The solubility curves of sulfates in the systems CuSO
4-NiSO
4-H
2O-C
2H
5OH and CuSO
4-CoSO
4-H
2O-C
2H
5OH at 298K were determined and the possibilities of industrial application of fractional crystallization method was discussed. The results are summarized as follows:
(1) The solubility curve for the system CuSO
4-NiSO
4-H
2O-C
2H
5OH can be devided into 2 portions which are characteristic to crystallization of CuSO
4.
5H
20 and NiSO
4.7H
20, respectively. Each crystalline phase contains only minute amount of other sulfate. The solubility of CuSO
4 at eutectic point decreases with increase in the concentration of ethanol from 0.78 to nearly zero, while that for NiSO
4 ranges from 2.18 to nearly zero.
(2) A similar solubility curve can be obtained for the solution system of CuSO
4-CoSO
4-H
2O-C
2H
5OH. However, the solid phase equilibrated with a saturated CoSO
4 solution was identified to be a mixed crystalline phase of (Co, Cu) SO
4.7H
20.
(3) The separation of CuSO
4 from the saturated CuSO
4 solutions containing NiSO
4 up to 1 mole is possible to produce almost pure crystals of chalcanthite with the yield ranging 70 to 98%. The required amount of ethanol for the crystallization of chalcanthite ranges from 0.23 to 0.43 kg per kg of water, leaving the resultant solution whose CuSO
4 concentrations are 0.35 to 0.01 moles per kg of water.
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