A device for continuous production of rubber vulcanization accelerator diphenylguanidine and production method thereof
A technology of rubber vulcanization and accelerators, which is applied in chemical instruments and methods, preparation of organic compounds, organic chemistry, etc. It can solve problems such as inaccurate control of reaction temperature, uneven stirring of reaction solution, yellowish and darker appearance of products, etc. Achieve the effects of improving equipment utilization efficiency, avoiding quality fluctuations, and reducing equipment investment
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Embodiment 1
[0033] Accompanying drawing is a kind of specific embodiment of the present invention. This embodiment comprises diphenylthiourea, ammonia-water mixed liquid metering pump 1, catalyst peristaltic metering pump 2, pipeline reactor 4, preheater 5, oxygen compressor 3, gas-liquid separator 6, gas-liquid washing tower 7, Continuous filtering device 8, ammonia water receiver 9. Diphenylthiourea, ammonia-water mixed solution metering pump 1 is connected to the bottom of pipeline reactor 4 through mixed solution pipeline 10, and mixed solution pipeline 10 is provided with diphenylthiourea, ammonia-water mixed solution flow regulating valve group 11; Catalyst peristaltic metering pump 2 is connected to the bottom of the pipeline reactor 4 through the catalyst pipeline 12, and the catalyst flow regulating valve group 13 is provided on the catalyst pipeline 12; the oxygen compressor 3 is connected to the bottom of the pipeline reactor 4 through the oxygen pipeline 14, and the oxygen pip...
Embodiment 2
[0039] Adopt the equipment shown in embodiment, the production method of continuous production rubber vulcanization accelerator diphenyl guanidine comprises:
[0040] Make diphenylthiourea and ammonia water at a molar ratio of 1:8, and the concentration of ammonia water at 20% to make a slurry, and use a metering pump at a rate of 1m per hour. 3 The amount of feed is pumped into the pipeline reactor, the catalyst is made into a 30% aqueous solution, and the peristaltic metering of 0.34L per hour is pumped into the pipeline reactor, and the new oxygen pressure is adjusted to 0.45Mpa, and the reactor is slowly boosted, and the pipeline reaction is opened at the same time When the steam in the jacket of the device is heated up to 50°C, the pressure of the belt system begins to drop. When the temperature starts to rise, change the heating steam to circulating water in time, and continue to pass oxygen. When the liquid level appears in the belt gas-liquid separator, when the pressur...
Embodiment 3
[0042] Adopt the equipment shown in embodiment, the production method of continuous production rubber vulcanization accelerator diphenyl guanidine comprises:
[0043] Make a slurry of diphenylthiourea and ammonia water at a molar ratio of 1:5 and a concentration of ammonia water of 30%, and use a metering pump at a rate of 1m per hour. 3The amount of feed is pumped into the pipeline reactor, the catalyst is made into a 30% aqueous solution, and the peristaltic metering of 0.34L per hour is pumped into the pipeline reactor, and the new oxygen pressure is adjusted to 0.45Mpa, and the reactor is slowly boosted, and the pipeline reaction is opened at the same time The steam in the jacket jacket is heated to 55°C, and the system pressure begins to drop. When the temperature starts to rise, change the heating steam to circulating water in time, and continue to pass oxygen. When the liquid level appears in the belt gas-liquid separator, when the pressure rises to 0.4Mpa, Turn on the ...
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