完整後設資料紀錄
DC 欄位 | 值 | 語言 |
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dc.contributor.author | Remya, Neelancherry | en_US |
dc.contributor.author | Lin, Jih-Gaw | en_US |
dc.date.accessioned | 2019-04-02T05:59:56Z | - |
dc.date.available | 2019-04-02T05:59:56Z | - |
dc.date.issued | 2011-01-14 | en_US |
dc.identifier.issn | 1383-5866 | en_US |
dc.identifier.uri | http://dx.doi.org/10.1016/j.seppur.2010.10.012 | en_US |
dc.identifier.uri | http://hdl.handle.net/11536/150232 | - |
dc.description.abstract | Carbofuran degradation in microwave (MW)-assisted granular activated carbon (GAC)/zero-valent iron (ZVI)/hydrogen peroxide (H2O2) system(s) was investigated under different reaction temperatures, i.e. 30 degrees C, 50 degrees C and 80 degrees C, and at varying pHs, i.e. 2, 4, 6, 8 and 10. Batch experiments were conducted using a modified-MW reactor (750W power and 2450 MHz frequency) at 100 mg L-1 carbofuran concentration. The lower MW-reaction temperatures, i.e. 30 degrees C and 50 degrees C, have produced poor carbofuran degradation efficiencies whereas complete carbofuran degradation (100%) was observed at 80 degrees C and pH 6 in all the systems, i.e. MW with GAC, ZVI and H2O2. Under the similar conditions, insignificant carbofuran removal/degradation (2-24%) was observed in the presence of GAC/ZVI/H2O2 without MW. On the other hand, the carbofuran degradation rate was accelerated under the alkaline pHs, i.e. pH 8 and 10 (at 80 degrees C), and 100% carbofuran degradation was observed within 10 min in all the MW-assisted systems. However, the complete carbofuran degradation was accomplished rapidly (5 min) in the MW-assisted GAC and ZVI systems under pH 10 and 80 degrees C. Carbofuran removal in the MW-assisted systems was modeled using the first-order reaction kinetics and a maximum removal rate constant of 4.17 min(-1) was obtained in the MW-assisted ZVI system. A maximum of 86% carbofuran mineralization was achieved in the MW-assisted GAC system via hydrolysis and the removal of carbamate group. The comparison of energy consumption in MW-assisted systems with other processes reveals that the MW-assisted process is highly efficient and cost-effective for carbofuran degradation and mineralization. (C) 2010 Elsevier B.V. All rights reserved. | en_US |
dc.language.iso | en_US | en_US |
dc.subject | Microwave | en_US |
dc.subject | Carbofuran | en_US |
dc.subject | Advanced oxidation | en_US |
dc.subject | Pesticide | en_US |
dc.subject | Energy consumption analysis | en_US |
dc.title | Microwave-assisted carbofuran degradation in the presence of GAC, ZVI and H2O2: Influence of reaction temperature and pH | en_US |
dc.type | Article | en_US |
dc.identifier.doi | 10.1016/j.seppur.2010.10.012 | en_US |
dc.identifier.journal | SEPARATION AND PURIFICATION TECHNOLOGY | en_US |
dc.citation.volume | 76 | en_US |
dc.citation.spage | 244 | en_US |
dc.citation.epage | 252 | en_US |
dc.contributor.department | 環境工程研究所 | zh_TW |
dc.contributor.department | Institute of Environmental Engineering | en_US |
dc.identifier.wosnumber | WOS:000286712600004 | en_US |
dc.citation.woscount | 28 | en_US |
顯示於類別: | 期刊論文 |