Arsenic Removal from Water Supplies in Northern Chile Using Ferric Chloride Coagulation

1999 ◽  
Vol 13 (3) ◽  
pp. 164-169 ◽  
Author(s):  
S. Karcher ◽  
L. Cáceres ◽  
M. Jekel ◽  
R. Contreras
2020 ◽  
Vol 725 ◽  
pp. 138351 ◽  
Author(s):  
Jie Ge ◽  
Biswarup Guha ◽  
Lee Lippincott ◽  
Stanley Cach ◽  
Jinshan Wei ◽  
...  

2008 ◽  
Vol 3 (3) ◽  
Author(s):  
D. Laky ◽  
B. László ◽  
I. Licskó

In laboratory experiments a traditional drinking water treatment method, coagulation/flocculation followed by solid/liquid phase separation has been applied in order to decrease arsenic concentration below 10 μg/L (which is the new Hungarian standard for arsenic). The goal of the research work was to examine the transition of the dissolved arsenic to solid form, to determine the factors which have significant effect on arsenic removal efficiency. The organic content of the water highly affected the arsenic removal process. The difference in the required coagulant dosage can be order of one magnitude depending on the organic content of the water. The phosphorous content also increases the required coagulant dose, since ferric phosphate precipitates are formed, decreasing the amount of coagulant available for arsenic removal. pH also proved to have significant influence when experiments were carried out at wide pH range. However, under more realistic conditions (pH is between 7.5 and 8), the effect of pH was not that significant. The inorganic carbon content at some extent favors the liquid/solid transition of arsenate, since it contributes to the buffering capacity of the water, therefore enhances the metal hydroxide formation process. However, the excess inorganic carbon has disadvantageous effect, since it competes with the arsenate ions for the free sites of metal hydroxides. Two oxidants (chlorine and potassium permanganate) and two coagulants (ferric chloride and aluminum sulfate) were studied in pilot scale experiments. The pilot plant was operated at Hajdúbagos, where the arsenic, iron and manganese concentration of the raw water is above the standard. In the experiments it was found the potassium permanganate + ferric chloride combination was the most efficient.


2018 ◽  
Vol 23 (6) ◽  
pp. 615-634 ◽  
Author(s):  
Eric C. Edwards ◽  
Oscar Cristi ◽  
Gonzalo Edwards ◽  
Gary D. Libecap

AbstractThis paper estimates the cost of a policy to restrict water trades to mining firms in northern Chile in order to protect riparian ecosystems and indigenous agriculture. In response to the policy, mining firms have developed high-cost desalination and pumping facilities to secure adequate water supplies. We develop a methodology and estimate the cost of market transactions that fail to occur due to the policy. Lost trade surplus is estimated at US$52 million per year. Without trade restrictions, around 86 per cent of the remaining agricultural water in the region would be transferred to mining.


Desalination ◽  
2009 ◽  
Vol 248 (1-3) ◽  
pp. 42-47 ◽  
Author(s):  
E. Awuah ◽  
R.T. Morris ◽  
P.A. Owusu ◽  
R. Sundell ◽  
J. Lindstrom

Author(s):  
Bijan Bina ◽  
Afshin Ebrahimi ◽  
Farid Hesami ◽  
MohammadMehdi Amin

2002 ◽  
Vol 2 (2) ◽  
pp. 281-288 ◽  
Author(s):  
M.M.T. Khan ◽  
K. Yamamoto ◽  
M.F. Ahmed

A variety of treatment processes have been used for arsenic removal from water. In a laboratory study using natural (tubewell) water, ferric chloride salt and alum were used, which are the most studied and widely used flocculents in water treatment due to their low price, comfortable availability and low risk usability. The solubility of arsenate(III) is much more than arsenite(V). Arsenate(III) was converted into arsenite(V) by proper oxidation using bleaching powder as an oxidizing agent before coagulation. The concentrations of ferric chloride salt and alum dose were varied from 10 mg/l to 200 mg/l, and pH was varied from 4 to 9. After intensive investigation, it was found that at pH 7 and for 100 mg/l to 125 mg/l dose of alum, the removal efficiency of arsenic and iron were around 82 to 86% and 92 to 95% respectively. Again, the optimum removal of arsenic and iron were around 90 to 93% and 97 to 100% respectively at pH 7 for 200 mg/l of ferric chloride salt. This research was carried out not only to observe the removal efficiency of arsenic, but also iron. Because most of the tubewells in Bangladesh, sometimes, contain higher amount of iron.


2009 ◽  
Vol 168 (1) ◽  
pp. 430-437 ◽  
Author(s):  
V. Fierro ◽  
G. Muñiz ◽  
G. Gonzalez-Sánchez ◽  
M.L. Ballinas ◽  
A. Celzard

1996 ◽  
Vol 88 (4) ◽  
pp. 155-167 ◽  
Author(s):  
Janet G. Hering ◽  
Pen-Yuan Chen ◽  
Jennifer A. Wilkie ◽  
Menachem Elimelech ◽  
Sun Liang

Sign in / Sign up

Export Citation Format

Share Document