Method for continuous purification of rubber vulcanization accelerator m by applying solvent
A vulcanization accelerator and rubber purification technology, which is applied in the field of purification of rubber vulcanization accelerator 2-mercaptobenzothiazole (accelerator M or MBT), can solve the problems of not reducing M loss, accelerator M loss, etc. Reach the effect of reducing energy consumption, reducing the total amount, and reducing the amount of distillation
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Embodiment 1
[0028] Take 800L of the last batch of toluene washing liquid from the washing liquid collection tank and put it into the extraction kettle, take 700kg of the accelerator M crude product into the extraction kettle, filter after stirring for 1h, and the filtered filtrate enters the toluene mother liquor tank, and the filtrate is first cooled to 20- Stand at 25°C to precipitate the dissolved accelerator M, and then recover the accelerator M by filtration. The toluene filtrate is distilled to obtain fresh recovered toluene, which is used for washing the next batch of accelerator M, and for the crude M filter cake. The fresh toluene recovered from the previous batch is washed, and the temperature of the washed toluene washing liquid is controlled at 20-30°C. The filtrate enters the washing liquid collection tank and is used for the purification and removal of impurities of the next batch of accelerator M crude product. The final filter cake was directly dried to obtain 605.5 kg of a...
Embodiment 2
[0030] Take 2500L of the last batch of toluene washing liquid from the washing liquid collection tank and put it into the extraction kettle, take 700kg of accelerator M crude product into the extraction kettle, filter after stirring for 3h, and enter the toluene mother liquor tank after filtering, and the filtrate is first cooled to 10- Accelerator M is recovered by crystallization at 15°C, and the remaining filtrate is distilled to obtain freshly recovered toluene, which is used for washing of the next batch of accelerator M. The crude product filter cake of M is washed with fresh toluene recovered from the previous batch. The temperature of the final toluene washing liquid is controlled at 10-15 °C, and the filtrate enters the washing liquid collection tank for the purification and removal of impurities in the next batch of accelerator M crude product. The washed filter cake is directly dried to obtain the pure accelerator M product. 607.6kg, the purity of accelerator M detec...
Embodiment 3
[0032] Take 3300L of the last batch of toluene washing liquid from the washing liquid collection tank and put it into the extraction kettle, take 700kg of accelerator M crude product into the extraction kettle, filter after stirring for 6h, and enter the toluene mother liquor tank after filtering, and the filtrate is first cooled to 0- Accelerator M was recovered by crystallization at 5°C, and the remaining filtrate was distilled to obtain fresh recovered toluene, which was used for washing the next batch of accelerator M. The filter cake was washed with fresh toluene recovered from the previous batch, and the washed toluene The temperature of the toluene washing liquid is controlled at 0-5°C, and the filtrate enters the washing liquid collection tank for the purification and removal of impurities of the next batch of accelerator M crude product. The washed filter cake is directly dried to obtain 612.5 kg of pure accelerator M. The purity of accelerator M detected by HPLC was 9...
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