Production process of pyrolysis cyanuric acid
A production process, cyanuric acid technology, applied in the direction of organic chemistry, etc., can solve the problems of large power consumption, gas leakage, large power consumption, etc., and achieve the effects of improving heat energy utilization, saving land occupation, and reducing heat loss
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Embodiment 1
[0032] Embodiment 1: the temperature is 135 ℃ of liquid urea with 5~6m / s flow velocity, 8m 3 / h flow rate is pumped into the continuous channel with a pressure of 3.5Mpa, a temperature of 460°C and a flow rate of 700m 3 The drum kiln with superheated steam per hour produces crude cyanuric acid after the polymerization reaction of urea at 265°C. The crude cyanuric acid leaving the drum kiln is mixed with water to make a slurry with a water content of 65%, and then concentrated sulfuric acid is added to control the sulfuric acid. The mass concentration is 28-30%, and the reaction temperature is 110-120°C. After 8-12 hours of reaction, the temperature is lowered, centrifuged, washed, and dried to obtain cyanuric acid with a purity of 98.5-99%. The superheated steam adopts Superheated steam produced by-product in sulfuric acid production.
Embodiment 2
[0033] Embodiment 2: the temperature is 132 ℃ liquid urea with 5~6m / s flow velocity, 5m 3 / h flow pumped into the continuous channel with 3Mpa, 450°C, flow rate of 500m 3 / h superheated steam drum kiln, urea polymerizes at 250°C to produce crude cyanuric acid, the crude cyanuric acid out of the drum kiln is mixed with water to make a slurry with a moisture content of 65%, and then concentrated sulfuric acid is added to control the sulfuric acid The mass concentration is 28-30%, and the reaction temperature is 110-120°C. After 8-12 hours of reaction, the temperature is lowered, centrifuged, washed, and dried to obtain cyanuric acid with a purity of 98.5-99%. The superheated steam adopts Superheated steam produced by-product in sulfuric acid production.
Embodiment 3
[0034] Embodiment 3: the temperature is 138 ℃ of liquid urea with 5~6m / s flow velocity, 8m 3 / h flow pumped into the continuous channel with 4Mpa, 500°C, flow rate of 800m 3 / h of superheated steam drum kiln, urea polymerizes at 280°C to produce crude cyanuric acid, which is continuously transported to the crude product storage tank by a screw conveyor, and the crude product cyanuric acid that exits the drum kiln is prepared by adding water Add concentrated sulfuric acid after forming a slurry with a water content of 65%, control the mass concentration of sulfuric acid at 28-30%, and react at a reaction temperature of 110-120°C. After reacting for 8-12 hours, cool down, centrifuge, wash, and dry to obtain The cyanuric acid has a purity of 98.5-99%. The superheated steam is the by-product superheated steam in the production of sulfuric acid.
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