Disinfection optimization by a better control of ozonation process

2009 ◽  
Vol 9 (6) ◽  
pp. 699-706
Author(s):  
Y. Jaeger ◽  
D. Lénès ◽  
M. Le Bihan ◽  
A. Ponthieux ◽  
A. Génin

Currently, ozonation installations in French drinking water treatment plants are operated in order to ensure an ozone residual of 0.4 mg/L at the outlet of the contactor with a contact time of 4 minutes which guarantee, with regards to the USEPA tables, a 4 log virus inactivation. Veolia Water has launched a thorough study concerning hydraulics in ozonation contactors which goals are (1) to reach the disinfection level desired through a better supervision of operating conditions, (2) to guarantee good hydraulic performances to reduce ozone production and ozonation-by products (bromates). The validation of these objectives is related to a relevant control of every ozonation tank with a Ct criteria considering from now their geometry, which condition their hydraulic efficiency. In comparison with CSTR method, the Ct10 method has been judged as the most relevant. Veolia is working with such a tank control, which definitely requires the determination of its hydraulic efficiency. Considering that numerical modelling of the ozonation contactors will be very long and expensive, the project team is working on the determination of an analytical model expression for hydraulic efficiency. The objective is to create an innovative tool which enables plant operators themselves to easily determine the hydraulic efficiency of inter or post ozonation tank.

2019 ◽  
Vol 3 (2) ◽  
pp. 44-57
Author(s):  
Esra Giresunlu ◽  
Arife Özüdoğru ◽  
Fulya Yaycılı ◽  
Hilal Uflaz ◽  
Cenk GÜMÜŞKAYA ◽  
...  

2012 ◽  
Vol 48 (1-3) ◽  
pp. 221-231 ◽  
Author(s):  
Qiang Zhang ◽  
Yan Liu ◽  
Yuanyuan Wei ◽  
Zhexue Quan ◽  
Yun Zhang ◽  
...  

2013 ◽  
Vol 777 ◽  
pp. 337-340
Author(s):  
Qiang Zhang ◽  
Bin Liu

The variation of disinfection by-products (DBPs) at several stages of drinking water treatment plants was investigated in two drinking water plants. The results clearly indicate that the low molecular weight total organic carbon (TOC) which has been identified as primary precursor for chlorinated DBPs was difficult to remove by coagulation. Plant A which used conventional coagulation/sedimentation could not decrease the species of trihalomethanes (THMs) and haloacetic acids (HAAs) formation potential. Biological activated carbon (BAC) was applied in Plant B which removed the maximum amount of TOC, while more kinds of microbial products were produced in BAC unit which could be the potential precursors of DBPs. Therefore, the species of DBPs formation potential still increased in the treatment processes of Plant B. Because different components of organic precursors produced different DBPs species, the processes of Plant B could decrease TOC efficiently but the species of THMs and HAAs formation potential.


2019 ◽  
Vol 149 ◽  
pp. 104008 ◽  
Author(s):  
Dávid Stefán ◽  
Norbert Erdélyi ◽  
Bálint Izsák ◽  
Gyula Záray ◽  
Márta Vargha

Author(s):  
H. Ates ◽  
M. E. Argun ◽  
N. Kurt

Abstract In this study, the fate of naphthalene was investigated with a supercritical water oxidation process (SCWO). Also, the effectiveness of different operating conditions including pressure, temperature, residence time and oxidant dose on the formation of by-products were determined. The experimental sets were determined by the experimental design program and the effect of the selected variables on the removal of the naphthalene was associated statistically. According to obtained results, naphthalene by SCWO process was mineralized up to 98.5%. Removal efficiencies in sub- and supercritical conditions were determined as between 94 and 100%. Derivatives of aldehyde, propanoic acid, benzene acetic acid and benzofuran were detected as by-products at many experimental conditions and also, some intermediates with a molecular weight higher than naphthalene were determined.


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