Method for reducing metal ion concentration in brain solution
A brine solution and brine technology, applied in the direction of separation methods, alkali metal compounds, alkali metal halides, etc., can solve problems such as reducing the concentration
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example 1
[0042] A saline solution derived from the polycarbonate manufacturing process and containing about 300 ppm sodium gluconate had the following polyvalent metal cation concentrations: about 3.1 ppm calcium, about 1.5 ppm magnesium and about 1.9 ppm iron. The pH of the brine solution was adjusted to above 10 with sodium hydroxide and exposed to about 10 g / l sodium carbonate. After filtering the precipitated solids, the recovered brine solution contained the following polyvalent metal cation concentrations: about 1.2 ppm calcium, about 0.03 ppm magnesium and about 0.6 ppm iron. Example 2
example 2
[0043] Take the Rohm and Haas Duolite C467 resin, made into a column with a chelating ion exchange resin with aminophosphonic acid functionalities. A brine containing approximately 250 ppm sodium gluconate and 10-13.2 ppm iron was passed through the column at a feed pH of 2.5 at a rate of 8 resin bed volumes per hour. The iron removal efficiency was at least 99.4% (10-13.2 ppm inlet; <0.06 ppm outlet) and the iron breakthrough point occurred at 120 hours when the outlet iron concentration exceeded about 0.06 ppm. Example 3
example 3
[0044] This example illustrates the effect of feed pH on iron removal efficiency. The procedure of Example 2 was repeated except that the brine solution contained about 0.29 ppm iron and 300 ppm sodium gluconate, the feed pH was 10-11, and a resin bed volume rate of 8 per hour was passed through the column. The iron removal efficiency is generally 41% (0.29ppm inlet; 0.17ppm outlet), and the iron breakthrough point (where no more iron is complexed by the resin) occurs at 32 hours. Example 4
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