Method for filling catalyst in tube type fixed bed reactor
A fixed-bed reactor and catalyst technology, applied in chemical instruments and methods, chemical/physical processes, etc., can solve problems such as uneven loading of catalysts, achieve good loading effect, uniform loading, and easy operation
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Embodiment 1
[0029] Install a blocking spring at the bottom of the reaction tube, and fill the upper part of the blocking spring with a 100mm high Φ3mm ceramic ball to avoid catalyst leakage during the filling process. Weigh 4kg of catalyst, evenly load the catalyst into the reaction tube, and control the rate of rise of the catalyst bed height to 40mm / s. After the catalyst is loaded, the bed pressure drop is measured and the data is recorded.
[0030] The above filling was repeated 20 times, and the bed pressure drop was counted. The statistical results are shown in Table 1.
[0031] Table 1 Example 1 bed pressure drop statistics
[0032] Bed pressure drop deviation
Embodiment 2
[0034] Install a blocking spring at the bottom of the reaction tube, and fill the upper part of the blocking spring with a 100mm high Φ3mm ceramic ball to avoid catalyst leakage during the filling process. Weigh 4kg of catalyst, evenly load the catalyst into the reaction tube, and control the rate of rise of the catalyst bed height to 20mm / s. After the catalyst is loaded, the bed pressure drop is measured and the data is recorded.
[0035] The above filling was repeated 20 times, and the bed pressure drop was counted. The statistical results are shown in Table 2.
[0036] Table 2 Example 2 bed pressure drop statistics
[0037] Bed pressure drop deviation
[0038] It can be seen from Example 1 and Example 2 that the method of the present invention is used for catalyst loading, the uniformity of catalyst loading is better, and the bed pressure drop can be controlled within ±5%.
Embodiment 3
[0040] On the basis of Example 2, the catalyst loading rounds were continued, and the pressure drop of the bed was lower than the average pressure drop of 3% when it was carried out to the 25th time. Another 0.1 kg of catalyst was loaded into the reactor at a constant speed, so that the rate of increase in the height of the catalyst bed was 5 mm / s. After the catalyst replenishment was completed, the pressure drop measurement was carried out. The pressure drop measurement conditions were the same as in Example 2, and the measured pressure drop was 0.5% higher than the average pressure drop.
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