Application of nanofiltration for recycling of paper regeneration wastewater and characterization of filtration resistance

被引:23
作者
Ahn, KH [1 ]
Cha, HY [1 ]
Yeom, IT [1 ]
Song, KG [1 ]
机构
[1] Korea Inst Sci & Technol, Environm Res Ctr, Seoul 130650, South Korea
关键词
D O I
10.1016/S0011-9164(98)00141-6
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The potential of using nanofiltration (NF) membranes in purification of the effluent from paper regeneration wastewater treatment plant was investigated. The change of filtration resistance for various NF membranes and the mechanisms responsible for the resistance were identified. The mahyority of the pollutants remaining in the wastewater were mostly nonbiodegradable and ware less than MWCO 3000 in size, indicating micro- or ultrafiltration may not be applicable. Among the five NF membranes used in this study, NTR-759HR showed the highest rejection efficiency; 98.5% and 99.5% for TOC and color, respectively. The TOC concentration of the permeate could be maintained at less than 0.7 mg/L regardless of the concentration of the feed solution. However, the permeate flux steadily decreased with time up to 50% of the initial value at the recovery rate of 89%, To investigate the possible mechanisms responsible for the reduction of permeate flux, the observed total filtration resistance was divided into three categories; (1) the intrinsic membrane resistance for pure water (R-m), (2) resistance due to concentration polarization (R-cp), and (3) resistance due to membrane fouling (R-f). The increase of filtration resistance for NTR 7410 could be explained by membrane fouling while those for NTR-759HR and NTR-7250 are attributed to the osmotic pressure build-up due to concentration polarization. The different mechanisms for the flux reduction were studied.
引用
收藏
页码:169 / 176
页数:8
相关论文
共 13 条
[1]   Nanofiltration of bleaching pulp and paper effluents in tubular polymeric membranes [J].
Afonso, MD ;
DePinho, MN .
SEPARATION SCIENCE AND TECHNOLOGY, 1997, 32 (16) :2641-2658
[2]  
APHA AWWA WEF, 1995, STAND METH EX WAT WA
[3]   Membrane performance with a pulp mill effluent: Relative contributions of fouling mechanisms [J].
DalCin, MM ;
McLellan, F ;
Striez, CN ;
Tam, CM ;
Tweddle, TA ;
Kumar, A .
JOURNAL OF MEMBRANE SCIENCE, 1996, 120 (02) :273-285
[4]  
GORGOV M, 1988, TAPPI J DEC, P175
[5]   NANOFILTRATION OF MODEL ACETATE SOLUTIONS [J].
HAN, IS ;
CHERYAN, M .
JOURNAL OF MEMBRANE SCIENCE, 1995, 107 (1-2) :107-113
[6]  
HONG SK, 1997, J MEMB SCI, V132, P158
[7]   MOLECULAR-WEIGHT DISTRIBUTIONS OF ORGANIC HALOGENS IN BLEACHED KRAFT PULP-MILL EFFLUENTS [J].
JOKELA, JK ;
SALKINOJASALONEN, M .
ENVIRONMENTAL SCIENCE & TECHNOLOGY, 1992, 26 (06) :1190-1197
[8]   Development of simulation system to combine production process and wastewater treatment: Calibration of bleached kraft process model through dissolved organic matter in fibreline [J].
Luonsi, A ;
Halttunen, S .
WATER SCIENCE AND TECHNOLOGY, 1997, 35 (2-3) :15-23
[9]  
NOURTILAJOKINEN J, 1996, J MEMB SCI, V119, P99
[10]   Characterization of cleaning results using combined flux and streaming potential methods [J].
Nystrom, M ;
Zhu, HH .
JOURNAL OF MEMBRANE SCIENCE, 1997, 131 (1-2) :195-205