Removal of monoethanolamine and phosphate from thin-film transistor liquid crystal display (TFT-LCD) wastewater by the fluidized-bed Fenton process

被引:39
|
作者
Su, Chia-Chi [1 ]
Chen, Chia-Min [1 ]
Anotai, Jin [2 ]
Lu, Ming-Chun [1 ]
机构
[1] Chia Nan Univ Pharm & Sci, Dept Environm Resources Management, Tainan 717, Taiwan
[2] King Mongkuts Univ Technol Thonburi, Fac Engn, Dept Environm Engn, Natl Ctr Excellence Environm & Hazardous Waste Ma, Bangkok 10140, Thailand
关键词
Fluidized-bed reactor; Fenton process; Kinetics; Monoethanolamine; Phosphate; SUPPORTED IRON-OXIDE; PHOSPHORUS REMOVAL; PRECIPITATION; OXIDATION; CRYSTALLIZATION; OPTIMIZATION; TECHNOLOGIES; DEGRADATION; RECOVERY;
D O I
10.1016/j.cej.2012.08.063
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Synthetic wastewater containing monoethanolamine (MEA) and phosphate, which was generated during the cleaning and etching processes for thin-film transistor liquid crystal displays (TFT-LCDs) was treated using a novel process. Degradation of MEA was studied and compared using the Fenton and fluidized-bed Fenton processes. Comparison results show that the Fe2+ concentration was an important factor for MEA and chemical oxygen demand (COD) removal in the fluidized-bed Fenton process. The degradation of MEA followed pseudo-first-order reaction kinetics. The MEA, COD and total organic carbon (TOC) removal efficiencies by the fluidized-bed Fenton process after 60 min were 15-26% higher than those by the Fenton process. The phosphate removal rate followed a first-order reaction. Phosphate removal was optimized by selecting sand grains sized (0.24-0.5 mm) and a molar ratio of Fe2+/P of 1.3 at pH 7. In the two stages, optimized conditions were Fe2+/P = 1.3 at pH 7 using 100 g SiO2 for phosphate removal, and 3 mM Fe2+ and 50 mM H2O2 at pH 3 for MEA removal; phosphate removal efficiency was 45% and MEA removal efficiency was 76%. (C) 2012 Published by Elsevier B.V.
引用
收藏
页码:128 / 135
页数:8
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