TWM457723U - Sorting treatment device of silicon wafer cutting sludge - Google Patents

Sorting treatment device of silicon wafer cutting sludge Download PDF

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Publication number
TWM457723U
TWM457723U TW102202178U TW102202178U TWM457723U TW M457723 U TWM457723 U TW M457723U TW 102202178 U TW102202178 U TW 102202178U TW 102202178 U TW102202178 U TW 102202178U TW M457723 U TWM457723 U TW M457723U
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flotation
filter press
tank
machine
concentrator
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TW102202178U
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Chinese (zh)
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ya-min Xie
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ya-min Xie
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Description

矽晶圓切削污泥的分選處理裝置 分Processing device for wafer cutting sludge

本創作係關於一種矽晶圓切削污泥的分選處理裝置,特別係指可使矽晶圓切削污泥經過分選處理裝置,可回收污泥中的矽及碳化矽等產品,可避免污泥對環境所造成之負荷、污染等問題,達到環保、資源再生與經濟等多重效益。 This creation is about a sorting and processing device for 矽 wafer cutting sludge, especially for the 矽 wafer cutting sludge passing through a sorting treatment device, which can recover bismuth and strontium carbide in the sludge, and can avoid contamination. The problems caused by mud on the environment, such as load and pollution, achieve multiple benefits such as environmental protection, resource regeneration and economy.

按,矽晶圓製造業使用的切削油係屬於磨料切削用之水溶性切削油,廢棄的水溶性切削油,由於污染濃度非常高,直接排入廢水處理場,將造成廢水處理系統負荷大增,影響處理水水質,多數工廠會將廢液予以單獨收集貯存或委託廢棄物代處理業處理,有些工廠採用蒸發濃縮後再委外處理方式,可將切削油濃縮至原有體積的1/10以下。 According to the cutting oil used in the wafer manufacturing industry, it is a water-soluble cutting oil for abrasive cutting. The waste water-soluble cutting oil is discharged into the wastewater treatment plant due to the high concentration of pollution, which will increase the load on the wastewater treatment system. Influencing the quality of treated water, most factories will collect and store the waste liquid separately or entrust the waste treatment industry. Some factories use evaporation and concentration and then the external treatment method, which can concentrate the cutting oil to 1/10 of the original volume. the following.

一般將去除切削油的金屬粉屑、油脂及其他雜質之處理技術稱為「過濾」,但事實上應細分為「過濾」和「分離」兩種不同的處理技術,廢切削油過濾與分離之設備,分離技術是利用欲分離物的物理特性(如比重不同),來去除切削油中的雜質,過濾技術則是利用濾材來濾除切削油的固態雜質,分離技術中最簡易的方法,乃是利用收集切削油的貯存槽做為固體雜質之沉澱槽,讓經加工機器流出含粉屑的切削油, 在未被重複流回機器前,在貯存槽中利用靜置沉澱方式,讓切削油中大顆粒的粉屑沉澱於槽底,再以人工方式剷除,或利用貯槽內置放可提式濾網收集籃以收集清除沉澱之粉屑。 Generally, the treatment technology for removing metal dust, grease and other impurities from cutting oil is called "filtration", but in fact it should be subdivided into two different treatment technologies: "filtration" and "separation". Waste cutting oil filtration and separation Equipment, separation technology is to use the physical properties of the separation object (such as different specific gravity) to remove impurities in the cutting oil, the filtration technology is to use the filter material to filter the solid impurities of the cutting oil, the easiest method in the separation technology, The storage tank for collecting the cutting oil is used as a sedimentation tank for solid impurities, and the processing machine discharges the cutting oil containing the powder. Before being returned to the machine without repeated flow, the static sedimentation method is used in the storage tank to precipitate the large particles of the cutting oil in the bottom of the tank, and then manually removed, or collected by using a removable filter in the storage tank. The basket is used to collect and remove the sediment.

由於切削油中含有氣泡、油滴及其他化學物質使得粉屑的沉降速度減緩,一般孔徑大於15微米的粒子在7~10分鐘可以沉降,但是小於15微米的金屬粉屑則需更長的時間才能沉降,甚至無法利用自然重力沉澱去除,因此,現有水力分離器(Hydro-cyclons)、遠心分離機(Screw Decanter Centrifuge)及磁力分離機等設備,水力分離器乃是利用離心力,使比重較大的粉屑等物質從比重較小的切削油中分離去除,藉由切削油流入分離機時的流速產生旋轉渦流,使切削油中的金屬粒子因離心力作用被拋移到裝置外緣,且外緣的渦流方向向下,使得金屬粒子被引減至分離機底部,潔淨的切削油則會由分離機的中央部份向頂部湧出,因分離機的渦流速度取決於切削油進流速度,所以進流速度愈快則分離效果愈佳,遠心分離機是用來分離二種以上的不同粉屑,同樣利用比重不同的性質進行不同轉速的分離,產生的離心力,就可以將固體與液體分離出來。 Due to the inclusion of bubbles, oil droplets and other chemicals in the cutting oil, the sedimentation speed of the dust is slowed down. Generally, particles with a pore diameter of more than 15 microns can settle in 7 to 10 minutes, but metal dust of less than 15 microns takes longer. It can be settled or even removed by natural gravity sedimentation. Therefore, existing hydraulic separators (Hydro-cyclons), telecentric separators (Screw Decanter Centrifuge) and magnetic separators, etc., hydraulic separators use centrifugal force to make the specific gravity larger. The powder and the like are separated and removed from the cutting oil having a small specific gravity, and the swirling vortex is generated by the flow velocity when the cutting oil flows into the separator, so that the metal particles in the cutting oil are thrown to the outer edge of the device by the centrifugal force, and The vortex direction of the edge is downward, so that the metal particles are led to the bottom of the separator, and the clean cutting oil will flow from the central part of the separator to the top, because the vortex speed of the separator depends on the cutting oil inflow speed, so The faster the inflow velocity, the better the separation effect. The telecentric separator is used to separate two or more different types of dust, and also uses different specific gravity. Separating different speeds, centrifugal force, can be separated from the liquid out of the solid.

矽晶圓片製造業所產生的無機污泥雖然含有Si及SiC,但目前國內再利用實績屬萌芽階段,幾乎業者均委由清除處理機構採掩埋處理,但掩埋處理方式易對環境造成污染,且無法資源再生利用。 Although the inorganic sludge produced by the wafer manufacturing industry contains Si and SiC, the current domestic recycling performance is in its infancy, and almost all of them are disposed of by the removal and disposal mechanism, but the buried treatment method is easy to pollute the environment. And resources cannot be recycled.

本創作係可解決習知矽晶圓廢棄污泥之處理方式無法有效改善污泥對環境所造成之負荷及污染等問題。 This creation department can solve the problem that the treatment of the waste sludge of the wafer can not effectively improve the load and pollution caused by the sludge to the environment.

本創作之目的係在提供一種矽晶圓切削污泥的分選處理裝置,可以回收矽與碳化矽之產品,可以作為陶瓷原料或二次工業利用,並可避免矽泥對環境所造成之負荷、污染等問題,達到環保、資源再生與經濟等多重效益。 The purpose of this creation is to provide a sorting processing device for 矽 wafer cutting sludge, which can recover bismuth and tantalum carbide products, can be used as ceramic raw materials or secondary industries, and can avoid the load caused by muddy soil. , pollution and other issues, to achieve environmental protection, resource regeneration and economic and other benefits.

矽晶圓切削污泥的污泥組成物是以碳化矽與矽為主,依據矽顆粒表面的疏水性質、以及在控制碳化矽顆粒凝聚的酸性pH值下,以浮選法分離兩種固體成分,從浮礦中取出矽,從沉礦中取出碳化矽等產品。 The sludge composition of the wafer cutting sludge is mainly composed of tantalum carbide and niobium. According to the hydrophobic nature of the surface of the niobium particles and the acidic pH value controlling the condensation of niobium carbide particles, the two solid components are separated by flotation. Remove the sputum from the floating ore and remove the products such as strontium carbide from the sinking ore.

本創作之矽晶圓切削污泥的分選處理裝置,係由調整槽、加藥機、粗選浮選機、浮礦精選浮選機、沉礦精選浮選機、第一濃縮機、第二濃縮機、第一壓濾機、第二壓濾機、第三壓濾機、第四壓濾機、第一攪拌槽、第二攪拌槽、第三攪拌槽、第四攪拌槽及第一乾燥機、第二乾燥機所構成,其中:該調整槽,係供暫存矽晶圓切削污泥調漿及加藥之用;該加藥機,係與該調整槽連接,該加藥機係於該調整槽中的污泥加入調整劑、捕集劑、起泡劑、水,使矽顆粒的表面與調整劑反應,強化表面疏水性,利於捕集,同時利用調整劑控制礦漿pH值,利於碳化矽凝聚沉降;該粗選浮選機,係與該調整槽連接,藉由該粗選浮選機將污泥予以分選為浮礦與沉礦;該浮礦精選浮選機,係與該粗選浮選機連接,將該粗選浮選 機內污泥中的浮礦輸送至該浮礦精選浮選機內進行浮選;該第一濃縮機,係與該浮礦精選浮選機連接,該第一濃縮機與該浮礦精選浮選機之間設有一第一馬達,該第一馬達係將該浮礦精選浮選機內的浮礦加壓輸送至該第一濃縮機內,藉由該第一濃縮機將浮礦漿予以濃縮,使其固液分離,固體礦漿係沉澱於該第一濃縮機之底部,液體則位於固體礦漿之上方,該液體則由一第一導水管輸送至該調整槽內;該第一攪拌槽,係與該第一濃縮機連接,該第一攪拌槽係供將濃縮後的浮礦漿予以攪拌;該第一壓濾機,係與該第一攪拌槽連接,該第一壓濾機與該第一攪拌槽之間設有一第二馬達,藉由該第二馬達將該第一攪拌槽內之浮礦漿予以加壓送至該第一壓濾機內,該第一壓濾機係將固液分離為小顆粒的含矽固體與濾液,該第一壓濾機內之液體則由一第二導水管輸送至該調整槽內;該第二攪拌槽,係與該第一壓濾機連接,藉由該第二攪拌槽將浮礦漿再次注水攪拌洗淨,形成浮礦精礦;該第二壓濾機,係與該第二攪拌槽連接,該第二壓濾機設有廢水排出口,藉由該第二壓濾機將該浮礦精礦再次固液分離,廢水則由該廢水排出口排放;該第一乾燥機,係與該第二壓濾機連接,該第一乾燥機係將該浮礦精礦予以乾燥,從浮礦精礦中取出矽產品;該沉礦精選浮選機,係與該粗選浮選機連接,將該粗選浮選機內污泥中的沉礦輸送至該沉礦精選浮選機內進行浮選;該第二濃縮機,係與該沉礦精選浮選機連接,該第二濃縮機 與該沉礦精選浮選機之間設有一第三馬達,該第三馬達係將該沉礦精選浮選機內的沉礦加壓輸送至該第二濃縮機內,藉由該第二濃縮機將沉礦漿予以濃縮,使其固液分離,固體礦漿係沉澱於該第二濃縮機之底部,液體則位於固體礦漿之上方,該液體則由一第三導水管輸送至該調整槽內;該第三攪拌槽,係與該第二濃縮機連接,該第三攪拌槽係供將濃縮後的沉礦漿予以攪拌;該第三壓濾機,係與該第三攪拌槽連接,該第三壓濾機與該第三攪拌槽之間設有一第四馬達,藉由該第四馬達將該第三攪拌槽內之沉礦漿予以加壓送至該第三壓濾機內,該第三壓濾機係將固液分離為大顆粒的含碳化矽固體與濾液,該第三壓濾機內之液體則由一第四導水管輸送至該調整槽內;該第四攪拌槽,係與該第三壓濾機連接,藉由該第四攪拌槽將沉礦漿再次注水攪拌洗淨,形成沉礦精礦;該第四壓濾機,係與該第四攪拌槽連接,該第四壓濾機設有廢水排出口,藉由該第四壓濾機將該沉礦精礦再次固液分離,廢水則由該廢水排出口排放;該第二乾燥機,係與該第四壓濾機連接,該第二乾燥機係將該沉礦精礦予以乾燥,從沉礦精礦中取出碳化矽產品。 The separation processing device for the wafer cutting sludge of the present invention is an adjustment tank, a dosing machine, a rough selection flotation machine, a flotation flotation machine, a sinking flotation machine, a first thickener, and a first a second concentrator, a first filter press, a second filter press, a third filter press, a fourth filter press, a first agitation tank, a second agitation tank, a third agitation tank, a fourth agitation tank, and a first The drying machine and the second dryer are configured, wherein: the adjusting tank is used for temporary storage, wafer cutting sludge slurrying and dosing; the dosing machine is connected with the adjusting tank, the dosing machine The sludge in the adjustment tank is added with a regulator, a trapping agent, a foaming agent, and water to react the surface of the cerium particles with the adjusting agent to strengthen the surface hydrophobicity, which is advantageous for trapping, and at the same time, the adjusting agent is used to control the pH value of the slurry. Condensation and sedimentation of the niobium carbide; the rough flotation machine is connected to the adjustment tank, and the sludge is sorted into a flotation mine and a sinking ore by the rough flotation machine; the flotation flotation machine is selected Connected to the rough selection flotation machine, the rough selection flotation The floating ore in the sludge in the machine is sent to the flotation flotation machine for flotation; the first concentrator is connected with the flotation flotation machine, and the first concentrator and the flotation flotation are selected A first motor is arranged between the machines, and the first motor is used to pressurize the floating ore in the flotation flotation machine to the first concentrator, and the floating syrup is concentrated by the first concentrator , the solid-liquid separation is carried out, the solid slurry is deposited at the bottom of the first concentrator, and the liquid is located above the solid slurry, and the liquid is transported into the adjustment tank by a first water conduit; the first agitation tank, And the first agitating tank is configured to stir the concentrated floating slurry; the first filter press is connected to the first agitating tank, the first filter press and the first a second motor is disposed between the stirring tanks, and the floating slurry in the first stirring tank is pressurized and sent to the first filter press by the second motor, the first filter press system is solid-liquid Separating into small particles of cerium-containing solids and filtrate, the liquid in the first filter press is from a second water conduit The second agitation tank is connected to the first filter press, and the floating slurry is refilled with water and stirred by the second agitation tank to form a flotation concentrate; the second filter press The machine is connected to the second agitating tank, and the second filter press is provided with a waste water discharge port, and the floating ore concentrate is again solid-liquid separated by the second filter press, and the waste water is discharged from the waste water discharge port. The first dryer is connected to the second filter press, the first dryer is used to dry the flotation concentrate, and the antimony product is taken out from the flotation concentrate; the sedimentation flotation machine is selected. And connecting to the rough flotation machine, conveying the sediment in the sludge in the rough flotation machine to the sinking flotation machine for flotation; the second concentrating machine is selected with the sinking Flotation machine connection, the second concentrator A third motor is disposed between the sinking and selecting flotation machine, and the third motor is used to pressurize the sinking in the sinking flotation machine to the second concentrator by the second concentrating The machine concentrates the slurry to separate the solid and liquid, the solid slurry is deposited at the bottom of the second concentrator, and the liquid is located above the solid slurry, and the liquid is transported to the adjusting tank by a third water conduit; The third agitation tank is connected to the second concentrator, the third agitation tank is for agitating the concentrated slurry; the third filter is connected to the third agitation tank, the third a fourth motor is disposed between the filter press and the third agitation tank, and the slurry in the third agitation tank is pressurized and sent to the third filter press by the fourth motor, the third pressure The filter system separates the solid liquid into large particles of cerium carbide-containing solids and filtrate, and the liquid in the third filter press is transported into the adjusting tank by a fourth water conduit; the fourth stirring tank is connected thereto The third filter press is connected, and the sinking slurry is refilled with water and stirred by the fourth stirring tank. a sedimentation concentrate; the fourth filter press is connected to the fourth agitation tank, the fourth filter press is provided with a waste water discharge port, and the sedimentation concentrate is re-solidified by the fourth filter press Separating, the waste water is discharged from the waste water discharge port; the second dryer is connected to the fourth filter press, the second dryer is used to dry the concentrate, and the carbonization is taken out from the sediment concentrate.矽 product.

本創作之矽晶圓切削污泥的分選處理裝置,其中,調整劑可以為氟酸或鹽酸或硫酸混合酸,適量添加以調整pH於2~6,捕集劑為中性捕集劑,添加量以1~5kg/t礦石為佳,起泡劑為松節油,添加量0.1~0.5kg/t礦石為佳,水添加量視礦漿 濃度而定,礦漿濃度以10~30%為佳。 The apparatus for sorting and processing the wafer cutting sludge in the present invention, wherein the adjusting agent may be a mixed acid of hydrofluoric acid or hydrochloric acid or sulfuric acid, and an appropriate amount is added to adjust the pH to 2-6, and the collecting agent is a neutral trapping agent. The amount of addition is preferably 1~5kg/t ore, the foaming agent is turpentine, the addition amount is 0.1~0.5kg/t ore, and the amount of water added is depending on the slurry. The concentration of the slurry is preferably 10 to 30% depending on the concentration.

本創作之矽晶圓切削污泥的分選處理裝置,其中,該第一濃縮機與該第二濃縮機內的礦漿用水含有浮選藥劑,藉由該第一導水管與該第三導水管分別將該第一濃縮機與該第二濃縮機內的礦漿用水輸入回該調整槽內,而該第一壓濾機與該第三壓濾機內的用水亦含有藥劑,藉由該第二導水管與該第四導水管分別將該第一壓濾機與該第三壓濾機內的用水輸入回該調整槽內,可以作為循環水使用,可節省藥劑及用水。 The apparatus for sorting and processing a wafer cutting sludge according to the present invention, wherein the slurry in the first concentrator and the second concentrator contains a flotation agent, wherein the first water conduit and the third water conduit The water in the first concentrator and the second concentrator is respectively input into the adjustment tank, and the water in the first filter press and the third filter press also contains a medicament, and the second The water conduit and the fourth water conduit respectively input the water in the first filter press and the third filter press into the adjustment tank, and can be used as circulating water, thereby saving medicine and water.

1‧‧‧調整槽 1‧‧‧Adjustment slot

2‧‧‧加藥機 2‧‧‧Dosing machine

3‧‧‧粗選浮選機 3‧‧‧Rough selection flotation machine

40‧‧‧浮礦精選浮選機 40‧‧‧Floating mine flotation machine

41‧‧‧第一濃縮機 41‧‧‧First Concentrator

42‧‧‧第一攪拌槽 42‧‧‧First Stirring Tank

43‧‧‧第一壓濾機 43‧‧‧First filter press

44‧‧‧第二攪拌槽 44‧‧‧Second agitation tank

45‧‧‧第二壓濾機 45‧‧‧Second filter press

450‧‧‧廢水排出口 450‧‧‧Wastewater discharge

46‧‧‧第一乾燥機 46‧‧‧First dryer

50‧‧‧沉礦精選浮選機 50‧‧‧Sink mining flotation machine

51‧‧‧第二濃縮機 51‧‧‧Second thickener

52‧‧‧第三攪拌槽 52‧‧‧ third stirring tank

53‧‧‧第三壓濾機 53‧‧‧ Third filter press

54‧‧‧第四攪拌槽 54‧‧‧fourth stirring tank

55‧‧‧第四壓濾機 55‧‧‧Four filter press

550‧‧‧廢水排出口 550‧‧‧Wastewater discharge

56‧‧‧第二乾燥機 56‧‧‧Second dryer

60‧‧‧第一馬達 60‧‧‧First motor

61‧‧‧第二馬達 61‧‧‧second motor

62‧‧‧第三馬達 62‧‧‧ Third motor

63‧‧‧第四馬達 63‧‧‧fourth motor

70‧‧‧第一導水管 70‧‧‧First water conduit

71‧‧‧第二導水管 71‧‧‧Second water conduit

72‧‧‧第三導水管 72‧‧‧ Third water conduit

73‧‧‧第四導水管 73‧‧‧fourth water conduit

第一圖所示係為本創作實施例處理裝置之配置示意圖。 The first figure is a schematic diagram of the configuration of the processing device of the present embodiment.

本創作矽晶圓切削污泥的分選處理裝置之實施例,請參閱第一圖所示,包括有:調整槽1、加藥機2、粗選浮選機3、浮礦精選浮選機40、沉礦精選浮選機50、第一濃縮機41、第二濃縮機51、第一壓濾機43、第二壓濾機45、第三壓濾機53、第四壓濾機55、第一攪拌槽42、第二攪拌槽44、第三攪拌槽52、第四攪拌槽54及第一乾燥機46、第二乾燥機56所構成,其中:該調整槽1,係供暫存矽晶圓切削污泥調漿及加藥之用;該加藥機2,係與該調整槽1連接,該加藥機2係於該調整槽1中的污泥加入少量的調整劑、捕集劑、起泡劑、水,使矽顆粒的表面與調整劑反應,強化表面疏水性,利於捕集,同時利用調整劑控制污泥(礦漿)pH值於2~6,利於碳化矽凝聚 沉降,調整劑可以為氟酸或鹽酸或硫酸混合酸,適量添加以調整pH,捕集劑添加量以1~5kg/t礦石為佳,起泡劑添加量0.1~0.5kg/t礦石為佳,水添加量視礦漿濃度而定,礦漿濃度以10~30%為佳;該粗選浮選機3,係與該調整槽1連接,藉由該粗選浮選機3將污泥(礦漿)予以分選為浮礦與沉礦;該浮礦精選浮選機40,係與該粗選浮選機3連接,將該粗選浮選機3內污泥中的浮礦輸送至該浮礦精選浮選機40內浮選;該第一濃縮機41,係與該浮礦精選浮選機40連接,該第一濃縮機41與該浮礦精選浮選機40之間設有一第一馬達60,該第一馬達60係將該浮礦精選浮選機40內的浮礦加壓輸送至該第一濃縮機41內,藉由該第一濃縮機41將浮礦漿予以濃縮,使其固液分離,固體礦漿係沉澱於該第一濃縮機41之底部,液體則位於固體礦漿之上方,該液體則由一第一導水管70輸送至該調整槽1內,該第一濃縮機41內的礦漿用水含有浮選藥劑,可以作為循環水使用,可節省藥劑及用水;該第一攪拌槽42,係與該第一濃縮機41連接,該第一攪拌槽42係供將濃縮後的浮礦漿予以攪拌;該第一壓濾機43,係與該第一攪拌槽42連接,該第一壓濾機43與該第一攪拌槽42之間設有一第二馬達61,藉由該第二馬達61將該第一攪拌槽42內之浮礦漿予以加壓送至該第一壓濾機43內,該第一壓濾機43係將固液分離為小顆粒的含矽固體與濾液,該第一壓濾機43內之液體則由一第二導水管71輸 送至該調整槽1內,該第一壓濾機43內的礦漿用水亦含有浮選藥劑,可以作為循環水使用,可節省藥劑及用水;該第二攪拌槽44,係與該第一壓濾機43連接,藉由該第二攪拌槽44將浮礦漿再次注水攪拌洗淨,形成浮礦精礦;該第二壓濾機45,係與該第二攪拌槽44連接,該第二壓濾機45設有廢水排出口450,藉由該第二壓濾機45將該浮礦精礦再次固液分離,廢水則由該廢水排出口450排放;該第一乾燥機46,係與該第二壓濾機45連接,該第一乾燥機46係將該浮礦精礦予以乾燥,從浮礦精礦中取出矽產品;該沉礦精選浮選機50,係與該粗選浮選機3連接,將該粗選浮選機3內污泥中的沉礦輸送至該沉礦精選浮選機50內浮選;該第二濃縮機51,係與該沉礦精選浮選機50連接,該第二濃縮機51與該沉礦精選浮選機50之間設有一第三馬達62,該第三馬達62係將該沉礦精選浮選機50內的沉礦加壓輸送至該第二濃縮機51內,藉由該第二濃縮機51將沉礦漿予以濃縮,使其固液分離,固體礦漿係沉澱於該第二濃縮機51之底部,液體則位於固體礦漿之上方,該液體則由一第三導水管72輸送至該調整槽1內,該第二濃縮機51內的礦漿用水含有浮選藥劑,可以作為循環水使用,可節省藥劑及用水;該第三攪拌槽52,係與該第二濃縮機51連接,該第三攪拌槽52係供將濃縮後的沉礦漿予以攪拌;該第三壓濾機53,係與該第三攪拌槽52連接,該第三壓濾機53與該第三攪拌槽52之間設有一第四馬達63,藉由該第四 馬達63將該第三攪拌槽52內之沉礦漿予以加壓送至該第三壓濾機53內,該第三壓濾機53係將固液分離為大顆粒的含碳化矽固體與濾液,該第三壓濾機53內之液體則由一第四導水管73輸送至該調整槽1內;該第四攪拌槽54,係與該第二壓濾機53連接,藉由該第四攪拌槽54將沉礦漿再次注水攪拌洗淨,形成沉礦精礦;該第四壓濾機55,係與該第四攪拌槽54連接,該第四壓濾機55設有廢水排出口550,藉由該第四壓濾機55將該沉礦精礦再次固液分離,廢水則由該廢水排出口550排放;該第二乾燥機56,係與該第四壓濾機55連接,該第二乾燥機56係將該沉礦精礦予以乾燥,從沉礦精礦中取出碳化矽產品。 The embodiment of the separation processing device for the wafer cutting sludge of the present invention is shown in the first figure, including: adjustment tank 1, dosing machine 2, rough selection flotation machine 3, flotation flotation machine 40. The sedimentation flotation machine 50, the first concentrator 41, the second concentrator 51, the first filter press 43, the second filter press 45, the third filter press 53, and the fourth filter press 55, The first agitation tank 42, the second agitation tank 44, the third agitation tank 52, the fourth agitation tank 54, the first dryer 46, and the second dryer 56 are configured, wherein the adjustment tank 1 is temporarily stored. The wafer cutting sludge is used for slurrying and dosing; the dosing machine 2 is connected to the adjusting tank 1, and the dosing machine 2 is added with a small amount of adjusting agent and trapping to the sludge in the adjusting tank 1. Agent, foaming agent, water, make the surface of the cerium particles react with the modifier, strengthen the surface hydrophobicity, which is conducive to trapping, and use the adjusting agent to control the pH value of the sludge (pulp) to 2~6, which is conducive to the enthalpy of carbonization Settling, the adjusting agent may be hydrofluoric acid or hydrochloric acid or sulfuric acid mixed acid, and the appropriate amount is added to adjust the pH. The amount of the trapping agent is preferably 1~5kg/t ore, and the foaming agent is added in an amount of 0.1~0.5kg/t ore. The amount of water added depends on the concentration of the slurry, and the concentration of the slurry is preferably 10 to 30%; the rough selection flotation machine 3 is connected to the adjustment tank 1, and the sludge is obtained by the coarse flotation machine 3 Dividing into flotation and sinking; the flotation flotation machine 40 is connected to the rough flotation machine 3, and the floating ore in the sludge in the rough flotation machine 3 is transported to the float The flotation machine 40 is floated in the flotation machine 40; the first concentrator 41 is connected to the flotation flotation machine 40, and the first concentrator 41 and the flotation flotation machine 40 are provided with a first The motor 60 is configured to pressurize the floating ore in the floating ore flotation machine 40 into the first thickener 41, and the first thickener 41 concentrates the floating slurry to make it Solid-liquid separation, the solid slurry is deposited at the bottom of the first concentrator 41, and the liquid is located above the solid slurry, and the liquid is delivered to the adjustment tank 1 by a first water conduit 70. The slurry in the first concentrator 41 contains a flotation agent, which can be used as circulating water to save chemicals and water. The first agitation tank 42 is connected to the first concentrator 41, and the first agitation tank 42 is connected. The first floating filter 43 is connected to the first agitating tank 42. A second motor 61 is disposed between the first filter press 43 and the first agitating tank 42. The floating slurry in the first agitation tank 42 is pressurized and sent to the first filter press 43 by the second motor 61. The first filter press 43 separates the solid-liquid into small particles. The solid and the filtrate, the liquid in the first filter press 43 is transported by a second water conduit 71 The slurry in the first filter press 43 also contains a flotation agent, which can be used as circulating water to save chemicals and water; the second agitation tank 44 is connected to the first pressure. The filter 43 is connected, and the floating slurry is refilled with water and stirred by the second stirring tank 44 to form a floating ore concentrate; the second filter press 45 is connected to the second stirring tank 44, and the second pressure is connected. The filter machine 45 is provided with a waste water discharge port 450, and the floating ore concentrate is again solid-liquid separated by the second filter press 45, and the waste water is discharged from the waste water discharge port 450; the first dryer 46 is connected thereto. The second filter press 45 is connected, the first dryer 46 is used to dry the flotation concentrate, and the antimony product is taken out from the flotation concentrate; the sedimentation flotation machine 50 is connected to the rough flotation The machine 3 is connected, and the sediment in the sludge in the rough flotation machine 3 is sent to the flotation flotation machine 50 for flotation; the second concentrator 51 is connected to the sediment flotation machine 50. Connected, a second motor 62 is disposed between the second concentrator 51 and the sinking selective flotation machine 50, and the third motor 62 is used in the sinking flotation machine 50. The sediment is pressurized and sent to the second concentrator 51, and the slurry is concentrated by the second concentrator 51 to be solid-liquid separated, and the solid slurry is deposited at the bottom of the second concentrator 51, the liquid Then, it is located above the solid slurry, and the liquid is transported to the adjusting tank 1 by a third water conduit 72. The slurry in the second thickener 51 contains a flotation agent, which can be used as circulating water to save the medicament and Water is used; the third agitation tank 52 is connected to the second concentrator 51 for agitating the concentrated slurry; the third filter 53 is connected to the third agitator a slot 52 is connected, and a fourth motor 63 is disposed between the third filter press 53 and the third agitating tank 52. The motor 63 pressurizes the slurry in the third agitation tank 52 to the third filter press 53, and the third filter press 53 separates the solid-liquid into large particles of the ruthenium carbide-containing solid and the filtrate. The liquid in the third filter press 53 is sent to the adjusting tank 1 by a fourth water conduit 73. The fourth stirring tank 54 is connected to the second filter press 53 by the fourth stirring. The tank 54 refills and sinks the sinking slurry to form a sinking concentrate; the fourth filter press 55 is connected to the fourth stirring tank 54, and the fourth filter press 55 is provided with a waste water discharge port 550. The sedimentation concentrate is again solid-liquid separated by the fourth filter press 55, and the waste water is discharged from the waste water discharge port 550; the second dryer 56 is connected to the fourth filter press 55, the second The dryer 56 is used to dry the concentrate, and the tantalum carbide product is taken out from the sinking concentrate.

本創作藉由上述之分選處理裝置,將矽晶圓切削污泥送入調整槽1內,調整礦漿使礦漿達到較佳條件,再利用浮選,將礦漿分為浮礦與沉礦,浮礦與沉礦再分別進入浮選機內再次浮選,利用多次精選可以逐步提高品位,利用多次精選分別逐步純化浮礦與沉礦,浮礦可以獲得矽品位99%,沉礦可以獲得碳化矽品位99%之兩種產品,可以作為陶瓷原料及二次工業利用。 The present invention uses the above-mentioned sorting processing device to feed the 矽 wafer cutting sludge into the adjusting tank 1, adjust the pulp to make the pulp reach better conditions, and then use the flotation to divide the slurry into floating ore and sinking, floating The mine and the sinking mine will then be re-floated separately into the flotation machine. The selection can be gradually improved by using multiple selections. The flotation and sedimentation can be gradually purified by multiple selections. The floating ore can obtain 99% of the grade, and the sinking can be obtained. Two products with 99% grade of tantalum carbide can be used as ceramic raw materials and secondary industry.

綜上所述,本創作確實已達到所預期之使用目的與功效,且更較習知者為之理想、實用,惟,上述實施例僅係針對本創作之較佳實施例進行具體說明而已,該實施例並非用以限定本創作之申請專利範圍,舉凡其它未脫離本創作所揭示之技 術手段下所完成之均等變化與修飾,均應包含於本創作所涵蓋之申請專利範圍中。 In summary, the present invention has achieved the intended use and effect, and is more desirable and practical than the prior art. However, the above embodiments are only specifically described for the preferred embodiment of the present invention. This embodiment is not intended to limit the scope of the patent application of the present invention, and other features not disclosed in the present disclosure. Equivalent changes and modifications made under the means of surgery shall be included in the scope of the patent application covered by this creation.

1‧‧‧調整槽 1‧‧‧Adjustment slot

2‧‧‧加藥機 2‧‧‧Dosing machine

3‧‧‧粗選浮選機 3‧‧‧Rough selection flotation machine

40‧‧‧浮礦精選浮選機 40‧‧‧Floating mine flotation machine

41‧‧‧第一濃縮機 41‧‧‧First Concentrator

42‧‧‧第一攪拌槽 42‧‧‧First Stirring Tank

43‧‧‧第一壓濾機 43‧‧‧First filter press

44‧‧‧第二攪拌槽 44‧‧‧Second agitation tank

45‧‧‧第二壓濾機 45‧‧‧Second filter press

450‧‧‧廢水排出口 450‧‧‧Wastewater discharge

46‧‧‧第一乾燥機 46‧‧‧First dryer

50‧‧‧沉礦精選浮選機 50‧‧‧Sink mining flotation machine

51‧‧‧第二濃縮機 51‧‧‧Second thickener

52‧‧‧第三攪拌槽 52‧‧‧ third stirring tank

53‧‧‧第三壓濾機 53‧‧‧ Third filter press

54‧‧‧第四攪拌槽 54‧‧‧fourth stirring tank

55‧‧‧第四壓濾機 55‧‧‧Four filter press

550‧‧‧廢水排出口 550‧‧‧Wastewater discharge

56‧‧‧第二乾燥機 56‧‧‧Second dryer

60‧‧‧第一馬達 60‧‧‧First motor

61‧‧‧第二馬達 61‧‧‧second motor

62‧‧‧第三馬達 62‧‧‧ Third motor

63‧‧‧第四馬達 63‧‧‧fourth motor

70‧‧‧第一導水管 70‧‧‧First water conduit

71‧‧‧第二導水管 71‧‧‧Second water conduit

72‧‧‧第三導水管 72‧‧‧ Third water conduit

73‧‧‧第四導水管 73‧‧‧fourth water conduit

Claims (6)

一種矽晶圓切削污泥的分選處理裝置,包括有:調整槽、加藥機、粗選浮選機、浮礦精選浮選機、沉礦精選浮選機、第一濃縮機、第二濃縮機、第一壓濾機、第二壓濾機、第三壓濾機、第四壓濾機、第一攪拌槽、第二攪拌槽、第三攪拌槽、第四攪拌槽及第一乾燥機、第二乾燥機所構成,其中:該調整槽,係供暫存矽晶圓切削污泥調漿及加藥之用;該加藥機,係與該調整槽連接;該粗選浮選機,係與該調整槽連接,藉由該粗選浮選機將污泥予以分選為浮礦與沉礦;該浮礦精選浮選機,係與該粗選浮選機連接,將該粗選浮選機內污泥中的浮礦輸送至該浮礦精選浮選機內進行浮選;該第一濃縮機,係與該浮礦精選浮選機連接,該第一濃縮機與該浮礦精選浮選機之間設有一第一馬達,該第一馬達係將該浮礦精選浮選機內的浮礦加壓輸送至該第一濃縮機內;該第一攪拌槽,係與該第一濃縮機連接,該第一攪拌槽係供將濃縮後的浮礦漿予以攪拌;該第一壓濾機,係與該第一攪拌槽連接,該第一壓濾機與該第一攪拌槽之間設有一第二馬達,藉由該第二馬達將該第一攪拌槽內之浮礦漿予以加壓送至該第一壓濾機內,該第一壓濾機係將固液分離為小顆粒的含矽固體與濾液;該第二攪拌槽,係與該第一壓濾機連接,藉由該第二攪拌槽 將浮礦漿再次注水攪拌洗淨,形成浮礦精礦;該第二壓濾機,係與該第二攪拌槽連接,該第二壓濾機設有廢水排出口,藉由該第二壓濾機將該浮礦精礦再次固液分離,廢水則由該廢水排出口排放;該第一乾燥機,係與該第二壓濾機連接,該第一乾燥機係將該浮礦精礦予以乾燥,從浮礦精礦中取出矽產品;該沉礦精選浮選機,係與該粗選浮選機連接,將該粗選浮選機內污泥中的沉礦輸送至該沉礦精選浮選機內進行浮選;該第二濃縮機,係與該沉礦精選浮選機連接,該第二濃縮機與該沉礦精選浮選機之間設有一第三馬達,該第三馬達係將該沉礦精選浮選機內的沉礦加壓輸送至該第二濃縮機內;該第三攪拌槽,係與該第二濃縮機連接,該第三攪拌槽係供將濃縮後的沉礦漿予以攪拌;該第三壓濾機,係與該第三攪拌槽連接,該第三壓濾機與該第三攪拌槽之間設有一第四馬達,藉由該第四馬達將該第三攪拌槽內之沉礦漿予以加壓送至該第三壓濾機內,該第三壓濾機係將固液分離為大顆粒的含碳化矽固體與濾液;該第四攪拌槽,係與該第三壓濾機連接,藉由該第四攪拌槽將沉礦漿再次注水攪拌洗淨,形成沉礦精礦;該第四壓濾機,係與該第四攪拌槽連接,該第四壓濾機設有廢水排出口,藉由該第四壓濾機將該沉礦精礦再次固液分離,廢水則由該廢水排出口排放;該第二乾燥機,係與該第四壓濾機連接,該第二乾燥機係將該沉礦精礦予以乾燥,從沉礦精礦中取出碳化矽產品。 The utility model relates to a sorting and processing device for a silicon wafer cutting sludge, comprising: an adjusting tank, a dosing machine, a roughing flotation machine, a flotation flotation machine, a sedimentation flotation machine, a first thickener, a second a concentrator, a first filter press, a second filter press, a third filter press, a fourth filter press, a first agitation tank, a second agitation tank, a third agitation tank, a fourth agitation tank, and a first drying The machine and the second dryer are configured, wherein: the adjusting tank is used for temporary storage, wafer cutting sludge slurrying and dosing; the dosing machine is connected with the adjusting tank; the rough selection flotation The machine is connected to the adjusting tank, and the sludge is sorted into floating ore and sediment by the roughing flotation machine; the flotation flotation machine is connected with the rough flotation machine, The flotation in the sludge in the rough flotation machine is sent to the flotation flotation machine for flotation; the first concentrator is connected to the flotation flotation machine, the first concentrator and the A first motor is disposed between the flotation flotation machine, and the first motor is pressurized to transport the floating ore in the flotation flotation machine to the first concentrator; a first agitation tank is connected to the first concentrator, the first agitation tank is configured to stir the concentrated pulverized slurry; the first filter press is connected to the first agitation tank, the first pressure a second motor is disposed between the filter and the first agitation tank, and the floating slurry in the first agitation tank is pressurized and sent to the first filter press by the second motor, the first filter press The machine separates the solid liquid into small particles of cerium-containing solids and filtrate; the second stirring tank is connected to the first filter press by the second stirring tank The floating slurry is refilled with water and stirred to form a floating ore concentrate; the second filter press is connected to the second agitating tank, and the second filter press is provided with a waste water discharge port, by the second pressure filter The machine re-solidifies the flotation concentrate, and the waste water is discharged from the waste water discharge port; the first dryer is connected to the second filter press, and the first dryer is used for the flotation concentrate Drying, removing the antimony product from the flotation concentrate; the sedimentation flotation machine is connected with the rough flotation machine, and the sediment in the sludge in the rough flotation machine is transported to the sediment selection Flotation is carried out in the flotation machine; the second concentrator is connected to the sinking flotation machine, and a third motor is arranged between the second concentrator and the sinking flotation machine, the third motor Cooling the sediment in the sedimentation flotation machine to the second concentrator; the third agitation tank is connected to the second concentrator, and the third agitation tank is for concentrating The slurry is stirred; the third filter is connected to the third agitation tank, and the third filter press and the third agitation tank a fourth motor is provided, and the slurry in the third agitation tank is pressurized and sent to the third filter press by the fourth motor, and the third filter press separates the solid liquid into large particles. a solid solution containing ruthenium carbide and a filtrate; the fourth agitation tank is connected to the third filter press, and the slurry is refilled with water and stirred by the fourth agitation tank to form a sinking concentrate; the fourth pressure filter The machine is connected to the fourth agitation tank, and the fourth filter press is provided with a waste water discharge port, and the sedimentation concentrate is again solid-liquid separated by the fourth filter press, and the waste water is discharged from the waste water discharge port. The second dryer is connected to the fourth filter press, and the second dryer is used to dry the concentrate, and the tantalum carbide product is taken out from the sinking concentrate. 如申請專利範圍第1項所述之矽晶圓切削污泥的分選處理裝置,其中,該加藥機係於該調整槽中的污泥加入調整劑、捕集劑、起泡劑、水,使矽顆粒的表面與調整劑反應,強化表面疏水性,利於捕集,同時利用調整劑控制礦漿pH值,利於碳化矽凝聚沉降。 The apparatus for sorting and processing a wafer cutting sludge according to the first aspect of the invention, wherein the dosing machine is added to the sludge in the adjusting tank by adding a adjusting agent, a collecting agent, a foaming agent, and water. The surface of the cerium particles is reacted with the adjusting agent to strengthen the surface hydrophobicity, which is favorable for the collection, and the adjusting agent is used to control the pH value of the slurry, which is beneficial to the coagulation and settlement of the cerium carbide. 如申請專利範圍第1項所述之矽晶圓切削污泥的分選處理裝置,其中,該第一濃縮機設有第一導水管,該第一導水管係將該第一濃縮機內的液體輸送回至該調整槽內。 The apparatus for sorting and processing a wafer-cutting sludge according to the first aspect of the invention, wherein the first concentrator is provided with a first water conduit, and the first water conduit is in the first concentrator The liquid is delivered back into the adjustment tank. 如申請專利範圍第1項所述之矽晶圓切削污泥的分選處理裝置,其中,該第一壓濾機設有第二導水管,該第二導水管係將該第一壓濾機內的液體輸送回至該調整槽內。 The apparatus for sorting and processing a wafer-cutting sludge according to the first aspect of the invention, wherein the first filter press is provided with a second water conduit, the second water conduit is the first filter press The liquid inside is transported back into the adjustment tank. 如申請專利範圍第1項所述之矽晶圓切削污泥的分選處理裝置,其中,該第二濃縮機設有第三導水管,該第三導水管係將該第二濃縮機內的液體輸送回至該調整槽內。 The apparatus for sorting and processing a wafer-cutting sludge according to the first aspect of the invention, wherein the second concentrator is provided with a third water conduit, wherein the third water conduit is in the second concentrator The liquid is delivered back into the adjustment tank. 如申請專利範圍第1項所述之矽晶圓切削污泥的分選處理裝置,其中,該第三壓濾機設有第四導水管,該第四導水管係將該第三壓濾機內的液體輸送回至該調整槽內。 The apparatus for sorting and processing a wafer-cutting sludge according to the first aspect of the invention, wherein the third filter press is provided with a fourth water conduit, the fourth water conduit is the third filter press The liquid inside is transported back into the adjustment tank.
TW102202178U 2013-01-31 2013-01-31 Sorting treatment device of silicon wafer cutting sludge TWM457723U (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112474694A (en) * 2019-09-12 2021-03-12 许树清 Waste residue treatment process after smelting of nonferrous noble metals

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112474694A (en) * 2019-09-12 2021-03-12 许树清 Waste residue treatment process after smelting of nonferrous noble metals

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