A method for reducing dicyandiamide content in 30% cyanamide solution
A technology of cyanamide and dicyandiamide, which is applied in the field of reducing the content of dicyandiamide in 30% cyanamide solution, can solve problems such as technical impossibility, affecting product quality, and undisclosed necessary technical features, so as to inhibit polymerization Effect
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Embodiment 1
[0029] A method for reducing the content of dicyandiamide in 30.0% cyanamide solution, the synthetic production steps are:
[0030] (1) Transfer mother liquor: add 4.0m 3 Mother liquor, accounting for 66.7% of the volume of the synthesis kettle, is fed with carbon dioxide, and the flow rate of carbon dioxide is controlled at 50.0m 3 / h, mother liquor pH=6.5, carbon dioxide continues to feed;
[0031] (2) Feeding: Open the synthesis kettle and stir, calcium cyanamide enters the synthesis kettle through the powder conveying system, the conveyor speed is 500 rpm, and the total amount of feeding is 1.0 tons, accounting for 16.7% of the synthesis kettle volume;
[0032] (3) Hydrolysis reaction: the flow rate of carbon dioxide fed to the synthesis kettle is adjusted to 150m 3 / h, the reaction temperature is controlled at 25.0°C by the cold water cooling system, the reaction time is 5.0 hours, pH=6.5;
[0033] (4) Heat preservation: The heat preservation time is 1.0 hours, and the...
Embodiment 2
[0039] A method for reducing the content of dicyandiamide in 30.0% cyanamide solution, the synthetic production steps are:
[0040] (1) Transfer mother liquor: add 4.0m 3 Mother liquor, accounting for 66.7% of the volume of the synthesis kettle, is fed with carbon dioxide, and the flow rate of carbon dioxide is controlled at 70.0m 3 / h, pH of the mother liquor=7.0, continuous feeding of carbon dioxide;
[0041] (2) Feeding: Open the synthesis kettle and stir, calcium cyanamide enters the synthesis kettle through the powder conveying system, the conveyor speed is 700 rpm, and the total amount of feeding is 1.0 tons, accounting for 16.7% of the synthesis kettle volume;
[0042] (3) Hydrolysis reaction: the flow of carbon dioxide fed to the synthesis kettle is adjusted to 100m 3 / h, the reaction temperature is controlled at 27.0°C by the cold water cooling system, the reaction time is 6.0 hours, pH=7;
[0043] (4) Heat preservation: The heat preservation time is 1.5 hours, and...
Embodiment 3
[0049] A method for reducing the content of dicyandiamide in 30.0% cyanamide solution, the synthetic production steps are:
[0050] (1) Transfer mother liquor: add 4.0m 3 Mother liquor, accounting for 66.7% of the volume of the synthesis kettle, is fed with carbon dioxide, and the flow rate of carbon dioxide is controlled at 60.0m 3 / h, mother liquor pH=6.5;
[0051] (2) Feeding: Open the synthesis kettle and stir, calcium cyanamide enters the synthesis kettle through the powder conveying system, the conveyor speed is 600 rpm, and the total amount of feeding is 1.0 tons, accounting for 16.7% of the synthesis kettle volume;
[0052] (3) Hydrolysis reaction: the flow rate of carbon dioxide fed to the synthesis kettle is adjusted to 130m 3 / h, the reaction temperature is controlled at 26.0°C by the cold water cooling system, the reaction time is 6.0 hours, pH=6.5;
[0053] (4) Heat preservation: The heat preservation time is 1.2 hours, and the carbon dioxide flow rate is contr...
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