A high-efficiency pyrolysis recovery method for silicone rubber waste
A technology of silicone rubber waste and recycling method, applied in the field of materials, can solve the problems of increased process difficulty, large acid dosage, high process temperature, etc., and achieves the effects of improving cracking efficiency, less basic catalyst, and lowering process temperature.
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Embodiment 1
[0042] (1) pulverization: the dimethyl silicone rubber waste is washed, cut into pieces, and dried, and after the surface impurities are cleaned by ultrasonic or mechanical vibration, the silicone rubber waste is pulverized into particles by a rubber crusher, and the particle size is 1-2mm;
[0043] (2) double cracking: put the crushed silicone rubber particles into the cracking reactor, then add phenyl ether solvent and the copper complex of 0.3% of sodium hydroxide by weight of silicone rubber and 0.3% by weight of sodium hydroxide by adding phenyl ether solvent Depolymerization was carried out at a high temperature of 150 °C under a nitrogen atmosphere for 3 h to obtain crude DMC with a content of 79% cracked products;
[0044] (3) polymerization rearrangement: the crude DMC is added to the rearrangement reactor, then the potassium hydroxide-methanol solution that the concentration is 1% is added, and the consumption is 15% of the crude DMC quality, and 1% of the crude DMC q...
Embodiment 2
[0047] (1) pulverization: the dimethyl silicone rubber waste is washed, cut into pieces, and dried, and after ultrasonic or mechanical vibration cleaning the surface impurities, the silicone rubber waste is pulverized into particles by a rubber crusher, and the particle size is 1-3mm;
[0048] (2) Double cracking: put the crushed silicone rubber particles into the cracking reactor, then add tetraethylene glycol dimethyl ether solvent and sodium hydroxide with an amount of 5% by weight of silicone rubber and 0.5% by weight of sodium hydroxide Depolymerization of the copper complex of fern base was carried out at a high temperature of 170 °C under nitrogen atmosphere for 3.5 h, to obtain crude DMC with a content of cracked products of 82%;
[0049] (3) polymerization rearrangement: the crude DMC is added to the rearrangement reactor, then the potassium hydroxide-methanol solution that the concentration is 1% is added, and the consumption is 15% of the crude DMC quality, and 1.5% ...
Embodiment 3
[0052] (1) pulverization: the dimethyl silicone rubber waste is washed, cut into pieces, and dried, and after ultrasonic or mechanical vibration cleaning the surface impurities, the silicone rubber waste is pulverized into particles by a rubber crusher, and the particle size is 2-3mm;
[0053] (2) double cracking: put the crushed silicone rubber particles into the cracking reactor, then add phenyl ether solvent and the amount of sodium hydroxide that is 5% of the weight of the silicone rubber, 0.4% of the weight of the sodium hydroxide, the nickel coordination of the Schiff base Depolymerization was carried out at a high temperature of 190 °C under nitrogen atmosphere for 5 h to obtain crude DMC with a content of 79% cracked products;
[0054] (3) polymerization rearrangement: the crude DMC is added to the rearrangement reactor, then the potassium hydroxide-methanol solution that the concentration is 1% is added, and the consumption is 15% of the crude DMC quality, and 1.5% of ...
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