Process and equipment for continuous production of diphenylguanidine
A biphenylguanidine and process technology, applied in the field of continuous production of diphenylguanidine production technology and equipment, can solve the problems that the operating conditions of each kettle cannot be completely unified, the quality of finished products is unstable, and increase equipment, etc., so as to improve the utilization rate of equipment and production efficiency, product quality improvement and stability, and the effect of reducing operators
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Embodiment 1
[0039] Embodiment 1. This embodiment provides equipment for continuous production of diphenylguanidine, including oxygen buffer tank 7, oxygen pipeline, diphenyl thiourea slurry metering pump 1, diphenyl thiourea slurry pipeline, catalyst feeding device 9, oxidation Heater 4, oxidation circulation pump 2, primary oxidation reactor 5, secondary oxidation reactor 6, water washing tank 8, discharge pump 3; the primary oxidation reactor 5 is provided with a Venturi mixer 14, so The upper part of the first-stage oxidation reactor 5 communicates with the upper part of the second-stage oxidation reactor 6 through an oxygen pipeline, communicates with the diphenylthiourea slurry metering pump 1 through a diphenylthiourea slurry pipeline, and communicates with a catalyst feeding device 9 through a catalyst feeding pipeline. Connected; the inlet end of the oxidation circulation pump 2 is connected to the bottom of the primary oxidation reactor 5 through a pipeline, the outlet end is conne...
Embodiment 2
[0040] Embodiment 2. This embodiment provides a process for the continuous production of diphenylguanidine, including the following steps: (1) Pump 3000L of 25% (W / W) ammonia water into the first-stage oxidation reactor through a metering pump, and stop the pump. Turn on the oxidation circulation pump;
[0041] (2) Add 0.5 kg of copper acetate from the catalyst feeding device;
[0042] (3) Adjust the valve group from the oxygen buffer tank to the secondary oxidation reactor to increase the pressure of the system to 0.45-0.5Mpa;
[0043] (4) Turn on the heater steam and heat up the ammonia to 60°C;
[0044] (5) The 50000L diphenylthiourea slurry prepared in advance is added to the first-stage oxidation reactor at 5000L / h through a metering pump, and the first-stage oxidation reactor is used to control the level of the first-stage oxidation reactor. At 2 meters, when the liquid level of the secondary oxidation reactor reaches 0.5 meters, start the stirring of the secondary oxidation re...
Embodiment 3
[0049] Embodiment 3, this embodiment provides a process for the continuous production of diphenylguanidine, including the following steps: (1) 3000L of 25% (W / W) ammonia water is pumped into the primary oxidation reactor through a metering pump, and the pump is stopped. Turn on the oxidation circulation pump;
[0050] (2) Add 2 kg of copper acetate from the catalyst feeding device;
[0051] (3) Adjust the valve group from the oxygen buffer tank to the secondary oxidation reactor to increase the pressure of the system to 0.45Mpa;
[0052] (4) Turn on the heater steam and heat up the ammonia to 65°C;
[0053] (5) The 50000L diphenylthiourea slurry prepared in advance is added to the first-stage oxidation reactor at 5000L / h through a metering pump, and the first-stage oxidation reactor is used to control the level of the first-stage oxidation reactor. At 2 meters, when the liquid level of the secondary oxidation reactor reaches 0.5 meters, start the stirring of the secondary oxidation r...
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