工业水处理
工業水處理
공업수처리
INDUSTRIAL WATER TREATMENT
2015年
6期
61-64
,共4页
饶力%汪晓军%陈振国%袁延磊%郭冠超
饒力%汪曉軍%陳振國%袁延磊%郭冠超
요력%왕효군%진진국%원연뢰%곽관초
响应面法%氧化铁红%高氨氮废水%磷酸铵镁
響應麵法%氧化鐵紅%高氨氮廢水%燐痠銨鎂
향응면법%양화철홍%고안담폐수%린산안미
response surface method%iron oxide red%high ammonia-nitrogen wastewater%magnesium ammonium phosphate
采用鸟粪石法对氧化铁红厂高氨氮废水进行处理,以pH、n(N)∶n(Mg)和n(N)∶n(P)为主要影响因素,通过响应面法对处理过程进行了优化设计,得到拟合程度高的二次响应曲面模型。预测的最佳实验条件:pH=9.40, n(N)∶n(Mg)∶n(P)=0.8∶1∶1,此条件下氨氮去除率为99.77%。通过对镁盐和磷酸盐投加量的分析得到,当n(N)∶n(Mg)∶n(P)=0.9∶1.25∶1时,出水氨氮能够达到排放标准的要求,且出水正磷酸盐浓度较低。 SEM和XRD表征结果显示,所得沉淀物大部分为磷酸铵镁。
採用鳥糞石法對氧化鐵紅廠高氨氮廢水進行處理,以pH、n(N)∶n(Mg)和n(N)∶n(P)為主要影響因素,通過響應麵法對處理過程進行瞭優化設計,得到擬閤程度高的二次響應麯麵模型。預測的最佳實驗條件:pH=9.40, n(N)∶n(Mg)∶n(P)=0.8∶1∶1,此條件下氨氮去除率為99.77%。通過對鎂鹽和燐痠鹽投加量的分析得到,噹n(N)∶n(Mg)∶n(P)=0.9∶1.25∶1時,齣水氨氮能夠達到排放標準的要求,且齣水正燐痠鹽濃度較低。 SEM和XRD錶徵結果顯示,所得沉澱物大部分為燐痠銨鎂。
채용조분석법대양화철홍엄고안담폐수진행처리,이pH、n(N)∶n(Mg)화n(N)∶n(P)위주요영향인소,통과향응면법대처리과정진행료우화설계,득도의합정도고적이차향응곡면모형。예측적최가실험조건:pH=9.40, n(N)∶n(Mg)∶n(P)=0.8∶1∶1,차조건하안담거제솔위99.77%。통과대미염화린산염투가량적분석득도,당n(N)∶n(Mg)∶n(P)=0.9∶1.25∶1시,출수안담능구체도배방표준적요구,차출수정린산염농도교저。 SEM화XRD표정결과현시,소득침정물대부분위린산안미。
MAP method has been used for treating the high ammonia-nitrogen wastewater from an iron oxide red factory. The three main influencing factors are as follows:pH,n (N)∶n (Mg)和n (N)∶n (P). The treatment course is optimized by response surface method (RSM),so as to obtain the quadratic response curved model with high fitting degree. Under the forecast optimum experiment conditions:pH=9.40,n (N)∶n (Mg)∶n (P)=0.8∶1∶1, the removing rate of ammonia-nitrogen could be 99.77%. By analyzing the dosages of Mg2+and PO43-,it is found that when n(N)∶n (Mg)∶n (P)=0.9∶1.25∶1,the effluent concentration of ammonia-nitrogen could meet the requirements for the emis-sion standard,and the concentration of orthophosphate could stay at a low level. The results of SEM and XRD chara-cterization show that the sediments obtained are mostly magnesium ammonium phosphate.