Method for continuously producing cyanamide
A technology for cyanamide and cyanamide material, applied in the field of continuous production of cyanamide, can solve the problems of cyanamide polymerization explosion, cyanamide loss and the like
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Embodiment 1
[0057] (1) Continuously inject mother liquor from the mother liquor tank to the synthesis kettle with a feed rate of 20t / h, and the liquid amount in the synthesis kettle is maintained at 4m 3 Afterwards stop injecting; Simultaneously, before mother liquor is transported into synthetic kettle, in mother liquor, inject ferric trichloride continuously, the consumption of described ferric chloride is 0.01% of mother liquor mass flow rate in mother liquor pipeline; Open stirring, control rotating speed is 150r / min, and carbon dioxide is introduced from the bottom of the synthesis kettle, and the amount of carbon dioxide introduced is controlled to be 100Nm 3 / h; start to add lime nitrogen, through the metering and feeding system, control the amount of lime nitrogen added to 220kg / h; during the synthesis process, control the temperature ≤ 30 ℃, control the pH ≤ 8.5.
[0058] (2) After feeding for 2 hours, turn on the material transfer pump and control the flow rate of the material ...
Embodiment 2
[0062] (1) Continuously inject mother liquor into the synthesis kettle with a feed rate of 20t / h from the mother liquor tank, and the liquid amount in the synthesis kettle is maintained at 3m 3 Stop injecting after; Simultaneously, before mother liquor is transported into synthetic kettle, in mother liquor, inject sodium sulfide continuously, the consumption of described sodium sulfide is 0.01% of mother liquor mass flow rate in mother liquor pipeline; Open stirring, control rotating speed is 150r / min, and Introduce carbon dioxide from the bottom of the synthesis kettle, and control the amount of carbon dioxide inflow to 120Nm 3 / h; start to add lime nitrogen, through the metering and feeding system, control the amount of lime nitrogen added to 220kg / h; during the synthesis process, control the temperature ≤ 30 ℃, control the pH ≤ 8.5.
[0063] (2) After feeding for 1 hour, turn on the material transfer pump and control the flow rate of the material transfer pump to 1m 3 / h, ...
Embodiment 3
[0067] (1) Continuously inject mother liquor into the synthesis kettle with a feed rate of 20t / h from the mother liquor tank, and the liquid amount in the synthesis kettle is maintained at 4m 3 Stop injecting after; Simultaneously, before mother liquor is conveyed into synthetic kettle, in mother liquor, inject ferric trichloride continuously, the consumption of described ferric chloride is 0.02% of mother liquor mass flow rate in the mother liquor pipeline; Open stirring, control rotating speed is 200r / min, and carbon dioxide is introduced from the bottom of the synthesis kettle, and the amount of carbon dioxide introduced is controlled at 120Nm 3 / h; start to add lime nitrogen, through the metering and feeding system, control the amount of lime nitrogen added to 220kg / h; during the synthesis process, control the temperature ≤ 30 ℃, control the pH ≤ 8.5.
[0068] (2) After feeding for 1 hour, turn on the material transfer pump and control the flow rate of the material transf...
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