Unlock instant, AI-driven research and patent intelligence for your innovation.

Uranium and plutonium separating technology with hydroxyamino acetic acid serving as reverse extracting reagent

The technology of hydroxylamine acetic acid and stripping reagent is applied in the field of uranium and plutonium separation technology, which can solve the problems of easy explosion, inability to effectively achieve deep separation of uranium and plutonium, and high risk, and achieves good operation stability, excellent separation effect, and simplified reagents. composition effect

Inactive Publication Date: 2016-07-20
CHINA INSTITUTE OF ATOMIC ENERGY
View PDF2 Cites 0 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] The uranium-plutonium separation process using the above-mentioned salt-free reducing agent system still has some problems to varying degrees, specifically: 1) The reducing agent system using the reducing agent + supporting reducing agent has a relatively complicated process and low economic efficiency; 2) ) The U(IV)-hydrazine system will cause reduction failure problems, and the purification coefficient of uranium in plutonium is low; 3) The hydroxylamine + hydrazine system cannot effectively realize the deep separation of uranium and plutonium; 4) The dimethyl hydroxylamine + monomethylhydrazine system It belongs to the double reagent system, and its danger is relatively high, and it is prone to explosion

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0019] Apply the uranium-plutonium separation process of the present invention to the uranium-plutonium separation process of the Purex process, using the following process conditions:

[0020] (1) The concentration of araminoacetic acid in 1BX is 0.7mol / L, and the concentration of nitric acid is 0.4mol / L;

[0021] (2) The uranium concentration of 1BF is 90g / L, and the plutonium concentration is 1.4g / L;

[0022] (3) The concentration of nitric acid in 1BS is 0.5mol / L;

[0023] (4) flow ratio 1BF:1BX:1BS=4:1:0.5;

[0024] (5) There are 11 stages of back-extraction and 5 stages of re-extraction.

[0025] After the separation of uranium and plutonium, the concentration of plutonium in 1BU is 40μg / L, and the separation factor of plutonium in uranium reaches 2.4×10 4 , indicating that the uranium-plutonium separation process of the present invention has excellent separation effect.

Embodiment 2

[0027] Apply the uranium-plutonium separation process of the present invention to the uranium-plutonium separation process of the Purex process, using the following process conditions:

[0028] (1) The concentration of araminoacetic acid in 1BX is 0.5mol / L, and the concentration of nitric acid is 0.2mol / L;

[0029] (2) The uranium concentration of 1BF is 80g / L, and the plutonium concentration is 0.5g / L;

[0030] (3) The concentration of nitric acid in 1BS is 0.3mol / L;

[0031] (4) flow ratio 1BF:1BX:1BS=8:1:0.5;

[0032] (5) There are 10 stages of back extraction and 6 stages of re-extraction.

[0033] After the separation of uranium and plutonium, the concentration of plutonium in 1BU is 18μg / L, and the separation factor of plutonium in uranium reaches 5.1×10 4 , indicating that the uranium-plutonium separation process of the present invention has excellent separation effect.

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

No PUM Login to View More

Abstract

The invention belongs to the field of nuclear fuel reprocessing and provides a uranium and plutonium separating technology with hydroxyamino acetic acid serving as a reverse extracting reagent to solve the problems in an existing salt-free reducing agent system in the uranium and plutonium separating technology. The technology includes the conditions that the concentration of hydroxyamino acetic acid of 1BX ranges from 0.5 mol / L to 0.8 mol / L, the concentration of uranium of 1BF ranges from 70 g / L to 95 g / L, the concentration of plutonium ranges from 0.1 g / L to 3 g / L, the concentration of nitric acid of 1BS ranges from 0.3 mol / L to 0.6 mol / L, the flow ratio of 1BF to 1BX to 1BS is 4-8:1:0.5, the reverse extracting level number is larger than or equal to 10, and the supplementing extracting level number is larger than or equal to 5. The uranium and plutonium separating technology is good in separating effect and particularly suitable for high-acid systems and achieves deep uranium and plutonium separating; and operation stability is good in the technology condition range, the use amount of the reagent is reduced, the economical efficiency is improved, and minimization of radioactive waste is facilitated.

Description

technical field [0001] The invention belongs to the field of nuclear fuel reprocessing, in particular to a process for separating uranium and plutonium using hydroxylamine acetic acid as a stripping reagent. Background technique [0002] The uranium-plutonium co-decontamination process for spent fuel reprocessing usually includes two key steps: uranium-plutonium co-extraction and uranium-plutonium separation. Wherein, the uranium-plutonium separation step uses a reducing agent to selectively reduce the plutonium and back-extract it into the water phase, thereby realizing the separation of uranium and plutonium. In the actual process of separating uranium and plutonium, the radiolysis of nitric acid in the water phase will produce a certain amount of nitrous acid. Since nitrous acid can quickly oxidize trivalent plutonium to tetravalent, which will affect the smooth progress of stripping, so in addition to the reducing agent , In the process of separating uranium and plutoni...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
Patent Type & Authority Applications(China)
IPC IPC(8): C22B60/04C22B60/02G21F9/12
CPCC22B60/026C22B60/04G21F9/125
Inventor 肖松涛刘协春罗方祥李丽杨贺兰天
Owner CHINA INSTITUTE OF ATOMIC ENERGY