Screening of combined zeolite-ozone system for phenol and COD removal

被引:49
作者
Amin, Nor Aishah Saidina [1 ]
Akhtar, Javaid [1 ]
Rai, H. K. [1 ]
机构
[1] Univ Teknol Malaysia, Fac Chem & Nat Resources Engn, CREG, Skudai 81310, Johor Darul Tak, Malaysia
关键词
Zeolites; HZSM-5; Phenol; Ozonation; Adsorption; HIGH-SILICA ZEOLITES; WASTE-WATER TREATMENT; AQUEOUS-SOLUTION; CATALYTIC OZONATION; DRINKING-WATER; DECOMPOSITION; ADSORPTION; DEGRADATION; OXIDATION; REACTOR;
D O I
10.1016/j.cej.2010.01.042
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
In this study, four zeolites in H-form (HZSM-5, H-Beta, H-Mordenite, and H-USY) were tested at different operating conditions for removal of phenol and COD by ozonation. The process variables include concentration of phenol in solution, ozonated airflow rates, pH of solution, temperature, and reaction time. According to experimental results, combination of zeolite and ozone was able to remove both phenol and COD effectively compared to without ozone. Zeolite mainly acted as adsorbent, providing surface for reaction between ozone and phenol. However, the adsorption capacity of zeolites decreased at higher pH due to the formation of OH radicals, which diminished the surface reactions, but enhanced the bulk removal of phenol. Large flow rates of zonated air and ambient temperature were suitable for removal of both phenol and COD. A maximum of 50.5% phenol was removed by HZSM-5(80) at 100 ppm of phenol concentration. HZSM-5(80) removed both phenol and COD effectively compared to other zeolites at all operating conditions except when phenol concentration was higher at which H-USY was a better catalyst. (C) 2010 Elsevier B.V. All rights reserved.
引用
收藏
页码:520 / 527
页数:8
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