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Clean production method for recovering uranium and molybdenum from wrapped uranium and molybdenum ores

A wrap-type, molybdenum ore technology, applied in the fields of chemical industry and metallurgy, can solve the problems of complex uranium and molybdenum metal recovery process, difficult solid-liquid separation of leaching slurry, and difficult solid-liquid separation, so as to save solid-liquid separation and save equipment costs. , The effect of operating environment friendly

Inactive Publication Date: 2018-02-27
BEIJING RESEARCH INSTITUTE OF CHEMICAL ENGINEERING AND METALLURGY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] For this type of refractory uranium-molybdenum ore, in order to improve the leaching rate of uranium and molybdenum, most of them adopt enhanced oxidation acid leaching technology, high pressure alkali leaching technology and oxidation roasting technology, among which the most commonly used method in enhanced oxidation acid leaching technology is permanganate Potassium enhanced oxidation leaching, hydrogen peroxide enhanced oxidation leaching and nitric acid enhanced oxidation leaching, etc. Although the enhanced oxidation leaching process can improve the leaching of uranium and molybdenum, there are problems such as large oxidant consumption and high production costs. In addition, because the ore itself is clay and the leaching solution There are many organic matters, which makes the solid-liquid separation of leached pulp extremely difficult
The use of high-pressure alkaline leaching technology has problems such as high equipment cost, high maintenance cost, difficult operation, difficult solid-liquid separation, and complicated recovery process of uranium and molybdenum metals.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0019] Crushing and grinding the uranium-molybdenum ore with uranium and molybdenum grades of 0.093% and 1.18% respectively to a particle size of less than -100 mesh, in which the sulfur content in the ore is 3.47%, mix it evenly according to the CaO / S molar ratio of 1.2, and then mix it with water for granulation , control the maximum particle size at 10mm, send it to the rotary kiln for roasting at 600°C for 3 hours, build up a heap and spray leaching after cooling, the concentration of sulfuric acid in the spraying leaching agent in the early stage of leaching is 120g / L, and the spraying intensity is 40L / ( m 2 h), the spraying time is 3 days; the concentration of sulfuric acid in the leaching agent in the later stage of leaching is 15g / L, spraying in intervals, spraying for 16 hours a day, and the spraying intensity is 20 / (m 2 h), the spraying time is 17 days.

[0020] After leaching, the slag analysis showed that the leaching rate of uranium was 90.1%, the leaching rate o...

Embodiment 2

[0022] Crush and grind uranium-molybdenum ore with uranium and molybdenum grades of 0.093% and 1.18% respectively to a particle size of less than -100 mesh, in which the sulfur content in the ore is 3.47%, and mix it evenly according to the CaO / S molar ratio of 1.5, then mix it with water and granulate , control the maximum particle size at 10mm, send it to the rotary kiln for roasting at 600°C for 3 hours, build up a heap and spray leaching after cooling, the concentration of sulfuric acid in the spraying leaching agent in the early stage of leaching is 120g / L, and the spraying intensity is 40L / ( m 2 h), the spraying time is 3 days; the concentration of sulfuric acid in the leaching agent in the later stage of leaching is 15g / L, spraying in intervals, spraying for 16 hours a day, and the spraying intensity is 20 / (m 2 h), the spraying time is 17 days.

[0023] After leaching, the slag analysis showed that the leaching rate of uranium was 90.2%, the rate of molybdenum leaching...

Embodiment 3

[0025] Crushing and grinding the uranium-molybdenum ore with uranium and molybdenum grades of 0.093% and 1.18% respectively to a particle size of less than -100 mesh, in which the sulfur content in the ore is 3.47%, mix evenly according to the CaO / S molar ratio of 2, and mix with water to granulate , control the maximum particle size at 10mm, send it to the rotary kiln for roasting at 600°C for 3 hours, build up a heap and spray leaching after cooling, the concentration of sulfuric acid in the spraying leaching agent in the early stage of leaching is 120g / L, and the spraying intensity is 40L / ( m 2 h), the spraying time is 3 days; the concentration of sulfuric acid in the leaching agent in the later stage of leaching is 15g / L, spraying in intervals, spraying for 16 hours a day, and the spraying intensity is 20 / (m 2 h), the spraying time is 17 days.

[0026] After leaching, the slag analysis showed that the leaching rate of uranium was 90.1%, the leaching rate of molybdenum was...

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Abstract

The invention discloses a clean production method for recovering uranium and molybdenum from wrapped uranium and molybdenum ores and belongs to the field of chemical engineering and metallurgy. The clean production method comprises the following steps of evenly mixing the crushed wrapped uranium and molybdenum ores with additives, and then adding water for pelletizing; conveying the pelletized ores into a rotary kiln for roasting; cooling the roasted ores and then conducting heaping; and then spraying a leaching agent to conduct leaching. According to the clean production method for recoveringthe uranium and molybdenum from the wrapped uranium and molybdenum ores, the ores and a sulfur-fixing agent are mixed evenly and are subjected to pelletizing; in the roasting process, not smoke and dust are generated; 95% or more of sulfur can be solidified in the ores; the roasted ores can be subjected to heap leaching; the leaching rates of the uranium and molybdenum in the ores can reach up to90% and 80% or more correspondingly; the solid-liquid separation step is omitted; the solid content of a leaching solution is low, and the leaching solution can be directly used for subsequent extraction separation. The clean production method has the advantages of being reasonable in technological process, high in production efficiency, high in metal recovery rate, friendly to the operating environment and the like.

Description

technical field [0001] The invention belongs to the fields of chemical industry and metallurgy, and in particular relates to a clean production method for recovering uranium and molybdenum from wrapped uranium-molybdenum ore. Background technique [0002] Encapsulated uranium-molybdenum ores are mainly distributed in the Hebei-Inner Mongolia metallogenic belt. They are medium-low temperature hydrothermal porphyry-type uranium-molybdenum ores. The properties of this type of ore are very complex, and its notable feature is that there is a special form of molybdenum minerals in the ore- Glysolite forms a dense sulfide package on the attached ore, which hinders the penetration of the leaching agent into the inclusion and the oxidation of the molybdenum mineral by the oxidant, increasing the difficulty of leaching uranium and molybdenum. Therefore, for this type of ore The extraction technology of uranium and molybdenum has become a hot issue in the metallurgical field. [0003]...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B34/34C22B60/02C22B1/02C22B3/08
CPCC22B34/34C22B1/02C22B3/08C22B60/0234
Inventor 向秋林师留印曾毅君杨剑飞李培佑刘会武刘忠臣贾秀敏陈天宝黄永刘智
Owner BEIJING RESEARCH INSTITUTE OF CHEMICAL ENGINEERING AND METALLURGY
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