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TW506860B - Reuse and product of calcium fluoride sludge - Google Patents

Reuse and product of calcium fluoride sludge Download PDF

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Publication number
TW506860B
TW506860B TW90102099A TW90102099A TW506860B TW 506860 B TW506860 B TW 506860B TW 90102099 A TW90102099 A TW 90102099A TW 90102099 A TW90102099 A TW 90102099A TW 506860 B TW506860 B TW 506860B
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Taiwan
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sludge
caf2
dry
product
calcium fluoride
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TW90102099A
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Chinese (zh)
Inventor
Huo-Sheng Lin
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Everglory Resource Technology
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Abstract

This invention provides a reuse method of calcium fluoride (CaF2) sludge, which includes following steps: (1) drying the CaF2 sludge at a temperature below 150 DEG C before crashing and sieving into CaF2 powder; (2) blending the dry CaF2 powder, a binder and a mineralizing agent in a dry state and pelletizing the mixture into A earth; (3) blending feldspar, kaolin, quartz and clay by ball mill before spraying for pellet and ageing into basic earth material; and (4) blending the A earth, the binder, the basic earth material, a sintered kaolin, a pottery stone and a ceramic pigment in a dry state before pelletizing, sieving, ageing and press forming, cup body drying and high temperature sintering to achieve an optimal product while concurrently solve environment problem of the CaF2 sludge and to provide benefit of product with applicable value.

Description

506860 案號90102099 年月日 修正 五、發明說明(1) 本發明提出一種氟化鈣污泥再利用方法及其製成品, 更特定言之,本發明係有關一種將污水處理廠所產生的C a F2污泥處理/再加工成為有用產品,特別者陶瓷體之方法 ,可同時解決CaF2污泥的環保問題及提供有應用價值的產 品之效益。 本案發明人有鑑於下列事實: 一、 由化學組成分析得知污水處理廠因使用不同中間物〔 CaC12 >aCa(OH)2 )與HF反應而有污泥組成CaF2 ACaC03 含量的明顯差異,這些數據差異對於後續高溫化學反 應時有顯著的影響。 二、 由單獨污泥燒結反應得知未添加任何礦物催化劑(礦 化劑)時其在1,1 0 0 °C 區間溫度仍屬安定化合物,燒 結情況並不理想。當添加礦化劑(如CaC03) 時其因化 學莫耳比不同,而有明顯降低反應溫度現象,以重量 比CaF2 1 : CaC03 1混合時其反應溫度約降低2 0 0 °C, 此可由熱差示性分析TG/DTA結果比較而得勉。 三、 CaF2由6 3 0 °C起即有明顯吸熱反應至81 9 °C止,顯示此 溫度區間礦物相已起變化,因此提供具高矽質(S i 02) 之低溫玻璃相的物質差同參與反應將·有助於形成氟化 鹽之高溫化合物(如F 2 S i 2 07 ),可有效穩定氟於高溫 T之活化性,而形成一能階之安定型礦物結晶相。 四、 添加適量高銘(A 1 2 0 3 )含量物質於配比中,可得到燒結506860 Case No. 90102099 Rev. V. Description of the invention (1) The present invention proposes a method for recycling calcium fluoride sludge and its products. More specifically, the present invention relates to a method for treating C generated from sewage treatment plants. a F2 sludge treatment / reprocessing becomes a useful product, especially the ceramic body method, which can simultaneously solve the environmental problems of CaF2 sludge and provide benefits of products with application value. The inventors of this case have considered the following facts: 1. The chemical composition analysis shows that the sewage treatment plant has obvious differences in the CaF2 ACaC03 content of the sludge composition CaF2 due to the reaction between different intermediates [CaC12 > aCa (OH) 2) and HF. The difference in data has a significant effect on subsequent high temperature chemical reactions. 2. It is known from the sintering reaction of separate sludge that when no mineral catalyst (mineralizing agent) is added, the temperature is still a stable compound in the range of 1,100 ° C, and the sintering situation is not ideal. When adding mineralizers (such as CaC03), the reaction temperature will be significantly reduced due to different chemical molar ratios. When the weight ratio CaF2 1: CaC03 1 is mixed, the reaction temperature will decrease by about 20 ° C. The results of differential analysis of TG / DTA were compared. 3. CaF2 has a significant endothermic reaction from 6 3 0 ° C to 81 9 ° C, showing that the mineral phase has changed in this temperature range, so the material difference of providing a low-temperature glass phase with high silica (S i 02) The high temperature compounds (such as F 2 S i 2 07) that will participate in the reaction will help to stabilize the activation of fluorine at high temperature T, and form a stable mineral crystal phase of energy level. 4. Add appropriate amount of high Ming (A 1 2 0 3) content substance in the proportion, can get sintered

900105901.ptc 第4頁 506860 _案號90102099_ 年月日 修正_ 五、發明說明(2) 體積之穩定性,有助於終產品之燒結成品尺寸穩定度 〇 五、 由實驗得知CaF2污泥不適合以濕式研磨、混拌、因製 程中需添加大量水份(約4 0 % ),於喷霧乾燥塔(S p r a y d r y e r )中瞬間最高乾燥溫度達6 5 0 °C以上,在高水氣 含量的空氣中恐將激發CaF2部份轉化成水解化合物而 有造成二次污染之虞。此外,乾燥過程之高耗熱能需 求亦不合環保與經濟原則。 六、 將CaF2污泥以低溫(1 5 0 °C )乾燥後利用乾式粉碎到粒 徑小於60微米可有效增加CaF2之比表面積並促使高溫 反應完整。 七、CaF2污泥猃常溫下無法與鹼性物質起反應,若以一般 方 式 常 溫 固 化 時 並 無 法 扼 止 氟 離 子 溶 於 水 中 , 此 將 造 成 二 次 水 污 染 0 以 溫 固 態 液 相 燒 結 時 可 將 氟 離 子 取 代 玻 璃 相Si丨 02 之 氧1 離 子 而 形 成 南 能 階 之· 安 定 型 礦: 物 結 晶 > 可 有 效 防 止 氟 離 子 溶 於 水 中 污 染 水 源 0 乃 根 據 本 案 發 明 人 多 年 經 驗 及 進 行 精 深 研 究 而 提 出 一 種 氟 化 鈣 污 泥 再 利 用 方 法 及 其 製 成 品 9 更 特 定 言 之 , 本 發 明 提 出 一 種 將 污 水 處 理 廠 所 產 生 的C a F2 污 泥 予 以 處 理 / 再 加 工 成 為 有 用 產 品 5 特 別 者 陶 瓷 體 y 之 方 法 5 可 同 時 解 決 Ca F2 污 泥 的 環 保 問 題 及 提 供 有 應 用 價 值 的 產 品 之 效 益 〇 本 發 明 氟 化 鈣 污 泥 再 利 用 方 法 包 括 如 圖 1 所 示 流 程 中 之 諸 主 要 階 段 • (1 ) 將C a F2 污 泥 於 1 50 °C 以 下 溫 度 乾 燥 粉 •碎 並 篩 分 至 約60 微 米 之 粉 料 成 為C a F2 乾 粉 ;900105901.ptc Page 4 506860 _Case No. 90102099_ Year, Month, and Day Amendment_ Five. Description of the invention (2) The stability of the volume contributes to the dimensional stability of the sintered product of the final product. 05. It is known from the experiment that CaF2 sludge is not suitable For wet grinding and mixing, due to the need to add a large amount of water (about 40%) in the process, the maximum drying temperature in the spray drying tower (S praydryer) can reach more than 650 ° C, and the moisture content is high. In the air, CaF2 may be partially converted into hydrolyzed compounds, which may cause secondary pollution. In addition, the high heat consumption requirements of the drying process are not in line with environmental protection and economic principles. 6. CaF2 sludge is dried at low temperature (150 ° C) and then pulverized to dryness to a particle diameter of less than 60 microns, which can effectively increase the specific surface area of CaF2 and promote the intact reaction at high temperature. 7. CaF2 sludge cannot react with alkaline substances at normal temperature. If it cannot be dissolved in water when solidified at ordinary temperature in normal way, this will cause secondary water pollution. The fluoride ion replaces the oxygen 1 ion of the glass phase Si 丨 02 to form a south-energy grade. The stable ore: crystallization of the substance can effectively prevent the fluoride ion from dissolving in the water to pollute the water source. 0 It is based on the inventor's many years of experience and intensive research. Propose a calcium fluoride sludge reuse method and its finished product 9 More specifically, the present invention proposes to treat / reprocess the C a F2 sludge produced by a sewage treatment plant into a useful product 5 in particular a ceramic body Method 5 can simultaneously solve the environmental protection problem of Ca F2 sludge and provide benefits of products with application value. The reuse method of calcium fluoride sludge of the present invention includes as shown in Figure 1. The main stages in the process: (1) Dry the Ca F2 sludge at a temperature below 150 ° C • Crush and sieve the powder to about 60 micrometers to form a dry Ca F2 powder;

900105901.ptc 第5頁 506860 年 案號 90102099 五、發明說明(3) 修正 (2 ) 將Ca F2乾 粉 5 粘 結 劑 和 礦 化 劑 乾 式 混 拌 和 造 粒 成 A 土 , (3 ) 將 長 石 、 尚 嶺 土 石 英 和 粘 土 球 磨 濕 式 混 拌 J 噴 霧 造 粒, 陳 化 成 為 基 本 土 料 ; 及 (4) 將 A 土、 粘 結 劑 基 本 土 料 鍛 燒 高 嶺 土 、 陶 石 粒 % 和陶 瓷 色 料 乾 式 混 拌 , 造 粒 篩 分 5 陳 化 j 壓 成型 j 坯 體 乾 燥 高 溫 燒 結 而 成 最 佳 產 品 〇 於 本 發 明 氟化 鈣 污 泥 再 利 用 方 法 的 第 一 階 段 中 5 係 將 Ca F2 污 泥 於1 5 0 °C以下 ,較佳者1 00 - 1 50 °C 溫 度 下 旋 窯 乾 燥 5 缺 後 密 閉 粉 碎 , 並 篩 分 取 &lt;20ι me s h 的 粒 子 成 為Ca F2 乾 粉 〇 於 本 發 明 氟化 鈣 污 泥 再 利 用 方 法 的 第 階 段 中 5 其 中 所 用 黏 結 劑 為 含矽 鋁 及 驗 金 屬 之 化 合 物 , 如S i ( ,Al2 〇3 而 所 用 礦 化 劑為Ca&lt; CO,等 〇 於 * it *段 .中 ’ CaF〇 污 泥 J 礦 化 劑 與 黏 結 劑 經 乾式 混 拌 後 亦 經 造 粒 成 為 粒 度 &lt;20 微 米 之 粒 子 〇 於 本 發 明 氟化 鈣 污 泥 再 科 用 方 法 的 第 三 階 段 中 係 將 長 石 嶺 土 、石 英 和 粘 土 予 以 球 磨 濕 式 混 拌 , 喷 霧 造 粒 成 有9 0%粒子的粒-度&lt;50 微 米 之 粒 子 5 缺 後 陳 化 成 為 基 本 土 料 〇 於 本 發 明 氟化 鈣 污 泥 再 利 用 方 法 的 第 四 階 段 中 , 係 將 A 土 粘 結 劑 、基 本 土 料 鍛 燒 嶺 土 陶 石 粒 和 陶 瓷 色 料 予 以 乾 式 混拌 5 造 粒 j 篩 分 取 粒 度 &lt;20 微 米 之 粒 子 ’ 妙; 後 陳 化 j 用- 4 0 0噸級油壓機高壓成型, ,於1 50 °C 下 將 坯 體 乾 燥 , 再 於1, 0 0 0 - 1, 2 8 0 °C下高ί 盈燒結ί 而成最終產品 0900105901.ptc Page 5 506860 Case No. 90102099 V. Description of the invention (3) Correction (2) Dry mixing and granulation of Ca F2 dry powder 5 binder and mineralizer into A soil, (3) feldspar, Shang Lingite quartz and clay ball mill wet mixing J spray granulation, aging to become the basic soil; and (4) A clay, binder basic soil calcined kaolin, pottery grain% and ceramic color dry mixing , Granulation and sieving 5 aging j compression molding j green body drying and high temperature sintering to obtain the best product 0 in the first stage of the calcium fluoride sludge reuse method of the present invention, the 5 series will be Ca F2 sludge at 150 Below ° C, preferably 1 00-1 50 ° C, dried in a rotary kiln at 5 ° C, then closed and pulverized, and sieved &lt; 20ι me sh particles into Ca F2 dry powder. In the calcium fluoride sludge of the present invention, In the first stage of the utilization method5, the binder used is silicon-containing aluminum Metal test compounds, such as Si (, Al2 0 3, and the mineralizer used is Ca &lt; CO, etc. 0 * * * section. Medium 'CaF〇 Sludge J Mineralizer and binder after dry mixing Granulated into particles with a particle size of <20 microns. In the third stage of the calcium fluoride sludge recycling method of the present invention, feldspar clay, quartz and clay are ball-milled and wet-mixed, and spray-granulated to form Particles with a particle size of 90% &lt; 50 micron particles 5 are aged and become the basic soil material. In the fourth stage of the calcium fluoride sludge reuse method of the present invention, the A soil binder, Basic material calcined kaolinite and ceramic pigments are dry-mixed. 5 Granulation j sieving to obtain particles with a particle size of <20 microns' Miao; post-ageing j high-pressure forming with a -400 ton hydraulic press, , Drying the green body at 1 50 ° C, and then at 1, 0 0 0-1, 2 8 0 Ί C under high interference from the final sintered product ί 0

900105901.ptc 第6頁 506860 案號90102099 年月日 修正 五、發明說明(4) 根據本發明方法製成之產品主要為陶瓷產品,包括用 於下列者: 1 .陶瓷質室外舖地或牆面建材。 2.多孔質透水陶瓷建材。 本發明要用下述實施例予以闡述,但本發明不受其所 限制。 實施例 i CaF〇污泥之基本化學分析〕 取自污泥處理廠的C a F 2污泥經分析其化學組成為 泥厫 FAB8-E. FAB-6A. FAB-8AB^ FAB-8F, 13.21%. 1.65%^ 5.42%. 1.81%. Αΐ2〇3^ 3.78^ 3.06^ 4.36- 4.2^ Na2〇 1.62. 0.47^ 0.08 0.41^ κ2ο. 0.05^ 0.10. 0.14 0.04 Μ名Ο 1.27^ 2.14 0.57. 2.52^ CaFy 74.92. 86_17v 51.95, 52.07^ Ti02, 0.02- 0.04. 0.02, 0.04. F02〇3^ 0.12^ 0.38. 0.13, 0.40^ CaC03 ‘ 麵_令;j —4? 25.60^ 26.21, 燃燒失量p 5.00. 6·0〇ρ 11·0〇ρ 12.30^ 合卟 100.00^ 100.00, 100.00, 100.00, 〔CaF9污泥之前處理〕 將CaF9污泥置於1 5 0 °C以下溫度旋窯乾燥、然後密閉 粉碎'並篩分至約60微米之粉料、成為CaF9乾粉。 〔陶瓷產品組成物之調配〕900105901.ptc Page 6 506860 Case No. 90102099 Amendment V. Description of the Invention (4) The products made according to the method of the present invention are mainly ceramic products, including those used for the following: 1. Ceramic outdoor flooring or wall surface Building materials. 2. Porous permeable ceramic building materials. The invention is illustrated by the following examples, but the invention is not limited thereto. Example i Basic chemical analysis of CaF0 sludge] The chemical composition of C a F 2 sludge from a sludge treatment plant was analyzed as loach FAB8-E. FAB-6A. FAB-8AB ^ FAB-8F, 13.21 %. 1.65% ^ 5.42%. 1.81%. Αΐ2〇3 ^ 3.78 ^ 3.06 ^ 4.36- 4.2 ^ Na2〇1.62. 0.47 ^ 0.08 0.41 ^ κ2ο. 0.05 ^ 0.10. 0.14 0.04 M name 〇 1.27 ^ 2.14 0.57. 2.52 ^ CaFy 74.92. 86_17v 51.95, 52.07 ^ Ti02, 0.02- 0.04. 0.02, 0.04. F02〇3 ^ 0.12 ^ 0.38. 0.13, 0.40 ^ CaC03 'face_order; j —4? 25.60 ^ 26.21, loss of combustion p 5.00. 6 · 0〇ρ 11 · 0〇ρ 12.30 ^ Porphyrin 100.00 ^ 100.00, 100.00, 100.00, [CaF9 sludge pre-treatment] CaF9 sludge is dried in a rotary kiln at a temperature below 150 ° C, and then closed and crushed. ' And sieved to about 60 microns of powder to become CaF9 dry powder. [Preparation of ceramic product composition]

將上面所製C a F9乾粉與S ί 09,A 19 0q和C a C 0q钻結齊丨j和礦 化劑進行乾式混拌,然後造粒成為粒度&lt; 2 0微米之粒子AThe C a F9 dry powder prepared above was drilled with S ί 09, A 19 0q and C a C 0q, j and mineralizers were dry-mixed, and then granulated into particles A with a particle size &lt; 20 microns.

900105901.ptc 第7頁 506860 _案號90102099_年月日 修正 五、發明說明(5) 化 劑 進 行 乾 式 混 拌 , 缺 後 造 粒 成 為 粒 度 &lt; 2 0微米之粒子A 土 〇 將 長 石 高 嶺 土 石 英 和 粘 土 球 磨 濕 式 混 拌 , 噴 霧 造 粒 成 有9 0 °/〇粒子的粒度&lt; 5 0 微 米 之 粒 子 j 妙; 後 , 陳 化 成 為 基 本 土 料 〇 ( 陶 瓷 產 品 之 製 造 將 上 面 所 製 A 土 粘 結 劑 基 本 土 料 % 鍛 燒 領 土 陶 石 粒 和 陶 瓷 色 料 予 以 乾 式 混 拌 , 造 粒 並 篩 分 取 粒 度 &lt; 20 微 米 之 粒 子 J 缺 後 陳 化 9 用 400 噸 級 油 壓 機 壓 成 型 於1 5 0 °C下將坯體乾燥 ,再於1 ,000 -1,280 °C 下 高 溫 燒 結 而 成 最 終 產 品 〇 C 陶 瓷 產 品 之 分 析 上 面 所 製 陶 瓷 產 品 經 分 析 其 化 學 組 成 如 下 所 示 • AJL2Q3 15.61% Si02 59.39% K20 2 . 9 9 % N a9〇 2 . 2 8 °/〇 CaO 1.57% MgO 0.22% CaF2 12.17% ‘燃燒失量 5. 77% 上面所製陶瓷產品可用下面的理論分子式表之: 1 (RO,R90,CaF9) :0.56 AUO, :3.67 S i 09 依上面所製人行舖道磚陶瓷產品具有下列根據C N S - 1 3 4 3 1檢驗之特性:900105901.ptc Page 7 506860 _Case No. 90102099_Year, month, day, amendment V. Description of the invention (5) The chemical agent is dry-mixed, and granulated into particles with a particle size of <20 micrometers A after the absence of feldspar kaolin quartz Wet-mix with clay ball milling, spray granulation into particles with a particle size of 90 ° / 〇 &lt; 50 micron particles; and then ageing to become the basic soil. Basic binder of soil binder% Dry-mixed terrarium granules and ceramic pigments are granulated and sieved to obtain particles with a particle size of &lt; 20 micron J. Aging after lacking 9 Use a 400-ton hydraulic press to form The green body is dried at 150 ° C, and then sintered at a high temperature of 1,000-1,280 ° C to obtain the final product. Analysis of ceramic products The chemical composition of the ceramic products produced above is analyzed as follows As shown • AJL2Q3 15.61% Si02 59.39% K20 2.9.9% N a9〇2. 2 8 ° / 〇CaO 1.57% MgO 0.22% CaF2 12.17% 'Lost combustion 5.77% The ceramic products made above can be used in the following Theoretical molecular formula table: 1 (RO, R90, CaF9): 0.56 AUO,: 3.67 S i 09 The sidewalk paving ceramic products manufactured according to the above have the following characteristics according to CNS-1 3 4 3 1 inspection:

900105901.ptc 第8頁 506860 案號 90102099 年 曰 修正 五、發明說明(6) 0 . 5 %之吸水率; 抗折強度可達33. 1 kgf/ cm ;及 耐 酸鹼 檢 驗 * 無 反 應 〇 本 發明 氟 化 鈣 污 泥 再 利用方法 之特徵與效益 在 於 1 1 · CaF9 污 泥 於 原 產 出 廠區即予 榨乾成泥餅塊 狀· 並 以 防封 袋 包 裝 , 防 止 貯存及運 輸過程造成漏 洩 污 染 0 2. 污水 處 理 廠 之Ca f2 污泥依各 廠產出量不同 而 δ又 計 成 10 0%完全再利用之添加比例使用於原料2 §己t匕' 5 故未 來 將 無 任 何 剩 餘之CaF2 污泥須做再處 理 〇 3. CaF2 污 泥 與 其 他 原 料依設計 配比調配後, 經 高 溫 固 態液 相 燒 結 可 轉 換 成非水溶 性且安定化之 陶 瓷 及 長 石等 晶 相 結 構 5 具 極穩定的 耐候性及耐化 學 性 等 特 性, 是Ca F2 污 泥 具 安全而有 效益的最終處 理 方 式 〇 4. C a F9 污 泥 經 混 拌 後 其CaF9平均含量高於60 % J : 符, 陶瓷 體 之 原 料 要 求。 5.添加CaF2污泥所成之陶瓷體其抗折強度可達3 3. 1 kg f/ cm,吸水率&lt; 1 % ,耐酸鹼性佳,而T C L P ( T o x i c i t y900105901.ptc Page 8 506860 Case No. 90102099 Amendment V. Description of the Invention (6) Water absorption of 0.5%; Flexural strength up to 33.1 kgf / cm; and Acid and alkali resistance test * No response The characteristics and benefits of inventing the reuse method of calcium fluoride sludge are: 1 1 · CaF9 sludge is squeezed into a cake-shaped cake in the original factory area · and packed in anti-seal bags to prevent leakage and pollution during storage and transportation 0 2. Ca f2 sludge of sewage treatment plant is different according to the output of each plant, and δ is counted as 10 0%. The proportion of total reuse is used for raw materials 2 § t 匕 ′ 5 So there will be no remaining CaF2 in the future The sludge must be reprocessed. 03. CaF2 sludge and other raw materials can be converted into non-water-soluble and stable crystalline phases such as ceramics and feldspar through high-temperature solid-state liquid-phase sintering after being formulated in accordance with the design ratio. 5 Very stable Weather resistance and chemical resistance, etc., is a safe and effective final treatment method for Ca F2 sludge. C a F9 sludge is mixed CaF9 than its average content of 60% J: raw material breaks, the ceramic body of the requirements. 5. The ceramic body formed by adding CaF2 sludge has a flexural strength of 3 3.1 kg f / cm, a water absorption rate <1%, good acid and alkali resistance, and T C L P (T o x i c i t y

Characteristic Leaching Procedure )毒物溶出試驗結 果有關Cr、Cu、Pb、Zn、Cd、Hg、As等含量也遠低於環保 法規(EPA )限值(1 ppm ),顯示以高溫固態液相燒結的 方逢所處理之C a F 2污泥是極具安全又一勞永逸的做法。(Characteristic Leaching Procedure) The results of the toxicant dissolution test related to the content of Cr, Cu, Pb, Zn, Cd, Hg, As, etc. are also far below the environmental protection regulations (EPA) limit (1 ppm). The treated C a F 2 sludge is a safe and once and for all approach.

900105901.ptc 第9頁 506860900105901.ptc Page 9 506860

900105901.ptc 第10頁900105901.ptc Page 10

Claims (1)

506860 _案號9Q102099_年月日__ 六、申請專利範圍 1 . 一種氟化鈣(CaF2)污泥再利用方法,其包括下列諸階段 (1 ) 將取自污泥處理廠的CaF9污泥置於150t:以下溫度 乾燥、粉碎、篩分成為CaF2乾粉; (2) 將CaF2乾粉,粘結劑和礦化劑乾式混拌和造粒成A 土, (3 ) 將長石、高嶺土、石英和粘土予以球磨麗式混拌, 喷霧造料,陳化成為基本土料;及 (4) 將A 土、粘結劑、基本土料、鍛燒高嶺土、陶石粒 、和陶瓷色料乾式混拌,造粒,篩分,陳化,高壓 成型,坏體乾燥,高溫燒結而成最佳產品。 2. 如申請專利範圍第1項之氟化鈣污泥再利用方法,其中 該污泥係以1 0 0 %處理再利用 ° 3. 一種含CaF9污泥之製品,其係用如申請專利範圍第1項 之方法所製成者。 4. 如申請專利範圍第3項之製品,其為陶瓷質室外舖地或 牆面建材,或為多孔質透水陶瓷建材。506860 _Case No. 9Q102099_Year Month Date__ VI. Application Patent Scope 1. A method for recycling calcium fluoride (CaF2) sludge, which includes the following stages (1) CaF9 sludge to be taken from a sludge treatment plant Place at 150t: dry, crush and sieve into CaF2 dry powder at the following temperature; (2) dry mix and granulate CaF2 dry powder, binder and mineralizer into A soil, (3) feldspar, kaolin, quartz and clay It is ball-milled and mixed by mixing, spraying materials, and aging to become basic soil; and (4) dry-mixing A soil, binder, basic soil, calcined kaolin, pottery grain, and ceramic color. , Granulation, sieving, aging, high pressure forming, bad body drying, high temperature sintering into the best product. 2. The calcium fluoride sludge reuse method as described in item 1 of the scope of patent application, wherein the sludge is treated and reused at 100% ° 3. A product containing CaF9 sludge, which is used as described in the patent application scope Produced by the method of item 1. 4. If the product in the scope of application for item 3 of the patent is ceramic outdoor flooring or wall building material, or porous water-permeable ceramic building material. 900105901.ptc 第11頁900105901.ptc Page 11
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI400134B (en) * 2009-10-19 2013-07-01 Univ Nat United Method for fabricating light aggregate using porcelain tile sludge and reservoir sediment
TWI610728B (en) * 2016-04-22 2018-01-11 林士凱 A calcium fluoride sludge recycling system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI400134B (en) * 2009-10-19 2013-07-01 Univ Nat United Method for fabricating light aggregate using porcelain tile sludge and reservoir sediment
TWI610728B (en) * 2016-04-22 2018-01-11 林士凱 A calcium fluoride sludge recycling system

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