Water purification of aqueous nickel sulfate solutions by air cooled natural freezing

2016 ◽  
Vol 294 ◽  
pp. 176-184 ◽  
Author(s):  
M. Hasan ◽  
M. Louhi-Kultanen
1942 ◽  
Vol 64 (10) ◽  
pp. 2379-2379
Author(s):  
R. W. Gelbach ◽  
H. M. Louderback

AIChE Journal ◽  
2017 ◽  
Vol 64 (1) ◽  
pp. 200-208 ◽  
Author(s):  
Mehdi Hasan ◽  
Roman Filimonov ◽  
Miia John ◽  
Joonas Sorvari ◽  
Marjatta Louhi-Kultanen

2008 ◽  
Vol 53 (1) ◽  
pp. 11-21 ◽  
Author(s):  
V. N. Makarov ◽  
I. P. Kremenetskaya ◽  
D. V. Makarov ◽  
O. P. Korytnaya ◽  
T. N. Vasil’eva

Author(s):  
Mykola Gomelya ◽  
Yana Kryzhanovska ◽  
Tetiana Shabliy

In this work the reagent purification of aqueous solutions from sulfates with the use of red sludge of the Nikolaev alumina plant processes were investigated. This sludge, according to chemical analysis, contains a sufficiently large amount of alumina (up to 18 %) and calcium oxide (up to 10 %) and along with calcium silicate and iron oxides contains sodium and calcium aluminates. The ability of sodium aluminate to be deposited from a solution of sulfates in the form of calcium sulfoaluminates was used in the work to purify water from sulfate anions. The process takes place when treating the solution with sludge and lime suspension. It is shown that when red sludge is applied in the amount of 1–50 g/dm3 during magnesium sulfate solutions liming, water is purified from sulfate anions. The degree of water purification reaches 50–70 %. It was found that the efficiency of sulfate extraction is significantly dependent on the consumption of lime and increases slightly with increasing sludge consumption over 1 g/dm3. The dependence of the efficiency of sulfate extraction from water on their initial concentration is determined. It was found that at the initial concentration of sulfates up to 1000 mg/dm3 at the expense of lime 3–12 mg-eq/dm3 the residual concentration of sulfates decreases to 236–460 mg/dm3, and at the concentration of sulfate anions about 2000 mg/dm3 their concentration decreases to 550–830 mg/dm3 at a lime consumption of 30 mg-eq/dm3 regardless of the sludge consumption. The degree of extraction of sulfates from solutions reaches 40–73 %.


2012 ◽  
Vol 51 (1-3) ◽  
pp. 597-605 ◽  
Author(s):  
M.C. Martí-Calatayud ◽  
M. García-Gabaldón ◽  
V. Pérez-Herranz ◽  
S. Sales ◽  
S. Mestre

2010 ◽  
Vol 86 (1) ◽  
pp. 75-81 ◽  
Author(s):  
Zhaowu Zhu ◽  
Yoko Pranolo ◽  
Wensheng Zhang ◽  
Chu Yong Cheng

2018 ◽  
Vol 180 ◽  
pp. 246-253 ◽  
Author(s):  
Yongfa Song ◽  
Guangxin Wang ◽  
Bin Yang ◽  
Yaming Wang

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