期刊文献+

硝酸活化活性炭吸附水中阿莫西林的研究 被引量:7

Research on Adsorption of Amoxicillin in Aqueous Solution Using Activated Carbon Modified with Hydrogen Nitrate
下载PDF
导出
摘要 研究了吸附时间、初始阿莫西林浓度和初始pH对硝酸活化活性炭吸附水中阿莫西林的影响,并根据吸附时间和初始阿莫西林浓度的变化探讨了活化活性炭吸附水中阿莫西林的动力学和吸附等温线模型。结果表明,常温下,对初始阿莫西林浓度分别为50.0和200.0 mg/L的溶液,0.100 0 g活化活性炭在60 min可达吸附平衡;初始pH为4~6时吸附效果较好;当初始阿莫西林浓度为193.7 mg/L,pH为4.05,0.100 0 g活化活性炭吸附60 min时,阿莫西林的吸附率为78.79%,吸附量为71.4 mg/g;活化活性炭吸附阿莫西林较符合Freundlich吸附等温线;伪二级动力学模型能较好地描述活化活性炭对水中阿莫西林的吸附动力学。 The adsorption of amoxicillin(AMX) in aqueous solution on activated carbon modified with hydrogen nitrate was investigated under different conditions,and the adsorption kinetics and adsorption isotherm models of activated carbon adsorbing AMX in aqueous solution were explored based on variation of adsorption time and initial AMX concentration.The results showed that the adsorption equilibrium time for initial AMX concentration of 50.0 mg/L and 200.0 mg/L,respectively was nearly 60 min with 0.100 0 g of activated carbon,and there had a well adsorption percentage when the initial pH of AMX solution was at 4-6.The adsorption percentage and the adsorption quantity were 78.79% and 71.4 mg/g,respectively,under the optimum condition of 193.7 mg/L of initial AMX with 4.05 of pH,60 min of adsorption time and 0.100 0 g of activated carbon modified with HNO 3.Freundlich adsorption isotherm could be used to describe the adsorption of AMX on activated carbon and the adsorption of activated carbon adsorbing AMX in aqueous solution was well fitted to the pseudo-second kinetics.
出处 《环境工程技术学报》 CAS 2013年第5期416-421,共6页 Journal of Environmental Engineering Technology
关键词 阿莫西林 活化活性炭 吸附等温线 吸附动力学 amoxicillin activated carbon adsorption isotherm adsorption kinetics
  • 相关文献

参考文献16

二级参考文献70

共引文献50

同被引文献61

  • 1芦春梅,李增文,姜桂兰.活性秸杆炭素吸附-化学氧化法在印染废水处理中的应用研究[J].工业水处理,2005,25(5):56-58. 被引量:12
  • 2徐涛,刘晓勤.花生壳活性炭研究进展[J].花生学报,2007,36(3):1-4. 被引量:29
  • 3吕昂,张俐娜.纤维素溶剂研究进展[J].高分子学报,2007,17(10):937-944. 被引量:119
  • 4VETHAAK A D, LAHR J, SCHRAP S M, et al. An integrated assessment of estrogenic contamination and biological effects in the aquatic environment of the Netherlands [ J ]. Chemosphere, 2005,59(4) :511-524.
  • 5GHOSH J P, TAYLOR K E, BEWTRA J K, et al. Laccase- catalyzed removal of 2, 4-dimethyphenol from synthetic wastewater: effect of polyethylene glycol and dissolved oxygen [ J ]. Chemosphere ,2008,71 ( 9 ) : 1709-1717.
  • 6GAO P, FENG Y, ZHANG Z, et al. Comparison of competitive and synergetic adsorption of three phenolic compounds on river sediment [ J ]. Environmental Pollution, 2011, 159 ( 10 ) : 2876-2811.
  • 7LESAGE N, SPERANDIO M, CABASSUD C. Study of a hybrid process: adsorption on activated carbon/membrane bioreactor for the treatment of an industrial wastewater [ J ]. Chemical Engineering and Processing ,2008,47 ( 3 ) :303-307.
  • 8WANG W, HAN H. Recovery strategies for tacking the impact of phenolic compounds in a UASB reactor treating coal gasification wastewater[J]. Bioresource Technology,2012,103 ( 1 ) :95-100.
  • 9KALLEL M, BELAID C, MECHICHI T, et al. Removal of organic load and phenolic compounds from olive mill wastewater by Fenton oxidation with zero-valent iron[ J]. Chemical Engineering Journal,2009,150(2/3 ) :391-395.
  • 10BARANSI K, DUBOWSKI Y, SABBAH I. Synergetic effect between photocatalytic degradation and adsorption process on the removal of phenolic compounds from olive mill wastewater [ J ]. Water Research ,2012,46 (3) :789-798.

引证文献7

二级引证文献15

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部