Silicone rubber polymerization by-product recovery treatment system and method
A technology for recycling and by-products, applied in the direction of silicon organic compounds, etc., can solve the problem of inability to effectively remove non-polymerized low-component odor substances and color-developing substances, and achieve fast evaporation, short residence time, and high heat transfer efficiency Effect
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Embodiment 1
[0026] like figure 1 As shown, the silicone rubber polymerization by-product recovery treatment system includes a defective DMC storage tank 1, a preheating delivery pump 2, a preheater 3, a thin film evaporator 4, a cooler 5, and a dry defective DMC storage tank connected in sequence. 6. Refining delivery pump 7, refining kettle 8, plate and frame filter press 9, and product storage tank 10.
Embodiment 2
[0028] A method for recovering and treating silicone rubber polymerization by-products, comprising the following steps:
[0029] (1) The defective DMC in the defective DMC storage tank is transported into the preheater through the preheating pump, and the defective DMC is heated to 65°C in the preheater, and then enters the film evaporation with a pressure of -50KPa In the thin-film evaporator, it is heated to 110°C, and continuous rapid vacuum distillation is performed to remove non-polymerizable low-components and trimethylamine; then, the temperature is lowered to below 60°C through a cooler and stored in dry defective product storage Standby in the tank; (defective DMC is called dry defective DMC after removing non-polymerizable low components and trimethylamine)
[0030] (2) Transport the dry defective product DMC to the refining kettle through the refining delivery pump, stop feeding when the raw material in the refining kettle reaches 80% of its volume, and add activate...
Embodiment 3
[0034] A method for recovering and treating silicone rubber polymerization by-products, comprising the following steps:
[0035] (1) The defective DMC in the defective DMC storage tank is transported into the preheater through the preheating pump, and the defective DMC is heated to 50°C in the preheater, and then enters the film evaporation with a pressure of -60KPa In the thin film evaporator, it is heated to 100°C, and continuous rapid vacuum distillation is performed to remove non-polymerizable components and trimethylamine; then, the temperature is lowered to below 60°C through a cooler and stored in dry defective product storage Standby in the tank; (defective DMC is called dry defective DMC after removing non-polymerizable low components and trimethylamine)
[0036] (2) Transport the dry defective product DMC to the refining kettle through the refining delivery pump, stop feeding when the raw material in the refining kettle reaches 80% of its volume, and add activated ca...
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