TWI490173B - Method for recovering waste silicon waste from cutting oil - Google Patents

Method for recovering waste silicon waste from cutting oil Download PDF

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TWI490173B
TWI490173B TW102140662A TW102140662A TWI490173B TW I490173 B TWI490173 B TW I490173B TW 102140662 A TW102140662 A TW 102140662A TW 102140662 A TW102140662 A TW 102140662A TW I490173 B TWI490173 B TW I490173B
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cutting oil
waste
sodium citrate
oil
carbide
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TW201518217A (en
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Univ Nat Cheng Kung
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含切削油廢矽泥資源回收之方法 Method for recovering waste mud resources from cutting oil

本發明是有關於一種廢棄物資源回收方法,特別是有關於從含切削油廢矽泥回收碳化矽、矽酸鈉及切削油之方法。 The invention relates to a method for recovering waste resources, in particular to a method for recovering tantalum carbide, sodium citrate and cutting oil from waste mud containing cutting oil.

矽晶片之製造過程中包含最初長晶、研磨、拋光、清洗及切片等相關步驟,而廢矽泥之主要來自切片過程。目前矽晶片切片之主要技術為多線式線鋸切割技術。此技術主要是利用金屬切割線(含銅鐵成分)與一種混合了碳化矽和切削油的油性研磨液來切削矽晶棒,此研磨液可以用來帶走切削過程中所產生的熱,並將被切削掉之矽晶片碎屑帶走,此含碳化矽、切削油、矽晶片碎屑與少量銅、鐵雜質之物質即為含切削油廢矽泥。 The manufacturing process of the germanium wafer includes the steps of initial crystal growth, grinding, polishing, cleaning and slicing, and the waste mud is mainly from the slicing process. At present, the main technology of wafer slicing is multi-wire wire saw cutting technology. This technology mainly uses a metal cutting line (containing copper and iron) and an oily slurry mixed with tantalum carbide and cutting oil to cut the crystal rod, which can be used to take away the heat generated during the cutting process, and The chip crumb that is cut off is taken away. The material containing tantalum carbide, cutting oil, crucible chip crumb and a small amount of copper and iron impurities is a waste mud containing cutting oil.

目前業界對於含切削油廢矽泥之資源回收,其中就切削油與固體(含矽成份+碳化矽+少量銅、鐵雜質)分離方法主要包括: At present, the industry is responsible for the recovery of resources containing cutting oil waste mud, among which the separation method of cutting oil and solid (containing strontium component + strontium carbide + small amount of copper, iron impurities) mainly includes:

1.過濾法:係以固液分離技術進行,而固液分離技術又大多使用壓濾技術(利用壓力過濾)。 1. Filtration method: It is carried out by solid-liquid separation technology, and most of the solid-liquid separation technology uses pressure filtration technology (using pressure filtration).

2.蒸餾法,加熱含油廢矽泥至切削油蒸發,及可得到無油矽泥,冷卻其氣化切削油,即可回收切削油。 2. Distillation method, heating oily waste mud to the cutting oil to evaporate, and obtaining oil-free mud, cooling the gasification cutting oil, and recovering the cutting oil.

3.滲透蒸發法:在溶液擴散至濾膜時,蒸發其濾液,以達到固液分離之目的。 3. Pervaporation method: When the solution is diffused to the filter membrane, the filtrate is evaporated to achieve the purpose of solid-liquid separation.

而就該含矽成份與碳化矽再進一步之分離方法則主要有: Further, the separation method of the antimony component and the niobium carbide is mainly as follows:

1.重力法:利用矽與碳化矽密度之差異,而形成不同的沉降速度 ,根據兩者沉降速度設計回收方法。 1. Gravity method: using the difference between the density of tantalum and tantalum carbide to form different sedimentation speeds According to the sedimentation speed of the two, the recycling method is designed.

2.浮選法:矽自身具有疏水性或經浮選藥劑作用增強疏水性,讓矽可在液-氣或水-油的界面發生聚集以收集回收。 2. Flotation method: The crucible itself has hydrophobicity or enhances hydrophobicity by the action of flotation agent, so that the crucible can be aggregated at the liquid-gas or water-oil interface to collect and recover.

3.電泳法:利用溶液中帶有不同量的電荷的陽離子或陰離子,在外加電場中以不同的遷移速度向電極移動,而達到分離目的的分析方法。 3. Electrophoresis method: Analytical method for separating the cation or anion with different amounts of charge in the solution and moving to the electrode at different migration speeds in an applied electric field.

4.溶媒萃取法:利用粉體表面親疏水性質的作用力並配合重力與粒子界面之靜電力來進行分離。 4. Solvent extraction method: The separation force is carried out by utilizing the force of the hydrophobic and hydrophobic nature of the powder surface and the electrostatic force of the gravity and particle interface.

而就前述之過濾過程中,經常可以發現,對於含油廢矽泥,由於含切削油廢矽泥中之矽成份固體之顆粒粒徑十分細小(0.4μm~8μm),因此在過濾之過程,矽成份容易卡在濾布上,而造成阻塞及過濾困難,並且使得後續之過濾效果不佳。且壓濾後所得之含有碳化矽與矽混合粉末固體,因粒徑細小兩者不易分離,以致無法回收再利用。 In the above filtration process, it is often found that for the oily waste mud, since the particle size of the solid component of the solid waste containing the cutting oil is very small (0.4 μm to 8 μm), during the filtration process, The components are easily stuck on the filter cloth, which causes blocking and filtration difficulties, and makes the subsequent filtration effect poor. Further, the powder solid obtained by pressure filtration and containing cerium carbide and cerium is difficult to separate due to the small particle size, so that it cannot be recycled.

此外,經查此類相關聯之先前技術,如台灣方面之專利申請案號:099118261,主要是針對碳化矽粉之回收及純化方法,其步驟係對含矽砂漿進行初步過濾,並將其加熱以去除殘液;再將其置於鹼性溶液中,使鹼液溶蝕碳化矽/矽混合物中的矽;將其鹼液去除後,以獲得經純化後之碳化矽。然而此先前技術其主要針對碳化矽之粉體純化研究,且並無發現有對於回收切削油有進一步之技術呈現。 In addition, the related prior art, such as the Taiwan patent application number: 099118261, is mainly for the recovery and purification of tantalum carbide powder, the steps of which are to initially filter and heat the mortar containing mortar. To remove the residual liquid; then, it is placed in an alkaline solution, and the alkali solution is used to dissolve the cerium in the cerium carbide/cerium mixture; after the lye is removed, the purified cerium carbide is obtained. However, this prior art is mainly directed to the powder purification study of tantalum carbide, and no further technical presentation for the recovery of the cutting oil has been found.

另台灣專利申請案號:099118266,主要利用過濾及加熱去除含矽砂漿去除液體,再將其碳化矽/矽混合物加入一液態介質中攪拌並靜置,可獲得沉澱之碳化矽/矽混合物及懸浮有矽之液態介質,將其懸浮有矽之液態介質純化可得矽粉;另一回收矽之方法 為,將去除殘液後之碳化矽/矽混合物固液分離,並置於液鹼性溶液中,得一溶有矽之鹼性溶液,自該鹼性溶液中在製一含矽產物。而由該先前技術並無發現回收切削油有進一步之技術呈現。 Another Taiwan patent application number: 099118266, mainly using filtration and heating to remove the mortar containing mortar to remove the liquid, and then adding the carbonized ruthenium / ruthenium mixture to a liquid medium, stirring and standing, to obtain a precipitated carbonized ruthenium / ruthenium mixture and suspension A liquid medium having a hydrazine, which is obtained by purifying a liquid medium suspended in hydrazine to obtain bismuth powder; another method for recovering hydrazine Therefore, the carbonized ruthenium/ruthenium mixture after removing the residual liquid is solid-liquid separated and placed in a liquid alkaline solution to obtain an alkaline solution in which ruthenium is dissolved, and a ruthenium-containing product is prepared from the alkaline solution. Further technical presentations of recovered cutting oil have not been found by this prior art.

另台灣專利申請案號:096112970,其主要利用酸洗去除矽泥中金屬物質,再以高溫使矽與碳化矽分離,藉以回收其中之矽。其回收流程中只回收矽泥中之矽,並無回收碳化矽及廢液。 Another Taiwan patent application number: 096112970, which mainly uses acid washing to remove metal substances in the mud, and then separates the barium from the barium carbide at a high temperature to recover the crucible therein. In the recycling process, only the mash in the mud is recovered, and no carbonized bismuth and waste liquid are recovered.

另台灣專利申請案號:098115605,此專利係利用粒子相轉移法,也就是透過多次靜置、離心及乾燥等步驟,以獲得矽粉。此專利係利用粒子相轉移法,此方法沉降速度依靠離心機轉速,若是大量回收時,可能耗時又耗能量。 Another Taiwan patent application number: 098115605, this patent uses the particle phase transfer method, that is, through multiple steps of standing, centrifuging and drying to obtain tantalum powder. This patent utilizes a particle phase transfer method in which the settling speed depends on the speed of the centrifuge, which can be time consuming and energy intensive if recovered in large quantities.

另台灣專利申請案號:095150091,其主要步驟係先以丙酮清洗並離心處理,在加入酸洗劑除鐵,接著以純水與丙酮清洗再清洗一次並乾燥,接續添加比重介於矽與碳化矽之間的浮選劑,經過離心後乾燥,即可得到矽。其回收項目只有矽,無法達到全回收之目的。 Another Taiwan patent application number: 095150091, the main steps are first washed with acetone and centrifuged, added with pickling agent to remove iron, then washed with pure water and acetone and then washed once and dried, and then added specific gravity between 矽 and carbonization The flotation agent between the crucibles is dried by centrifugation to obtain a crucible. The recycling project is only flawed and cannot achieve the purpose of full recycling.

另台灣專利申請案號:099133041,其主要回收對象為切削矽漿中之切削油,其流程為,將切削矽漿置於貧氧狀態、溫度為150~350℃至其切削油氣化,將該氣化切削油收集並冷卻,及可得到切削矽漿之切削油。其主要回收對象為切削矽漿中之切削油,其經過高溫加熱後之矽泥可能變質,造成無法回收。 Another Taiwan patent application number: 099133041, the main object of which is the cutting oil in the cutting slurry, the flow is that the cutting slurry is placed in an oxygen-poor state, the temperature is 150~350 °C until the cutting oil and gas, the The gasification cutting oil is collected and cooled, and a cutting oil for cutting the slurry is obtained. The main object of the recovery is the cutting oil in the cutting slurry, which may deteriorate after being heated at a high temperature, resulting in failure to recover.

有鑑於先前技術,尤其是過濾法之問題,本發明之目的就是在提供一種從含切削油廢矽泥回收碳化矽、矽酸鈉及切削油之方法,且提供一種方法以解決含切削油廢矽泥過濾過程中因矽顆粒過於 細小,以致造成切削油不易過濾且過濾後含有碳化矽之固體與矽不易分離回收之問題。為此,根據本發明的目的,本發明人設置一種含切削油廢矽泥資源回收之方法,其步驟至少包括:1.將含切削油廢矽泥混合均勻;2.將該含切削油廢矽泥加入氫氧化鈉,令該含切削油廢矽泥:氫氧化鈉體積比例為1:1至1:10混合與震盪,藉該氫氧化鈉對該含切削油廢矽泥中之矽成份溶解而成矽酸鈉溶液而可供其容易通過濾網;以令形成混有矽酸鈉溶液、含有碳化矽之固體與切削油;3.令該矽酸鈉溶液與切削油通過濾網;而令該碳化矽濾阻於網外,取得該含有碳化矽之固體;4.將濾得之矽酸鈉溶液與切削油靜置,因兩者不互溶以及比重差而產生分層,上層為含熱值之切削油,下層為矽酸鈉溶液;5.在70℃~90℃對該下層矽酸鈉溶液進行晶析,得到矽酸鈉固體;藉由本發明之方法,可大大減少步驟、處理時間及藥品消耗,且利用過濾前將該含切削油廢矽泥加入氫氧化鈉,藉氫氧化鈉對該含切削油廢矽泥中之矽成份溶解而成矽酸鈉溶液而可供其容易通過濾網,降低後續之過濾作業中,矽成份對於濾網之卡阻所形成之阻塞及過濾困難。並且有效的回收碳化矽、矽酸鈉及切削油。且利用本發明之方法,除了可避免含切削油廢矽泥任意丟棄及對人體與環境產生危害之外,同時亦可達到其所含的有價資源永續循環之功效。 In view of the problems of the prior art, especially the filtration method, the object of the present invention is to provide a method for recovering tantalum carbide, sodium citrate and cutting oil from waste mud containing cutting oil, and providing a method for solving waste containing cutting oil. In the mud filtration process, the particles are too It is so small that the cutting oil is not easily filtered and the solids containing tantalum carbide after filtration are difficult to separate and recover. To this end, according to the object of the present invention, the inventors set a method for recovering waste mud resources containing cutting oil, the steps of which at least include: 1. mixing the waste oil containing the cutting oil uniformly; 2. scraping the cutting oil Adding sodium hydroxide to the mud, so that the cutting oil contains waste mud: the volume ratio of sodium hydroxide is 1:1 to 1:10 mixed and oscillated, and the sodium hydroxide is used in the waste oil containing the cutting oil. Dissolved into a sodium citrate solution for easy passage through the sieve; to form a solid solution containing a sodium citrate solution, containing barium carbide and a cutting oil; 3. passing the sodium citrate solution and cutting oil through the filter; And the carbonized ruthenium is filtered outside the mesh to obtain the solid containing cerium carbide; 4. The filtered sodium citrate solution and the cutting oil are allowed to stand, because the two are not mutually soluble and the specific gravity is poor, and the upper layer is The cutting oil with calorific value, the lower layer is sodium citrate solution; 5. The crystallization of the lower layer of sodium citrate solution at 70 ° C ~ 90 ° C to obtain sodium citrate solid; by the method of the invention, the steps can be greatly reduced Processing time and drug consumption, and using the cutting oil to waste mud before filtration Sodium hydroxide, which dissolves the bismuth component in the waste oil containing cutting oil by sodium hydroxide to form a sodium citrate solution, which can be easily passed through the filter screen to reduce the subsequent filtration operation, and the 矽 component for the filter card It is difficult to block and filter the resistance. And effective recovery of tantalum carbide, sodium citrate and cutting oil. Moreover, by using the method of the invention, in addition to avoiding the discarding of the waste oil containing the cutting oil and causing harm to the human body and the environment, the effect of the sustainable circulation of the valuable resources contained therein can also be achieved.

第一圖係為本發明實施步驟流程圖。 The first figure is a flow chart of the steps of the implementation of the present invention.

第二圖係為本發明所使用之含切削油廢矽泥外觀。 The second figure is the appearance of the waste oil containing cutting oil used in the present invention.

第三圖係為利用本發明方法所得之切削油外觀。 The third figure is the appearance of the cutting oil obtained by the method of the present invention.

第四圖係為利用本發明方法所得之矽酸鈉外觀。 The fourth figure is the appearance of sodium citrate obtained by the method of the present invention.

第五圖係為利用本發明方法所得之碳化矽外觀。 The fifth figure is the appearance of niobium carbide obtained by the method of the present invention.

以下藉由圖式之輔助,說明本發明之技術內容、特色與實施例,俾使貴審對於本案有進一步之瞭解。 The technical content, features and embodiments of the present invention will be described below with the aid of the drawings, so that you can have a better understanding of the case.

請參閱第一圖,其係為本發明之含切削油廢矽泥資源回收之方法的步驟流程圖。 Please refer to the first figure, which is a flow chart of the steps of the method for recovering waste oil resources of cutting oil of the present invention.

第一圖中,本發明之方法可包含下列步驟: In the first figure, the method of the present invention may comprise the following steps:

步驟1:將含切削油廢矽泥混合均勻(其外觀如第二圖所示)。 Step 1: Mix the waste oil containing cutting oil evenly (the appearance is as shown in the second figure).

步驟2:將該含切削油廢矽泥加入1N~6N濃度之氫氧化鈉,令該含切削油廢矽泥:氫氧化鈉體積比例為1:1至1:0混合後,進行超音波震盪1-4hr,藉該氫氧化鈉對該含切削油廢矽泥中之矽成份溶解而成矽酸鈉溶液而可供其容易通過濾網;以令形成混有矽酸鈉溶液、含有碳化矽之固體與切削油; Step 2: Adding the cutting oil waste mud to the sodium hydroxide of 1N~6N concentration, so that the cutting oil waste sludge: sodium hydroxide volume ratio is 1:1 to 1:0 mixed, then ultrasonic vibration 1-4hr, by using the sodium hydroxide to dissolve the cerium component in the cutting oil waste mud to form a sodium citrate solution, which can be easily passed through the sieve; so as to form a mixed sodium citrate solution containing strontium carbide Solid and cutting oil;

步驟3:過濾,令該矽酸鈉溶液與切削油通過濾網;而令該碳化矽濾阻於網外,取得該含有碳化矽之固體; Step 3: filtering, passing the sodium citrate solution and the cutting oil through the sieve; and filtering the carbonized ruthenium outside the mesh to obtain the solid containing the cerium carbide;

步驟4:將濾得之矽酸鈉溶液與切削油靜置,因兩者不互溶以及比重差而產生分層,上層為含熱值之切削油(如第三圖),下層為矽酸鈉溶液。該上層切削油可做為輔助燃料。 Step 4: The filtered sodium citrate solution and the cutting oil are allowed to stand, because the two are not mutually soluble and the specific gravity is poor, and the stratification is carried out. The upper layer is the cutting oil with calorific value (as shown in the third figure), and the lower layer is sodium citrate. Solution. The upper cutting oil can be used as an auxiliary fuel.

步驟5:在70℃~90℃對該下層矽酸鈉溶液進行1-4hr之晶析,得到矽酸鈉固體(如第四圖)。 Step 5: The lower sodium citrate solution is subjected to crystallization at 70 ° C to 90 ° C for 1-4 hr to obtain a sodium citrate solid (as shown in the fourth figure).

此外,本發明更可以將前述所濾阻之含有碳化矽之固體,加入1N~6N濃度之硫酸與濃度30%之過氧化氫,令該含有碳化矽之固體:1N~6N濃度硫酸:30%之過氧化氫之比例為1(g):10(ml):0.02(ml),然後進行1-4hr靜置,藉以溶解而去除銅、鐵雜質固體,得到高純度之碳化矽(如第五圖)。此高純度之碳化矽或許仍有少量之矽成份,本發明方案中較佳實施例,可以更進一步再以氫氧化鈉加入此高純度之碳化矽,以溶解其中之矽成份,以得到更為純化之碳化矽固體。依此類推,可以再為純化之次數不侷限。 In addition, in the present invention, the solid solution containing barium carbide can be added with 1N~6N sulfuric acid and 30% hydrogen peroxide, so that the solid containing barium carbide: 1N~6N concentration sulfuric acid: 30% The ratio of hydrogen peroxide is 1 (g): 10 (ml): 0.02 (ml), and then allowed to stand for 1-4 hr, thereby dissolving to remove copper and iron impurity solids, thereby obtaining high-purity carbonized ruthenium (such as the fifth). Figure). The high-purity niobium carbide may still have a small amount of antimony component. In the preferred embodiment of the present invention, the high-purity niobium carbide may be further added with sodium hydroxide to dissolve the niobium component therein to obtain more Purified tantalum carbide solid. By analogy, the number of times of purification can be further limited.

綜上所述,本發明確實符合產業利用性,且未於申請前見於刊物或公開使用,亦未為公眾所知悉,且具有非顯而易知性,符合可專利之要件,爰依法提出專利申請。惟上述所陳,為本發明產業上一較佳實施例,舉凡依本發明申請專利範圍所作之均等變化,皆屬本案訴求標的之範疇。 In summary, the present invention is indeed in line with industrial utilization, and is not found in publications or publicly used before application, nor is it known to the public, and has non-obvious knowledge, conforms to patentable requirements, and patents are filed according to law. . However, the above description is a preferred embodiment of the industry of the present invention, and all the equivalent changes made by the scope of the patent application of the present invention are within the scope of the claim.

Claims (2)

一種含切削油廢矽泥資源回收之方法,步驟至少包括:1.將含切削油廢矽泥混合均勻;2.將該含切削油廢矽泥加入氫氧化鈉,令該含切削油廢矽泥:氫氧化鈉體積比例為1:1至1:10混合與震盪,該震盪為進行超音波震盪1-4h,藉該氫氧化鈉對該含切削油廢矽泥中之矽成份溶解;以令形成混有矽酸鈉溶液、含有碳化矽之固體與切削油;其中該氫氧化鈉濃度為1N~6N;3.令該矽酸鈉溶液與切削油通過濾網;而令該碳化矽濾阻於網外,取得該含有碳化矽之固體;4.將濾得之矽酸鈉溶液與切削油靜置,因兩者不互溶以及比重差而產生分層,上層為含熱值之切削油,下層為矽酸鈉溶液;5.在70℃~90℃對該下層矽酸鈉溶液進行晶析,得到矽酸鈉固體。 A method for recovering waste mud resources of cutting oil, the steps comprising at least: 1. mixing the waste oil containing the cutting oil uniformly; 2. adding the waste oil containing the cutting oil to the sodium hydroxide, and depleting the cutting oil. Mud: the volume ratio of sodium hydroxide is 1:1 to 1:10 mixing and oscillating, and the oscillation is for ultrasonic oscillating 1-4h, and the cerium component in the cutting oil waste mud is dissolved by the sodium hydroxide; Forming a solid solution of sodium citrate mixed with barium carbide and cutting oil; wherein the concentration of the sodium hydroxide is 1N~6N; 3. passing the sodium citrate solution and the cutting oil through the filter; Obtaining the solid containing carbonized ruthenium outside the net; 4. The filtered sodium citrate solution and the cutting oil are allowed to stand, because the two are not mutually soluble and the specific gravity is poor, and the upper layer is the cutting oil with calorific value. The lower layer is a sodium citrate solution; 5. The lower layer of sodium citrate solution is crystallized at 70 ° C to 90 ° C to obtain a sodium citrate solid. 如申請專利範圍第1項所述之含切削油廢矽泥資源回收之方法,步驟3所濾阻之含有碳化矽之固體,加入1N~6N濃度之硫酸與30%之過氧化氫,令該含有碳化矽之固體:1N~6N濃度硫酸:30%之過氧化氫之比例為1(g):10(ml):0.02(ml),藉以溶解而去除銅、鐵雜質固體,得到高純度之碳化矽。 For the method for recovering the waste oil containing cutting oil according to the first aspect of the patent application, the solid containing the niobium carbide in the step 3 is added with 1% to 6N sulfuric acid and 30% hydrogen peroxide. Solid containing cerium carbide: 1N~6N concentration sulfuric acid: 30% hydrogen peroxide ratio is 1 (g): 10 (ml): 0.02 (ml), thereby dissolving and removing copper and iron impurity solids to obtain high purity Carbide.
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