High nutrient removal in the three-sludge sewage treatment system: Results and economic evaluation

被引:2
作者
Marsman, EH
Roeleveld, PJ
Rensink, JH
机构
[1] HASKONING,NL-6500 AD NIJMEGEN,NETHERLANDS
[2] AGR UNIV WAGENINGEN,DEPT ENVIRONM TECHNOL,NL-6700 EV WAGENINGEN,NETHERLANDS
关键词
three-sludge sewage treatment system; high loaded biological phosphorus removal; nitrifying biofilm reactor; denitrifying biofilm reactor; compact; high load; economical competing;
D O I
10.2166/wst.1997.0375
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The Three-sludge sewage treatment system proved to he a stable process for the treatment of wastewater. This new concept consists of three separated bioreactors. Biological removal of phosphorus and COD takes place in the first high loaded activated sludge bioreactor with an intermediate settler. The second reactor is a nitrifying biofilm reactor. Nitrate is removed in the third denitrifying biofilm reactor. Pilot plant research (scale 2-3 p.e.) showed that at a constant flow rate during night and day a minimal hydraulic retention time of 10.4 hours, inclusive, the settler, could be obtained and yet still the stringent effluent standards (10 mg Nil and 1 mg P/l) were met. At a dynamic flow rate with day/night rhythm and at a storm-weather peak flow rate of 2.5 times the dry weather flow rate the standards were still met. However, at a flow rate of three times the dry-weather flow rate the concentration of P-total increased which indicates instability of the dephosphatating bioreactor under the set process conditions. The nitrification and the denitrification capacity remained excellent. The economical evaluation showed that the Three-sludge sewage treatment system can compete with conventional low loaded activated sludge plants in The Netherlands. Moreover, this advanced technology only occupies 40% of the space of conventional plants. (C) 1997 IAWQ. Published by Elsevier Science Ltd.
引用
收藏
页码:129 / 136
页数:8
相关论文
共 7 条
[1]  
ANDERSON B, 1993, WAT SCI TECH, V29, P47
[2]  
BOLLER M, 1993, WAT SCI TECH, V29, P1
[3]  
DIRKZWAGER AH, 1994, EUROPEAN WATER POLLU, V4, P9
[4]  
HONG SN, 1982, US EPA WORKSH BIOL P
[5]  
ROELEVELD PJ, 1994, IN PRESS P AS WAT TE
[6]  
RYHINER G, 1993, WAT SCI TECH, V29, P111
[7]  
WOUDA TWM, 1987, H2O, V20, P384