Calcium-magnesium carbonate composite and method for the preparation thereof

A method for the preparation of a calcium-magnesium carbonate composite consisting of calcium carbonate and magnesium carbonate hydroxide which comprises the steps of:

• (a) preparing an aqueous slurry of calcium hydroxide, of which an aqueous suspension in a concentration of 400 q/liter has a viscosity of at least 1500 centipoise at 25.degree. C., and magnesium hydroxide in a weight proportion in the range from 95:5 to 50:50 by weight, the solid content of the aqueous slurry being in the range from 100 to 250 g/liter, calculated by taking the amount of the magnesium hydroxide to be equal to the equimolar amount of calcium hydroxide;
• (b) keeping the aqueous slurry at a temperature of 30.degree. C. or higher;
• (c) introducing carbon dioxide gas either as such or as diluted with a non-reactive gas into the aqueous slurry at a rate in the range from 1 to 3 liters (N.T.P.) per minute per kg of the calcium hydroxide in the aqueous slurry prepared in step (a) until the aqueous slurry has a value of pH not higher than 10;
• and
• (d) introducing carbon dioxide gas either as such or as diluted with a non-reactive gas into the aqueous slurry after step (c) at a rate of at least 5 liters (N.T.P.) per minute per kg of the magnesium hydroxide in the aqueous slurry prepared in step (a) until the aqueous slurry has a value of pH not higher than 8.

A method for the preparation of a calcium-magnesium carbonate composite consisting of calcium carbonate and magnesium carbonate hydroxide which comprises the steps of:

• (a1) preparing an aqueous slurry of calcium hydroxide, of which an aqueous suspension in a concentration of 400 g/liter has a viscosity of at least 1500 centipoise at 25.degree. C., and magnesium hydroxide in a weight proportion in the range from 95:5 to 50:50 by weight, the solid content of the aqueous slurry being in the range from 100 to 250 g/liter, calculated by taking the amount of the magnesium hydroxide to be equal to the equimolar amount of calcium hydroxide;
• (b1) keeping the aqueous slurry at a temperature in the range from 5.degree. to 30.degree. C.;
• (c1) introducing carbon dioxide gas either as such or as diluted with a non-reactive gas into the aqueous slurry at a rate in the range from 7 to 15 liters (N.T.P.) per minute per kg of the calcium hydroxide in the aqueous slurry prepared in step (a1) until conversion of the calcium hydroxide into calcium carbonate is in the range from 5 to 15%;
• (d1) introducing carbon dioxide gas either as such or as diluted with a non-reactive gas into the aqueous slurry after step (c1) at a rate in the range from 0.5 to 2 liters (N.T.P.) per minute per kg of the calcium hydroxide in the aqueous slurry prepared in step (a1) until conversion of the calcium hydroxide into calcium carbonate is in the range from 40 to 60%;
• (e1) introducing carbon dioxide gas either as such or as diluted with a non-reactive gas into the aqueous slurry after step (d1) at a rate exceeding 2.5 liters (N.T.P.) per minute per kg of the magnesium hydroxide in the aqueous slurry prepared in step (a1) until the aqueous slurry has a value of pH not higher than 10;
• and
• (f1) introducing carbon dioxide gas either as such or as diluted with a non-reactive gas into the aqueous slurry after step (e1) at a rate of at least 5 liters (N.T.P.) per minute per kg of the magnesium hydroxide in the aqueous slurry prepared in step (a1) until the aqueous slurry has a value of pH not higher than 8.

A method for the preparation of a calcium-magnesium carbonate composite consisting of calcium carbonate and magnesium carbonate hydroxide which comprises the steps of:

• (a2) dispersing a hydrate of calcined dolomite in water to give an aqueous slurry of calcium hydroxide and magnesium hydroxide, the solid content of the aqueous slurry being in the range from 100 to 250 g/liter calculated by taking the amount of the magnesium hydroxide to be equal to the equimolar amount of calcium hydroxide;
• (b2) keeping the aqueous slurry at a temperature of 30.degree. C. or higher;
• (c2) introducing carbon dioxide gas either as such or as diluted with a non-reactive gas into the aqueous slurry at a rate in the range from 1 to 3 liters (N.T.P.) per minute per kg of the calcium hydroxide in the aqueous slurry prepared in step (a2) until the aqueous slurry has a value of pH not higher than 10;
• and
• (d2) introducing carbon dioxide gas either as such or as diluted with a non reactive gas into the aqueous slurry after step (c2) at a rate of at least 5 liters (N.T.P.) per minute per kg of the magnesium hydroxide in the aqueous slurry prepared in step (a2) until the aqueous slurry has a value of pH not higher than 8.

A method for the preparation of a calcium-magnesium carbonate composite consisting of calcium carbonate and magnesium carbonate hydroxide which comprises the steps of:

• (a3) dispersing a hydrate of calcined dolomite in water to give an aqueous slurry of calcium hydroxide and magnesium hydroxide, the solid content of the aqueous slurry being in the range from 100 to 250 g/liter calculated by taking the amount of the magnesium hydroxide to be equal to the equimolar amount of calcium hydroxide;
• (b3) keeping the aqueous slurry at a temperature in the range from 5.degree. to 30.degree. C.;
• (c3) introducing carbon dioxide gas either as such or as diluted with a non reactive gas into the aqueous slurry at a rate in the range from 7 to 15 liters (N.T.P.) per minute per kg of the calcium hydroxide in the aqueous slurry prepared in step (a3) until conversion of the calcium hydroxide into calcium carbonate is in the range from 5 to 15%;
• (d3) introducing carbon dioxide gas either as such or as diluted with a non reactive gas into the aqueous slurry after step (c3) at a rate in the range from 0.5 to 2 liters (N.T.P.) per minute per kg of the calcium hydroxide in the aqueous slurry prepared in step (a3) until conversion of the calcium hydroxide into calcium carbonate is in the range from 40 to 60%;
• (e3) introducing carbon dioxide gas either as such or as diluted with a non-reactive gas into the aqueous slurry after step (d3) at a rate larger than 2.5 liters (N.T.P.) per minute per kg of the magnesium hydroxide in the aqueous slurry prepared in step (a3) until the aqueous slurry has a value of pH not higher than 10;
• and
• (f3) introducing carbon dioxide gas either as such or as diluted with a non-reactive gas into the aqueous slurry after step (e3) at a rate of at least 5 liters (N.T.P.) per minute per kg of the magnesium hydroxide in the aqueous slurry prepared in step (a3) until the aqueous slurry has a value of pH not higher than 8.