浮石及其载羟基化锌催化臭氧氧化对氯硝基苯的研究
[Abstract]:With the rapid development of industry and the improvement of people's living standards, water pollution has become a widespread concern. Some refractory toxic and harmful pollutants in water, though low in concentration, are harmful and difficult to remove. Traditional water treatment processes can not effectively remove these toxic and harmful micro-pollutants, which directly threaten urban water supply. Heterogeneous catalytic ozonation has become a research hotspot because of its high efficiency, easy separation of catalysts, low cost and simple process.
Based on the preparation of pumice-based transition metal hydroxide catalysts, the removal of refractory organic compounds from water by catalytic ozonation of pumice and its composite catalysts is studied in this paper. A new catalytic ozonation technology is obtained. The microstructure, surface characteristics and catalysis of the catalysts are discussed. This kind of catalyst has the advantages of easy source, low cost and simple preparation, so it has a good market prospect.
As a catalyst, pumice exhibited strong catalytic activity for the ozonation of p-chloronitrobenzene (pCNB) in water. Compared with the ozonation process alone, the removal rate of pCNB and TOC in water by the pumice catalytic ozonation process was significantly improved. Pumice and ozone had synergistic effect on the degradation of pCNB in water, and pumice had weak adsorption capacity for pCNB.
Zinc hydroxide (ZnOOOH) / Pumice catalyst was successfully prepared in the experiment. The material has a certain adsorption capacity and adsorption capacity for gases. It was found that the surface contains abundant surface hydroxyl groups. ZnOOH / Pumice has obvious catalytic capacity. The removal rate of pCNB catalyzed ozonation increased from 55.7% to 93.4%, which is higher than that of pumice. The removal rate of pCNB by catalytic ozonation was increased by 21 percentage points. The adsorption capacity of ZnOOOH/pumice to pCNB was stronger than that of pumice.
The efficiency and influencing parameters of ZnOOH/pumice catalytic ozonation of pCNB in water were investigated. The results showed that the removal rate of pCNB was positively correlated with ozone concentration, catalyst dosage, reaction temperature and initial concentration of pCNB; the removal rate of pCNB increased with the decrease of water purity; the removal rate of Ca2+, Mg2+, Cl-, NO-3, K+ and Na+ in water was positively correlated with ZnOH/pumice catalytic ozonation. The removal rate of oxidized pCNB can be neglected, SO2 - has a certain surface complexation ability, so that the catalytic activity of pumice decreased, 4ZnOOOH / PO3 - 4 can significantly inhibit the catalytic activity of ZnOOH / pumice; CO2 - 3 / HCO - 3 basicity has a significant impact on the removal rate of catalytic ozonation of pCNB, high basicity significantly reduced the removal rate of pCNB with the reverse; With the increase of humic acid concentration, the removal rate of catalytic ozonation pCNB increased first and then decreased; the catalytic activity of ZnOOH / Pumice decreased with the increase of calcination temperature; the removal rate of pCNB was stable and maintained good catalytic activity after the catalyst was reused.
The decomposition rate constants of ozone in water were increased by 1.19 and 2.84 times, respectively. OH was detected in both catalytic systems. Tertiary butanol could significantly inhibit the degradation of pCNB in the catalytic ozonation process, which proved that the oxygen of pCNB in the catalytic ozonation process was inhibited. The catalytic activity of the catalyst is strongest at pH_pHpzc, indicating that the surface of - OH state can initiate ozone decomposition to form OH.
Catalyst surface hydroxyl group is the active site of ozone decomposition in water. Catalysts with higher catalytic activity usually have higher surface hydroxyl density. Catalyst surface active hydroxyl group adsorbs ozone in water and then produces chain decomposition reaction. OH with high oxidation is formed in the reaction process.
【学位授予单位】:哈尔滨工业大学
【学位级别】:博士
【学位授予年份】:2013
【分类号】:TU991.2
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