期刊文献+

Zero-valent iron doped carbons readily developed from sewage sludge for lead removal from aqueous solution 被引量:3

Zero-valent iron doped carbons readily developed from sewage sludge for lead removal from aqueous solution
原文传递
导出
摘要 Low-cost but high-efficiency composites of iron-containing porous carbons were prepared using sewage sludge and ferric salts as raw materials. Unlike previous time- and energy-consuming manufacturing procedures, this study shows that pyrolyzing a mixture of sludge and ferric salt can produce suitable composites for lead adsorption. The specific surface area, the total pore volume and the average pore width of the optimal composite were 321 m^2/g, 0.25 cm^3/g, and 3.17 nm, respectively. X-ray diffraction analysis indicated that ferric salt favored the formation of metallic iron, while Fourier transform infrared spectroscopy revealed the formation of hydroxyl and carboxylic groups. The result of batch tests indicated that the adsorption capacity of carbons activated with ferric salt could be as high as 128.9 mg/g, while that of carbons without activation was 79.1 mg/g. The new manufacturing procedure used in this study could save at least 19.5 k J of energy per gram of activated carbon. Low-cost but high-efficiency composites of iron-containing porous carbons were prepared using sewage sludge and ferric salts as raw materials. Unlike previous time- and energy-consuming manufacturing procedures, this study shows that pyrolyzing a mixture of sludge and ferric salt can produce suitable composites for lead adsorption. The specific surface area, the total pore volume and the average pore width of the optimal composite were 321 m^2/g, 0.25 cm^3/g, and 3.17 nm, respectively. X-ray diffraction analysis indicated that ferric salt favored the formation of metallic iron, while Fourier transform infrared spectroscopy revealed the formation of hydroxyl and carboxylic groups. The result of batch tests indicated that the adsorption capacity of carbons activated with ferric salt could be as high as 128.9 mg/g, while that of carbons without activation was 79.1 mg/g. The new manufacturing procedure used in this study could save at least 19.5 k J of energy per gram of activated carbon.
出处 《Journal of Environmental Sciences》 SCIE EI CAS CSCD 2015年第10期1-8,共8页 环境科学学报(英文版)
基金 supported by the National Key Technologies R&D Program of China(No.2012BAJ25B02)
关键词 Adsorption Energy-saving Iron-containing porous carbon Lead Sludge Adsorption Energy-saving Iron-containing porous carbon Lead Sludge
  • 相关文献

参考文献1

二级参考文献13

  • 1[1]Andrey B, Teresa J B, 2002. H2 S adsorption on materials obtained using sulfuric acid activation of sewage sludge-derived fertilizer[J]. Journal of Collid and Interface Science, 252: 188-194.
  • 2[2]Bacaoui A, Yaacoubi A, Dahbi A, 2001. Optimization of conditions for the preparation of activated carbons from olive-waste cakes [ J ]. Carbon, 39:425-432.
  • 3[3]Box G, Hunter W G, Hunter J S, 1978. Statics for experimenters, an introduction to design, data analysis and model building [ M ]. New York:Wiley. 306-604.
  • 4[4]Chen X G, Jeyaseelan S, Graham N, 2002. Phyical and chemical properties study of the activated carbon made from sewage sludge [ J ]. Waste Management, 22: 755-760.
  • 5[5]Doehlert D H, 1970. Uniform shell designs[J]. Applied Statistics, 19: 231-239.
  • 6[6]Inguanzo M, Domingguez A, Blanco C G, 2002. On the pyrolysis of sewage sludge: the influence of conditions on solid, liquid and gas fractions [ J ].Journal of Analytical and Applied Pyrolysis, 63: 209-222.
  • 7[7]Myers R H, Montgomery D C, 1995. Response suface methodology: process and product optimization using designed experiments [ M ]. New York: John Wiley & Sons.
  • 8[8]Naozumi K, Aki M, Yoshinori I, 2002. Adsorption removal of pollutions by active cokes produced from sludge in the energy recycle process of wastes[J].Waste Management, 22: 399-404.
  • 9[9]Rivera-Utrilla J, Utrera-Hidalgo E, Ferro-Garcia M A et al. , 1991. Comparison of activated carbons prepared from agricultural raw materials and Spanish lignites when removing chlorophenols from aqueous solutions [ J]. Carbon,29: 613-619.
  • 10[10]StummW, Morgan J J, 1981. Aquatic chemistry[M]. 2nd ed. New York:Wiley, Inter-Science.

共引文献15

同被引文献57

引证文献3

二级引证文献7

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