Method for efficiently preparing monocyanamide solution
A cyanamide solution technology, which is applied in the field of preparation of cyanamide solution, can solve problems such as high carbon dioxide concentration requirements, incomplete filtration of cyanamide waste residue, and high calcium ion content, so as to shorten the production cycle, shorten the hydrolysis time, and reduce the The effect of calcium content
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Embodiment 1
[0029] (1) Hydrolysis and decalcification process: Start the vacuum pump, add 1230kg of water into the hydrolysis kettle, and open the kiln gas inlet valve of the hydrolysis kettle to observe the kiln gas bubbling. The mass content of carbon dioxide in the kiln gas is 31%. Put lime nitrogen into the silo through the bucket elevator; open the screw feeder to put 300kg of lime nitrogen (20.5% nitrogen) into the hydrolysis kettle in batches, the feeding temperature of lime nitrogen is 15°C, and the feeding speed is controlled at 8kg / min. The reaction temperature is 20°C, continue to pass the kiln gas until the pH value of the system is 7, the lime nitrogen feeding is completed, and the kiln gas is fed for another 10 minutes before stopping, and then the reaction solution is put into the suction filter tank for microporous filtration to obtain 692kg Cyanamide crude solution and black slag; filtered cyanamide aqueous solution enters the storage tank, and the black slag is washed wit...
Embodiment 2
[0033] (1) Hydrolysis and decalcification process: Start the vacuum pump, add 1800kg of water into the hydrolysis kettle, and open the kiln gas inlet valve of the hydrolysis kettle to observe the kiln gas bubbling. The mass content of carbon dioxide in the kiln gas is 30%. Put the lime nitrogen into the silo through the bucket elevator; open the screw feeder to put 300kg of lime nitrogen (21% nitrogen) into the hydrolysis kettle in batches, the feeding temperature of lime nitrogen is 20°C, and the feeding speed is controlled at 9kg / min. The reaction temperature is 30°C, continue to pass the kiln gas until the pH value of the system is 7, the lime nitrogen feeding is completed, and the kiln gas is passed in for another 10 minutes before stopping, and then the reaction solution is put into the suction filter tank for microporous filtration to obtain 845g Cyanamide crude solution and black slag; filtered cyanamide aqueous solution enters the storage tank, and the black slag is was...
Embodiment 3
[0037] (1) Hydrolysis decalcification process: Start the vacuum pump, add 1500kg of water into the hydrolysis kettle, and open the kiln gas inlet valve of the hydrolysis kettle to observe the kiln gas bubbling. The mass content of carbon dioxide in the kiln gas is 32%, and the lime nitrogen point bag is measured Finally, put lime nitrogen into the silo through the bucket elevator; open the screw feeder and put 300kg of lime nitrogen (21% nitrogen) into the hydrolysis kettle in batches, the feeding temperature of lime nitrogen is 10°C, and the feeding speed is controlled at 10kg / min , the reaction temperature is 40°C, continue to pass the kiln gas until the pH value of the system is 8 o'clock, the lime nitrogen feeding is completed, the kiln gas is passed in for another 10 minutes and then stopped, and then the reaction solution is put into the suction filter tank for microporous filtration to obtain 844kg cyanamide crude solution and black residue; the filtered cyanamide aqueou...
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