M333951 八、新型說明： 【新型所屬之技術領域】 本創作係關於含揮發性有機物(Volatile Organic Componds，VOCs)廢氣之 活性碳脫附處理技術，更詳而言之，乃指一種能達成回收活性碳之處理回收熱 之流動床式活性礙脫附裝置。 【先前技術】 按’揮發性有機氣體(Volatile Organic Componds，VOCs)最大使用類別為 _ 有機溶劑，且廣泛的用於各種行業，如塗裝業、油漆業、化工業及半導體封裝 業之溶劑回收及半導體晶圓製造業、光電業之稀釋及清洗。 目前國内常用之有機溶劑主要種類包括：醇類—甲醇、異丙醇、丁醇及 異丁醇等。（2)酮類-丙_、丁酮、環己酮等。⑶麵—醋酸乙醋、醋酸丁醋。 (4)含氯溶劑-三氯甲烷、四氯化碳、二氯甲烷等。（5)其它—苯、甲苯、二甲苯 等。此外尚有-些製程溶劑。又v〇c於環境、安全及衛纽面之主要特性有⑴ 毒害性。⑵何生性空氣污染。⑶臭氧層破壞。⑷爆炸安全性，因此對於耽 擊必須有適當之處理技術及受法條所管制。 關於·控制技術分為有一部份為活性碳吸附方式，通常用活性碳吸附無 法重複使用相田浪費且使用後的之污染問題亦難處理；故以目前所慣用之處 理技術而言，均有其未盡理想之處。 有鑑於此，為徹底改善對活性碳無法重複使用所存在之缺失與弊病，本發 明人乃秉躲務大眾之決心’麟_該行_積之專業素養，經反覆潛 心研九、、於有此更只用之「流動床式活性碳脫附裝置」產生。 【新型内容】 5 M333951 本創作之目的在於提供-種流動床式活性破脫附裝置，其主要為一種將揮 發有機物VQC廢氧利用雜狀活性碳予以吸附，並採用電熱及觸媒氧化器產 生,、、、風正壓風車輸送熱氣送入活性碳流動床進行脫附，再將脫附後之廢熱使 用廢熱雜熱交換器回收廢熱，再將此熱量回㈣以活性额生裝置，使用電 熱而不須使用瓦斯或者重油造成二次污染，更大幅提高產業競爭優勢。 兹進-步配合圖式，以說明本裝置之較佳實施例，俾令貴審委員能對本 創作有更深入且具體的瞭解。 • 【實施方式】 請參閱第-騎示，係本創作—較佳實施例之活性碳流動床式脫附装置 圖，其組成至少包括有： 一活性碳吸附塔⑴’主歸性碳比表面積大之躲（⑽―麵 產生大面積觸效果達到排放乾淨之空氣之法規標準；依圖中所示，該 活性竣吸附塔⑴’配設㈣—活性碳輸縣（i G)，細蝴财 式輸送活性碳域動床式雖碳_床（2)上方送人，—旦發生異常時，該 第一活性碳輸送泵（1〇)會停止輸送。 X /、 " * 一流動床式活性碳脫附床⑵，依圖中所示，吸附voc污染物之活制 式雜厌脫附床⑵上方一側送入，且將經加熱後約縱C熱風量由 墙入，於流動床式活性碳脫附床⑵内設有連串之多個沖孔板（2㈤ 弟二圖所示’且外部亦配設有獨立輸送之第二活性碳輸送泵(2 1〇 ,藉以利 咖縮使細她嫩聰嫩^ ;顧峨卿脫附 2)利用流動式之原理方式，使吸附於活性破之v〇c污染物得以脫附，脫丨 出之廢熱_後段_氧储（3 i )回收，錄再生之乾淨雜碳則由下 6 M333951 輸出後再送回活性破桶槽（1)内繼續使用。 一觸媒氧化裔（3 1 )，用以回收廢熱，並使外部空氣由一側輸入後具有預 熱效果’進-步使用有-電熱式加熱器（3)及—正壓風車（3◦)，該電熱式 加熱器（3 )，係利用電熱加熱方式控制麵空氣之脫附溫度（脫附溫度24(rc )， 且僅需要4許電ΐ便可達成將脫輕氣立即加熱輯需之颜溫度，再送入流 動床式活性碳_床⑵内，該正壓風車（3 Q )败顧正壓力將熱空氣 經電熱式加熱器（3 )送人流絲式潍碳脫附床（2 )内；例如# lc丽空氣 流量溫度從2_熱至歡_要謂HR電量，目回㈣量雜回收能源， 所以經觸縣㈣（3 1 )熱是相#魏_倾，因此棚此一回收再 生能源之特性將使其操作過程更加省能源。 依據上賴叙摘作「流練式潍销随置」，當其在實際地實施 上，大體上可分為三個過程進行，即制、流動床式贿及廢熱回收熱處理。 其中.吸附部分與制並無差異，特別是：流動床式脫附及廢熱回收熱處理兩 部分為技術特徵之所在。換言之’即是流動床式活性碳脫附床(2)於活性碳 脱附過程中進—步包括：對外部空錄人經觸媒氧化W 3 i )做預熱作用， 讀輪加触（3 )戦城至_溫度之錄雜；供細媒氧化 器（3 i )欲將耽加熱至靴之部分能源，以減低其電量輸出。 ==紙恤細床⑵、觸嫩器⑴）、電熱加熱器 (3)荨所而之犯源或熱量，部分 邱可 ^(31) 雜由nrr床式雜碳脫随置’解決了傳統活性細易脫附的 齡+魏及贿所使狀雜絲麵处找氣滅火安 7 M333951 全機制，且利用生產排放的廢氣V〇C可燃燒特性產生熱源，而不須使用瓦斯或 者重油造成二次污染之操作成本降低，及環保排放標準之處理效率相當高，足 可大幅提高產業競爭優勢。 細上所述，本創作「流動床式活性碳脫附裝置」確可達到預期之目的與功 效，且未見諸任何公開使用者，符合專利實用性、新穎性之要件，爰依法向釣 局提出專利申請。 而陳明者’以上所述乃是本發明之較锃實施例，如依本發明之構想所作之 改變’其產生之魏、侧仍未超出細書細式所涵蓋之精神時，_切應屬 本新型裝置之範圍内，合予陳明^ 【圖式簡單說明】 第-圖係補作-較佳實蘭之流動床式活性碳脫附裝置麟配置圖。 第-圖係本創作-健實關之流動床式活性碳脫附床_體化示意 【主要元件符號說明】 活性碳吸附塔（1) 流動床式活性碳脫附床（2) 第二活性碳輸送泵（21) 電熱式加熱器（3) 觸媒氧化器（31 ) 第一活性碳輸送泵（1〇) 沖孔板（2 0) 正壓風車（3 0 ) 8M333951 VIII. New Description: [New Technology Field] This creation is about the activated carbon desorption treatment technology of Volatile Organic Componds (VOCs) waste gas. More specifically, it refers to a kind of recovery activity. The carbon treatment recovers the heat of the fluid bed type active desorption device. [Prior Art] According to 'Volatile Organic Componds (VOCs), the largest use category is _ organic solvents, and is widely used in various industries, such as coating, paint, chemical and semiconductor packaging. And semiconductor wafer manufacturing, photovoltaic industry dilution and cleaning. At present, the main types of organic solvents commonly used in China include: alcohols - methanol, isopropanol, butanol and isobutanol. (2) ketones - propyl ketone, methyl ethyl ketone, cyclohexanone, and the like. (3) Noodle - ethyl acetate, butyl acetate. (4) Chlorine-containing solvent - chloroform, carbon tetrachloride, dichloromethane, and the like. (5) Others - benzene, toluene, xylene, etc. In addition, there are some process solvents. The main characteristics of the environment, safety and health are also (1) toxic. (2) What is the air pollution? (3) Destruction of the ozone layer. (4) Explosion safety, therefore, it must be properly handled and controlled by the law. About · Control technology is divided into a part of activated carbon adsorption, usually with activated carbon adsorption can not be reused phase waste, and the pollution problem after use is also difficult to deal with; therefore, in the current processing technology, there are Not ideal. In view of this, in order to completely improve the lack of disadvantages and disadvantages of the inability to reuse activated carbon, the inventor is determined to hide the public's determination of 'Lin _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ This is only used in the "flowing bed type activated carbon desorption device". [New content] 5 M333951 The purpose of this creation is to provide a fluidized bed type active debonding device, which mainly uses a volatile activated carbon VQC waste oxygen to be adsorbed by heterogeneous activated carbon, and is produced by electrothermal and catalytic oxidizer. , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , It does not require the use of gas or heavy oil to cause secondary pollution, and greatly enhances the competitive advantage of the industry. The following is a step-by-step diagram to illustrate the preferred embodiment of the apparatus and to enable the audit committee to have a deeper and more specific understanding of the creation. • [Embodiment] Please refer to the first-riding diagram, which is a diagram of an activated carbon fluidized bed desorption apparatus according to the present invention, and the composition thereof includes at least: an activated carbon adsorption tower (1) 'mains carbon specific surface area Dazhizhi ((10)-face produces a large-area touch effect to achieve the emission of clean air standards; as shown in the figure, the active 竣 adsorption tower (1)' is equipped with (four) - activated carbon to the county (i G), fine The transporting activated carbon domain moving bed type is given above the carbon_bed (2), and when the abnormality occurs, the first activated carbon transfer pump (1〇) stops conveying. X /, " * A fluid bed type The activated carbon desorption bed (2), as shown in the figure, is fed on the upper side of the activated anaerobic desorption bed (2) which adsorbs voc contaminants, and is heated by the longitudinal C hot air volume into the wall, in a fluidized bed type The activated carbon desorption bed (2) is provided with a series of multiple perforated plates (2 (5) shown in the second figure' and externally equipped with a second activated carbon transfer pump (2 1 〇, by means of Fine her tender and tender ^; Gu Yuqing detachment 2) using the flow of the principle of the way to make the adsorption of active broken v〇c pollutants It can be desorbed, and the waste heat from the _ _ _ _ oxygen storage (3 i ) is recovered, and the clean mixed carbon recorded by the next 6 M333951 is sent back to the active vat tank (1) for further use. (3 1 ), used to recover waste heat, and has external warm air from one side to have a preheating effect. 'Into-step use-electric heater (3) and - positive pressure windmill (3◦), the electric heating The heater (3) uses the electrothermal heating method to control the desorption temperature of the surface air (desorption temperature 24 (rc), and only needs 4 electric enthalpy to achieve the desired temperature for the degassing of the air immediately. And then fed into the fluidized bed type activated carbon_bed (2), the positive pressure windmill (3Q) loses the positive pressure to send the hot air to the flow-type carbon desorption bed (2) through the electric heater (3); for example # lc丽 air flow temperature from 2_热到欢_ to HR power, eye back (four) amount of miscellaneous energy recovery, so the contact county (four) (3 1) heat is the phase #魏_倾, therefore the shed this recycling energy Its characteristics will make its operation process more energy-efficient. According to Shang Lai's abstract "streaming-type credit-selling", when it is actually implemented In general, it can be divided into three processes, namely, system, fluid bed bribery and waste heat recovery heat treatment. Among them, there is no difference between the adsorption part and the system, especially: the fluid bed type desorption and the waste heat recovery heat treatment are technical features. In other words, the flow bed type activated carbon desorption bed (2) in the process of desorption of activated carbon includes: preheating the externally occluded human oxidized W 3 i ), the read wheel Touch (3) 戦城至_temperature recording; for the fine oxidizer (3 i ) to heat the 耽 to part of the energy of the boot to reduce its power output. ==paper bed (2), toucher (1)), electric heater (3) guilty of the source or heat, part of Qiu Ke ^ (31) Miscellaneous by nrr bed type carbon-carbon de-supplement 'solved the traditional active fine easy to desorb the age + Wei and bribe The whole mechanism of the gas-fired fire safety system is used, and the heat source is generated by the combustion characteristic of the exhaust gas V〇C produced by the production, without the use of gas or heavy oil to reduce the operating cost of secondary pollution, and environmental protection emissions. The standard processing efficiency is quite high, which can greatly improve the industrial competitive advantage.As described above, the “Flower Bed Activated Carbon Desorption Device” of this creation can achieve the intended purpose and efficacy, and has not seen any public users, and meets the requirements of patent practicability and novelty. File a patent application. And the above description is a comparative example of the present invention, such as the change made according to the concept of the present invention, the Wei and the side of the invention are still beyond the spirit covered by the fine book, and the genus Within the scope of the novel device, it is combined with Chen Ming ^ [Simple description of the drawing] The first-picture complement--the preferred configuration of the fluid bed-type activated carbon desorption device. The first picture is the creation of this type - the fluid bed type activated carbon desorption bed of Jianshiguan _ body diagram [main symbol description] activated carbon adsorption tower (1) fluid bed activated carbon desorption bed (2) second activity Carbon transfer pump (21) Electrothermal heater (3) Catalytic oxidizer (31) First activated carbon transfer pump (1〇) Punching plate (2 0) Positive pressure windmill (3 0 ) 8