Method for eliminating phenomena that organic silicon crude monomer hydrolysate is not layered and adhered to equipment
A technology of organosilicon and hydrolyzate, applied in recycling technology, plastic recycling, etc., can solve the problem of non-stratification of organosilicon crude monomer hydrolyzate, and achieve the effects of reducing production costs, high safety factor, and low reaction temperature
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Embodiment 1-9
[0031] Add a certain amount of potassium hydroxide to the crude monomer hydrolyzate of dimethyldichlorosilane (adhesive state where water and oil are not layered), stir for 30 minutes, then add 90wt% toluene, heat up, and reflux at 130°C Take water for 2 hours, remove part of the water, and then let it stand to observe the stratification of the hydrolyzate and the adhesion of the equipment.
[0032] The potassium hydroxide consumption of embodiment 1-9, hydrolyzate delamination situation and adhesion equipment situation are as shown in table 1:
[0033] The potassium hydroxide consumption of table 1 embodiment 1-9, hydrolyzate delamination situation and adhesion equipment situation
[0034]
[0035] Under the same reflux time, such as 2h, the amount of alkali has an important influence on the non-stratification of water and oil. It can be seen from Table 1 that when the amount of potassium hydroxide is less than 5%, the breakage of the silicon-oxygen-silicon bond cannot be...
Embodiment 10-18
[0037] Add 15wt% potassium hydroxide to the crude monomer hydrolyzate of methylethyldichlorosilane (adhesive state in which water and oil do not delaminate), stir for 30 minutes, then add a certain amount of toluene, heat up, at 130°C Reflux with water for 2 hours, remove part of the water, and then let it stand to observe the stratification of the hydrolyzate and the adhesion of the equipment.
[0038] The toluene consumption of embodiment 10-18, hydrolyzate delamination situation and adhesion equipment situation are as shown in table 2:
[0039] The toluene consumption of table 2 embodiment 10-18, hydrolyzate delamination situation and adhesion equipment situation
[0040]
[0041] Under the same reflux time condition, such as 2h, when the amount of toluene is not the same, there is a significant difference in the layering speed. As can be seen from Table 2, when the amount of toluene is lower than 40%, the phenomenon of non-stratification of water and oil still exists o...
Embodiment 19
[0043] Add 10wt% sodium hydroxide to the crude monomer hydrolyzate of methylpropyldichlorosilane (a liquid state in which water and oil are not separated), stir for 20 minutes, then add 70wt% toluene, heat up, and reflux at 135°C Carry water, remove part of the water, and after standing still, the water and oil two-phase layer will separate; take the oil layer and carry out vacuum distillation under the conditions of 70 ° C and -0.098 MPa to remove toluene to obtain transparent silicone oil, which can be reused after recovery of toluene.
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