Optimization of oxygen transfer in clean water by fine bubble diffused air system and separate mixing in aeration ditches

被引:9
作者
Deronzier, G [1 ]
Duchene, P [1 ]
Heduit, A [1 ]
机构
[1] Cemagref, Grp Antony, Div Qual Eaux, F-92185 Antony, France
关键词
clean water; diffused air; full scale; horizontal flow; mixing; oxygen transfer;
D O I
10.2166/wst.1998.0170
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The influence of design parameters on the transfer of oxygen was studied in different ring ditches equipped with fine bubble membrane air diffusers and separate mixing. The results produced evidence that the oxygen transfer efficiency (OTE) decreases when the air flow rate per diffuser increases. OTE increases asymptotically with the horizontal water flow (50% for velocity up to 0.5 m/sec). It increases also when the diffuser modules are brought closer together. Theoretical analysis enabled ranking of the impact of the design parameters on which the oxygen transfer is dependent, namely the interfacial area (a) and the oxygen transfer coefficient (K1). The increase in the air flow rate per diffuser essentially reduces the interfacial area by an increase in the diameter of the initial air bubbles and by a reduction of the contact time due to an acceleration of the "spiral flows" (vertical rotation of water flow). The horizontal rotation of water increases the interfacial area most probably by decreasing the diameter of the initial air bubbles and by a lengthening of the contact time resulting from a reduction in the large spiral flows. Bringing the diffuser modules closer together makes longer the contact time by a reduction in the large spiral flows. (C) 1998 Published by Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:35 / 42
页数:8
相关论文
共 19 条
[11]   TESTS ON AERATORS - CONCLUSIONS DRAWN FROM 500 CLEAN WATER TESTS CONDUCTED IN 200 DIFFERENT SEWAGE-TREATMENT PLANTS .2. DATA INTERPRETATION [J].
HEDUIT, A ;
RACAULT, Y .
WATER RESEARCH, 1983, 17 (03) :289-297
[12]  
KUPFERBERG A, 1969, TRANS INST CHEM ENG, V47, pT241
[13]   REGIMES OF BUBBLING AT A SUBMERGED ORIFICE [J].
MCCANN, DJ ;
PRINCE, RGH .
CHEMICAL ENGINEERING SCIENCE, 1971, 26 (10) :1505-&
[14]   BUBBLE FORMATION AND WEEPING AT A SUBMERGED ORIFICE [J].
MCCANN, DJ ;
PRINCE, RGH .
CHEMICAL ENGINEERING SCIENCE, 1969, 24 (05) :801-&
[15]   COALESCENCE AND BREAKUP OF BUBBLES IN LIQUIDS [J].
OTAKE, T ;
TONE, S ;
NAKAO, K ;
MITSUHASHI, Y .
CHEMICAL ENGINEERING SCIENCE, 1977, 32 (04) :377-383
[16]  
Pasveer A, 1965, J Water Pollut Control Fed, V37, P1267
[17]  
ROQUES H, 1979, TECHNIQUE DOCUMENTAT, V2, P1015
[18]  
Treybal R.E., 1980, MASS TRANSFER OPERAT, P139
[19]  
VANDERGRAAF JHJM, 1979, PROG WATER TECHNOL, V11, P127