工业用水与废水
工業用水與廢水
공업용수여폐수
INDUSTRIAL WATER & WASTEWATER
2014年
5期
14-18
,共5页
韩琦%王宏杰%董文艺%尹玉磊%范洪凯
韓琦%王宏傑%董文藝%尹玉磊%範洪凱
한기%왕굉걸%동문예%윤옥뢰%범홍개
高铁酸盐%臭氧%双酚 A%干扰离子%生物毒性
高鐵痠鹽%臭氧%雙酚 A%榦擾離子%生物毒性
고철산염%취양%쌍분 A%간우리자%생물독성
ferrate%ozone%bisphenol A%interfering ions%biotoxicity
通过烧杯试验,对比研究了不同因素对高铁酸盐和臭氧氧化降解双酚 A 的影响,并对试验过程中的生物毒性进行了对比分析。试验结果表明:针对质量浓度为1 mg / L 的双酚 A 模拟废水,在高铁酸盐和臭氧的投加量分别为5.0和1.20 mg/ L 的条件下,高铁酸盐降解双酚 A 的能力更强,去除率达到91.6%,而臭氧氧化法仅为80.9%;同时,高铁酸盐法具有更广的 pH 值(3~11)和温度(10~50℃)适应性。不同的干扰离子对氧化体系的影响不同, HCO3-对2个氧化体系均具有一定的促进作用; Fe3+的存在具有催化作用,有利于臭氧氧化降解双酚 A,但是不利于高铁酸盐的稳定性从而不利于双酚 A 的脱除。2种方法处理后水的生物毒性均随反应时间的延长呈先升高后降低的趋势,相对而言,高铁酸盐法对处理后水的毒性控制效果更佳。
通過燒杯試驗,對比研究瞭不同因素對高鐵痠鹽和臭氧氧化降解雙酚 A 的影響,併對試驗過程中的生物毒性進行瞭對比分析。試驗結果錶明:針對質量濃度為1 mg / L 的雙酚 A 模擬廢水,在高鐵痠鹽和臭氧的投加量分彆為5.0和1.20 mg/ L 的條件下,高鐵痠鹽降解雙酚 A 的能力更彊,去除率達到91.6%,而臭氧氧化法僅為80.9%;同時,高鐵痠鹽法具有更廣的 pH 值(3~11)和溫度(10~50℃)適應性。不同的榦擾離子對氧化體繫的影響不同, HCO3-對2箇氧化體繫均具有一定的促進作用; Fe3+的存在具有催化作用,有利于臭氧氧化降解雙酚 A,但是不利于高鐵痠鹽的穩定性從而不利于雙酚 A 的脫除。2種方法處理後水的生物毒性均隨反應時間的延長呈先升高後降低的趨勢,相對而言,高鐵痠鹽法對處理後水的毒性控製效果更佳。
통과소배시험,대비연구료불동인소대고철산염화취양양화강해쌍분 A 적영향,병대시험과정중적생물독성진행료대비분석。시험결과표명:침대질량농도위1 mg / L 적쌍분 A 모의폐수,재고철산염화취양적투가량분별위5.0화1.20 mg/ L 적조건하,고철산염강해쌍분 A 적능력경강,거제솔체도91.6%,이취양양화법부위80.9%;동시,고철산염법구유경엄적 pH 치(3~11)화온도(10~50℃)괄응성。불동적간우리자대양화체계적영향불동, HCO3-대2개양화체계균구유일정적촉진작용; Fe3+적존재구유최화작용,유리우취양양화강해쌍분 A,단시불리우고철산염적은정성종이불리우쌍분 A 적탈제。2충방법처리후수적생물독성균수반응시간적연장정선승고후강저적추세,상대이언,고철산염법대처리후수적독성공제효과경가。
Through the beaker tests, the degradation of bisphenol A(BPA) by ferrate and ozone oxidation was studied contrastively by investigating the effects of different influencing factors as well as analyzing the vari-ation of biotoxicity during the two processes. The results of the test showed that, on the premise that the dosage of BPA and ozone were 5.0 and 1.20 mg / L respectively, ferrate showed a stronger degrading ability when treating BPA simulated wastewater with mass concentration of 1 mg/L. The removal rate of BPA reached 91.6% by ferrate while only 80.9% by ozone oxidation. In addition, ferrate oxidation process had a wider pH value(3 ~ 11) and temperature(10 ~ 50 ℃) adaptive range. Different interfering ions had different effects on the oxidization system. HCO3- showed a certain promoting effect on the said two systems, Fe3+ played a catalytic role during the reaction, which was favorable for BPA degradation by ozone; however, it was not conductive to the stability of the ferrate, thus was not beneficial to BPA degradation. The biotoxicity of the effluent water from the said two processes showed the tendency that increased first and then decreased with the prolonging of the reaction time. It could be seen that, compared to ozone, ferrate had a better effect for water toxicity controlling.