Adsorption of polyethylene glycol (PEG) from aqueous solution onto hydrophobic zeolite

被引:93
作者
Chang, CY
Tsai, WT [1 ]
Ing, CH
Chang, CF
机构
[1] Chia Nan Univ Pharm & Sci, Dept Environm Engn & Hlth, Tainan 717, Taiwan
[2] Natl Taiwan Univ, Grad Inst Environm, Taipei 106, Taiwan
关键词
liquid-phase adsorption; polyethylene glycol; hydrophobic zeolite; isotherm; kinetic modeling; restrictive diffusion;
D O I
10.1016/S0021-9797(02)00174-1
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
In the present study, a hydrophobic zeolite was used as an adsorbent for the adsorption of polyethylene glycol (PEG) in water solution and electroplating solution at 25 degreesC. The adsorption capacities were determined through the adsorption isotherms in a thermostated shaker. The rate of adsorption, on the other hand, was investigated in a batch adsorber under controlled process parameters such as initial PEG concentration (30, 70, 110, 150, 200, and 300 mg dm(-3)), agitation speed (200, 800, and 1000 rpm), and adsorbent particle size (0.72, 1.44, and 2.03 mm). A batch kinetic model, according to a pseudo-second-order mechanism, has been tested to predict the rate constant of adsorption, equilibrium adsorption capacity, time of half-adsorption, and equilibrium concentration by the fitting of the experimental data. The results of the adsorption isotherm and kinetic studies show that the adsorption process can well be described with the Langmuir and Freundlich models and the pseudo-second-order equation, respectively. Comparing the values of adsorption parameters of PEG in water solution and electroplating solution, there are no significant differences. In addition, the effective diffusion coefficient of the PEG molecule in the microporous adsorbent has been estimated at about 3.20 x 10(-8) cm(2) s(-1) based on the restrictive diffusion model. (C) 2003 Elsevier Science (USA). All rights reserved.
引用
收藏
页码:273 / 279
页数:7
相关论文
共 31 条
  • [1] Adsorption of dyes using shale oil ash
    Al-Qodah, Z
    [J]. WATER RESEARCH, 2000, 34 (17) : 4295 - 4303
  • [2] Kinetics and mechanisms of polyethyleneglycol fragmentation by ozone in aqueous solution
    Andreozzi, R
    Caprio, V
    Insola, A
    [J]. WATER RESEARCH, 1996, 30 (12) : 2955 - 2960
  • [3] [Anonymous], J CHEM ENG JPN
  • [4] [Anonymous], 1992, ADSORPTION TECHNOLOG
  • [5] Polyethylene glycol adsorption equilibrium on activated carbon
    Arbuckle, WB
    Osman, MY
    [J]. ENVIRONMENTAL ENGINEERING SCIENCE, 2000, 17 (03) : 147 - 158
  • [6] Bansal R.C., 1988, ACTIVE CARBON
  • [7] HYDROPHOBIC ZEOLITE ADSORBENT - A PROVEN ADVANCEMENT IN SOLVENT SEPARATION TECHNOLOGY
    BLOCKI, SW
    [J]. ENVIRONMENTAL PROGRESS, 1993, 12 (03): : 226 - 230
  • [8] Adsorption equilibrium of polyethylene glycol in the copper electroplating solution on activated carbon
    Chang, CF
    Chang, CY
    Tsai, WT
    Wu, SC
    [J]. JOURNAL OF COLLOID AND INTERFACE SCIENCE, 2000, 232 (01) : 207 - 209
  • [9] Kinetics of decomposition of polyethylene glycol in electroplating solution by ozonation with UV radiation
    Chang, CY
    Chen, YH
    Li, H
    Chiu, CY
    Yu, YH
    Chiang, PC
    Ku, Y
    Chen, JN
    [J]. JOURNAL OF ENVIRONMENTAL ENGINEERING-ASCE, 2001, 127 (10): : 908 - 915
  • [10] CHANG CY, 2000, J CHIN I ENV ENG TAI, V10, P69