TY - GEN
T1 - Heterogeneous catalytic ozonation of P-chloronitrobenzene promoted by waterglass- supported zinc hydroxide in water using continuous flow mode
AU - Liu, Yue
AU - Chen, Zhong Lin
PY - 2009
Y1 - 2009
N2 - Waterglass-supported zinc hydroxide, a stable and efficient catalyst prepared in the laboratory, has been successfully used in the decomposition of ozone and trace quantities of p-chloronitrobenzene in water in continuous flow test. The decomposition rate of aqueous ozone was increased with the increase of waterglass-supported zinc hydroxide dose, and the ozone decomposition was affect by the solution pH value. Increasing the catalyst adding amount from 0mg/Lto 500mg/L the removal efficiency of p-chloronitrobenzene was from 0 to 97.5%, and the degradation efficiency increasing with the residence time prolonging. Furthermore, the existing HCO3-could inhibit the ozonation process of the p-chloronitrobenzene, the degradation efficiency of p-chloronitrobenzene is between 83% and 42% as the HCO3- concentration in the range of 50-200 mg/L. After 3d continuous stable operation in the continuous flow mode test, the catalyst remained stable in the catalytic ozonation of p-chloronitrobenzene.
AB - Waterglass-supported zinc hydroxide, a stable and efficient catalyst prepared in the laboratory, has been successfully used in the decomposition of ozone and trace quantities of p-chloronitrobenzene in water in continuous flow test. The decomposition rate of aqueous ozone was increased with the increase of waterglass-supported zinc hydroxide dose, and the ozone decomposition was affect by the solution pH value. Increasing the catalyst adding amount from 0mg/Lto 500mg/L the removal efficiency of p-chloronitrobenzene was from 0 to 97.5%, and the degradation efficiency increasing with the residence time prolonging. Furthermore, the existing HCO3-could inhibit the ozonation process of the p-chloronitrobenzene, the degradation efficiency of p-chloronitrobenzene is between 83% and 42% as the HCO3- concentration in the range of 50-200 mg/L. After 3d continuous stable operation in the continuous flow mode test, the catalyst remained stable in the catalytic ozonation of p-chloronitrobenzene.
KW - Catalytic ozonation
KW - Continuous flow mode
KW - P-chloronitrobenzene
UR - https://www.scopus.com/pages/publications/77949522040
U2 - 10.1109/ICEET.2009.552
DO - 10.1109/ICEET.2009.552
M3 - 会议稿件
AN - SCOPUS:77949522040
SN - 9780769538198
T3 - 2009 International Conference on Energy and Environment Technology, ICEET 2009
SP - 361
EP - 364
BT - 2009 International Conference on Energy and Environment Technology, ICEET 2009
T2 - 2009 International Conference on Energy and Environment Technology, ICEET 2009
Y2 - 16 October 2009 through 18 October 2009
ER -