TWM380164U - Liquid filter system - Google Patents

Liquid filter system Download PDF

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Publication number
TWM380164U
TWM380164U TW98215994U TW98215994U TWM380164U TW M380164 U TWM380164 U TW M380164U TW 98215994 U TW98215994 U TW 98215994U TW 98215994 U TW98215994 U TW 98215994U TW M380164 U TWM380164 U TW M380164U
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TW
Taiwan
Prior art keywords
liquid
aeration
filter
filtration system
main
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TW98215994U
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Chinese (zh)
Inventor
Ya-Fu Huang
ji-zhong Xiong
Shi-Yang Chen
Lei-Di Huang
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Ef Materials Ind Inc
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Priority to TW98215994U priority Critical patent/TWM380164U/en
Publication of TWM380164U publication Critical patent/TWM380164U/en

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五、新型說明: 【新型所屬之技術領域】 本新型涉及-種過齡統,尤其是_種液體過渡系統。 【先前技術】 隨時代魏’產業結構的變化,不論民生或工業製程皆 需要大量的水㈣、,水靴設備的轉性無定財是決定水 回收可仃與否之重點之一,然而,傳統的廢水處理程序並無法 有效地處理特性曰新月異的廢水,而且使得處理成本曰益增 加’處理水質亦不穩定。 近年來傳統活性污泥結合薄膜單元發展出薄膜生物反 應槽(Membranebioreac^MBR),利用薄膜取代沉澱池,達 到固液分離的效果’改善傳統活性污泥法技術之綱,具有物 理消毒與保持高生物質量之優點。MBr以縮小廢水處理設施 的佔地面積及獲得更佳的處理水質。又因薄膜製造技術的改良 等因素’使其設置及操作成本有機會降低,增加MBR的市場 競爭力。 由於MBR處理程序能對各種廢水有相當程度的去除 效率,且出流水可達放流水標準,已經廣泛應用於都市污水、 家庭廢水、工廠廢水、甚至垃圾場滲出水的處理。主要發展 MBR系統的國家以日本及法國最為成熟。 有鑑於薄膜生物反應槽(Membrane bioreactor, MBR) 具有成為水處理主流技術的趨勢,因此仍有必要開發操作穩 定、維護簡便的MBR,提供液體過濾使用。 【新型内容】 雲於上述之背景中,為了符合產業上某些利益之需求, 本新型提供一種液體過濾系統可用以解決上述傳統之液體過 濾系統未能達成之標的。 本新型之一目的係提供一種液體過濾系統,其包含一肋 狀曝氣裝置、複數個過濾板與一主收集管。 上述之曝氣裝置包含一主曝氣管與複數個支曝氣管,其 中支曝氣管分職主曝氣管之周綱形成雜4氣體經 由主曝氣管輸送至支曝氣管後,即會經由每—個支曝氣管之複 數個氣孔輸出形成複數個氣泡。 上述之複數個過濾板係設置於肋狀曝氣裴置上,其中每 -個過滤㈣藉由至少—過_航覆,並且每—個過遽板皆 連結一支收集管。 另外,每-個支收集管分別連結至主收集管。當該液體 過渡系統放㈣巾時,域娜卩可進储空錄,使液 體透過每-過濾薄膜輯後經由每一個板及其支收集管 匯=至上述之主收集管嘴後,經由主收集管輸出之液體即為 過滤後之乾淨滤液。 【實施方式】 本新型在此聰討财肖為— 徹底:解本新型,將在下列的謝提_= =殊,行並未限定__系統之技藝者 述於細科騎壯敝錢步職未描 會如&、 4 _必要之關。本新型的較佳 歹|詳細描述如下,然而除了這些詳細描述之外,本新型 射以廣泛地施行在其他的實施例中,且本新型的範圍不受限 定,其以之後的專利範圍為準。 參考第-圖與第二圖所示,其係為一液體顧系統卿 之結構示意圖。液體過濾系統100包含-肋狀曝氣裝置110、 複數個過攄板120與一主收集管丨3〇。 上述之曝氣裝置11〇包含一主曝氣管112與複數個支曝 氣吕114’其中支曝氣管114分別設置於主曝氣管112之周側, 並且每-個支曝氣管114係垂直於主曝氣管ιΐ2設置以形成肋 狀。當氣體經由主曝氣管112輸送至支曝氣管m後,即會經 由每-個支曝氣官丨14之複數個氣孔116輸出形成複數個氣 泡0 上述之複數個過濾板120係設置於肋狀曝氣裝置ι10 上,其中每一個過濾板120係藉由至少一過濾薄膜包覆,並且 每一個過濾板120皆連結一支收集管124。根據本新型之一較 佳實施例,過濾板係為一中空結構,其兩側表面各具有複數個 通孔,每一個過濾板120係藉由二過濾薄膜包覆於過濾板120 M380164 之相對兩面通孔之上’並且過滤板12〇之支收集管i24係連結 於過遽板120之一側邊。 另外,每一個支收集管124分別連結至主收集管13〇。 當該液體過濾系統1〇〇放置於液體中時,主收集管13〇即可進 行真空抽取,使液體透過每一過濾薄膜過遽後經由每一個過遽 板120及其支收集管124匯集至上述之主收集管13〇。隨後, 經由主收集管130輸出之液體即為過遽後之乾淨遽液。 再者’因為過濾板120係設置於肋狀曝氣裝置11〇上方 故上述每-氣孔116輸出之氣泡會在液體中向上飄浮,如第二 圖所示,藉此可將猶時附著於每—過_膜上之雜質或遽餅 移除。而上述之複_過濾板12〇彼此相互平行,並且每一個 過滤板120鼓於鱗氣管112,使氣泡可沿著顧薄膜清除 雜質或濾餅。 如第三A圖與第三b圖所示’上述之液體過滤系統⑽ 更包含二個具有複數溝槽之絲對位元件14G。此二對位元件 140設置於過濾板1:20之相對兩侧邊,並且每一個過遽板⑼ 之相對兩側邊係分別定位於一對位元件14〇之一溝槽142,其 中上述之二對位元件140係平行於主曝氣管112。 請再參考第-圖、第三A圖與第四圖所示,上述之液 ^§遽系、统100更包含一邊框15〇與二個可旋式條狀角鐵 160 ’其巾此一邊框⑼j裒燒架構於過滤板w顯,並且對 位兀件M0之兩端係固定於邊框ls〇之上。上述之可旋式條狀 6 角鐵⑽包含-_部162與—旋轉箱,其恤釋 係固定於邊_上,使旋轉部16何旋轉扣壓上述之複數個 過遽板12G ’避免當液體過觀統丨⑽置於㈣中時,過減板 120會因㈣浮力錢Μ軸,導致麟㈣過齡統 100。第四_為當可旋式條狀角職制啟時之結構示意 圖。於本新型之-較佳範例中,上述每一條狀對位元件140的 兩端係固定於邊框之上。 當液體過濾系統100運作一段時間後,附著於過滤薄膜 上之雜質亦會逐精加’例如:形成較厚之_,使得氣泡無 法完整地清除雜質或遽餅。因此,上述之主收集管別可將滤 液逆向往每-個錢鮮124輸送,液自過敵120内部 向外穿透過濾細,藉此移除畴於過㈣膜上之雜質或滤 餅。再者,為了加強液體過齡統勘之過遽功效,更可藉由 -柱狀抽換元件170穿過每—個過濾、板12G之抽換孔126以進 行過遽板120之統-抽換,可免除逐一抽換過滤板12〇之繁瑣 耗時,如第五圖所示。 顯然地,依照上面實施例中的描述,本新型可能有許多 的修正與差異。因此需要在其附加的權利要求項之範圍内力口以 理解’除了上述詳細的描述外,本新型還可以廣泛地在其他的 實施例中施行。上述僅為本新型之較佳實施例而已,並非用以 限定本新型之申請專利範圍;凡其它未脫離本新型所揭示之精 神下所完成的等效改變或修飾,均應包含在下述申請專利範圍 M380164 内。 f圖式簡單說明】 第一圖係為一液體過遽系統之結構示意圖; 第二圖係為一肋狀曝氣裝置之結構示意圖; 、為二對位元件之結構示意圖 條狀麵之結構示意圖,·以及V. New description: [New technology field] The new type involves a kind of overage system, especially the liquid transition system. [Prior Art] Any change in the industrial structure of Wei's at any time, regardless of whether the people's livelihood or industrial processes require a large amount of water (4), the turnover of water-skid equipment is one of the key points to determine whether water recycling is feasible or not. The traditional wastewater treatment process is not able to effectively treat the wastewater with the characteristics of the new moon, and the treatment cost is increased. The treatment water quality is also unstable. In recent years, the traditional activated sludge-bonded membrane unit has developed a membrane bioreactor (Membranebioreac^MBR), which replaces the sedimentation tank with a membrane to achieve the effect of solid-liquid separation. It improves the traditional activated sludge process technology and has physical disinfection and high retention. The advantages of biological quality. MBr is designed to reduce the footprint of wastewater treatment facilities and achieve better water quality. In addition, factors such as improvements in thin film manufacturing technology have reduced opportunities for installation and operation costs, and increased MBR's market competitiveness. Because the MBR process can have a considerable degree of removal efficiency for various wastewaters, and the outflow water can reach the discharge water standard, it has been widely used in the treatment of urban sewage, domestic wastewater, factory wastewater, and even landfill seepage water. The countries that mainly develop the MBR system are the most mature in Japan and France. In view of the trend of Membrane bioreactor (MBR) as a mainstream technology for water treatment, it is still necessary to develop an MBR that is stable in operation and easy to maintain, and provides liquid filtration. [New content] In the above background, in order to meet the needs of certain industrial interests, the present invention provides a liquid filtration system that can be used to solve the above-mentioned problems of the conventional liquid filtration system. One object of the present invention is to provide a liquid filtration system comprising a ribbed aeration device, a plurality of filter plates and a primary collection tube. The aeration device comprises a main aeration pipe and a plurality of aeration pipes, wherein the auxiliary aeration pipe is divided into a main aeration pipe to form a mixed gas, which is transported to the branch aeration pipe through the main aeration pipe. That is, a plurality of bubbles are formed through a plurality of vents of each of the aeration tubes. The above plurality of filter plates are disposed on the rib-shaped aeration device, wherein each of the filters (four) is connected by at least one-passing, and each of the filter plates is connected to a collecting pipe. In addition, each of the collection tubes is connected to the main collection tube. When the liquid transition system puts the (four) towel, the domain can enter the storage, so that the liquid passes through each filter film and then passes through each plate and its collecting pipe to the main collecting nozzle, and then through the main The liquid output from the collection tube is the clean filtered filtrate. [Embodiment] This new type of confession is here - thoroughly: to solve this new type, will be in the following Xie _ = = special, the line is not limited __ system of the art is described in the fine family riding strong money step Jobs are not described as &, 4 _ necessary. The preferred embodiment of the present invention is described in detail below, but in addition to the detailed description, the present invention is widely practiced in other embodiments, and the scope of the present invention is not limited, which is subject to the scope of the following patents. . Referring to the first and second figures, it is a schematic diagram of the structure of a liquid system. The liquid filtration system 100 includes a ribbed aeration device 110, a plurality of dampers 120, and a main collection tube 丨3〇. The aeration device 11A includes a main aeration pipe 112 and a plurality of branch aerations 114', wherein the branch aeration pipes 114 are respectively disposed on the circumferential side of the main aeration pipe 112, and each of the aeration pipes 114 is provided. It is disposed perpendicular to the main aeration tube ι 2 to form a rib shape. After the gas is sent to the branch aeration pipe m via the main aeration pipe 112, a plurality of bubbles 104 are output through the plurality of holes 116 of each of the aeration bureaus 14. The plurality of filter plates 120 are disposed on the plurality of filter plates 120. On the rib aeration device ι10, each of the filter plates 120 is covered by at least one filter film, and each of the filter plates 120 is coupled to a collection tube 124. According to a preferred embodiment of the present invention, the filter plate is a hollow structure, and each of the two sides has a plurality of through holes, and each of the filter plates 120 is coated on the opposite sides of the filter plate 120 M380164 by two filter films. Above the through hole 'and the collecting plate i24 of the filter plate 12 is coupled to one side of the dam plate 120. In addition, each of the branch collection tubes 124 is coupled to the main collection tube 13A, respectively. When the liquid filtration system 1 is placed in a liquid, the main collection tube 13 can be vacuum-extracted, and the liquid is passed through each filter film and then collected through each of the filter plates 120 and its collection tubes 124. The main collection tube 13 described above. Subsequently, the liquid output through the main collection tube 130 is a clean sputum after the sputum. Furthermore, since the filter plate 120 is disposed above the rib-shaped aeration device 11 , the air bubbles output from the above-mentioned air holes 116 float upward in the liquid, as shown in the second figure, whereby the time can be attached to each - Removal of impurities or cake on the film. The above-mentioned plurality of filter plates 12 are parallel to each other, and each of the filter plates 120 is bulged in the gas pipe 112 so that the bubbles can remove impurities or filter cake along the film. As shown in Figures 3A and 3b, the liquid filtration system (10) described above further comprises two wire alignment elements 14G having a plurality of grooves. The two alignment elements 140 are disposed on opposite sides of the filter plate 1:20, and the opposite side edges of each of the transition plates (9) are respectively positioned on a groove 142 of the pair of bit elements 14 ,, wherein the above The second alignment element 140 is parallel to the main aeration tube 112. Please refer to the first figure, the third figure A and the fourth figure. The above liquid system 100 includes a frame 15〇 and two rotatable strip angle irons 160' The frame (9) is not shown in the filter plate, and both ends of the alignment member M0 are fixed on the frame ls〇. The above-mentioned rotatable strip-shaped 6-angle iron (10) comprises a - portion 162 and a rotating box, and the shirt release system is fixed on the side _, so that the rotating portion 16 rotates to press the plurality of the damper plates 12G to avoid liquid When the Guanxun (10) is placed in (4), the over-reduction plate 120 will cause the (four) over-age 100 due to the (iv) buoyancy. The fourth _ is a schematic diagram of the structure when the rotatable strip corner is started. In a preferred embodiment of the present invention, the ends of each of the strip-shaped alignment elements 140 are secured to the bezel. When the liquid filtration system 100 is operated for a period of time, the impurities adhering to the filtration membrane are also fined, e.g., formed thicker, so that the bubbles do not completely remove the impurities or the cake. Therefore, the main collection tube described above can transport the filtrate backwards to each of the fresh 124, and the liquid penetrates the filter finely from the inside of the enemy 120 to remove impurities or filter cakes on the membrane. Furthermore, in order to enhance the effect of the over-age of the liquid over-age, it is also possible to pass through the perforation plate 126 of each of the filters and plates 12G through the column-shaped displacement element 170 to perform the extraction of the raft 120. Change, can eliminate the tedious and time-consuming replacement of the filter plate 12 one by one, as shown in the fifth figure. Obviously, the present invention may have many modifications and differences as described in the above embodiments. Therefore, it is to be understood that within the scope of the appended claims, the invention may be practiced in other embodiments. The above are only the preferred embodiments of the present invention, and are not intended to limit the scope of the present invention; any equivalent changes or modifications made without departing from the spirit of the present invention should be included in the following patent application. Within the range M380164. f is a simple description of the diagram] The first diagram is a schematic diagram of the structure of a liquid passing system; the second diagram is a schematic diagram of the structure of a rib-shaped aeration device; ,·as well as

【主要元件符號:抽換元件抽_^^ 100液體過濾系統 110 肋狀曝氣裝置 112 主曝氣管 114支曝氣管 116 氣孔[Main component symbol: replacement component pumping_^^ 100 liquid filtration system 110 ribbed aeration device 112 main aeration pipe 114 aeration pipe 116 vent

120過濾板 124支收集管 126抽換孔 130主收集管 140對位元件 142 溝槽 150 邊框 160可旋式條狀角鐵 ^62 固定部 8 M380164 164 旋轉部 170 抽換元件120 filter plate 124 collection tube 126 extraction hole 130 main collection tube 140 registration element 142 groove 150 frame 160 rotatable strip angle iron ^62 fixing part 8 M380164 164 rotating part 170 replacement element

Claims (1)

六、申請專利範圍: L 一種液體過濾系統,包含: 一肋狀曝氣裝置,包含一主曝氣管與複數個支曝氣管,其 中該些支曝氣管分別设置於該主曝氣管之周側,當氣體經由該 主曝氣管輸送至該些支曝氣管後,再經由每一支曝氣管之複數 個氣孔輸出形成複數個氣泡; 複數個過濾板,設置於該肋狀曝氣裝置上,其中每一個過 濾板係藉由至少一過濾薄膜包覆,並且連結一支收集管;以及 一主收集管,與該些支收集管連結,當該液體過濾系統放 置於液體中時,該主收集管即可藉由一驅動方式,使液體透過 每一過濾薄膜過濾後經由每一個過濾板及其支收集管匯集至該 主收集管。 2. 根據申請專利範圍第1項之液體過遽系統,其中上述之複數個 過濾板彼ιΜ目互平行,並且每—個碱㈣餘該主曝氣管, 使該些氣泡可沿著過濾薄膜清除雜質或濾餅。 3. 根據申請專利範圍第1項之液體過滤系統,更包含-邊框環繞 架構於該些過濾板周圍。 4·根據申請專利範圍第3項之液體過濾系统,更包含二個具有複 溝槽之條狀對位元件設置於該些過紐之相對兩側邊,並且 lVlJOUlU^t lVlJOUlU^t 項之液體過濾系統,其中該二對位元件 5.根據申請專利範圍第4 係固定於邊框之上。Sixth, the scope of application for patents: L A liquid filtration system comprising: a rib-shaped aeration device comprising a main aeration pipe and a plurality of aeration pipes, wherein the aeration pipes are respectively disposed in the main aeration pipe On the circumferential side, after the gas is sent to the aeration tubes through the main aeration tube, a plurality of bubbles are formed through a plurality of pores of each aeration tube; a plurality of filter plates are disposed on the ribs In the aeration device, each of the filter plates is covered by at least one filter film and connected to a collection tube; and a main collection tube is coupled to the collection tubes when the liquid filtration system is placed in the liquid The main collection tube can be filtered by a driving method to collect liquid through each filter membrane and then collected to the main collection tube via each of the filter plates and their collection tubes. 2. The liquid passing system according to item 1 of the patent application, wherein the plurality of filter plates are parallel to each other, and the main aeration tube is left for each alkali (four), so that the bubbles can be along the filter film. Remove impurities or filter cake. 3. The liquid filtration system according to claim 1 of the patent application, further comprising a frame surrounding structure around the filter plates. 4. The liquid filtration system according to item 3 of the patent application scope further comprises two strip-shaped alignment elements having a complex groove disposed on opposite sides of the plurality of crossings, and the liquid of the item 1VlJOUlU^t lVlJOUlU^t A filtration system in which the two alignment elements are fixed to the frame according to the fourth aspect of the patent application. 6·根據中請專利細第3項之賴過齡統,更包含二個可旋式 條狀角鐵’並且該可旋式條狀角鐵包含一固定部與一旋轉部, 其中該固定部係固定於該邊框上,使該旋轉部可旋轉扣壓_ 過液'板。 -7·根據申請專利制第4項之液體過齡統,其巾該過驗係為 一中空結構,其相對兩侧表面各具有複數個通孔。 —8.根據申請專利翻第7項之液體過齡統,其中該過濾板係藉 由一過;慮薄膜包覆於該過遽板之相對兩侧面上之通孔,並且該 過濾板之支收集管係連結於該過濾板之一側邊。 9. 根據申請專利範圍第4項之液體過濾系統,其中該過濾板之上 方設置一抽換孔。 10. 4艮據申請專利範圍第9項之液體過濾系統,可藉由一柱狀抽換 11 M380164 元件穿過每一個過濾板之抽換孔以進行過濾板之抽換。 11. 根據申請專利範圍第1項之液體過濾系統,其中上述之每一個 支曝氣管係垂直於該主曝氣管。 12. 根據申請專利範圍第1項之液體過濾系統,其中上述之驅動方 式係為真空抽取。6. According to the third paragraph of the patent application, the second embodiment includes two rotatable strip angle irons, and the rotatable strip angle iron comprises a fixing portion and a rotating portion, wherein the fixing portion It is fixed on the frame so that the rotating portion can be rotated to press the _ liquid 'board. -7. According to the liquid overage system of the fourth application of the patent system, the towel is a hollow structure, and each of the opposite sides has a plurality of through holes. 8. The liquid overage system according to claim 7, wherein the filter plate is passed through; the film is coated on the opposite sides of the opposite sides of the dam plate, and the filter plate is supported A collection tube is attached to one side of the filter plate. 9. The liquid filtration system of claim 4, wherein a perforation hole is disposed above the filter plate. 10. 4 According to the liquid filtration system of claim 9 of the patent application, the filter plate can be exchanged by a column-shaped 11 M380164 element passing through the exchange hole of each filter plate. 11. The liquid filtration system of claim 1, wherein each of the aeration tubes is perpendicular to the main aeration tube. 12. The liquid filtration system of claim 1, wherein the driving method is vacuum extraction.
TW98215994U 2009-08-31 2009-08-31 Liquid filter system TWM380164U (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI503288B (en) * 2011-09-30 2015-10-11 Kolon Inc Aeration unit and filtering apparatus comprising the same

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI503288B (en) * 2011-09-30 2015-10-11 Kolon Inc Aeration unit and filtering apparatus comprising the same
US9795926B2 (en) 2011-09-30 2017-10-24 Kolon Industries, Inc. Aeration unit and filtering apparatus comprising the same

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