Process for continuously preparing methyl silicone resin
A technology for the preparation of methyl silicone resin, which is applied in the field of continuous preparation of methyl silicone resin, and can solve the problems of hazards, large investment in equipment, and low production efficiency.
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Embodiment 1
[0033] A continuous preparation process of methyl silicone resin, carried out as follows:
[0034] Feed according to the following raw material ratio:
[0035] Methyltrichlorosilane: 100kg / h; Dimethyldichlorosilane: 22kg / h; Xylene: 260kg / h.
[0036] Washing dilute acid water: 400kg / h; ethanol: 20kg / h.
[0037] a. Hydrolysis
[0038] Methyltrichlorosilane, dimethyldichlorosilane, and xylene are mixed at a ratio of 5:1:13, and after being initially mixed in a static mixer 11, they enter the tubular hydrolysis reactor 12, where they are washed with dilute acid water and ethanol at a ratio of 20: The ratio of 1 enters the tubular hydrolysis reactor 12, and the washing dilute acid water is dilute hydrochloric acid with a mass concentration of 0.8% (the washing water after the first-level washing in the washing process of the previous kettle material can also be used). The hydrolysis temperature of the material is controlled at 15°C in the hydrolysis system. After the feeding is ...
Embodiment 2
[0052] A continuous preparation process of methyl silicone resin, carried out as follows:
[0053] Feed according to the following raw material ratio:
[0054] Methyltrichlorosilane: 90kg / h; Dimethyldichlorosilane: 32kg / h; Xylene: 250kg / h.
[0055] Washing dilute acid water: 400kg / h; ethanol: 10kg / h.
[0056] a. Hydrolysis
[0057] Methyltrichlorosilane, dimethyldichlorosilane, and xylene are mixed at a ratio of 3:1:8, initially mixed in a static mixer 11, and then entered into a tubular hydrolysis reactor 12, and washed with dilute acid water and ethanol at a ratio of 40: The ratio of 1 enters the tubular hydrolysis reactor 12, and the dilute acid water for washing is dilute hydrochloric acid with a mass concentration of 0.9% (the washing water after the first-level washing in the washing process of the material in the previous kettle can also be used). The hydrolysis temperature of the material is controlled at 20°C in the hydrolysis system. After the feeding is completed...
Embodiment 3
[0071] A continuous preparation process of methyl silicone resin, carried out as follows:
[0072] Feed according to the following raw material ratio:
[0073] Methyltrichlorosilane: 85kg / h; Dimethyldichlorosilane: 35kg / h; Xylene: 240kg / h.
[0074] Washing dilute acid water: 400kg / h; ethanol: 8kg / h.
[0075] a. Hydrolysis
[0076] Methyltrichlorosilane, dimethyldichlorosilane, and xylene are mixed in a ratio of 2.5:1:7, and then enter the tubular hydrolysis reactor 12 after being initially mixed in a static mixer 11, and washed with dilute acid water and ethanol at a ratio of 50: The ratio of 1 enters the tubular hydrolysis reactor 12, and the dilute acid water for washing is dilute hydrochloric acid with a mass concentration of 0.9% (the washing water after the first-level washing in the washing process of the material in the previous kettle can also be used). The hydrolysis temperature of the material is controlled at 25°C in the hydrolysis system. After the feeding is co...
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