Process for producing naturally purified salt products
A salt product, a natural technology, applied in the direction of alkali metal halide purification, magnesium halide, magnesium chloride, etc., to achieve the effect of small material loss
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Embodiment 1
[0093] In a first example, 163 gallons of a 24% by weight magnesium chloride solution were pumped into a 300 gallon jacketed mixing kettle. The solution was mixed using an axial impeller at a rate of 2500 gallons per minute (gpm) and heated to 135°F (57°C) with low pressure steam through the kettle jacket. Then 765 pounds (Lbs) of salt mixture were added to the mixing tank to produce a first slurry. The kettle was mixed for 18 minutes while maintaining a temperature of 122°F (50°C). At the completion of the residence time, the slurry was pumped to a Baker Perkins Model S-8 horizontal piston pusher centrifuge. This centrifuge basket has a 13 / 10 inch screen opening and runs at 1800 revolutions per minute (RPM). The first slurry contained 39% by weight suspended solids. The first solid comprising sodium chloride is separated from the first slurry to produce a second slurry. The second slurry continued into a second jacketed mixing tank (surge tank) of the same design as the m...
Embodiment 2
[0102] In a second example, 173 gallons of a 26% by weight magnesium chloride solution were pumped into a 300 gallon jacketed mixing kettle. The solution was mixed using an axial impeller at a rate of 2500 gallons per minute (gpm) and heated to 135°F (57°C) with low pressure steam through the kettle jacket. 739 pounds (Lbs) of salt mixture were then added to the mixing tank to produce a first slurry. The kettle was mixed for 22 minutes while maintaining a temperature of 123°F (51°C). At the completion of the residence time, the slurry was pumped to a Baker Perkins Model S-8 horizontal piston pusher centrifuge. This centrifuge basket has a 13 / 10 inch screen opening and runs at 1800 revolutions per minute (RPM). The first slurry contained 35% by weight suspended solids. The first solid comprising sodium chloride is separated from the first slurry to produce a second slurry. The second slurry continued into a second jacketed mixing tank (surge tank) of the same design as the ...
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