TWI339136B - Separation treatment for ceramic sludge - Google Patents
Separation treatment for ceramic sludge Download PDFInfo
- 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
- Authority
- TW
- Taiwan
- Prior art keywords
- sludge
- mud
- ceramic
- separation
- fine
- Prior art date
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/91—Use of waste materials as fillers for mortars or concrete
Landscapes
- 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)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
TW97111672A TWI339136B (en) | 2008-03-31 | 2008-03-31 | Separation treatment for ceramic sludge |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
TW97111672A TWI339136B (en) | 2008-03-31 | 2008-03-31 | Separation treatment for ceramic sludge |
Publications (2)
Publication Number | Publication Date |
---|---|
TW200940195A TW200940195A (en) | 2009-10-01 |
TWI339136B true TWI339136B (en) | 2011-03-21 |
Family
ID=44867910
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
TW97111672A TWI339136B (en) | 2008-03-31 | 2008-03-31 | Separation treatment for ceramic sludge |
Country Status (1)
Country | Link |
---|---|
TW (1) | TWI339136B (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109225187B (en) * | 2018-11-16 | 2021-06-11 | 南京工业大学 | Preparation method and application of sludge-based ceramic-based catalyst |
-
2008
- 2008-03-31 TW TW97111672A patent/TWI339136B/en not_active IP Right Cessation
Also Published As
Publication number | Publication date |
---|---|
TW200940195A (en) | 2009-10-01 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US5833863A (en) | Concrete reclamation system | |
CN104843955A (en) | Oil and gas field drilling mud waste while-drilling processing system and processing method thereof | |
EA031107B1 (en) | Method for separating liquid from suspended matter in a sludge and device for same | |
CN109721191A (en) | A kind of sandstone building stones production wastewater treatment system | |
JP2006035176A (en) | Dehydration auxiliary material, and dehydration method and recycling method of high water ratio sludge | |
CN104829070A (en) | Oil and gas field drilling fluid waste treatment-while-drilling system | |
JP6112475B2 (en) | Extraction device | |
TWI339136B (en) | Separation treatment for ceramic sludge | |
JP4178557B2 (en) | How to treat dredged mud | |
JP2002316198A (en) | Sludge dehydration method and sludge dehydration apparatus | |
CN204644081U (en) | A kind of oilfield drilling mud waste is with brill treatment system | |
CN108409073A (en) | Ditch mud processing method | |
JP2012166170A (en) | Washing method for incineration ash and method for converting the incineration ash into cement raw material | |
JP2004261795A (en) | Method of removing nonvolatile contaminant in soil | |
JP2015054287A (en) | Sludge treatment method | |
JP2005262076A (en) | Method for cleaning soil contaminated with oil | |
JP6199154B2 (en) | Radioactive substance removal equipment | |
JP2016064332A (en) | Desalination-cement raw material formation method of mixed ash and device | |
JP6905337B2 (en) | Main ash desalination / cement raw material method and equipment | |
KR101094321B1 (en) | Poor soil treating method using a consecutive filtering system | |
KR101573624B1 (en) | Dredged processing device using a magnetic field | |
JP6433214B2 (en) | Method and apparatus for desalination of mixed ash and raw material for cement | |
JP2008207167A (en) | Purification method of suspension water, treatment method of suspension water using the purification method, and treatment system of suspension water for executing this treatment method | |
JP2016064323A (en) | Muddy water treatment system and muddy water treatment method | |
CN204644080U (en) | A kind of oilfield drilling mud waste is with brill treatment system |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
MM4A | Annulment or lapse of patent due to non-payment of fees |