Fixed bed reactor for catalytic reduction of hexavalent uranium by hydrazine nitrate, and application thereof

A fixed bed reactor and catalytic bed technology is applied in the field of reactor devices for reducing hexavalent uranium to generate tetravalent uranium, and can solve the problems of increasing solid waste, slow reaction process, catalyst deactivation and the like

Inactive Publication Date: 2020-06-09
DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The characteristics of the reaction process are: 1. The reaction temperature must be controlled at 40-60 degrees. The reaction temperature is lower than 40 degrees. The consumption rate of hydrazine nitrate in the reaction process is too fast, so that there is a risk of deactivation of the catalyst due to the low concentration of hydrazine nitrate in the later stage of the reaction; 2. The acid concentration must be maintained at 0.5-0.8M in the reaction process. Nitric acid participates in the reduction reaction of hexavalent uranium, and also inhibits the decomposition of hydrazine nitrate. When the acid concentration is lower than 0.5M, the hydrazine nitrate will be consumed excessively. When the acid concentration is higher than 0.8M, the catalyst will be oxidized and deactivated by nitric acid. danger

Method used

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  • Fixed bed reactor for catalytic reduction of hexavalent uranium by hydrazine nitrate, and application thereof
  • Fixed bed reactor for catalytic reduction of hexavalent uranium by hydrazine nitrate, and application thereof

Examples

Experimental program
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Embodiment 1

[0032] The reaction liquid processing capacity is 13.8kg / h, wherein the mass content of UO2(NO3)2 is 0.31, N2H5NO3 is 0.11, HNO3 content is 0.05 and H2O content is 0.54; the diameter of the reactor is 300x2mm, and the catalyst is loaded in three stages. The diameter of the particles is 5mm, the length of the catalytic bed of each reactor is 300mm, the diameter of the top and bottom of each catalytic bed is 10mm, and the length is 50mm. The diameter of the heat exchange tube is 30x1.5mm, and the heat exchange tube is distributed in a regular triangle The quantity is 20, and the length of the heat exchange tube is 50cm; the acid regulating distributor is composed of figure 2The composition of the cross structure shown is a stainless steel pipe with a diameter of 25x1.5mm, the diameter of the opening is 1.0mm, the hole spacing is 20mm, the flow rate of 50% nitric acid is 0.5kg / h; the reaction liquid inlet temperature is 40 degrees, and the cooling water inlet The outlet temperat...

Embodiment 2

[0034] Compared with Example 1, the difference is that the length of each catalyst section is 400 mm, which is due to the increase in the length of the catalyst, and the transition consumption of hydrazine nitrate makes the tetravalent uranium generated by the reaction further oxidized to hexavalent uranium in the later stage of the reaction, and the hexavalent uranium is converted into The rate becomes 75%, the export tetravalent uranium content is 150g / L, and the conversion rate of hydrazine nitrate is 95%;

Embodiment 3

[0036] Compared with Example 1, the difference is that the number of heat exchange tubes is 50, the average temperature of the reactor is 45 degrees, the conversion rate of hexavalent uranium is 70%, the content of tetravalent uranium in the outlet is 140g / L, and the conversion rate of hydrazine nitrate is 60%;

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Abstract

The invention discloses a novel multi-section adiabatic fixed bed reactor device for producing tetravalent uranium through catalytic reduction of hexavalent uranium by hydrazine nitrate. The main function of the device is to control the reaction liquid residence time distribution, the reaction temperature and the acidity in a reaction process in the form of a multi-section adiabatic fixed bed reactor so as to enable the reaction liquid to be in the optimal operation interval, so that minimization of solid high-level radioactive waste discharge is achieved, and the purposes that the content oftetravalent uranium at an outlet meets the requirement and a catalyst is prevented from being oxidized and inactivated due to excessive consumption of hydrazine nitrate. In the optimal implementationscheme, the conversion rate of hexavalent uranium at the outlet of the reactor is greater than 98%, the conversion rate of hydrazine nitrate is lower than 35%, and the content of tetravalent uranium at the outlet of the reactor is greater than 200 g / L.

Description

technical field [0001] The invention relates to a multi-stage adiabatic fixed-bed reactor for reducing hexavalent uranium to generate tetravalent uranium, in particular to a reactor that can be used to reduce hexavalent uranium to generate tetravalent uranium by using hydrazine nitrate as a reducing agent device. Background technique: [0002] With the large-scale development and application of nuclear power, the clean treatment and efficient recycling of nuclear spent fuel have become the key to the further development of nuclear power. At present, the technology mainly adopted by domestic and foreign reprocessing plants is the Purex process. In the process of this process, the valuable uranium and plutonium elements are first extracted into the organic phase through the extraction unit, so as to be separated from most of the splinter elements to achieve the purpose of decontamination; The valence plutonium is reduced to trivalent and enters the water phase, but the hexav...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J8/02B01J8/00
CPCB01J8/001B01J8/02
Inventor 赵许群侯宝林史海张涛
Owner DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI
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