Vulcanizing accelerator MBT and preparation method thereof
A vulcanization accelerator and catalyst technology, applied in the field of rubber additives, can solve problems such as high safety risk, high equipment investment, and product quality impact, and achieve the effects of stable process parameters, improved purification effect, and reduced process risk
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Embodiment 1
[0022] A new synthetic method of sulfur accelerator MBT. The method includes using aniline, carbon disulfide and sulfur as raw materials, using DNW type temperature-resistant strong acid cation exchange resin as a catalyst, and catalyzing the synthesis of the promoter MBT.
[0023] First, mix the raw material sulfur and carbon disulfide, stir and prepare the sulfur carbon disulfide solution, and control the mass ratio of sulfur and carbon disulfide to 1:2.6;
[0024] Secondly, the carbon disulfide solution of aniline and prepared sulfur is pumped into the fixed bed reactor at a mass ratio of 1:1.7, and the feed mass space velocity is controlled to 0.4h -1 , Carry out continuous feeding; control the temperature during the reaction to be 190-200°C, and the reaction pressure to be 7.5-8.0Mpa.
[0025] The product flowing out of the reactor enters the toluene solution for extraction, the crude MBT obtained by suction filtration is washed twice with toluene, and the finished product MBT i...
Embodiment 2
[0028] A new synthetic method of sulfur accelerator MBT. The method includes using aniline, carbon disulfide and sulfur as raw materials, using DNW type temperature-resistant strong acid cation exchange resin as a catalyst, and catalyzing the synthesis of the promoter MBT.
[0029] First, mix the raw material sulfur and carbon disulfide, stir and prepare the sulfur carbon disulfide solution, and control the mass ratio of sulfur and carbon disulfide to 1:2;
[0030] Secondly, the carbon disulfide solution of aniline and the configured sulfur is pumped into the fixed bed reactor according to the mass ratio of 1:2, and the feed mass space velocity is controlled to 1h -1 , Carry out continuous feeding; control the temperature during the reaction to be 190-200°C, and the reaction pressure to be 8.0-8.5Mpa.
[0031] The product flowing out of the reactor enters the toluene solution for extraction, the crude MBT obtained by suction filtration is washed twice with toluene, and the finished p...
Embodiment 3
[0034] A new synthetic method of sulfur accelerator MBT. The method includes using aniline, carbon disulfide and sulfur as raw materials, using DNW type temperature-resistant strong acid cation exchange resin as a catalyst, and catalyzing the synthesis of the promoter MBT.
[0035] First, mix the raw material sulfur and carbon disulfide, stir and prepare the sulfur carbon disulfide solution, and control the mass ratio of sulfur and carbon disulfide to 1:2.6;
[0036] Secondly, the carbon disulfide solution of aniline and prepared sulfur is pumped into the fixed bed reactor at a mass ratio of 1:1.2, and the feed mass space velocity is controlled to 0.11h -1 , Carry out continuous feeding; control the temperature during the reaction to be 190-200°C, and the reaction pressure to be 8.0-8.5Mpa.
[0037] The product flowing out of the reactor enters the toluene solution for extraction, the crude MBT obtained by suction filtration is washed twice with toluene, and the finished product MBT ...
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