TWI339136B - Separation treatment for ceramic sludge - Google Patents

Separation treatment for ceramic sludge Download PDF

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Publication number
TWI339136B
TWI339136B TW97111672A TW97111672A TWI339136B TW I339136 B TWI339136 B TW I339136B TW 97111672 A TW97111672 A TW 97111672A TW 97111672 A TW97111672 A TW 97111672A TW I339136 B TWI339136 B TW I339136B
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sludge
mud
ceramic
separation
fine
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TW97111672A
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Chinese (zh)
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TW200940195A (en
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Kun Sen Chang
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Univ Nat United
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/91Use of waste materials as fillers for mortars or concrete

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  • Treatment Of Sludge (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Treatment Of Water By Oxidation Or Reduction (AREA)

Description

1339136 -九、發明說明: 【發明妍屬之技術領域】 本發明係與陶瓷污泥再利用之技術領域有關,更 詳而言之是一種陶瓷研磨污泥之前·處理技術,·俾利污 泥回用於原製雇或作其他再利用。 , ♦ ^ 【先前技術】 陶瓷廠衍生之研磨污泥雖為無害之一般事業廢棄 鲁物,唯因含熟坏之粉屑與細泥、研磨片掉落之顆粒與 成分、廢水處理及污泥脫水添加之混凝劑/助凝劑/調理 劑等’故難以回用於原製程,而多作棄土、填土或掩 埋覆土,實為資源之浪費。本發明係開發陶瓷研磨污 泥再利用之前處理技術,主要包括污泥之顆粒分離及 分離後污泥之臭氧處理技術。 先前有關污泥或其他物質之分離相關技術,如中 • 華民國發明第384232號「水力旋流分離器’分離器總 成,旋流分離器,過濾穀物漿之方法,及組裝與拆卸 分離器總成的方法」、第455502號「砂泥污水分離法 及其裝置」、第470668號「礦砂快速洗滌及省水之方 法及裝置」、第494018號「篩屑裝置」、第52722〇 號「纖維/固體分離系統」、第541383號「篩網裝置」、 第550113號「旋轉型膜分離裝置及使用旋轉型膜裝置 之膜分離方法」、第U77609號「有害金屬污泥分離 1339136 方法」、第1.288019號「用於懸濁液分離之分離流路 模組、分離單元與分離船」等專利案。 另先前有關臭氧處理水體之相關技術,如中華民 國發明嘌490757黎「提供臭氧化處理流體之裝置芩使 用其之方法」、第574152號「化學機制控制高濃度臭 ^氧/反應液體產生系統及方法j、第1293286號「供應 r 恆濃臭氧化水之方法」等專利案。 . 進一步探討前揭關於污泥或其他物質之分離及 臭氧處理水體之專利技術,在分離技術方面,多針對 所設計之設備或裝置提出其分離方法,如旋流分離器 。(第384232號專利案)、振動篩及旋風式槽(第4555〇2 號專利案)、洗砂分離筒及遽砂機(第470668號專利 案)、製紙原料篩體及筛網(第494〇18號及第541383 號專利案)、旋轉型膜分離裝置(第55〇113號專利 案)、分離流路裝置(第·〇19號專利案)等,並 無本發明提出之旋轉篩分離陶究污泥之技術。此外, 在臭氧處理水體方面,多為臭氧注入流體之裝置(第 號專利案)、控制臭氧濃度方法(第574152 )' 1293286號專利案)等,並無以臭氧處理陶瓷 巧泥之技術。 理想之環境保護及珍惜地球有限資源而言,回 廠衍生廢棄物處理之最佳目標,故若能將陶究 研磨廢棄污泥,經由有效之前處理技 ^39136 術,再力回用於原製程或作其他再利肖,將可達到零 廢棄、資·源再利用之目的。 【發明内容】 - .、本發明之主要目的係提供一種陶瓷污泥之處理方 >法,其可將陶究薇所產生之含陶究研磨污泥廢水以及 #積之陶兗研磨脫水污泥,處理成細泥及粗泥,以供 再利用,達到「零廢棄」、「資源再利用」之理想環 保目的。 緣是,為達成前述之目的,本發明所提供之一種 陶瓷污泥之處理方法,至少包含以下步驟: ㈣:利用一旋轉篩裝置將含陶瓷污泥之廢水分 離為細泥及粗泥; 臭氧曝氣處理:將細泥置於一密閉式反應槽内與 • 臭氧充分曝氣反應,用以分解細泥尹之有機物質; 沉澱··將經臭氧曝氣處理之細泥予以沉澱; • 去除水分:將已沉澱之細泥脫水或乾燥; - 再利用··將粗泥及去除水分後之細泥回收再利用。 【實施方式】 以下兹舉本發明二較佳實施例並配合圖式作進 一步之詳細說明如後: 1339136 首先’請參閱圖一至圖四所示,本發明一較佳實 施例之陶究污泥之處理方法,包含有下列步驟:1339136 - IX, invention description: [Technical field of invention genus] The present invention relates to the technical field of ceramic sludge reuse, and more specifically to a ceramic grinding sludge before treatment technology, 俾 sludge Reuse for original employment or for other reuse. , ♦ ^ [Prior Art] Although the grinding sludge derived from the ceramics factory is harmless to the general business, it is only due to the inclusion of fine powder and fine mud, particles and components falling from the abrasive sheet, wastewater treatment and sludge. Dehydration added coagulant / coagulant / conditioning agent, etc. 'It is difficult to return to the original process, and more spoil, fill or buried soil, is a waste of resources. The invention develops a prior art treatment technology for re-use of ceramic abrasive sludge, mainly including particle separation of sludge and ozone treatment technology of sludge after separation. Previous technologies related to the separation of sludge or other substances, such as China·Republic of China invented No. 384232 "Hydraulic cyclone separator" separator assembly, cyclone separator, method for filtering grain slurry, and assembly and disassembly separator Method of Assembly", No. 455502 "Sand Sediment Separation Method and Apparatus", No. 470668 "Method and Apparatus for Rapid Washing and Water Saving of Mineral Sand", No. 494018 "Sifting Device", No. 52722" "Fiber/solid separation system", No. 541383 "Screen device", No. 550113 "Rotary membrane separation device and membrane separation method using rotary membrane device", U77609 "Hazardous metal sludge separation method 1339136", Patent No. 1.288019, "Separating flow path module for suspension separation, separation unit and separation ship". Other related technologies related to ozone treatment of water bodies, such as the Republic of China invented 嘌 757 757 嘌 嘌 「 「 「 " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " Method j, No. 1293286 "Provision of r-enriched ozonated water" and other patent cases. Further discussion of the patented technology for the separation of sludge or other substances and ozone treatment of water bodies, in the separation technology, the separation method is proposed for the equipment or device designed, such as cyclone separator. (Patent No. 384232), vibrating screen and cyclone tank (patent No. 4555-2), sand washing separation cylinder and sand blasting machine (patent No. 470668), paper-making raw material sieve and screen (No. 494) No. 18 and No. 541383), a rotary membrane separation device (Patent No. 55-113), a separation flow device (No. 19 patent), and the like, and there is no rotary sieve separation proposed by the present invention. Pottery sludge technology. In addition, in the case of ozone-treated water bodies, most of them are devices for injecting fluids into ozone (No. Patent No.), methods for controlling ozone concentration (No. 574, 152), and No. 1293286, and there is no technique for treating ceramics with ozone. The ideal environmental protection and cherish the limited resources of the earth, the best goal of returning to the factory for waste treatment, so if the ceramics can be ground to waste sludge, through the effective pre-treatment technology, 39136, and then return to the original process Or for other re-sharp, it will achieve the purpose of zero waste, capital and source reuse. SUMMARY OF THE INVENTION The main object of the present invention is to provide a method for treating a ceramic sludge, which can grind and dewater the ceramic slurry containing the ceramics produced by the pottery researcher. The mud is treated as fine mud and coarse mud for reuse, achieving the ideal environmental protection objective of "zero waste" and "reuse of resources". In order to achieve the foregoing objective, the method for treating a ceramic sludge provided by the present invention comprises at least the following steps: (4): separating a wastewater containing ceramic sludge into fine mud and coarse mud by using a rotary sieve device; Aeration treatment: The fine mud is placed in a closed reaction tank and • Ozone is fully aerated to decompose the organic matter of the fine mud Yin; Precipitate··Precipitate the sludge treated by ozone aeration; • Remove Moisture: dewatering or drying the precipitated fine mud; - Recycling · Recycling the coarse mud and the fine mud after removing the water. [Embodiment] Hereinafter, the second preferred embodiment of the present invention will be further described in detail with reference to the following: 1339136 First, please refer to FIG. 1 to FIG. 4, a ceramic sludge according to a preferred embodiment of the present invention. The processing method includes the following steps:

本發明之第一步驟係分離110:利用一旋轉篩裝 置10將含陶瓷污界之廢水分離為細泥-及·粗泥。陶篆污 泥係陶瓷研磨污返,該旋轉篩裝置10包含一基座12, 該基座12内容納有水;一旋轉篩14,可轉動地傾斜 s又置於該基座12並部分浸入水令,具有一不銹鋼支標 框架141’該支撐框架141内設有一中空圓柱型篩體 142,係不銹鋼細網;一轉軸143,穿經該篩體142中 央軸心並固接支撐框架141而架設於基座12;該篩體 142之篩孔孔徑為ASTM 200號(75微米)、傾斜角 度為5 - 20。、轉速為2 - 30 rpm、浸入水中高度為ι/6 _ 1/2。含陶瓷污泥之廢水係輸入該旋轉篩14進行分離, 通過篩孔之細泥為粒徑小於篩孔之污泥,而經該旋轉 篩14排除之粗泥為粒徑大於篩孔之污泥。 本發明之第二步驟係臭氧曝氣處理12〇:係將細 泥置於-㈣式反應槽2G内與臭氧充分曝氣反應,用 以分解細泥t之有機物質。該密閉式反應槽2〇包含一 槽體22,細泥係輸入該槽體22,數中空管μ,立設 於該槽體22内,臭氧係輸入各該中空管2B4而喷入ς 體22’用以藉由氣流攪拌槽體22内之細泥,使細泥 與臭氧充分反應,進而分解細泥中之有機物質。該槽 體22内液固比係大於3,每公斤乾細泥所需臭氧^於 1339136 .2-10公克,牝外,該密閉式反應槽20更包含一自動 洩壓裝置26,係設置於該槽體22 —端。 本發明之第三步驟係沉澱130 :將經臭氧曝氣處 理之細泥予-以沉澱,係-將細泥置於一沉澱槽(圖中未 示)中藉重力沉降方式洱澱。 - 本發明之第四步驟係去除水分140 :將已沉戮之 ‘ 細泥脫水或乾燥,以去除細泥之水分。脫水之方式係 馨 利用壓濾、真空過濾或離心等方式將已沉澱之細泥脫 水’而乾燥之方式係利用加熱使已沉澱之細泥乾燥, 加熱溫度為100-200eC。 本發明之最後步驟係再利用150:將粗泥及脫水 後之細泥回收再利用,粗泥係可供混凝土細骨材或其 他用途,而細泥可作為原陶瓷製程原料之一部分或供 作其他用途。 ” 由上可知,本發明陶瓷污泥之處理方法,可將陶 鲁錢所產生之含陶究研磨污泥之廢水分離出細泥及粗 泥,再將細泥經臭氧曝氣、沉澱及去除水分等處理, .最後二種污泥均可再利用’為一「零廢棄」、「資源 再利用」之甚具環保創新方法。 此外’ 一般陶究薇常有堆積陶究研磨脫水污泥不 易處理之問題,亦可透過本發明之方法予以處理再利 用,如圖五所示,係本發明另一較佳實施例之陶免污 泥之處理方法’其步驟大體上與前揭較佳實施例相 10 :驟、不.:77離、臭氧曝氣處理、沉澱及去除水分等 驟〆不同之處在於:其分離步驟前更包含有下列步 判斷210·研判是否要辱合既有之陶究研磨脫水污 陶究廠右有堆積陶究研磨脫水污泥且未捧入其他 物質或遭污染’即可進行後續與含陶竟污泥之原廢水 混合之步驟;反之,則不需混合。 混σ 220.將陶瓷脫水污泥與含陶瓷污泥之原廢水 置於-混合攪拌槽(圖中未示)内進行混合,兩者混 合後液固比係大於3。 藉此,將陶瓷廠堆積之陶瓷研磨脫水污泥混合含 陶瓷研磨污泥之廢水後,即可進行後續之分離、臭氧 曝氣處理、沉澱及去除水分等步驟之處理,而亦可將 粗泥及脫水後之細泥回收再利用。 綜上所述,本發明陶瓷污泥之處理方法,其可將 陶瓷廠所產生之含陶瓷研磨污泥廢水以及堆積之陶兗 研磨脫水污泥處理成細泥及粗泥,俾可分別再利用, 而達成「零廢棄」、「資源再利用」之環保效果;緣 是,本發明確實符合發明專利之要件,爰依法提出申 請0 1339136 【圖式簡單祝明】 圖一係本發明一較佳實施例之流程圖。 圖二係本發明一較佳實施例中旋轉篩裝置之示意 圖。 · - .. 圖三係本發明一較佳實施例中旋轉篩之皂輝圖。 圖四係本發明一較佳實施例中密閉式反應槽之示 意圖。 圖五係本發明另一較佳實施例之流程圖。 【主要元件符號說明】 分離110 臭氧曝氣處理120沉澱130 去除水分140 再利用150 旋轉篩裝置1〇 基座12 旋轉篩14 支撐框架141 密閉式反應槽20 自動洩壓裝置26The first step of the present invention is the separation 110: the use of a rotary screen apparatus 10 to separate the wastewater containing ceramic fouling into fine mud-and-rough mud. The terracotta sludge ceramics grinds back, the rotary screen device 10 includes a susceptor 12, the susceptor 12 contains water therein; a rotating screen 14 is rotatably tilted s and placed on the susceptor 12 and partially immersed The water ring has a stainless steel support frame 141'. The support frame 141 is provided with a hollow cylindrical sieve body 142, which is a stainless steel fine mesh; a rotating shaft 143 passes through the central axis of the sieve body 142 and is fixed to the support frame 141. The sieve body 142 has a mesh aperture of ASTM 200 (75 micrometers) and an inclination angle of 5-20. The speed is 2 - 30 rpm and the height of the immersion water is ι/6 _ 1/2. The wastewater containing ceramic sludge is input into the rotary sieve 14 for separation, and the fine mud passing through the sieve hole is sludge having a particle diameter smaller than the sieve hole, and the coarse mud discharged through the rotary sieve 14 is sludge having a larger particle diameter than the sieve hole. . The second step of the present invention is ozone aeration treatment 12: the fine mud is placed in the -(4) type reaction tank 2G to sufficiently aerate with ozone to decompose the organic matter of the fine mud. The closed reaction tank 2A includes a tank body 22 into which the fine mud is fed, a plurality of hollow tubes μ, which are erected in the tank body 22, and ozone is introduced into each of the hollow tubes 2B4 to be sprayed into the tank. The body 22' is used to agitate the fine mud in the tank body 22 by the airflow to sufficiently react the fine mud with ozone, thereby decomposing the organic matter in the fine mud. The tank body 22 has a liquid-solid ratio of more than 3, and the ozone required per kilogram of dry fine mud is 1339136.2-10 g. In addition, the closed reaction tank 20 further includes an automatic pressure relief device 26, which is disposed on The trough body 22 is at the end. The third step of the present invention is the precipitation 130: precipitating the fine mud treated by ozone aeration, and depositing the fine mud in a sedimentation tank (not shown) by means of gravity sedimentation. - The fourth step of the present invention is to remove moisture 140: dewatering or drying the already degraded 'fine mud to remove moisture from the fine mud. The method of dehydration is to dehydrate the precipitated fine mud by means of pressure filtration, vacuum filtration or centrifugation, and the method of drying is to dry the precipitated fine mud by heating, and the heating temperature is 100-200 eC. The final step of the present invention is to reuse 150: the coarse mud and the dehydrated fine mud are recycled and reused, the coarse mud is used for concrete fine aggregate or other purposes, and the fine mud can be used as a part of the original ceramic process raw material or for use as a raw material. Other uses. It can be seen from the above that the treatment method of the ceramic sludge of the present invention can separate the wastewater containing the ceramic slurry produced by Tao Luqian into fine mud and coarse mud, and then aerate, precipitate and remove the fine mud by ozone. Moisture treatment, etc. The last two types of sludge can be reused as a “zero waste” and “resource reuse” environmentally innovative method. In addition, the general ceramics often have the problem that the stacked ceramics and the dewatered sludge are not easy to be treated, and can also be treated and reused by the method of the present invention. As shown in FIG. 5, it is a ceramic exemption of another preferred embodiment of the present invention. The sludge treatment method's steps are substantially different from the previous preferred embodiment: the steps of: the separation of 77, the ozone aeration treatment, the precipitation and the removal of moisture are different: before the separation step Including the following steps to judge 210. Whether to judge whether to insult the existing ceramics, grinding, dewatering and staining pottery factory, there is a pile of ceramics, grinding and dewatering sludge, and not holding other substances or being contaminated. The step of mixing the raw wastewater of the sludge; otherwise, no mixing is required. Mixed σ 220. The ceramic dewatered sludge and the raw wastewater containing ceramic sludge are mixed in a mixing tank (not shown), and the liquid-solid ratio system is greater than 3 after mixing. In this way, after mixing the ceramic grinding dewatered sludge accumulated in the ceramic factory with the wastewater containing the ceramic grinding sludge, the subsequent separation, ozone aeration treatment, sedimentation and moisture removal steps can be performed, and the coarse mud can also be processed. And the fine mud after dewatering is recycled and reused. In summary, the method for treating ceramic sludge of the present invention can treat the ceramic-containing grinding sludge wastewater generated by the ceramics factory and the stacked ceramic mortar and dewatered sludge into fine mud and coarse mud, and can be reused separately. The environmental protection effect of "zero waste" and "recycling of resources" is achieved; the reason is that the present invention does meet the requirements of the invention patent, and the application is made according to law 0 1339136. [Figure 1 is a simple wish] Figure 1 is a preferred embodiment of the present invention. Flow chart of the embodiment. Figure 2 is a schematic view of a rotary screen apparatus in accordance with a preferred embodiment of the present invention. - Figure 3 is a soap diagram of a rotary screen in accordance with a preferred embodiment of the present invention. Figure 4 is a schematic illustration of a closed reaction vessel in accordance with a preferred embodiment of the present invention. Figure 5 is a flow chart of another preferred embodiment of the present invention. [Main component symbol description] Separation 110 Ozone aeration treatment 120 Precipitation 130 Removal of moisture 140 Reuse 150 Rotary sieve device 1〇 Base 12 Rotary sieve 14 Support frame 141 Closed reaction tank 20 Automatic pressure relief device 26

篩體142 轉軸143 槽體22 中空管24 判斷210 混合220 12Sieve 142 Rotary shaft 143 Slot 22 Hollow tube 24 Judging 210 Mixing 220 12

Claims (1)

丄州136 •十、申請專利範圍: 1.種陶瓷污泥之分離處理方法,至少包含以下 步驟: 刀藏利用—旋轉篩裝置將含陶曼污泥之廢水分 離為細泥及粗泥; 六氧曝氣處理.將細泥置於一密閉式反應槽内與 臭氧充分曝氣反應’用以分解細泥中之有機物質; • 沉澱.將經臭氧曝氣處理之細泥予以沉澱; 去除水分:將已沉澱之細泥脫水或乾燥;及 再利用:將粗泥及去除水分後之細泥回收再利用。 申叫專利範圍第1項所述陶瓷污泥之分離處 ^方法,其令’分離步驟前’更包含有-混合步驟, ::將既有之陶瓷脫水污泥與含陶瓷污泥之原廢水予以 所述陶瓷污泥之分離肩 更包含有一判斷步驟, 泥是否有掺入其他物屬 未掺入其他物質或遭3 ’則不需混合。 所述陶瓷污泥之分離處 係將既有之陶完脫水污 此合攪拌槽内進行混丄州136 • Ten, the scope of application for patents: 1. The separation process of the ceramic sludge, including at least the following steps: The knife-use-rotating sieve device separates the wastewater containing the terracotta sludge into fine mud and coarse mud; Oxygen aeration treatment. The fine mud is placed in a closed reaction tank and fully aerated with ozone to 'decompose the organic matter in the fine mud; · Precipitate. Precipitate the ozone-treated aerated mud; remove moisture : Dewatering or drying the precipitated fine mud; and recycling: recycling and recycling the coarse mud and the fine mud after removing the water. The method for separating the ceramic sludge described in the first paragraph of the patent scope is as follows: the 'pre-separation step' further includes a mixing step, :: the existing ceramic dewatered sludge and the raw wastewater containing the ceramic sludge The separating shoulder of the ceramic sludge further comprises a judging step, whether the mud is mixed with other substances, not mixed with other substances or 3', and no mixing is required. The separation of the ceramic sludge is performed by mixing the existing ceramics into the mixing tank. 3.如申請專利範圍第2項 理方法,I中’混合步驟前, 係研判既有之陶瓷研磨脫水污 或遭污染該陶究脫水污泥 木’則可進行混合步驟;反之 4♦如申請專利範圍第2項 理方法’丨中,混合步驟中, 泥與含陶究污泥之原廢水置於 合。 • C奶:垮 • 5.如申請·專利範圍第4 理太士 U 相究污泥之分離處 理方法,其中,混合步驟中 人陶念、—νβu 无有之陶瓷脫水污泥與 3陶“泥之原廢水混合後液固比係大於3。 6.如申請專利範圍第丨 、 1ψ ^ . 、处陶瓷污泥之分離處 理方法,其中,分離步驟 亡 ^ u ^ ^ 5玄知轉篩裝置包含一基 座’該基座内容納有水,一 罢於兮盆广、,A \ 疋1^師,可轉動地傾斜設 置於该基座亚部分浸入水φ, 9λλ d. , 其師孔之孔徑為ASTM 200號(75微米)。 理方H請Φ專利範Μ 6項所述陶£污泥之分離處 Π法30該旋㈣之傾斜角度〇轉速 ^ ^ ' j(J rpm ° 8.如申請專利範圍第 理太、i 〇丄 貞所迷陶:允污泥之分離處 王万法,其中’該旋轉篩包含— _L. 支稽框架’由不錄鋼 .衣成,一中空圓柱型篩 不钴h β又;表该支撐框架内,係 不銹鋼細網;一轉軸,穿妹 擇框架而架設於基座。 Α中央轴心並固接支 理方9>如^專利範圍$ 6項所述陶m之分離處 x方法’其中,含陶咨$,、ρ + @ υ 行分離^ ,尤/可尼之疋水係輸入該旋轉筛進 泥 少μ,通過篩孔之細泥為粒徑小於篩孔之污 ,經該旋轉薛排除之粗泥為粒徑大於薛孔之污泥。 埋方、去,2 °月專利乾圍第1項所述陶瓷污泥之分離處 槽包二二ΐΐ,臭氧曝氣處理步驟中,該密閉式反應 彳9祖細泥係輸入該槽體,數中空管,立設 14 1339136 ·—»»·. ·.〜:fl<r F! ’ ·於^亥槽體内,·臭氡係輸入各該中办j ^ . 丁上首而喷入梓辦,用 以藉由氣流攪拌槽體内之細泥 、9 ••應而分解細泥中之有機物質。細泥與臭氧充分反 - Π.如申請專利範圍第丨項所、+、^ # ^ 〇 貝所述陶瓷污泥之分離處 理方法,其中,臭氧曝氣處理 地允y门,β ~中’該密閉式反應 槽内液固比係大於3,每公斤龄纟 in /V . 乾、,,田泥所需臭氧介於2 _ 1 〇公克。 12.如申請專利範圍第1〇 j旨邮、+、 •汐理方本甘士 員所述陶究污泥之分離 處理方法,其中,該密閉式 姑吳〆 、久I槽更包含一自動洩壓 4置’係設置於該槽體一端。 理方Γ:Γ利範圍第1項所述陶細之分離處 ::,其中’沉卿中,係將細泥置於一沉殿槽 中措重力沉降方式沉澱。 二如申請專利範圍第】項所述陶究污泥之分離處 万法,其中,去除水分步 ..^ 刀/ ν宁,係利用壓濾、真空 過處或離心等脫水方式將已沉殿之細泥脫水。 請專職㈣I項所述m泥之分離處 p、”法’其中’去除水分步驟中’係利用加熱方式使 儿焱之細泥乾燥,加熱溫度為】⑽〜2001。 理方K如申請專利範圍第1項所述陶究污泥之分離處 A法,其中,再利用步驟中,粗泥係可供混凝土細 二材或其他用途’細泥可作為原陶t製程原料之-部 分或供作其他用途。 15 1339136 if (i j . 1 7.如申請專利範圍第1項所述陶瓷污泥之分離處 理方法,其中,該陶瓷污泥係陶瓷研磨污泥。3. If the method of claim 2 of the scope of patent application is applied, the mixing step is carried out before the 'mixing step, and the existing ceramic grinding dewatering or polluting the ceramic dewatering sludge wood' can be carried out; In the second method of the patent scope, in the mixing step, the mud is placed in combination with the raw wastewater containing the ceramic sludge. • C milk: 垮 • 5. If the application is patented, the fourth section of the Rectifier U is to separate the sludge treatment method. Among them, in the mixing step, the human Tao Nian, νβu has no ceramic dewatered sludge and 3 pottery. The liquid-solid ratio system of the raw wastewater of the mud is greater than 3. 6. If the application scope is 丨, 1ψ ^., the separation and treatment method of the ceramic sludge, wherein the separation step is dead ^ u ^ ^ 5 Xuanzhi rotary sieve device Including a pedestal 'the pedestal contains water, one is in the basin, and the A 疋1^ division is rotatably disposed on the pedestal sub-portion immersed in water φ, 9λλ d. The pore size is ASTM No. 200 (75 micron). The formula H is Φ patent Μ Μ 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 6 For example, if you apply for a patent, the scope of the patent is too much, and the i 〇丄贞 : : : : : 允 允 允 允 允 允 允 允 允 允 允 允 允 允 允 允 允 允 允 允 允 允 允 允 允 允 允 允 允 允 允 允 允 允 允The sieve is not cobalt h β; in the support frame, it is a stainless steel fine mesh; a shaft, wearing a frame of the girl On the pedestal. ΑThe central axis is fixed to the support side 9> As ^The patent range is $6, the separation of the pottery m is the method x which contains the pottery $, ρ + @ υ line separation ^, especially / The water of the 可 疋 输入 输入 输入 输入 输入 输入 输入 输入 可 可 可 可 可 可 可 可 可 可 可 可 可 可 可 可 可 可 可 可 可 可 可 可 可 可 可 可 可 可 可 可 可 可 可 可 可Go, 2 ° month patent dry circumference, the separation of the ceramic sludge mentioned in the first paragraph of the tank is two or two, in the ozone aeration treatment step, the closed reaction 彳 9 祖 fine mud system is input into the tank, the number is hollow Tube, stand 14 1339136 ·—»»·. ·.~:fl<r F! ' ·In the body of the ^H, the skunk system is input to each of the j ^. It is used to agitate the organic matter in the fine mud by stirring the fine mud in the tank, and the fine mud and ozone are fully anti--. For example, the scope of the patent application, +, ^ # ^ The separation and treatment method of the ceramic sludge mentioned in the mussels, wherein the ozone aeration treatment allows the y door, and the liquid-solid ratio system in the closed reaction tank of β~中′ is greater than 3 per kilogram.纟in /V . Dry,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,, The separation processing method, wherein the closed type of Kuwan, the long-term I-slot further comprises an automatic pressure-relieving 4-set is disposed at one end of the tank body. The formula is: the separation of the ceramic fines according to the first item of the profit range ::, In the 'Shen Qingzhong, the fine mud was placed in a sinking tank to measure the gravity sedimentation method. 2. For example, the method for separating the sludge from the pottery mentioned in the scope of the patent application is to remove the moisture step.. ^ knife / ν 宁, using the dewatering method such as pressure filtration, vacuum or centrifugation The fine mud is dehydrated. Please take full-time (4) I item m mud separation point p, "Fa" in the 'moisture removal step' is to use the heating method to make the baby's fine mud dry, the heating temperature is (10) ~ 2001. The method A of the separation of the sludge in the ceramics according to the first item, wherein, in the reuse step, the coarse mud is available for the concrete two or the other use 'fine mud can be used as part of the raw material of the original ceramics process or for supply The use of the ceramic sludge as described in claim 1, wherein the ceramic sludge is a ceramic slurry. 1616
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