Method for continuously precipitating plutonium oxalate

A technology of plutonium oxalate and oxalic acid, which is applied in the field of continuous precipitation of plutonium oxalate, which can solve the problems of reactor wall sticking, low plutonium oxalate production, and small particle size, so as to increase production, reduce sticking and agglomeration , the effect of increasing the amount of precipitation

Pending Publication Date: 2022-04-29
CHINA INSTITUTE OF ATOMIC ENERGY
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Problems solved by technology

[0008] The purpose of this disclosure is to provide a method for continuous precipitation of plutonium oxalate. The purpose is to solve the problem that during the continuous precipitation of plutonium oxalate, the particle size of plutonium oxalate precipitation particles is small, and the production capacity of plutonium oxalate per unit time is not high. It is easy to have problems such as sticking or agglomeration on the reactor wall

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  • Method for continuously precipitating plutonium oxalate
  • Method for continuously precipitating plutonium oxalate
  • Method for continuously precipitating plutonium oxalate

Examples

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Embodiment 1

[0058] Add 500.0 mL of combined reagents (2.60 mol / L nitric acid and 0.10 mol / L oxalic acid) preheated to 50 ° C into a 650.0 mL plutonium oxalate precipitation reactor and stir at 550 r / min to make the combined reagents form a flow field; then Heat plutonium(IV) nitrate feed solution (2.4mol / L nitric acid and 25.0g / L Pu(IV) solution) and oxalic acid feed solution (2.2mol / L nitric acid and 0.60mol / L oxalic acid solution) to 50 After ℃, it is continuously added to the plutonium oxalate precipitation reactor for continuous precipitation reaction. The reaction conditions of the continuous precipitation reaction are: the stirring blade is a three-blade propeller, the angle between the three-blade propeller type stirring blade and the horizontal plane is 45 degrees, the stirring paddle is 1.0 cm away from the bottom of the plutonium oxalate precipitation reactor, and the diameter of the stirring paddle is 3.5cm, the stirring rate is 550r / min; adjust plutonium (IV) nitrate feed liqu...

Embodiment 2

[0060] The method for the continuous precipitation of plutonium oxalate is the same as in Example 1, the difference being that the plutonium (IV) nitrate and oxalic acid feed solutions are fed to the central vortex area, and the oxalic acid feed solution is added to the peripheral vortex area.

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Abstract

The invention relates to a plutonium oxalate continuous precipitation method which comprises the following steps: adding a combined reagent into a plutonium oxalate precipitation reactor and stirring to enable the combined reagent to form a flow field; then continuously adding the plutonium nitrate (IV) feed liquid and the oxalic acid feed liquid into a plutonium oxalate precipitation reactor for continuous precipitation reaction; the reaction conditions of the continuous precipitation reaction are as follows: the ratio of the flow of the plutonium (IV) nitrate feed liquid to the flow of the oxalic acid feed liquid is (1-1.5): 1, the reaction temperature is 40-58 DEG C, and the reaction time is 10-50 minutes. By adopting the method disclosed by the invention for continuous precipitation of the plutonium oxalate, the production quantity of the plutonium oxalate in unit time can be increased, the precipitation quantity of large plutonium oxalate particles can be increased, and the phenomena of wall sticking and caking of the plutonium oxalate precipitation particles on the inner wall of a plutonium oxalate precipitation reactor can be reduced.

Description

technical field [0001] The present disclosure relates to the field of nuclear waste treatment, in particular to a method for continuous precipitation of plutonium oxalate. Background technique [0002] In order to finally convert the plutonium-containing feed solution into PuO 2 Plutonium powder is stored or made into fast reactor nuclear fuel elements, usually using oxalic acid as a precipitant to directly convert plutonium(III) nitrate into plutonium(III) oxalate for precipitation; or oxidize plutonium(III) nitrate into plutonium(IV) nitrate And then converted to plutonium oxalate precipitation. The generated plutonium (III, IV) oxalate precipitate particles and mother liquor are then passed through the next continuous filtration process section and continuous calcination process section, and finally converted into PuO 2 The powder realizes the conversion of plutonium ions in solution to solid plutonium oxide. Compared with the plutonium(III) oxalate precipitation metho...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): G21F9/10G21F9/00
CPCG21F9/10G21F9/008
Inventor 李传博王博晏太红郑卫芳
Owner CHINA INSTITUTE OF ATOMIC ENERGY
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