工业安全与环保
工業安全與環保
공업안전여배보
Industrial Safety and Environmental Protection
2015年
9期
94-96
,共3页
李新柱%连新平%胡兆平%郭宗端%李伟%张自祥%王建全%裴海荣
李新柱%連新平%鬍兆平%郭宗耑%李偉%張自祥%王建全%裴海榮
리신주%련신평%호조평%곽종단%리위%장자상%왕건전%배해영
磷酸%乙酸%多次萃取%磷酸三丁酯%正辛烷
燐痠%乙痠%多次萃取%燐痠三丁酯%正辛烷
린산%을산%다차췌취%린산삼정지%정신완
phosphoric acid%acetic acid%multiple extraction%tributyl phosphate%normal octane
为了利用半导体行业产生的磷酸、乙酸混合废液中的磷酸,实验室条件下采用多次萃取法,以磷酸与乙酸质量分数分别为25.35%与1.00%的混合溶液作为萃取对象,磷酸三丁酯为萃取剂,正辛烷为稀释剂萃取分离回收磷酸。实验结果表明,在磷酸三丁酯与正辛烷质量比为1∶2条件下,萃取等质量磷酸乙酸混合溶液,萃取4次后,乙酸质量分数降至0.15%,而磷酸质量分数变化不大,为23.93%,相比未萃取前仅损失了5.60%,并且不同萃取次数之间磷酸的损失基本相同。萃余液可以作为生产磷肥的原料,节约了资源。
為瞭利用半導體行業產生的燐痠、乙痠混閤廢液中的燐痠,實驗室條件下採用多次萃取法,以燐痠與乙痠質量分數分彆為25.35%與1.00%的混閤溶液作為萃取對象,燐痠三丁酯為萃取劑,正辛烷為稀釋劑萃取分離迴收燐痠。實驗結果錶明,在燐痠三丁酯與正辛烷質量比為1∶2條件下,萃取等質量燐痠乙痠混閤溶液,萃取4次後,乙痠質量分數降至0.15%,而燐痠質量分數變化不大,為23.93%,相比未萃取前僅損失瞭5.60%,併且不同萃取次數之間燐痠的損失基本相同。萃餘液可以作為生產燐肥的原料,節約瞭資源。
위료이용반도체행업산생적린산、을산혼합폐액중적린산,실험실조건하채용다차췌취법,이린산여을산질량분수분별위25.35%여1.00%적혼합용액작위췌취대상,린산삼정지위췌취제,정신완위희석제췌취분리회수린산。실험결과표명,재린산삼정지여정신완질량비위1∶2조건하,췌취등질량린산을산혼합용액,췌취4차후,을산질량분수강지0.15%,이린산질량분수변화불대,위23.93%,상비미췌취전부손실료5.60%,병차불동췌취차수지간린산적손실기본상동。췌여액가이작위생산린비적원료,절약료자원。
To recycle the phosphoric acid from the mixture of phosphoric acid and acetic acid in semiconductor industry , tributyl phosphate is used as extraction agent and normal octane as diluent recycled phosphoric acid from the mixture of phos-phoric acid(mass fraction 25 .35% ) and acetic acid(mass fraction 1 .00% ) in laboratory bymultiple extraction .The results show that if the mass ratio of tributyl phosphate and normal octane is 1∶2 ,after 4 times of extraction ,the concentration of acetic acid is decreased to 0 .15% ,but concentration of phosphoric acid changes less and remains 23 .93% ,just lost 5 .60% , and the lost of phosphoric acid for each extraction is almost the same .The raffinate can be used as raw materials for phos-phatic fertilizer and so the resources can be saved .