Uranium trioxide fluidized bed hydrogen reduction process
A uranium trioxide and fluidized bed technology, applied in the field of uranium trioxide fluidized bed hydrogen reduction technology
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[0024] The present invention will be further described below in conjunction with the accompanying drawings and embodiments.
[0025] According to the above process flow, establish a 100kgU / h process system and carry out an engineering test system.
[0026] At the temperatures of 550±10°C, 580±10°C, 600±10°C, 620±10°C, 640±10°C, the hydrogen excess is about 100% (based on 100kgU per hour), and the molar ratio of nitrogen to hydrogen is 1:3, and the reaction time was 8h, and the reduction reaction was carried out. The analysis results of product UO2 are shown in Table 1. From the data in Table 1, it can be known that as the temperature increases, the reduction conversion rate also increases. When it reaches 600±10°C, the reduction conversion rate of UO3 basically no longer increases, so the optimal reaction temperature is 600±10°C.
[0027] Table 1UO 3 The relationship between reduction conversion rate and temperature
[0028]
[0029] The reduction reaction was carried o...
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