Adsorption of creatinine on active carbons with nitric acid hydrothermal modification

被引:32
作者
Cao, Yuhe [1 ]
Gu, Yan [2 ]
Wang, Keliang [1 ]
Wang, Xiaomin [1 ]
Gu, Zhengrong [1 ]
Ambrico, Tyler [3 ]
Castro, Maria Andrea [4 ]
Lee, Joun [5 ]
Gibbons, William [6 ]
Rice, James A. [7 ]
机构
[1] South Dakota State Univ, Agr & Biosyst Engn Dept, Brookings, SD 57007 USA
[2] Inst Chem Ind Forest Prod, Nanjing, Jiangsu, Peoples R China
[3] SUNY Stony Brook, Dept Phys & Astron, Stony Brook, NY 11794 USA
[4] Univ Iowa, Dept Chem, Iowa City, IA 52242 USA
[5] Univ Iowa, Cent Microscopy Res Facil, Iowa City, IA USA
[6] South Dakota State Univ, Dept Biol & Microbiol, Brookings, SD 57007 USA
[7] South Dakota State Univ, Dept Chem & Biochem, Brookings, SD 57007 USA
基金
美国国家科学基金会;
关键词
Creatinine; Active carbon; Nitric acid; Hydrothermal; Adsorption; SURFACE-CHEMISTRY; RENAL-FAILURE; SULFUR-COMPOUNDS; BUTANOL VAPOR; NITROGEN; OXIDATION; REMOVAL; FIBERS; LIQUID; FUNCTIONALITIES;
D O I
10.1016/j.jtice.2016.06.008
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The adsorption of creatinine on active carbons was studied. Original active carbon (AC) and AC samples modified by nitric acid hydrothermal modification were assessed for their ability to adsorb creatinine. The pore structure and surface properties of the AC samples were characterized by N-2 adsorption, temperature programmed desorption (TPD), Fourier Transform Infrared spectroscopy (FTIR), and X-ray photoelectron spectrometer (XPS). It indicated that 4M HNO3 hydrothermal modification with 180 degrees C was an efficient method in improvement of the creatinine adsorption. The improved adsorption capacity can be attributed mainly to an increase in the acidic oxygen-containing functional groups. The adsorption of creatinine over AC may involve an interaction with the acidic oxygen-containing groups on AC. Langmuir and Freundlich adsorption models were applied to describe the experimental isotherm and isotherm constants. Equilibrium data fitted very well to the Freundlich model in the entire saturation range (3.58-59.08 mg L-1). The maximum adsorption capacities of AC modified with 180 degrees C is 62.5 mg g(-1) according to the Langmuir model. Pseudo first-order and second-order kinetic models were used to describe the kinetic data and the rate constants were evaluated. The experimental data fitted well to the second-order kinetic model, which indicates that the chemical adsorption was the rate-limiting step, instead of mass transfer. Published by Elsevier B.V. on behalf of Taiwan Institute of Chemical Engineers.
引用
收藏
页码:347 / 356
页数:10
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