COD removal from textile industry effluent: pilot plant studies

被引:40
作者
Walker, GM
Weatherley, LR
机构
[1] Queens Univ Belfast, Sch Chem Engn, Belfast BT9 5AG, Antrim, North Ireland
[2] Univ Canterbury, Dept Chem & Proc Engn, Christchurch 1, New Zealand
关键词
adsorption; pilot plant; activated carbon; textile process effluent; bed depth service time model;
D O I
10.1016/S1385-8947(01)00197-8
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
This work involved the treatment of industrial waste water from a nylon carpet printing plant. As dyeing of nylon is particularly difficult, acid dyes, fixing agents, thickeners, finishing agents, are required for successful colouration and cause major problems with the plant's effluent disposal in terms of chemical oxygen demand (COD). Granular activated carbon (GAC) Filtrasorb 400 was used to treat a simulated process plant effluent containing all the pollutants. Equilibrium isotherm experiments were established and experimental data obtained showed good empirical correlation with Langmuir isotherm theory. Column experimental data, in terms of COD were correlated using the bed depth service time (BDST) model. Solid phase loading in the columns were found to approach that in equilibrium studies indicating an efficient use of adsorbent. The results from the BDST model were then used to design a pilot adsorption rig at the plant. The performance of the pilot plant column were accurately predicted by scale-up from the bench scale columns. (C) 2001 Elsevier Science BN. All rights reserved.
引用
收藏
页码:125 / 131
页数:7
相关论文
共 15 条
[1]   An examination of the treatability of a simulated textile wastewater containing Maxilon Red BL-N [J].
Basibuyuk, M ;
Forster, CF .
PROCESS BIOCHEMISTRY, 1997, 32 (06) :523-527
[2]   GAC adsorption of ozonated secondary textile effluents for industrial water reuse [J].
Bergna, G ;
Bianchi, R ;
Malpei, F .
WATER SCIENCE AND TECHNOLOGY, 1999, 40 (4-5) :435-442
[3]  
Bohart G.S., 1920, J CHEM SOC, V42
[4]   The adsorption characteristics of EDTA-chelated copper ion by activated carbon in a column test [J].
Chang, C ;
Ku, Y .
SEPARATION SCIENCE AND TECHNOLOGY, 1998, 33 (04) :483-501
[5]   Evaluation of granular activated carbon for removal of trace organic compounds in drinking water [J].
Chen, PH ;
Jenq, CH ;
Chen, KM .
ENVIRONMENT INTERNATIONAL, 1996, 22 (03) :343-359
[6]   Equilibrium uptake, sorption dynamics, process development, and column operations for the removal of copper and nickel from aqueous solution and wastewater using activated slag, a low-cost adsorbent [J].
Gupta, VK .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1998, 37 (01) :192-202
[7]  
HUTCHINS RA, 1973, CHEM ENG-NEW YORK, V80, P133
[8]   The adsorption of mixed dyes (acidic and basic) on to hardwood in a fixed bed [J].
Magdy, YH .
ADSORPTION SCIENCE & TECHNOLOGY, 1996, 13 (05) :367-375
[9]   SIMPLIFIED OPTIMIZATION PROCEDURE FOR FIXED-BED ADSORPTION SYSTEMS [J].
MCKAY, G ;
BINO, MJ .
WATER AIR AND SOIL POLLUTION, 1990, 51 (1-2) :33-41
[10]  
Perrotti A., 1974, AICHE S SER, V70, P317