Hydrogenation reaction device and method for continuously hydrogenating conjugated diene polymers using the device
A technology for hydrogenation reaction and conjugated diene, which is applied to a hydrogenation reaction device and the hydrogenation field where the device is applied, can solve the problems of shortening the working time of a hydrogenation catalyst, increasing the temperature, and reducing the hydrogenation rate of a conjugated diene-based polymer.
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Embodiment 1
[0134] Example 1: Continuous Hydrogenation of Conjugated Diene-Based Polymers
[0135] The conjugated diene polymer SBS-1 is 0.246g / hr (0.71 millimole / hr), 1.05g / hr, 0.57g / hr feed amount, and cooperate solvent cyclohexane to import such as figure 1 Form a reaction mortar (solid content 15% by weight) after stirring and mixing in the shown mixing tank 21; Above-mentioned reaction mortar is imported such as figure 1 In the hydrogenation reaction device, and each hydrogenation reactor of the hydrogenation reaction device is built with several filling parts as shown in Figure 3, and introduces hydrogen into the numbering A, C, E (as described later) in the hydrogenation reactor at the same time, so that each The hydrogen inlet pressure in the hydrogenation reactor was maintained at 9kg / cm 2 g, and by controlling the interlayer water temperature and heat exchangers 12, 12' of each hydrogenation reactor 11, 11' (numbered A, B, C, D, E and F from upflow to downflow) to remove Heat...
Embodiment 2~4
[0137] Embodiments 2 to 4 carry out the hydrogenation reaction with the same hydrogenation reaction device and steps as in Embodiment 1. The difference is that the embodiments 2 to 4 use the conjugated diene polymer SBS- 1 or conjugated diene polymer SBS-2, and dicyclopentadienyl titanium dichloride, polymethylhydrogensiloxane and n-butyl lithium in different feed amounts, and different hydrogenation conditions to obtain hydrogenated Table 1 also lists the conjugated diene polymer and the hydrogenation rate of the hydrogenated conjugated diene polymer obtained therefrom.
[0138] From the results of the above examples, it is known that when the continuous hydrogenation reactor of the present invention is used to hydrogenate a conjugated diene polymer, the filler 5 in the hydrogenation reactor 11, 11' can slow down the downward flow of the polymer. The rate and then prolong the reaction time, so that the hydrogenation reaction of the polymer with hydrogen and the hydrogenation ...
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