A hydrogenation reactor with a buffer component
A technology of hydrogenation reactors and reactors, applied in chemical instruments and methods, chemical/physical processes, etc., can solve the problems of reducing the service life of catalysts, damaging catalyst performance, and varying degrees of reaction, so as to achieve fine adjustment and stable The effect of uniform inlet conditions and low installation accuracy requirements
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Embodiment 1
[0041] Compared with Comparative Example 1, the embodiment 1 of the present invention adopts the hydrogenation reactor of the present invention, and in the upper head of the hydrogenation reactor, the shock-reducing equalizer plate of the present invention is arranged, and adopts such as figure 2 The surge reducing equalizer disc shown is used in combination with a common ERI type bubble cap gas-liquid distributor. The ring-plate type shock-reducing flow equalizer includes a tower tray and a distributor, and the distributor is arranged concentrically on the tray by 8 layers of shock-reducing ring plates. Downpipe 2 for collecting and discharging material. The height of the impact-reducing ring plate is 80mm; the lower edge of the impact-reducing ring plate is provided with a semicircular hole as a liquid phase channel, and the total cross-sectional area of the holes opened on each layer of the impact-reducing ring plate is 0.8 times the cross-sectional area of the reactor...
Embodiment 2
[0043] Same as Example 1, the difference is that the conventional ERI gas-liquid distributor in the field in the original hydrogenation reactor is canceled, and only the buffering and equalizing plate provided in the present invention is retained, the bed radial temperature and See Table 1 for the temperature difference.
[0044] Table 1 Application Results
[0045] Temperature measurement point location Comparative example 1 Example 1 Example 2 a 280.2 281.4 281.6 b 285.4 281.5 282.0 c 293.0 282.0 283.3 d 284.8 282.4 281.7 e 286.8 282.5 282.7 Maximum bed radial temperature difference, °C 12.8 1.1 1.7
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