Method for preparing high transpolybutadiene by utilizing gas-phase polymerization and catalyst used in method
A gas-phase polymerization and polybutadiene technology, which is applied in the field of gas-phase polymerization and its catalyst preparation, can solve problems affecting rubber processing and application performance, etc.
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Embodiment 1
[0030] (1) Preparation of catalyst
[0031] The catalyst consists of VCl 3 , AlEt 3 It is composed of four components, including silicon dioxide with a particle size range of 10-250 μm and nano-particle carbon black with a particle size range of 5-300 nm. The solvent used in the catalyst preparation process is n-hexane, the first component VCl 3 The amount is 1.2mmol, the second component AlEt 3 The amount of carbon black is 3.6mmol, the amount of the third component silicon dioxide is 4.8g, and the amount of the fourth component carbon black is 2.9g. After stirring evenly, the solvent was removed, and finally 8.3g of powdered catalyst A was obtained 1 .
[0032] (2) Butadiene gas phase polymerization process
[0033] In the purified stirred reactor, add the 8.3g powder catalyst A prepared above under the protection of nitrogen 1 , evacuate nitrogen, start stirring, feed butadiene gas, react under 0.1MPa pressure, 70°C for 1 hour, and dry after post-treatment to obtain ...
Embodiment 2
[0041] (1) Preparation of catalyst
[0042] The catalyst consists of VOCl 3 , AlEt 3 , carbon black with a particle size range of 10-250 μm, and nano-particle titanium dioxide with a particle size range of 5-300 nm. The solvent used in the catalyst preparation process is toluene, the first component VOCl 3 The amount is 1.0mmol, the second component AlEt 3 The amount of carbon black is 5.0mmol, the amount of the third component carbon black is 10.0g, and the amount of the fourth component titanium dioxide is 10.0g. After stirring evenly, the solvent is removed, and the powdered catalyst B is finally obtained. 1 20.7 g.
[0043] (2) Butadiene gas phase polymerization process
[0044] In the purified stirred reactor, add the powder catalyst B prepared above under the protection of nitrogen 1 20.7g, evacuate nitrogen, start stirring, feed butadiene gas, react at 70°C for 1 hour under 0.1MPa pressure, and dry after post-treatment to obtain 1801.6g of polymer product. Cata...
Embodiment 3
[0052] (1) Catalyst preparation
[0053] The catalyst consists of TiCl 4 , AlEt 3 , magnesium chloride with a particle size range of 10-250 μm, and nano-particle silica with a particle size range of 5-300 nm. The solvent used in the catalyst preparation process is n-heptane, of which the first component TiCl 4 The amount is 1.0mmol, the second component AlEt 3 The amount of the magnesium chloride is 10.0mmol, the amount of the third component magnesium chloride is 25.0g, and the amount of the fourth component silicon dioxide is 50.0g. After stirring evenly, the solvent is removed, and the powdery catalyst C is finally obtained. 1 76.3g.
[0054] (2) Butadiene gas phase polymerization process
[0055] In the purified stirred reactor, add the powder catalyst C prepared above under the protection of nitrogen. 1 76.3g, evacuate nitrogen, start stirring, feed butadiene gas, react at 60°C for 1 hour under 0.1MPa pressure, and dry after post-treatment to obtain 1501.4g of polym...
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