Anaerobic-aerobic biotreatment of simulated textile effluent containing varied ratios of starch and azo dye

被引:131
作者
O'Neill, C
Hawkes, FR [1 ]
Hawkes, DL
Esteves, S
Wilcox, SJ
机构
[1] Univ Glamorgan, Sch Appl Sci, Pontypridd CF37 1DL, M Glam, Wales
[2] Univ Glamorgan, Sch Design & Adv Technol, Pontypridd CF37 1DL, M Glam, Wales
关键词
azo dye; anaerobic-aerobic biotreatment; UASB reactor;
D O I
10.1016/S0043-1354(99)00395-4
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Combined anaerobic-aerobic treatment was used to treat a simulated textile industry wastewater (overall HRT 1.8 days). The azo dye (PROCION Red H-E7B) and starch concentrations were varied in a series of 1-week experiments to determine the effect of starch:dye ratio on GOD, BOD and colour removal. The treatment efficiency of the system at 1.9 g 1(-1) starch and 0.15 g 1(-1) dye remained constant over 130 days despite seven intervening 1-week periods of operation at other starch:dye ratios. Most colour removal occurred in the UASB reactor (1 d HRT), and the BOD:COD of the UASB reactor effluent increased by up to 47%. The maximum overall COD removal was 88% and the BOD removal was up to 99%. A maximum of 77% colour removal overall was achieved with starch and dye concentrations of 3.8 and 0.15 g 1(-1), giving a final true colour of 0.21 TCU. At both 0.15 and 0.75 g 1(-1) dye a starch concentration of 3.8 g 1(-1) rather than 1.9 g 1(-1) gave a significant improvement in colour removal. However, at 3.8 g 1(-1) starch volatile fatty acid levels in the UASB reactor rose, while at 2.9 g 1(-1) starch they did not. It is recommended that if colour removal efficiency decreases, carbohydrate should be added to the anaerobic reactor at a maximum sludge loading rate between 0.11 and 0.15 kg COD kg(-1) TVS d(-1). (C) 2000 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:2355 / 2361
页数:7
相关论文
共 27 条
[1]   Biological treatment of dye wastewaters using an anaerobic-oxic system [J].
An, H ;
Qian, Y ;
Gu, XS ;
Tang, WZ .
CHEMOSPHERE, 1996, 33 (12) :2533-2542
[2]  
ANGENENT LT, 1995, 50 PURD IND WAST C P, P365
[3]  
[Anonymous], 1989, STANDARD METHODS EXA, V17th
[4]  
[Anonymous], COLOUR DYEHOUSE EFFL
[5]   The use of sequential anaerobic/aerobic processes for the biotreatment of a simulated dyeing wastewater [J].
Basibuyuk, M ;
Forster, CF .
ENVIRONMENTAL TECHNOLOGY, 1997, 18 (08) :843-848
[6]  
BOE RW, 1993, HAZARDOUS IND WASTES
[7]  
Carliell CM, 1996, WATER SA, V22, P225
[8]  
CARLIELL CM, 1994, WATER SA, V20, P341
[9]   REMOVAL OF DYEWASTE COLOR FROM SEWAGE EFFLUENT - THE USE OF A FULL-SCALE OZONE PLANT [J].
CHURCHLEY, JH .
WATER SCIENCE AND TECHNOLOGY, 1994, 30 (03) :275-284
[10]  
Delée W, 1998, J CHEM TECHNOL BIOT, V73, P323, DOI 10.1002/(SICI)1097-4660(199812)73:4<323::AID-JCTB976>3.3.CO