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Method for preparing uranium nitrate through catalytic hydrogenation reduction of uranyl nitrate

A technology for catalytic hydrogenation and uranyl nitrate, applied in chemical instruments and methods, uranium compounds, inorganic chemistry, etc., can solve problems such as difficulties in industrialization, reduction of conversion rate of hexavalent uranium, etc., to avoid side reactions, good economy, The effect of high gas conversion rate

Active Publication Date: 2021-10-22
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

In the relevant reactor, reaction (1) and reaction (2) are a parallel reaction process, if the reaction solution residence time is not enough, reaction (1) can not be carried out completely, and the uranyl nitrate conversion rate is relatively large, but when the reaction If the residence time of the solution is too long, the catalytic decomposition reaction (2) of hydrazine nitrate proceeds transitionally, so that the product liquid changes from a reduced state to an oxidized state, and the tetravalent uranium nitrate generated by the reaction is further oxidized to hexavalent uranyl nitrate, so that the hexavalent uranium nitrate lower conversion rate
Therefore, in order to obtain a higher conversion rate of uranyl nitrate in this process, it is necessary to control the residence time of the reaction solution more accurately so that the conversion rate of hydrazine nitrate is 30%-40%. This special requirement for the residence time of the reactor, Brings great difficulties to the industrialization of the process

Method used

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  • Method for preparing uranium nitrate through catalytic hydrogenation reduction of uranyl nitrate

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0030] The reaction liquid processing capacity is 62.5kg / h, and the UO in the raw material liquid storage tank 2 (NO 3 ) 2 The mass content is 0.31 (31%), HNO 3 The content is 0.1 (10%) and H 2The O content is 0.59 (59%), and the hexavalent uranium concentration is 208g / L; after adding hydrazine nitrate dropwise online, ensure that the final mass content of hydrazine nitrate in the high-pressure gas-liquid separation tank is 2%; the average particle size of the catalyst is 100 microns Pt / SiO 2 (1% precious metal loading). The reactor is a fluidized bed reactor. The flow rate of hydrogen is 180Nm 3 / h, the reactor temperature is 30 degrees centigrade and the pressure is 4.0Mpa (gauge pressure), the conversion rate of outlet uranyl nitrate is 98%, and the content of tetravalent uranium in the product liquid is 204g / L.

Embodiment 2

[0032] Different from Example 1 in that (the rest and the process are the same), in the raw material liquid storage tank, UO 2 (NO 3 ) 2 The mass content is 0.20 (20%), HNO 3 The content is 0.1 (10%) and H 2 The O content is 0.7 (70%), the concentration of hexavalent uranium is 134.2g / L, the conversion rate of exported uranyl nitrate is 98%, and the content of tetravalent uranium in the product liquid is 131.5g / L.

Embodiment 3

[0034] Different from Example 2 in that (the rest and the process are the same) UO in the raw material liquid storage tank 2 (NO 3 ) 2 The mass content of HNO 3 The content is 0.2 (20%) and H 2 The O content is 0.6 (60%), the concentration of hexavalent uranium is 134.2g / L, the conversion rate of exported uranyl nitrate is 98.1%, and the content of tetravalent uranium in the product liquid is 132g / L.

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Abstract

The invention discloses a method for preparing uranium nitrate (tetravalent uranium) by using catalytic hydrogenation reduction of uranyl nitrate (hexavalent uranium).The method comprises the following steps: mixing uranyl nitrate in a raw material liquid storage tank with nitric acid, feeding the mixture and circulating hydrogen into a high-pressure hydrogenation reactor filled with a catalyst through one end of the reactor, and catalytically reducing uranyl nitrate into uranium nitrate by hydrogen; and flowing the excessive hydrogen and product uranium nitrate out of the reactor through the other end of the reactor; dropwise adding a hydrazine nitrate or hydrazine solution on line into the gas-liquid mixture to convert the solution from an oxidation state to a reduction state, then feeding the gas-liquid mixture into a high-pressure gas-liquid separator for separation, absorbing and separating the nitrogen oxides in a gas phase through alkali liquor, pressurizing hydrogen through a compressor, and then feeding the hydrogen into a high-pressure hydrogen storage tank; and discharging a liquid-phase product from the bottom of a separator and enters a normal-pressure liquid-phase product hydrogen replacement tower, and removing the dissolved hydrogen in the liquid phase by using a nitrogen bubbling device in the tower, so that the safety of a subsequent process is ensured, and the obtained gas enters a high-emission tail gas treatment system.

Description

technical field [0001] The invention relates to a process for preparing tetravalent uranium, in particular to a process for preparing uranium nitrate (quaternary uranium) by catalytically hydrogenating and reducing uranyl nitrate (hexavalent uranium). Background technique [0002] With the large-scale development and application of nuclear power, the clean treatment and efficient recycling of spent nuclear 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 this process, the valuable uranium and plutonium elements are firstly 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 plutonium is reduced to trivalent and enters the water phase, but the hexavalent uranium remains in the oil phase, thereby achieving efficient separation and pur...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01G43/00
CPCC01G43/00Y02P10/20
Inventor 高德扬侯宝林赵许群梁兵连史海李雪张旭
Owner DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI
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