Method for desulfurization regeneration of vulcanized rubber by employing double-screw extruder
A twin-screw extruder and vulcanized rubber technology, which is applied in recycling technology, plastic recycling, etc., can solve the problems of complex equipment, long operation time, large-area site, etc., and achieve low cost, homogeneous desulfurization and regeneration, and simple method Effect
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Embodiment 1
[0016] Embodiment 1: with the mixture of 2 parts of coumarone (the said part in the implementation all refers to mass parts), 8 parts of pine tar oil, 4 parts of phenyl mercaptans, 5 parts of n-butylamine, 10 parts of water is regeneration agent, Mix 100 parts of waste vulcanized rubber powder with a particle size of 10 mm in a high-speed mixer (1500 rpm) and regenerant at 100 ° C, and then feed it into the first twin-screw extruder (D = 60, L / D=30, compression ratio=3, all adopt the extruder of this type in the following examples) rotating speed=100 rev / min, pressurization, through forward and backward multi-stage pressure mixing, make the temperature reach 200 ℃, after the pressure reaches 2Mpa, it is directly connected to the second twin-screw extruder (D=50, L / D=30, compression ratio=3) through the machine head sideways, and this type of extruder is used in the following examples Machine) rotating speed=200 rpm, carry out secondary pressurization, heating, reach 250 ℃, pre...
Embodiment 2
[0018] Example 2: Using a mixture of 1 part of coumarone, 10 parts of pine tar, 3 parts of phenylmercaptan, 7 parts of n-butylamine and 5 parts of water as a regenerant, 100 parts of waste vulcanized rubber powder with a particle size of 6 mm , mixed evenly with the regenerant in a high-speed mixer (1500 rpm) at 90°C, and then fed into the first twin-screw extruder (rotational speed = 150 rpm) through a feeding device to pressurize, pass through, Inverse multi-stage pressurized mixing, so that the temperature reaches 220°C and the pressure reaches 2.5Mpa, and then it is directly connected to the second twin-screw extruder (speed = 300 rpm) through the machine head sideways for secondary pressurization and pressurization. temperature to 280°C and pressure to 4Mpa, the prepared desulfurized regenerated rubber has the following properties: tensile strength 18.48MPa, tear strength 35.91KN / m, elongation at break 567.35%, and Mooney viscosity 58.74.
[0019] Original rubber-like pro...
Embodiment 3
[0020] Example 3: Using a mixture of 3 parts of coumarone, 5 parts of pine tar, 1 part of phenylmercaptan, 2 parts of n-butylamine, and 15 parts of water as a regenerant, 100 parts of waste vulcanized rubber powder with a particle size of 1 mm , mixed evenly with the regeneration agent in a high-speed mixer (1500 rpm) at 80°C, and then fed into the first twin-screw extruder (rotational speed = 170 rpm) through a feeding device to pressurize, pass through, Reverse multi-stage pressurized mixing, so that the temperature reaches 230°C, and the pressure reaches 3Mpa, and then it is directly connected to the second twin-screw extruder (screw speed 400 rpm) through the machine head sideways for secondary pressurization and heating , reached 300°C, and the pressure reached 5Mpa, that is, the prepared desulfurized reclaimed rubber had the following properties: tensile strength 16.26MPa, tear strength 30.17KN / m, elongation at break 535.51%, and Mooney viscosity 53.28.
[0021] Original...
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