爆破器材
爆破器材
폭파기재
2014年
4期
52-56
,共5页
王时亮%杨爱江%李清%吴欣琪
王時亮%楊愛江%李清%吳訢琪
왕시량%양애강%리청%오흔기
DDNP%催化剂%臭氧催化氧化%活性炭吸附%活性炭再生
DDNP%催化劑%臭氧催化氧化%活性炭吸附%活性炭再生
DDNP%최화제%취양최화양화%활성탄흡부%활성탄재생
DDNP%catalyst%ozone catalyzed oxidation%activated carbon adsorption%regeneration of activated carbon
采用臭氧催化氧化-活性炭吸附方法处理DDNP废水,与单独臭氧氧化相比,催化剂的加入可以提高反应后期酸性环境下臭氧的氧化效率。试验选用Fe-活性炭催化组合,在曝气量为70 L/min,臭氧质量浓度为11.5 mg/L的情况下处理500 mL废水,1 h后废水中 COD、色度、硝基酚类化合物去除率分别达到72.6%、94.3%、80.6%;活性炭吸附处理臭氧催化氧化后DDNP废水可达到?兵器工业水污染排放标准?。当活性炭饱和导致水质超标时,采用臭氧对活性炭进行再生20 min,经反复10次试验,出水水质中COD稳定在131.47~152.96 mg/L,色度和硝基酚类化合物的含量低于排放标准,处理效果良好,具有可重复性。
採用臭氧催化氧化-活性炭吸附方法處理DDNP廢水,與單獨臭氧氧化相比,催化劑的加入可以提高反應後期痠性環境下臭氧的氧化效率。試驗選用Fe-活性炭催化組閤,在曝氣量為70 L/min,臭氧質量濃度為11.5 mg/L的情況下處理500 mL廢水,1 h後廢水中 COD、色度、硝基酚類化閤物去除率分彆達到72.6%、94.3%、80.6%;活性炭吸附處理臭氧催化氧化後DDNP廢水可達到?兵器工業水汙染排放標準?。噹活性炭飽和導緻水質超標時,採用臭氧對活性炭進行再生20 min,經反複10次試驗,齣水水質中COD穩定在131.47~152.96 mg/L,色度和硝基酚類化閤物的含量低于排放標準,處理效果良好,具有可重複性。
채용취양최화양화-활성탄흡부방법처리DDNP폐수,여단독취양양화상비,최화제적가입가이제고반응후기산성배경하취양적양화효솔。시험선용Fe-활성탄최화조합,재폭기량위70 L/min,취양질량농도위11.5 mg/L적정황하처리500 mL폐수,1 h후폐수중 COD、색도、초기분류화합물거제솔분별체도72.6%、94.3%、80.6%;활성탄흡부처리취양최화양화후DDNP폐수가체도?병기공업수오염배방표준?。당활성탄포화도치수질초표시,채용취양대활성탄진행재생20 min,경반복10차시험,출수수질중COD은정재131.47~152.96 mg/L,색도화초기분류화합물적함량저우배방표준,처리효과량호,구유가중복성。
DDNP wastewater was treated by ozone catalyzed oxidation and activated carbon adsorption. Experimental results show that compared with ozone oxidation alone,adding the catalyst can improve the oxidation efficiency of ozone in acidic environment of the later stage reaction. Fe-activated carbon was used as catalyst in experiment. When aeration rate is 70 L/min,and concentration of ozone is 11. 5mg/L,COD,chromaticity color,nitro-phenolic compounds degradation rates of the wastewater could respectively reach to 72. 6%,94. 3% and 80. 6% after 1 h treatment. The wastewater after treat-ment by activated carbon adsorption and zone catalyzed oxidation could meet to “weapons industrial water pollution dis-charge standards”. When the water quality was beyond standard because of the saturated activated carbon,ozone was used to regenerate activated carbon for 20min for 10 times. Then,COD in the yielding water is stable at 131. 47-152. 96 mg/L,chromaticity color and concentration of nitro-phenolic compounds are below the emission standard. The treatment effect is good,and the materials could be reused.