TWI379061B - - Google Patents

Download PDF

Info

Publication number
TWI379061B
TWI379061B TW100125074A TW100125074A TWI379061B TW I379061 B TWI379061 B TW I379061B TW 100125074 A TW100125074 A TW 100125074A TW 100125074 A TW100125074 A TW 100125074A TW I379061 B TWI379061 B TW I379061B
Authority
TW
Taiwan
Prior art keywords
air
clean room
purification
cylinder
porous
Prior art date
Application number
TW100125074A
Other languages
Chinese (zh)
Other versions
TW201205009A (en
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed filed Critical
Priority to TW100125074A priority Critical patent/TW201205009A/en
Publication of TW201205009A publication Critical patent/TW201205009A/en
Application granted granted Critical
Publication of TWI379061B publication Critical patent/TWI379061B/zh

Links

Description

1379061 ι〇ι年《Ί月y β修正替換— 六、發明說明: 【發明所屬之技術領域】 本發明係有關一種空氣淨化裝置,尤指一種於一筒體 内部分隔出複數個淨化室,且於各該淨化室填充有淨化 材,而於該筒體内部形成有連通該進氣口、各該淨化室及 該出氣口之氣流通道,俾以利用單一結構體將待淨化氣體 進行連續性淨化程序之設計者。1379061 ι〇ι年《Ί月 y β Revision Replacement—VI. Description of the Invention: [Technical Field] The present invention relates to an air purification device, and more particularly to a plurality of clean rooms separated inside a cylinder, and Each of the clean room is filled with a purification material, and an air flow passage connecting the air inlet, each of the clean room and the air outlet is formed inside the cylinder, and the gas to be purified is continuously purified by using a single structure. The designer of the program.

【先前技術】[Prior Art]

按,半導體晶圓製造廠及TFT-LCD面板或太陽能光電 製造業製程中,在濕蝕刻製程會使用到無機酸(硝酸、硫 酸、氫氟酸、鹽酸)及有機酸(如醋酸)等酸液,而在乾餘刻 製程或洗淨程序會使用到大量的氟化合物(如PFC : NF3、 SF6、CF4、C2F6 ),經淨化設備分解處理後衍生無機酸(硝酸、 氫氟酸);其中,有機酸及無機酸之比例配置不盡相同,主 要之蝕刻作用由無機酸進行,加入有機酸(如醋酸)主要是 使無機酸更穩定,提高蝕刻的良率,然而卻造成大量之毒 性氣體、臭氣、白煙、N〇2黃煙或厭惡性異味排放。 次按,懸浮微粒(Suspended particulate)泛指在氣流 中懸浮之固態或液態粒子,在提及一般空氣品質時多以此 為評估項目,在測量時則以高量採樣器作水平向過濾採氣 測定。而懸沣微粒因不同粒徑之顆粒進入人體呼吸系統之 能力差異極大,且一般醫學界認為10微米以下之顆粒方可 進入人體呼吸道,其中又以2. 5微米以下之顆粒對呼吸系 統之危害最為強烈。目前一般環保單位對於空氣懸浮微粒 -3 - 1379061 __ p丨年η月v} Ei修正替換頁 - jl—丨丨· |邏· — 之污染程度多改用「粒徑小於等於1 〇微米之懸浮微粒 (Particulate matters 10" m,簡稱 PM10)」,在公衛界則 夕採用「粒徑小於等於2.5微米之懸浮微粒(Particulate matters 2· 5 "m’簡稱PM2. 5)」以評估污染對健康之影響。 此2. 5微米以下之微粒因此又被稱為「可呼吸性懸浮粒子 (Respirable suspended particle)」。 然而’以傳統冷凝法及吸收法目前最常採用的淨化設 . 備(諸如以抽風與簡易滤網或一般吸附或水洗洗條處理), 並無法元全去除上述存在於空氣中之懸浮微粒及酸性氣體 (硝酸、硫酸、氫氟酸、鹽酸、氨、n〇2;尤其是氫氟酸、n〇2) 等難處理之分子污染物,而且該等懸浮粒子若為人體吸入 將引發身體健康之安危;同時該等酸性氣體於低濃度下即 會產生惡臭,並易於排放管道產生次微米微粒之白煙或/及 黃煙現象,極易影響廠房周圍生活環境而引發民眾抗議, 同時也影響到廠房周圍其他高科技廠高階製程之產品良 率。再者,尚有運用觸媒濾材來淨化處理空氣中含硫化合 ^ 物、硝酸及醋酸...等物質氣體之方法,該觸媒濾材淨化氣 體之優點為含硫化合物、硝酸及醋酸.·.等物質氣體之脫除 - 效率高、反應溫度低、能源消耗低、避免生成二次污染物 等,是一種環境友好的催化淨化技術。 - ' 【發明内容】 . 本發明之主要目的,係欲提供一種空氣淨化裝置,而 具有設備體積小之功效。 本發明之另一目的,則具有利用線上再生而提升淨化 效率之功效。 -4- 1379061 、<^年*1月 日酱正替換頁 為達上述功效,本發明之結構特徵,係於 分隔出複數個淨化室’且於各該淨化室填充有淨化材,並 於該筒體形成有進氣口與出氣口,而於該筒體内部形成有 連通該進氣口、各該淨化室及該出氣π之氣流通道;藉此, 待淨化氣體由該進氣口導入,進而利用填充於不同淨化室 :::材進订連續性之淨化,並由該出氣口將淨化後氣體 導出者。 -中’該筒體内部以-橫向設置之第—多孔板與頂天設 置之第-縱隔板分隔出第一淨化室,另以橫向設置之第二 夕孔板與立地叹置之第二縱隔板分隔出第二淨化室 該第一縱隔板與該第二縱隔板之間分隔出連通該第-淨化 室底側與該第二淨化室頂侧之通道室,並令該進氣口之形 2位置對胁該第—淨化室頂側,該出氣π之形成位置對 该第二:化室底側,進而於該筒體内部形成有連通該 π第該:一淨化室頂側、該第-淨化室底側、該通道 氣流=頂侧'該第二淨化室底側及該出氣口之 配填筒體為圓形°x,各該淨化室各自填充或級 -_真充有不心化屬性之多孔性淨化材。3,填充於 =化室之多孔性淨化材為活性碳、活性氧化紹、陶究或 後’填充於該第二淨化室之多孔性淨化材為 =、活性氧化紹、奈米碳管、多孔性樹月_石。質再= 體底二?=爭Γ各自設置有再生液_,並於該筒 體底U有再生液之排洩口。另者,進门 生液錢輯結㈣生液循環單元,各該再生液循環2 1379061 1〃1 年月 Θετ 各將一循環管之吸取端設置於該筒體底部,各該循環管之 排放端則與各該再生液喷灑器連結,且於各該循環管設置 有循環泵,並將再生液容器藉供給管連結至各該循環管之 低壓段。又一,各該淨化室之多孔性淨化材填充高度可彈 性應用,較佳為30〜60公分。 【實施方式】 首先,請參閱第一圖所示,本發明之實施例,係於一In the process of semiconductor wafer fabrication, TFT-LCD panel or solar photovoltaic manufacturing, acid solutions such as inorganic acids (nitric acid, sulfuric acid, hydrofluoric acid, hydrochloric acid) and organic acids (such as acetic acid) are used in the wet etching process. In the dry process or the cleaning process, a large amount of fluorine compounds (such as PFC: NF3, SF6, CF4, C2F6) are used, and the inorganic acid (nitric acid, hydrofluoric acid) is decomposed by the purification equipment; The ratio of organic acid to inorganic acid is not the same. The main etching effect is carried out by inorganic acid. The addition of organic acid (such as acetic acid) is mainly to make the inorganic acid more stable and improve the etching yield. However, it causes a lot of toxic gases. Odor, white smoke, N〇2 yellow smoke or aversive odor emissions. Suspended particulate refers to solid or liquid particles suspended in a gas stream. It is used as an evaluation item when referring to general air quality, and horizontally filtered by a high-volume sampler during measurement. Determination. However, the ability of suspended particles to enter the human respiratory system varies greatly, and the general medical community believes that particles below 10 microns can enter the human respiratory tract, and the damage of the respiratory system caused by particles below 2.5 microns. The strongest. At present, the general environmental protection unit for the airborne particles -3379061 __ p丨年η月v} Ei correction replacement page - jl - 丨丨 · | LOG · - the degree of pollution is changed to use "particle size less than or equal to 1 〇 micron suspension Particles (Particulate matters 10 " m, referred to as PM10), in the public health sector, the use of "particle size of 2.5 microns or less suspended particles (Particulate matters 2 · 5 " m 'referred to PM 2. 5)" to assess pollution pairs The impact of health. The particles below 2.5 microns are therefore also referred to as "Respirable suspended particles". However, the conventional purification and absorption methods are currently the most commonly used purification equipment (such as treatment with suction and simple filters or general adsorption or washing), and it is impossible to remove the above-mentioned suspended particles present in the air. Acidic gases (nitric acid, sulfuric acid, hydrofluoric acid, hydrochloric acid, ammonia, n〇2; especially hydrofluoric acid, n〇2) and other intractable molecular pollutants, and these suspended particles will cause health if inhaled by the human body. At the same time, these acid gases will produce malodor at low concentrations, and will easily discharge white smoke or yellow smoke from sub-micron particles in the pipeline, which will easily affect the living environment around the plant and cause public protests. Product yield of high-end processes in other high-tech plants around the plant. Furthermore, there is a method of purifying a gas containing a sulfurized compound, a nitric acid, an acetic acid, and the like in a treated air filter medium, and the catalytic filter material has the advantages of purifying a sulfur compound, nitric acid, and acetic acid. The removal of substances such as gases - high efficiency, low reaction temperature, low energy consumption, avoiding the formation of secondary pollutants, etc., is an environmentally friendly catalytic purification technology. - 'Contents of the Invention>> The main object of the present invention is to provide an air purifying device which has the effect of being small in size. Another object of the present invention is to enhance the efficiency of purification by utilizing on-line regeneration. -4- 1379061, <^年*1月日酱正换页 In order to achieve the above-mentioned effects, the structural feature of the present invention is that a plurality of clean rooms are separated and each of the clean rooms is filled with a purification material, and The cylinder body is formed with an air inlet and an air outlet, and an air flow passage connecting the air inlet, each of the clean room and the air outlet π is formed inside the cylinder; thereby, the gas to be purified is introduced from the air inlet Further, the purification is completed by filling in different clean rooms::: material, and the purified gas is exported by the gas outlet. - in the middle of the cylinder - the horizontally disposed first - perforated plate is separated from the first - vertical partition of the top of the first clearing chamber, and the second laterally disposed second outer plate and the second in the ground The vertical partition partitions the second clean room, and the first vertical partition and the second vertical partition separate the passage between the bottom side of the first clean room and the top side of the second clean room, and the The shape of the gas port 2 is opposite to the top side of the first purification chamber, and the position of the gas outlet π is formed on the bottom side of the second chamber: and the inside of the cylinder is formed to communicate with the π: the clean room top The side, the bottom side of the first purifying chamber, the air flow of the channel = the top side 'the bottom side of the second clean room and the filling cylinder of the air outlet are circular ° x, and each of the purifying chambers is filled or graded - A porous purification material filled with unintentional properties. 3. The porous purification material filled in the chemical conversion chamber is activated carbon, active oxidized, oxidized or post-filled in the second purification chamber, and the porous purification material is =, active oxidized, carbon nanotube, porous Sex tree month _ stone. Quality = body bottom two? = disputes are each set with regenerant _, and at the bottom of the cylinder U there is a discharge of regenerant. In addition, the door is filled with liquid money (4) raw liquid circulation unit, each of the regeneration liquid circulation 2 1379061 1〃1 year Θ ετ each set the suction end of a circulation tube at the bottom of the cylinder, the discharge end of each circulation tube Then, the regenerating liquid sprayer is connected to each of the circulation pipes, and a circulation pump is disposed in each of the circulation pipes, and the regeneration liquid container is connected to the low pressure section of each of the circulation pipes by a supply pipe. Further, the porous purification material of each of the clean rooms is filled with a highly elastic application, preferably 30 to 60 cm. [Embodiment] First, referring to the first figure, an embodiment of the present invention is

橫置之圓形筒體30内部以橫向設置之第一多孔板37a與頂 天設置之第一縱隔板34a分隔出第一淨化室31,另以橫向 設置之第二多孔板37b與立地設置之第二縱隔板_分隔 出第二淨化室32,且於㈣淨化室3卜32填充有淨化材 40a、_,而於該第-縱隔板34a與該第二縱隔板灿之 間分隔出連通該第…淨化室31底側與該第二淨化室%頂 側之通道室33,並令-進氣σ 35之形成位置對應於該第一 淨化室31頂側,另令—出氣σ3β之形成位㈣應於該第 二淨化室32底側,進而於該筒體3Q内部形成有連通該進The horizontally disposed cylindrical body 30 is internally separated from the first vertical plate 37a and the first vertical partition 34a disposed above the first clean room 31, and the second porous plate 37b is disposed laterally. The second vertical partition plate _ is disposed to separate the second clean room 32, and the (four) clean room 3b is filled with the purification material 40a, _, and the second vertical partition 34a and the second vertical partition Separating the passage chamber 33 connecting the bottom side of the first clean room 31 and the top side of the second clean room 31, and forming a position of the intake air σ 35 corresponding to the top side of the first clean room 31, - the formation position (4) of the outgassing σ3β is on the bottom side of the second clean room 32, and further, the inside of the cylindrical body 3Q is formed to communicate with the inlet

氣口 35、該第一淨化室31頂側、該第—淨化室31底側、 "亥至33該第—淨化室32頂側、該第二淨化室32底 側及該出氣口36之氣流通道^此,待淨化諸由該進氣 口 35導人’進而利用填充於不同淨化室心犯之淨化材 _、傷進行連續性之淨化,並由該出氣^將淨化後氣 體導出者。 此外各》亥淨化室(第—淨化室31與該第二淨化室犯) 各自填充不同淨化屬性之多孔性淨化材術、傷,或是將 不同淨化屬性之多孔性淨化材杨、40b級配(分級配置)填 1379061 替換頁 充,俾以淨化不同之汙染物,而其填充高度為_< 更佳為30〜60公分;其中,填充於該第一淨化室μ 夕 孔性淨化材40a可為活性碳、活性氧化鋁、陶I或沸^多 而可用以淨化待淨化氣體中之懸浮微粒;又填充於1第 二淨化室32之多孔性淨化材4〇b可為經改質> / 又貞之活性碳、活 性氧化鋁、奈米碳管、多孔性樹脂或沸石,而可用以淨化 待淨化氣體中之酸性氣體。The air port 35, the top side of the first clean room 31, the bottom side of the first clean room 31, the top side of the first clean room 32, the bottom side of the second clean room 32, and the air flow of the air outlet 36 The channel is to be cleaned and guided by the air inlet 35, and then the purification material filled with the different clean room is used to clean the continuity, and the purified gas is led out by the outlet gas. In addition, each of the "Hai clean room (the first clean room 31 and the second clean room) are filled with different purification properties of the porous purification material, injury, or different purification properties of the porous purification material Yang, 40b grade (graded configuration) fills 1370906 to replace the page charge, to purify different contaminants, and the filling height is _< more preferably 30 to 60 cm; wherein, the first clean room μ is filled with the purification material 40a It can be used for purifying the suspended particles in the gas to be purified for activated carbon, activated alumina, ceramic I or boiling; and the porous purification material 4〇b filled in the second clean room 32 can be modified &gt And / activated carbon, activated alumina, carbon nanotubes, porous resin or zeolite, and can be used to purify the acid gas in the gas to be purified.

再者’進-步於該第-淨化室31設置有再生液喷灌器 5〇a,而對填充於該第—淨化室31之多孔性淨化材術喷 灑水(熱水更佳),俾令該多孔性淨化材4〇a洗滌再生,·另, 進步於該第二淨化室32設置有再生液喷灑器5〇b,而對 填充於該第二淨化室32之多孔性淨化材她噴壤水或驗溶 液(如:KOH、NaOH、KMn〇4或CnS〇4或其任一組合),俾令該 多孔性淨化材40b改質再生。然而,由於該筒體3()為圓形 且底部設置有排洩口 123,該筒體30底部乃可供所噴灑之 再生液蓄積且方便由排洩口 123排洩。Further, the step-purifying chamber 31 is provided with a regenerating liquid sprinkler 5〇a, and the porous purifying material filled in the first purifying chamber 31 is sprayed with water (better of hot water), 俾The porous purification material 4〇a is washed and regenerated, and further, the second purification chamber 32 is provided with a regenerant liquid sprayer 5〇b, and the porous purification material filled in the second clean room 32 is used. Spraying the water or the test solution (for example, KOH, NaOH, KMn〇4 or CnS〇4 or any combination thereof), the porous purification material 40b is modified and regenerated. However, since the barrel 3() is circular and the bottom is provided with a drain port 123, the bottom of the barrel 30 is allowed to accumulate the sprayed regeneration liquid and is easily drained by the drain port 123.

另者,進一步相對各該再生液噴灑器5〇a、5〇b連結有 再生液循環單元6〇a、60b,各該再生液循環單元6〇a、6〇b 各將一循環管61a、61b之吸取端設置於該筒體3〇底部, 各該循環管61a、61b之排放端則與各該再生液喷灑器5〇a、 5〇b連結,且於各該循環管61a、61b設置有循環泵62a、 62b ’並將再生液容器63a、63b藉供給管64a、64b連結至 各該循環管61a、61b之低壓段。 基於如是之構成,本發明係於一筒體3〇内部分隔出複 數個淨化室(第一淨化室31與該第二淨化室32),且於各該 1379061 淨化至填充有淨化材4〇a、伽,並於該筒體3〇形成有進氣 1 口 35與出氣口 36’而於該筒體洲内部形成有連通該進氣 二口 35二各該淨化室(第一淨化室31與該第二淨化室犯)及 δ亥出就D 36之氣流通道;藉此,待淨化氣體由該進氣口 35 導入it而利用填充於不同淨化室之淨化材4〇a、働進行 連續f生之淨化,並由$出氣σ 將淨化後氣體導出。Further, the regenerant circulating units 6a and 60b are further connected to the regenerant liquid sprayers 5a and 5b, and each of the regenerant circulating units 6a and 6bb has a circulation pipe 61a. The suction end of 61b is disposed at the bottom of the cylinder 3, and the discharge ends of the circulation pipes 61a, 61b are connected with the regenerant liquid sprayers 5a, 5B, and in each of the circulation pipes 61a, 61b The circulation pumps 62a, 62b' are provided and the regeneration liquid containers 63a, 63b are connected to the low pressure sections of the respective circulation pipes 61a, 61b by the supply pipes 64a, 64b. Based on the configuration, the present invention separates a plurality of clean rooms (the first clean room 31 and the second clean room 32) inside a cylinder 3, and is purified to be filled with the purification material 4〇a in each of the 1370906 And the galax, and the inlet 3 and the air outlet 36' are formed in the cylinder 3, and the clean room (the first clean room 31 and the second air inlet 35) are connected to the inside of the cylinder body. The second clean room is arbitrarily and the air flow passage of D 36 is taken out; thereby, the gas to be purified is introduced into the inlet port 35, and the purification material 4〇a and 填充 filled in the different clean rooms are continuously f Purification of the raw, and the purified gas is exported by the gas σ.

是故,本發明利用單一結構體將待淨化氣體連續進行 連貝性之淨化程序(習知方式則必須—將兩結構冑串連方可 連續進仃兩次之淨化程序);是以,具有設備體積小之功 效’又’忒再生液噴灑器5〇a、5〇b與該再生液循環單元6〇a、 6〇b之設置,遂可令該多孔性淨化材4〇a、4此於線上直接 再生(不必停機取出再生),則具有利用線上再生而提升淨 化效率之功效;,然而,通過各該淨化室3卜32之氣流流向 係與再生液之喷灑方向相同(皆向下),而得以較低之壓損 進行線上再生(喷麗再生液)之過程。 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。 惟,上述所揭露之圖式、說明,僅為本發明之較佳實 施例,大凡熟悉此項技藝人士,依本案精神範疇所作之修 .飾或等效變化’仍應包括在本案申請專利範圍内。 〆 1379061 _ 年1月Θ日修正替換頁 【圖式簡單說明】 第一圖係本發明實施例之結構說明圖。 【主要元件符號說明】 30筒體 31第一淨化室 32第二淨化室 33通道室 _ 34a第一縱隔板Therefore, the present invention utilizes a single structure to continuously perform the purification process of the gas to be purified (the conventional method must be the same as the purification process in which the two structures are connected in series and can be continuously fed twice); The function of the small volume of the device is ''', the regenerating liquid sprayer 5〇a, 5〇b and the regenerant circulation unit 6〇a, 6〇b are arranged, so that the porous purification material 4〇a, 4 Direct regeneration on the line (without stopping to take out regeneration) has the effect of improving the purification efficiency by using online regeneration; however, the flow direction of the airflow through each of the clean rooms 3 is the same as that of the regeneration liquid (both down) ), and the process of on-line regeneration (spray regenerant) can be carried out with a lower pressure loss. 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 be granted by the bureau. German sense. However, the drawings and descriptions disclosed above are only preferred embodiments of the present invention. Those skilled in the art who are familiar with the art, the modifications or equivalent changes made in accordance with the spirit of the present case shall still be included in the scope of patent application in this case. Inside. 〆 1379061 _ January 1st revised replacement page [Simplified description of the drawings] The first figure is a structural explanatory diagram of an embodiment of the present invention. [Main component symbol description] 30 cylinder 31 first clean room 32 second clean room 33 passage room _ 34a first vertical partition

34b第二縱隔板 35進氣口 36出氣口 37a第一多孔板 37b第二多孔板 123排洩口 40a、40b多孔性淨化材 50a、50b再生液喷灑器 60a、60b再生液循環單元 61a、61b循環管 62a、62b循環泵 63a、63b再生液容器 64a、64b供給管 9·34b second vertical partition 35 air inlet 36 air outlet 37a first porous plate 37b second porous plate 123 drain port 40a, 40b porous purification material 50a, 50b regeneration liquid sprayer 60a, 60b regeneration liquid circulation unit 61a, 61b circulation pipes 62a, 62b circulation pumps 63a, 63b regeneration liquid containers 64a, 64b supply pipes 9·

Claims (1)

U/9061 七 |l0丨年月>35修正替換頁 申請專利範圍: 〜~-~— 1 . 一種空氣淨化裝置’係於一筒體内部分隔出複數 =化室’且於各歸化轉充有淨㈣並於該筒體形 進氣口與出氣口,而於該筒體内部形成有連通該進氣 二2淨化室及該出氣口之氣流通道;其令’該筒體内 :场向設置之第一多孔板與頂天設置之第_縱隔板分隔 第一淨化室’另以橫向設置之第二多孔板與立地設置之 第-㈣板分隔出第二淨化室’而於該第—縱隔板與該第 二縱隔板之間分隔出連通該第一淨化室底側與該第二淨化 ,頂,之通道室’並令該進氣口之形成位置對應於該第一 〆至頂側5亥出氣口之形成位置對應於該第二淨化室底 ,,進而於該筒體内部形成有連通該進氣口、該第一淨化 至頂側、该第一淨化室底侧、該通道室、該第二淨化室頂 5第/爭化至底側及該出氣口之氣流通道;藉此,待 ^氣體由β亥進氣口導入,進而利用填充於不同淨化室之 淨化材進行連續性之淨化,並由該出氣口將淨化後氣體導 出者。 2 .如申請專利範圍第丄項所述之空氣淨化裝置,盆 中,該筒體為圓形。 3如申請專利範圍第2項所述之空氣淨化裝置,其 中各。亥淨化室各自填充或級配填充有不同淨化屬性之多 孔性淨化材。 -10· 丄J/yuu丄 1«^年〇月修替換頁I 4 .如’請專利範圍第3項所述之空氣淨^^"^一一1 中,填充於該第—淨化室 =置= =r:—一淨=: 石性破、活性氧化銘,奈米破管、多孔性樹 5如_明專利範圍第4項所述之空氣淨化裝置,其U/9061 七|l0丨年月>35 correction replacement page application patent scope: ~~-~-1. An air purification device 'separates a complex number inside the cylinder and turns it into a chemical chamber' Filled with a net (four) and in the cylinder-shaped air inlet and outlet, and an air flow passage connecting the air inlet and the second clean room and the air outlet is formed inside the cylinder; The first porous plate is disposed to be separated from the first cleaning chamber by the first vertical partition, and the second porous plate disposed laterally is separated from the first (four) plate disposed in the vertical to separate the second clean room The first longitudinal partition and the second vertical partition are separated from the bottom side of the first clean room and the second clean, top, and the passage chamber', and the position of the air inlet is corresponding to the first The formation position of the first to the fifth side air outlet corresponds to the bottom of the second clean room, and further, the inner side of the cylinder is formed to communicate with the air inlet, the first purification to the top side, and the first clean room bottom. a side, the passage chamber, the second clean room top 5 / advancing to the bottom side and the air flow passage of the air outlet; This, to be introduced from the gas port ^ β Hai intake, and further with a filler material different from the purge chamber to the purification of the continuity of the purification, the rear by the purge gas outlet out of those guide. 2. The air purifying device of claim 2, wherein the cylinder is circular in the basin. (3) The air purifying device of claim 2, wherein each of the air purifying devices. The purifying chambers are each filled or gradated with a multi-porous purification material filled with different purification properties. -10· 丄J/yuu丄1«^年〇月修修页 I 4 . Fill in the first clean room in the air net ^^"^一一1 described in the third paragraph of the patent scope = set = = r: - a net =: stone breaking, active oxidation, nano tube breaking, porous tree 5, such as the air purifying device described in Item 4 of the patent scope, 於各4淨化室各自設置有再生液喷M.器,並於 该㈣底部設置有再生液之排茂口。 6如申味專利範圍第5項所述之空氣淨化裝置,其 中’進f步相對各該再生液喷^連結有再生液循環單 各°亥再生液循環單元各將一循環管之吸取端設置於該 ^體底部’各該循環管之排放端則與各該再生液喷麗器連 結,且於各該循環管設置有循環泵,並將再生液容器藉供 給管連結至各該循環管之低壓段。 7·如申請專利範圍第6項所述之空氣淨化裝置,其 中’各該淨化室之多孔性淨化材填充高度為30〜60公分。 -11 -Each of the four clean rooms is provided with a regenerating liquid spray M., and a bottom portion of the regenerated liquid is disposed at the bottom of the (four). [6] The air purifying device according to claim 5, wherein the step of the recirculating liquid is connected to each of the regenerating liquids, and the recirculating unit of each of the regenerating liquid circulating units is provided with a suction end of a circulating tube. The discharge end of each of the circulation pipes is connected to each of the regeneration liquid sprayers, and a circulation pump is disposed in each of the circulation pipes, and the regeneration liquid container is connected to each of the circulation pipes by a supply pipe. Low pressure section. 7. The air purifying device according to claim 6, wherein the porous purification material of each of the cleaning chambers has a filling height of 30 to 60 cm. -11 -
TW100125074A 2011-05-31 2011-07-15 Air purification device TW201205009A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
TW100125074A TW201205009A (en) 2011-05-31 2011-07-15 Air purification device

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
TW100209774 2011-05-31
TW100125074A TW201205009A (en) 2011-05-31 2011-07-15 Air purification device

Publications (2)

Publication Number Publication Date
TW201205009A TW201205009A (en) 2012-02-01
TWI379061B true TWI379061B (en) 2012-12-11

Family

ID=46761478

Family Applications (2)

Application Number Title Priority Date Filing Date
TW101115077A TW201247305A (en) 2011-05-31 2011-07-15 Air purification device
TW100125074A TW201205009A (en) 2011-05-31 2011-07-15 Air purification device

Family Applications Before (1)

Application Number Title Priority Date Filing Date
TW101115077A TW201247305A (en) 2011-05-31 2011-07-15 Air purification device

Country Status (1)

Country Link
TW (2) TW201247305A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107477700A (en) * 2017-07-31 2017-12-15 中山市思诺得环保科技有限公司 A kind of air purifier with the combination of a variety of purification units

Also Published As

Publication number Publication date
TW201205009A (en) 2012-02-01
TW201247305A (en) 2012-12-01

Similar Documents

Publication Publication Date Title
CN205392101U (en) Chemical engineering exhaust gas purifies absorbing device
CN209490640U (en) A kind of papermaking exhaust treating purifier
CN208660820U (en) A kind of lacquer spraying technique photocatalysis deodorizing device
CN204799049U (en) Wet process micron order particulate matter entrapment air purification device
CN104624006B (en) A kind of multistage filtering formula waste gas purification apparatus
CN205402941U (en) Indoor device for air purification
CN104259037B (en) Paint mist collecting and purifying device of paint spray booth
CN105688624A (en) Waste gas purifier
CN207024929U (en) A kind of NACF purifies organic tail gas purifier
CN108261917A (en) A kind of industry hot waste gas processing unit and treatment process
CN107774063A (en) Renewable circulating liquid formula air cleaning unit and purification method
CN104645752B (en) A kind of negative pressure exhausting water-washing type air purification equipment
TWI379061B (en)
CN105879619A (en) VOCs (volatile organic compounds) tail gas treatment device and method
CN211159179U (en) Organic waste gas treatment device
CN207307586U (en) A kind of high-concentration waste air purifying apparatus
TW201036689A (en) An apparatus for purifying suspended particles and inorganic gases in gas
CN105879539B (en) A kind of high-pressure electrostatic plasma smoke treated equipment
CN208320315U (en) A kind of oil flue waste gas processing system
CN203837092U (en) Air purifying device for air-gas fusion and separation
CN203540286U (en) Cleaning device for volatile gases
CN104815505A (en) Cyclic waste gas recovery purification device
CN102671508A (en) Air cleaning equipment
CN204699552U (en) A kind of circulating waste gas recovery purifier
CN210845812U (en) Acid mist absorption device