发明名称 Process for recovery of fluoride from wastewater produced in crystalline silicon solar cell manufacturing
摘要 A method for processing fluoride-containing wastewaters from a factory, which includes the following steps: Step 1: collecting the fluoride-containing wastewaters into three pools: an acidic high-fluoride wastewater, an acidic low-fluoride wastewater, and an alkaline wastewater; Step 2: adding a calcium compound to the acidic low-fluoride wastewater to produce a calcium-containing solution; Step 3: reacting a portion of the calcium-containing solution with the acidic high-fluoride wastewater at a calcium-to-fluoride molar ratio of from about 0.5:1 to about 1.5:1 to produce a mixture comprising calcium fluoride particles suspended in a mother liquor; Step 4: separately collecting the calcium fluoride particles and the mother liquor; Step 5: diluting the mother liquor with a diluent to produce a mixed solution; and Step 6: introducing the mixed solution, the calcium-containing solution, and the alkaline wastewater into a fluidized bed reactor, which contains a calcium fluoride crystallization seed material, to form calcium fluoride crystals.
申请公布号 US9469549(B2) 申请公布日期 2016.10.18
申请号 US201314099452 申请日期 2013.12.06
申请人 Beijing Guohuan Tsinghua Environment Engineering Design & Research Institute Co., Ltd. 发明人 Wang Cheng-Wen;Li Yan;Fu Hongxiang;Zhao Xuefeng
分类号 C02F1/28;B01D21/01;C02F1/52;B01D21/26;B01D29/00;B01J8/18;C01F11/22;B01D21/24;B01J8/24;C02F1/58;C02F1/66;B01D21/00;B01D15/00;C02F1/00;B03D3/00;B01D37/00;B01J8/00;C01F11/00;B01D15/02;B01D21/02;C02F103/34;C02F103/40;C02F101/14 主分类号 C02F1/28
代理机构 Osha • Liang LLP 代理人 Osha • Liang LLP
主权项 1. A method for processing fluoride-containing wastewaters from a factory, comprising the following steps: Step 1: collecting the fluoride-containing wastewaters into three pools: an acidic high-fluoride wastewater that contains fluoride at a concentration higher than a first threshold concentration, an acidic low-fluoride wastewater that contains fluoride at a concentration lower than a second threshold concentration which is less than or equal to the first threshold concentration, and an alkaline wastewater; Step 2: adding a calcium compound to a portion of the acidic low-fluoride wastewater to produce a calcium-containing solution that contains calcium at a concentration of about 10-300 g/L; Step 3: reacting a portion of the calcium-containing solution with the acidic high-fluoride wastewater at a calcium-to-fluoride molar ratio of from about 0.5:1 to about 1.5:1 to produce a mixture comprising calcium fluoride particles suspended in a mother liquor; Step 4: processing the mixture to separately collect the calcium fluoride particles and the mother liquor; Step 5: diluting the mother liquor with a diluent to produce a mixed solution having a pH value of about 2-6 and containing a fluoride concentration of about 80-500 mg/L; and Step 6: introducing the mixed solution from Step 5, a remaining portion of calcium-containing solution from Step 2 which is not reacted in Step 3, and the alkaline wastewater from Step 1 into a fluidized bed reactor, which contains a calcium fluoride crystallization seed material, to form calcium fluoride crystals, wherein the alkaline wastewater is used to adjust a pH of a fluid in the fluidized bed reactor to a value between 5 and 8, wherein a molar ratio between the calcium in the calcium containing solution from Step 2 and the fluoride in the mixed solution from Step 5 is controlled at 0.5:1 to 2:1, wherein an effluent from the fluidized bed reactor is added to an inlet of the fluidized bed reactor to control a fluoride concentration at 150 mg/L or lower in an inlet region of the fluidized bed reactor, wherein a flow rate in the fluidized bed reactor is controlled at 100-20,000 m/hr.
地址 Beijing CN