Reversibility of adsorption of aromatic compounds onto powdered activated carbon (PAC)

被引:48
作者
deJonge, RJ [1 ]
Breure, AM [1 ]
vanAndel, JG [1 ]
机构
[1] NATL INST PUBL HLTH & ENVIRONM PROTECT,3720 BA BILTHOVEN,NETHERLANDS
关键词
activated sludge; activation method; adsorptive capacity; 3-chlorobenzoic acid; o-cresol; desorption; irreversible adsorption; leaching; 2-methylphenol; oxidative polymerization; oxygen; wastewater treatment;
D O I
10.1016/0043-1354(95)00248-0
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Desorption of sorbed compounds is an important process in the powdered activated carbon-activated sludge (PAC-AS) wastewater treatment system, where sorption and biodegradation interact. To assess the extent of desorption to be expected in the PAC-AS system, reversibility of adsorption was investigated using isotherm studies and a leaching technique under the conditions prevalent in the PAC-AS system. Two aromatic compounds, o-cresol and 3-chlorobenzoic acid (3-CB), and two types of powdered activated carbon (PAC) were used to study desorption. High degrees of irreversible adsorption were observed with both desorption techniques, depending on the type of PAC and the compound. The thermally activated, peat-based PAC (SA4) showed a high degree of irreversible adsorption compared to the chemically activated, wood-derived PAC (CA1). The phenolic compound, o-cresol, could be desorbed to a lesser extent than 3-CB from both types of PAC. Contact time between the PAC and the compound was found to affect the desorption of o-cresol adversely. Oxygen availability enhanced the adsorptive capacity of SA4 for o-cresol. Sorption of 3-CB proved unaffected by either contact time or oxygen. Oxidative polymerization as a probable mechanism for the irreversible adsorption observed is also discussed. Desorption kinetics from SA4 showed a first phase of rapid desorption followed by a second phase of slow desorption. CA1 displayed the first rapid desorption phase only.
引用
收藏
页码:883 / 892
页数:10
相关论文
共 27 条
[21]   ROLE OF DISSOLVED-OXYGEN ON THE ADSORPTIVE CAPACITY OF ACTIVATED CARBON FOR SYNTHETIC AND NATURAL ORGANIC-MATTER [J].
VIDIC, RD ;
SUIDAN, MT .
ENVIRONMENTAL SCIENCE & TECHNOLOGY, 1991, 25 (09) :1612-1618
[22]   BIOLOGICAL ACTIVATED CARBON IN FLUIDIZED-BED REACTORS FOR THE TREATMENT OF GROUNDWATER CONTAMINATED WITH VOLATILE AROMATIC-HYDROCARBONS [J].
VOICE, TC ;
PAK, D ;
ZHAO, XD ;
SHI, J ;
HICKEY, RF .
WATER RESEARCH, 1992, 26 (10) :1389-1401
[23]   MICROBIAL-DEGRADATION OF POLYCYCLIC AROMATIC-HYDROCARBONS - EFFECT OF SUBSTRATE AVAILABILITY ON BACTERIAL-GROWTH KINETICS [J].
VOLKERING, F ;
BREURE, AM ;
STERKENBURG, A ;
VANANDEL, JG .
APPLIED MICROBIOLOGY AND BIOTECHNOLOGY, 1992, 36 (04) :548-552
[24]   FATE OF TOXIC ORGANIC-COMPOUNDS IN ACTIVATED-SLUDGE AND INTEGRATED PAC SYSTEMS [J].
WEBER, WJ ;
JONES, BE ;
KATZ, LE .
WATER SCIENCE AND TECHNOLOGY, 1987, 19 (3-4) :471-482
[25]  
WEISSENFELS WD, 1992, APPL MICROBIOL BIOT, V36, P689, DOI 10.1007/BF00183251
[26]   SINGLE-SOLUTE IRREVERSIBLE ADSORPTION ON GRANULAR ACTIVATED CARBON [J].
YONGE, DR ;
KEINATH, TM ;
POZNANSKA, K ;
JIANG, ZP .
ENVIRONMENTAL SCIENCE & TECHNOLOGY, 1985, 19 (08) :690-694
[27]  
NORIT TESTING METHOD