内的尚沸物質或聚合物燒除或分解，例如美國專利U.S. 4,957,721;日本公開特許62_282639及63-156542 等所揭 示之方法。此種方法雖可將滯留於吸附劑孔隙内之高沸點被 吸附質有效的分解脫除，但往往易造成吸附劑孔洞結構的破 壞而失去對特定物質的吸附能力，或因而劣化粉碎而損失。 此外再吸附劑的裝卸過程亦會有二次污染的問題存在。此外 如吸附系統是以吸附轉輪方式設計時，因限於吸附轉輪各吸 附劑間週邊封填物質的不耐高溫特性，而必須將整個吸附轉 輪解體成吸附劑原來之單元塊狀，焙燒再生後再行組合，非 常的不方便。 為了改善現在長期使用而老化不祕生的缺點，坊 間以一溶劑清洗或萃取的方法，以連續線上再生的方式將吸 附能力已降低而無法以-般之蒸汽、熱空氣或惰性氣體再生 之吸附劑或吸附系統再生，以延長吸附劑之使用期限。圖一 係為習用廢氣吸附處理系統喷灑式再生裝置之系統侧視結構 (請先閱讀背面之注意事項再填寫本頁) 裝--------訂---------線赢Field of the Invention: Printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economics The present invention relates to a regeneration device and method for an exhaust gas adsorption treatment system, in particular, a two-stage cleaning exhaust gas adsorption treatment system using clean air as a button Regeneration device and method. Background of the Invention: In the general industry, adsorption methods are widely used to treat exhaust gas, and the porous nature of adsorbents is used to physically or chemically adsorb organic gases, odors or toxic substances contained in exhaust gases emitted by the industry to make them adsorb. The pores of the adsorbent are aged to achieve the purpose of purifying industrial exhaust gas. However, after the adsorbent is saturated, the adsorbed substance (such as volatile organic molecules, high boiling point chemicals, etc.) filled in the adsorbent must be removed through a regeneration process before it can be reused. At present, the most commonly used methods in the industry can be divided into two methods: on-line regeneration or off-line regeneration. On-line regeneration usually uses steam or high temperature inert gas to drive out organic molecules adsorbed in the pores. For example, Japanese Publication No. 63- 232823 discloses the method of desorption by steam (110 ~ 175.〇, the method of removing organic molecules adsorbed in activated carbon by steam replacement. Another example is the British patent Britl, 546,437 and the German patent Ger. Offen 2,419,827 disclosed The adsorbed substance adsorbed in the activated carbon is blown off with a high temperature (120 ~ 300 ° inert gas); Japanese Publication No. Sho 63-310636 teaches a method of removing organic matter adsorbed in a zeolite runner by heating air. Online The advantage of recycling is that it can be operated continuously and can avoid the complicated loading and unloading process of the adsorbent. However, this method of recycling often cannot effectively remove high-boiling-point chemicals, which causes its residues to be absorbed in the paper. The Chinese national standard ( CNS) A4 specification (210 X 297 mm) -------- ^ ------ (Please read the note on the back before filling this page) 505537 Member of Intellectual Property Bureau, Ministry of Economic Affairs Printed by the Industrial and Consumer Cooperatives A7 B7 V. Description of the invention (>) The pores of the adjuvant may be decomposed or polymerized into oligomers to affect the ability of the adsorbent to re-adsorb; HMDS, Trimethylsilanol, etc. decompose into solids of silicon hydroxide in the presence of water vapor, or such as ethanolamine (MEA) will polymerize at a certain temperature and remain on the surface of the adsorbent to cause adsorption The adsorption capacity of the adsorbent is gradually decreasing, and the industrial exhaust gas cannot be effectively treated to the emission standard stipulated by environmental protection regulations. At this time, the only way to replace the adsorbent or to withdraw the adsorbent from the adsorption tank is to increase the temperature outside the production line (usually 300 ~ 100 (TC) directly heated or treated with high-temperature oxygen-containing gas (such as steam, carbon monoxide or oxygen, etc.) to burn off the still boiling substances or polymers remaining in the pores of the adsorbent Or decomposition, such as the methods disclosed in U.S. Patent No. 4,957,721; Japanese Laid-open Patent Nos. 62_282639 and 63-156542. Although this method can effectively remove the high boiling point retained in the pores of the adsorbent by the adsorbent, it can be effectively removed, but Often it is easy to cause the pore structure of the adsorbent to lose its ability to adsorb specific substances, or it will be degraded and lost. In addition, the process of re-adsorbent loading and unloading will also cause secondary pollution. In addition, if the adsorption system is converted by adsorption, In the design of the wheel method, due to the limited high temperature resistance of the surrounding packing material between the adsorbents of the adsorbent wheel, the entire adsorbent wheel must be disassembled into the original unit block of the adsorbent, which can be combined after regeneration and regeneration. Inconvenience. In order to improve the shortcomings of long-term use and aging, the adsorption capacity has been reduced by a solvent cleaning or extraction method in a continuous online regeneration mode, which cannot be used with ordinary steam, hot air or inert gas. Regenerated adsorbent or adsorption system is regenerated to extend the useful life of the adsorbent. Figure 1 is the system side view structure of the conventional spray adsorption regeneration system of the exhaust gas adsorption treatment system (please read the precautions on the back before filling this page) -Line win
505537 A7 五、發明說明（）） 示意圖，該系統裝置係以一裝設有高溶解力之混合溶劑，以 喷水器31將混合溶劑在脫附操作之前，將吸附劑淋浴喷灑清 洗，或是將清洗溶劑裝於一溶劑貯槽2内，將吸附系統中某 部分的吸附劑浸泡於其中，而使吸附劑的孔隙内的高沸有機 物質、寡聚體或塵埃等妨礙吸附能力的物質溶解或滌除，再 藉由一脫附風車32將濃縮廢氣送至一氧化分解爐33，圖二 係為習用廢氣吸附處理系統喷灑式再生裝置吸附轉輪結構示 意圖。在吸附轉輪式之吸附濃縮系統中，可在吸附轉輪j之 一再生區Π的前端另外加設一清洗區13。在清洗區13内安 設整排的喷嘴（圖中未示出），將清洗溶劑淋浴噴灑於吸附轉 輪1内之表面，而將其内之高沸有機質或募聚體滌除，圖三 係為習用廢氣吸附處理系統浸泡式再生裝置吸附轉輪結構示 意圖。採取浸泡方式操作時，可在吸附轉輪丨的下半部設該 溶劑貯槽2，内部裝有清洗液，每當吸附轉輪丨轉動至下半 部時即進行清洗，將殘留於吸附劑孔道内之高沸物質或寡聚 物溶解，此即可將吸附轉輪1内之吸附劑連續再生為增加清 洗之效並，可在槽内裝設超音波清洗器，如吸附系統為流體 化床式，則可在進入再生脫附區之前段增設一喷洗區（圖中 未示出），將附著於吸附劑内之高沸物質或寡聚體滌除。 、經由上述之廢氣吸附處理系統之再生裝置須以溶劑清洗 或萃取，無形中增加購買溶劑之費用，產生大量清洗後之廢 溶劑以及環境之破壞，無形中造成了該產業支付成本之增 加’此乃產業間急需解決之問題，以降低支付成本提昇產業 之競爭力，該問題之突破解決實為刻不容缓。 本紙張尺度適用中國國家標準（CNS)A4規格⑵◦ χ 297公羞 505537 經濟部智慧財產局員工消費合作社印製 A7 B7 五、發明說明（ψ) 發明概述： 本發明之主要目的在於提供一種廢氣吸附處理系統之再 生裝置及方法，該廢氣吸附處理系統之再生裝置及方法可達 到深入清洗吸附轉輪内部增進吸附轉輪之效能提升。 本發明之另一目的在於提供一種廢氣吸附處理系統之再 生裝置及方法，該廢氣吸附處理系統之再生裝置及方法可達 到降低廢水量減少清洗成本之功效。 為達上述之目的’該廢氣吸附處理系統其係將一第一容 置空間之氣體經由一吸附轉輪進入一第二容置空間，本發明 之廢氣吸附處理系統之再生裝置其係包括有：一導通道、至 少一喷嘴、一第一進氣道、一第二進氣道以及一抽離機構。 該導通道其係設於該第二容置空間之一中空立體結構。 該喷嘴其係可與該導通道相連接，可提供將一液體霧化 進入該導通道。 該第一進氣道其係可與該導通道相連接，該第一進氣道 可提供清淨之氣體進入該導通道。 該第二進氣道其係設於與該第一容置空間相對應適當位 置處，該第二進氣道可提供清淨之氣體進入該第一容置空間。 該抽離機構其係設於與該第二容置空間相對應適當位置 處，該抽離機構可提供將該第二容置空間之氣體抽離。 因此經由上述之廢氣吸附處理系統之再生裝置可使得本 發明之廢氣吸附處理系統之再生方法，其係包括有下列步驟： 步驟（a):提供一廢氣吸附處理系統，該廢氣吸附處理 系統其係將一第一容置空間提供之氣體經由一吸附轉輪進入 • 5 - t紙張尺度適用中國@標準（CNS)A4規格（21G x 297公^ - (請先閱讀背面之注意事項再填寫本頁) ，裝--------訂---------線赢 505537 Α7 Β7 五 經濟部智慧財產局員工消費合作社印製 發明說明（f) 一第二容置空間。 步驟（b):將〆導通道設於該第二容置空間，可提供一 液體霧化之至少/噴嘴與可提供適當速度清淨氣體之一第一 進氣道連接於該導通道，可提供適當速度清淨氣體之一第二 進氣道設於與該第/容置空間，可提供將氣體抽離之一抽離 機構設於與該第二容置空間相對應適當位置處。 步驟（C):導入該霧化液體以及第一進氣道之適當速度 清淨氣體進入該導通道通過該吸附轉輪。 步驟（d):導入第二進氣道之適當速度清淨氣體進入該 第一容置空間通過該吸附轉輪。 步驟（e):以該抽離機構將該第二容置空間以及吸附轉 輪之氣體抽離。 為使貴審查委員對於本發明能有更進一步的了解與認 同，茲配合圖式作一詳細說明如后。 圖式之簡單說明： 圖一係為習用廢氣吸附處理系統噴灑式再生襞置之系統側視 結構不意圖。 ’' 圖二係為制廢氣吸附處理系統噴灑式再生裝置吸附轉輪結 構示意圖。 圖三係為_廢氣_處絲概泡式再生裝置_ 構示意圖。 … 圖氣吸附處理系統之再生裝置較佳實施例立 (讀先閱讀背面之注意事項再填寫本頁) 零--------丨訂--------- %· 6- 505537 A7 B7 五、發明說明（t) 圖五係為本發明廢氣吸附處理系統之再生方法較佳實施例流 程示意圖。 (請‘先閱讀'f面之注意事項再填寫本頁) 圖式之圖號說明： 1〜吸附轉輪 11〜再生區 12〜吹除區 13〜清洗區 2〜溶劑貯槽 31〜喷水器 32〜脫附風車 33〜氧化分解爐 51〜第一容置空間 52〜第二容置空間 53〜吸附轉輪 61〜導通道 62〜喷嘴 經濟部智慧財產局員工消費合作社印製 621〜電磁閥 63〜抽離機構 64〜第一進氣道 641〜第一風門 65〜第二進氣道 651〜第二風門 81〜提供一廢氣吸附處理系統 本紙張尺度適用中國國家標準（CNS)A4規格（210 X 297公釐） ⑽537 ⑽537 經濟部智慧財產局員工消費合作社印製 A7 B7 五、發明說明（？） 82〜裝置一廢氣吸附處理系統之再生裝置 83〜乾淨氣體為載流’載動霧化液體進入導通、f 84〜乾淨氣體進入第一容置空間 、 85〜抽離機構將第二容置㈣以及吸轉輪 86〜加熱吸附轉輪 虱體抽離 發明詳細說明： 本發明之廢氣吸附處理系統之再生裝置及方法 一 ===氣氣流為載流，將霧化之液體攜入該 進仃延洗’再該吸轉輪内部水 二階段式清洗該吸附轉輪。 八 請參閱圖四所示，其係為本發明廢氣吸附處理系统之再 生肢較佳實_立體賴示賴。本發明制之廢氣吸附 處理系統較佳實施例其係將—第—容置⑽51之氣體經由 一吸附轉輪53進入-第二容置空間52，藉由該吸附轉輪％ 職第—容置空間51之廢氣中所含有機氣體、臭味或毒性物 為產生物理或化學之吸附，使其吸附於該吸附劑之孔隙内， 排放至该第二容置空間52，以達到將產業排放廢氣加以淨化 之目的’該廢氣吸附處理系統其係可為一清洗潤濕之功效系 統者，而該吸附轉輪53係指塗佈有吸附材、裝有吸附材的堆 積床或流動床者，或係吸收式處理床、生物式過濾處理床其 中一種之廢氣處理系統，而本發明該廢氣吸附處理系統之再 生裝置其可將該該廢氣吸附處理系統作洗清或潤滑功效，其 中較佳者係於該廢氣吸附處理系統裝設有：一導通道61、至 :297公釐） ------1·壯衣--------tr---------% (-tt先閱讀.背面之注意事項再填寫本頁) 505537 經濟部智慧財產局員工消費合作社印制衣 A7 B7 五、發明說明（/ ) 少一喷嘴62、第一進氣道64、第二進氣道65、以及一抽離 機構63。 於本發明較佳實施中，該導通道61其係為設於該第二容 置空間52之一中空立體結構，該喷嘴62其係可與該導通道 61相連接，該喷嘴62可提供高壓將一液體霧化進入該導通 道61，考慮成本及環保之選擇下，其中該液體係以水來加以 使用，其中該液體進入該噴嘴62之液量其係更以一電磁閥 621控制，而於本發明較佳實施中該噴嘴62其係為三個，當 然亦可為其他個數，如此數量之變化設計，係為熟知此類技 藝人士皆能明瞭，適當而作些微的改變及調整，仍將不失本 發明之要義所在，亦不脫離本發明之精神和範圍。 、於本發明較佳實施中，該第一進氣道64其係可與該導通 道61相連接，鄕-聽道64可提供清淨之進入該導 I道61，且咸第一進氣道64更設有一第一風門，該第一 ，門641可控制進入該第一進氣道64之氣流量，而該第二進 =道仍、其係設於與該第-容置空間51相對應適當位置處， 〜第-進氣道65亦是提供清淨之氣體進人該第—容置空間 以提供加速因通過該吸附轉輪％而減速之該霧化液體， =仃4二隨之觀_輪53清洗工作，t賴第二進氣道 ^設有—第二風門651，該第二風_可控舰入該第 二乳道65魏缝’於树雜讀财，該第一進氣道 及該第"進紐65 為齡妓之氣舰流，以該 =機構63可提供將該第二容置空間52之氣體以及該吸附 轉輪53之氣體抽離，而該抽離機構63其係為一風扇，或為 (讀先閱讀.背面之注意事項再填寫本頁}505537 A7 V. Description of the invention ()) The schematic diagram of the system is a mixed solvent equipped with a high dissolving power. The mixed solvent is sprayed and cleaned by a water sprayer 31 before the desorption operation, or The cleaning solvent is contained in a solvent storage tank 2 and a part of the adsorbent in the adsorption system is immersed therein, so that high-boiling organic substances, oligomers, or dust in the pores of the adsorbent, such as substances that hinder the adsorption ability, are dissolved. Or, it is removed, and then the concentrated exhaust gas is sent to an oxidation decomposition furnace 33 through a desorption windmill 32. FIG. 2 is a schematic diagram of the structure of an adsorption runner of a spray regeneration device of a conventional exhaust gas adsorption treatment system. In the adsorption-wheel-type adsorption concentration system, a cleaning zone 13 may be additionally provided at the front end of a regeneration zone Π of the adsorption wheel j. Set a whole row of nozzles (not shown in the figure) in the cleaning area 13, shower spray the cleaning solvent on the surface inside the adsorption rotor 1, and remove the high-boiling organic matter or aggregates in it. This is a schematic diagram of the structure of an adsorption runner of a conventional exhaust gas adsorption treatment system immersion regeneration device. When the immersion operation is adopted, the solvent storage tank 2 can be set in the lower half of the adsorption rotor 丨 with a cleaning liquid inside. When the adsorption rotor 丨 rotates to the lower half, it is cleaned and will remain in the adsorbent holes The high-boiling substances or oligomers in the channel are dissolved, and the adsorbent in the adsorption runner 1 can be continuously regenerated to increase the cleaning effect. An ultrasonic cleaner can be installed in the tank. If the adsorption system is a fluidized bed In addition, a spray washing zone (not shown in the figure) can be set up before entering the regeneration desorption zone to remove high-boiling substances or oligomers attached to the adsorbent. The regeneration device passing the above-mentioned exhaust gas adsorption treatment system must be cleaned or extracted with a solvent, which substantially increases the cost of purchasing the solvent, resulting in a large amount of waste solvent after cleaning and environmental damage, which virtually increases the cost of the industry's payment. It is an urgent problem among industries to reduce the cost of payment and improve the competitiveness of the industry. The breakthrough of this problem is urgent. This paper size applies to China National Standard (CNS) A4 specifications ⑵ χ 297 public shame 505537 printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs A7 B7 V. Description of the invention (ψ) Summary of the invention: The main purpose of the present invention is to provide an exhaust gas The regeneration device and method of the adsorption treatment system, and the regeneration device and method of the exhaust gas adsorption treatment system can achieve deep cleaning of the interior of the adsorption runner to improve the performance of the adsorption runner. Another object of the present invention is to provide a regeneration device and method for an exhaust gas adsorption treatment system. The regeneration device and method for the exhaust gas adsorption treatment system can achieve the effect of reducing the amount of wastewater and reducing the cleaning cost. In order to achieve the above-mentioned purpose, the exhaust gas adsorption treatment system is to pass the gas of a first containing space into a second containing space through an adsorption runner. The regeneration device of the exhaust gas adsorption treatment system of the present invention includes: A guide channel, at least one nozzle, a first air inlet, a second air inlet, and an extraction mechanism. The guide channel is a hollow three-dimensional structure provided in one of the second accommodation spaces. The nozzle can be connected with the guide channel, and can provide atomization of a liquid into the guide channel. The first air inlet can be connected with the guide channel, and the first air inlet can provide clean gas to enter the guide channel. The second air inlet is disposed at an appropriate position corresponding to the first accommodation space, and the second air inlet can provide clean gas to enter the first accommodation space. The evacuation mechanism is disposed at an appropriate position corresponding to the second accommodating space, and the evacuation mechanism can provide evacuation of the gas in the second accommodating space. Therefore, the regeneration method of the exhaust gas adsorption treatment system of the present invention can be implemented through the regeneration device of the exhaust gas adsorption treatment system described above, which includes the following steps: Step (a): Provide an exhaust gas adsorption treatment system. The gas provided by a first accommodating space is entered through an adsorption wheel. • 5-t paper size is applicable to China @standard (CNS) A4 specifications (21G x 297 mm ^-(Please read the precautions on the back before filling this page) ), Install -------- order --------- line win 505537 Α7 Β7 five printed by the Intellectual Property Bureau of the Ministry of Economic Affairs employee consumer cooperatives invention description (f) a second accommodation space. (B): The puppet guide channel is provided in the second accommodating space, which can provide at least a liquid atomizer / nozzle and one of the first air inlets which can provide clean gas at an appropriate speed. One of the second air inlets of the speed-cleaning gas is provided in the first / receiving space, which can provide an evacuation mechanism for removing the gas in an appropriate position corresponding to the second accommodating space. Step (C) : Introduce the atomized liquid and the first inlet The cleaning gas at an appropriate speed enters the guide passage and passes through the adsorption runner. Step (d): The cleaning gas at an appropriate speed introduced into the second intake passage enters the first accommodation space and passes through the adsorption runner. Step (e): Use the The extraction mechanism extracts the gas from the second accommodating space and the adsorption runner. In order for your review committee to have a better understanding and approval of the present invention, a detailed description is given below in conjunction with the drawings. Brief description: Figure 1 is a schematic view of the side structure of the conventional spray adsorption regeneration system of the exhaust gas adsorption treatment system. '' Figure 2 is a schematic diagram of the structure of the adsorption runner of the spray regeneration equipment of the exhaust gas adsorption treatment system. _Exhaust gas_probable bubble type regeneration device_ Schematic diagram.… Figure The preferred embodiment of the regeneration device for the gas adsorption treatment system is established (read the precautions on the back before filling in this page) Zero --------丨 Order ---------% · 6- 505537 A7 B7 V. Description of the invention (t) Figure 5 is a schematic flow chart of a preferred embodiment of the regeneration method of the exhaust gas adsorption treatment system of the present invention. (Please 'read first' 'F side notes refill (This page) Description of drawing numbers: 1 ~ Adsorption runner 11 ~ Regeneration zone 12 ~ Blow-out zone 13 ~ Washing zone 2 ~ Solvent storage tank 31 ~ Water sprayer 32 ~ Desorption windmill 33 ~ Oxidation decomposition furnace 51 ~ 第One accommodating space 52 ~ second accommodating space 53 ~ adsorption runner 61 ~ guide passage 62 ~ nozzle Printed by employee consumer cooperative of the Intellectual Property Bureau of the Ministry of Economy 621 ~ solenoid valve 63 ~ extraction mechanism 64 ~ first air inlet 641 ~ First damper 65 ~ Second air inlet 651 ~ Second damper 81 ~ Provide an exhaust gas adsorption treatment system The paper size is applicable to China National Standard (CNS) A4 (210 X 297 mm) ⑽537 ⑽537 Intellectual Property Bureau, Ministry of Economic Affairs Printed by employees' consumer cooperatives A7 B7 V. Invention Description (? ) 82 ~ Regeneration device of an exhaust gas adsorption treatment system 83 ~ Clean gas is the carrier current, which carries the atomized liquid into conduction, f 84 ~ Clean gas enters the first containing space, 85 ~ The extraction mechanism places the second containing ㈣ and suction wheel 86 ~ heating and adsorption wheel lice body extraction Detailed description of the invention: Regeneration device and method of the exhaust gas adsorption treatment system of the present invention === Air current is the carrier current, and the atomized liquid is carried into the inlet仃 Extended washing 'and then the adsorption wheel is cleaned in two stages by the water inside the suction wheel. 8 Please refer to FIG. 4, which is a better representation of the regeneration limb of the exhaust gas adsorption treatment system of the present invention. The preferred embodiment of the exhaust gas adsorption treatment system made by the present invention is to enter the gas of the first-receiving ⑽51 through an adsorption rotor 53 into the second accommodating space 52. The organic gas, odor or toxic substance contained in the exhaust gas in the space 51 is physically or chemically adsorbed, and is adsorbed in the pores of the adsorbent, and is discharged into the second accommodation space 52 to achieve exhaust emissions from the industry. Purification purpose 'The exhaust gas adsorption treatment system can be a system for cleaning and wetting, and the adsorption rotor 53 refers to a stacked bed or a fluidized bed coated with an adsorption material, and equipped with the adsorption material, or It is an exhaust gas treatment system of one of the absorption treatment bed and the biological filtration treatment bed, and the regeneration device of the exhaust gas adsorption treatment system of the present invention can use the exhaust gas adsorption treatment system for cleaning or lubricating effect. The better one is The exhaust gas adsorption treatment system is equipped with: a guide channel 61, to: 297 mm) ------ 1 · Zhuang Yi -------- tr ---------% (-tt Read first. Note on the back before filling out this page) 505537 Ministry of Economy Wisdom Printed clothes for employees' cooperatives of the Property Bureau A7 B7 V. Description of the invention (/) One nozzle 62, the first air inlet 64, the second air inlet 65, and an extraction mechanism 63 are missing. In a preferred implementation of the present invention, the guide channel 61 is a hollow three-dimensional structure provided in one of the second accommodation spaces 52, and the nozzle 62 is connected to the guide channel 61. The nozzle 62 can provide high pressure A liquid is atomized into the guide channel 61. Considering the cost and environmental protection options, the liquid system is used with water, and the amount of liquid that enters the nozzle 62 is controlled by a solenoid valve 621. In the preferred implementation of the present invention, the number of the nozzles 62 is three, of course, it can also be other numbers. The change in the number is designed for those skilled in the art to understand and make slight changes and adjustments as appropriate. The essence of the present invention will not be lost, nor will it depart from the spirit and scope of the present invention. In a preferred implementation of the present invention, the first air inlet 64 can be connected to the guide channel 61, and the 听 -listening channel 64 can provide clean access to the guide I channel 61, and the first air inlet 64 is further provided with a first damper, the first, door 641 can control the air flow entering the first air inlet 64, and the second inlet is still in the same phase as the first accommodation space 51 Corresponding to the appropriate position, the ~ -inlet 65 is also to provide clean gas into the first-receiving space to provide the atomized liquid which accelerates and decelerates due to passing through the adsorption wheel%, = 仃 4 2 followed by Watching the cleaning work of wheel 53, the second air inlet is provided with a second air door 651, and the second wind controllable ship enters the second milkway 65 and is sewn in the tree miscellaneous reading, the first The air inlet and the " into 65 " are the carrier flow of the aging prostitute, and the = mechanism 63 can provide the gas of the second accommodating space 52 and the gas of the adsorption runner 53, and the pumping Li Institution 63 is a fan, or (Read it first. Note on the back, then fill out this page}
--------訂--------I 氏張尺度適用中關家標準（CNS)A4規格（210 : 297公釐） 505537 A7 ----------- B7___ 五、發明說明（7 ) 一可產生氣體流動之機構，且該抽離機構63設於與該第二容 置空間52相對應適當位置處。 、 該本發明廢氣吸附處理系統之再生方法可藉由設置上述 之該廢氣吸喊理祕之再生裝置，加以執行實施完成，請 參閱圖五所不，其係為本發明廢氣吸喊理純之再生方法 較佳實施例流程示意圖。其中本發明廢氣吸附處理系統之再 生方法其係包括有下列步驟，其中圖式編號叩说科炎 係分別對應步驟（a)至步驟（e): 步驟（a):提供一廢氣吸附處理系統，該廢氣吸附處理 系統其係將-第-容置空間提供之氣體經由—吸_輪進入 一第二容置空間。 步驟（b):將一導通道設於該第二容置空間，可提供一 液，霧化之至少—噴嘴與可提供適當速度清淨氣體之-第一 進^道連接_導通道，可提供適#速度清淨氣體之一第二 進氣道設於與鄕—容数間，可提供職體抽離之一抽離 機構设於與該第二容置空間相對應適當位置處。 、主步驟（c):導入該霧化液體以及第一進氣道之適當速度 /月淨氣體進入該導通道通過該吸附轉輪，此時該霧化液體以 及乾淨氣_過觀_輪進行逆洗之程序，聽時通過該 $附轉輪之霧化液體會朝重力方向滲附至該吸附轉輪下方^ >步驟⑷：導入第二進氣道之適當速度清淨氣體進入該 第一容置空間通過該吸附轉輪，以提供加速因通過該吸附轉 輪而減速之該霧化液體，以便進行第二階段之該吸附轉輪清 -10 --------- Order -------- I's scale is applicable to Zhongguanjia Standard (CNS) A4 specification (210: 297 mm) 505537 A7 ---------- -B7___ V. Description of the invention (7) A mechanism capable of generating gas flow, and the extraction mechanism 63 is provided at an appropriate position corresponding to the second accommodation space 52. The regeneration method of the exhaust gas adsorption treatment system of the present invention can be implemented by setting up the above-mentioned regeneration device of the exhaust gas absorption principle, please refer to FIG. 5 for the regeneration of the exhaust gas absorption and purity of the present invention. Method flow diagram of the preferred embodiment. The regeneration method of the exhaust gas adsorption treatment system of the present invention includes the following steps, wherein the drawing number indicates that the Keyan system corresponds to steps (a) to (e), respectively: Step (a): providing an exhaust gas adsorption treatment system, In the exhaust gas adsorption treatment system, the gas provided by the first storage space is passed into the second storage space through the suction wheel. Step (b): A guide channel is provided in the second accommodating space, which can provide at least one liquid and atomize-the nozzle is connected with the first inlet channel which can provide clean gas at an appropriate speed-the guide channel can provide One of the second air inlets of the clean air at a suitable speed is provided between the space and the capacity, and an extraction mechanism that can provide professional evacuation is provided at an appropriate position corresponding to the second accommodation space. Main step (c): Introduce the atomized liquid and the appropriate velocity / monthly net gas of the first air inlet into the guide channel and pass the adsorption runner, at this time, the atomized liquid and clean gas_overview_wheel are performed The process of backwashing, when listening, the atomized liquid passing through the $ attachment wheel will permeate under the adsorption runner in the direction of gravity ^ > Step ⑷: The clean gas with an appropriate speed introduced into the second air inlet enters the first The accommodating space passes through the adsorption runner to provide the atomized liquid which accelerates and decelerates due to passing through the adsorption runner, so as to perform the second stage of the adsorption runner cleaning.
本紙張尺度_ -中國賴χ 297公^ J (.tt先閱讀嘴面之注意事項再填寫本頁) --------訂----Dimensions of this paper _-China Lai χ 297 ^ ^ (.tt first read the notes on the mouth and then fill out this page) -------- Order ----
n n ϋ I 經濟部智慧財產局員工消費合作社印製 經濟部智慧財產局員工消費合作社印製 505537 A7 B7 _ 五、發明說明（ 洗工作。 步驟（e):以該抽離機構將該第二容置空間以及吸附轉 輪之氣體抽離，此時因滲附至該吸附轉輪之液體由另一端面 被該抽離機構抽離時會通過該吸附轉輪之内部，因此可有效 進行二階段之吸附轉輪清洗或潤濕工作。 當然本發明之較佳實施中該步驟（e)之後更可包括有步 驟⑴：加熱該吸附轉輪86，以提供高溫活化再生該吸附轉 輪。當然本發明逕是提供一線上清洗之裝置及方法，當然將 噴嘴或導通道位置變更或將該吸附轉輪拆離後以相同之清洗 設備及程序洗清或潤濕該吸附轉輪，如此之變化設計，係為 熟知此類技藝人士皆能明瞭，適當而作些微的改變及調整， 仍將不失本發明之要義所在，亦不脫離本發明之精神和範圍。 由以上本發明之廢氣吸附處理系統之再生裝置及方法， 確實可達到深入清洗吸附轉輪内部增進吸附轉輪之效能提升 以及降低廢水量減少清洗成本之功效，實是克服習用技;術之 缺失’滿足產業界之需求並提高產業競爭力。 以上所述係利用較佳實施例詳細說明本發明，而非限制 本發明之範圍，而且熟知此類技藝人士皆能明瞭，適當而作 些微的改變及調整，仍將不失本發明之要義所在，亦不脫離 本發明之精神和範圍。 綜上所述，本發明實施之具體性，誠已符合專利法中所 規定之發明專利要件，謹請貴審查委員惠予審視，並賜准 專利為禱。 -11- 本紙張尺度適用中國國家標準（CNS)A4規格x 297公爱）nn ϋ I Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs printed 505537 A7 B7 _ V. Description of the invention (Washing work. Step (e): Use the extraction agency to copy the second volume The space is drawn away from the adsorption wheel. At this time, because the liquid that has adhered to the adsorption wheel is evacuated by the extraction mechanism from the other end surface, it will pass through the interior of the adsorption wheel, so the two-stage can be effectively performed. The cleaning or wetting of the adsorption rotor. Of course, after the step (e) in the preferred implementation of the present invention, it may include a step ⑴: heating the adsorption rotor 86 to provide high-temperature activation and regeneration of the adsorption rotor. The invention is to provide a device and method for online cleaning. Of course, after changing the position of the nozzle or guide channel or detaching the adsorption rotor, the adsorption rotor is cleaned or wetted with the same cleaning equipment and procedures. For those who are familiar with such arts can understand that making appropriate changes and adjustments will still not lose the essence of the invention, nor depart from the spirit and scope of the invention. The regeneration device and method of the exhaust gas adsorption treatment system of the present invention can indeed achieve the effect of deeply cleaning the interior of the adsorption runner, improving the efficiency of the adsorption runner, reducing the amount of waste water, and reducing the cost of cleaning. The needs of the industry and improve the competitiveness of the industry. The above is a detailed description of the present invention using preferred embodiments, rather than limiting the scope of the invention, and those skilled in the art will be able to understand and make slight changes and adjustments as appropriate. , Still will not lose the essence of the invention, nor depart from the spirit and scope of the invention. In summary, the specificity of the implementation of the invention has already met the requirements of the invention patent stipulated in the Patent Law. The members are grateful for the review and granted the patent as a prayer. -11- This paper size applies the Chinese National Standard (CNS) A4 specification x 297 public love)