Effects of dissolved oxygen on formation of corrosion products and concomitant oxygen and nitrate reduction in zero-valent iron systems with or without aqueous Fe2+

2005 ◽  
Vol 39 (9) ◽  
pp. 1751-1760 ◽  
Author(s):  
Yong H. Huang ◽  
Tian C. Zhang
2012 ◽  
Vol 133 (1) ◽  
pp. 205-211 ◽  
Author(s):  
H.B. Liu ◽  
T.H. Chen ◽  
D.Y. Chang ◽  
D. Chen ◽  
Y. Liu ◽  
...  

2015 ◽  
Vol 146 ◽  
pp. 227-234 ◽  
Author(s):  
Xuejun Guo ◽  
Zhe Yang ◽  
Hong Liu ◽  
Xiaofang Lv ◽  
Qiansi Tu ◽  
...  

2018 ◽  
Vol 4 (10) ◽  
pp. 1651-1661 ◽  
Author(s):  
Ghulam Hussain Qasim ◽  
Sangwook Lee ◽  
Giehyeon Lee ◽  
Woojin Lee ◽  
Yongseok Hong ◽  
...  

Absence of dissolved oxygen and presence of nitrate in groundwater increases Hg(0) during the Hg(ii) removal using pumice supported nZVI.


2018 ◽  
Vol 32 (3) ◽  
pp. 243-251 ◽  
Author(s):  
Youngpyoe Hong ◽  
Younggyo Seo ◽  
Hyowon Kim ◽  
Yuhoon Hwang

Author(s):  
Maria Villen-Guzman ◽  
Juan Manuel Paz-Garcia ◽  
Brahim Arhoun ◽  
Maria del Mar Cerrillo-Gonzalez ◽  
Jose Miguel Rodriguez-Maroto ◽  
...  

Zero valent iron (ZVI) is being used in permeable reactive barriers (PRB) for the removal of oxidant contaminants, from nitrate to chlorinated organics. A sound design of these barriers requires a good understanding of kinetics. Here we present a study of the kinetics of nitrate reduction under relatively low values of pH, from 2 to 4.5. We use a particle size of 0.42 mm, which is within the recommended size for PRBs (0.2 mm to 2.0 mm). In order to avoid possible mass-transfer limitations, a well-stirred reactor coupled with a fluidized bed reactor was used. The experiments were performed at constant pH values using a pH controller that allows to accurately track the amount of acid added. Since the reduction of H + to H 2 by the oxidation of ZVI will always be present for these pH values, blank experiments (without nitrate) were performed and the rate of this H + reduction obtained. This rate of reduction was studied using three kinetic models: a regular empirical one, the Shrinking-Core Model (SCM), and the Surface Kinetics Model (SKM). The best performance was obtained from the SKM model. Therefore, this model was also used to study the results for the nitrate reduction, also with satisfactory results. In both cases, some assumptions are introduced to maintain a moderate number of fitting parameters.


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