Method for decomposing bastnaesite through calcification transformation-leaching

A technology of calcification transformation and bastnaesite, which is applied in the field of calcification transformation-leaching and decomposition of bastnaesite, can solve the problems of rare earth loss, waste of fluorine resources, high energy consumption, etc., achieve efficient separation and comprehensive recovery, reduce fuel consumption, The effect of low firing temperature

Active Publication Date: 2013-07-24
NORTHEASTERN UNIV
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Problems solved by technology

The above process has the advantages of short process flow, small investment, and low production cost of cerium products, but there are problems such as discontinuous process, low product purity, difficult recovery of thorium and fluorine dispersed in slag and waste water, and pollution to the environment.
For example, Chinese Patent (Application No.) 200410031180.6 discloses a method for decomposing bastnaesite with hydrochloric acid. In this method, after oxidizing and roasting bastnaesite, sodium hydroxide is used to remove fluoride, and hydrochloric acid is optimally soluble-completely soluble. In this method, hydrogen The consumption of sodium oxide is large, and a large amount of alkaline wastewater is produced at the same time
Chinese patents (application numbers) 2004100031179.3 and 200410070199.1 disclose a method for decomposing bastnaesite by sulfuric acid leaching. These methods all have defects such as high energy consumption, large amount of waste water and serious pollution, and serious waste of fluorine resources
The impurities in the concentrate will significantly affect the product quality and reduce the recovery rate of rare earths. Therefore, the concentrate must be removed by chemical beneficiation before decomposing impurity minerals such as fluorspar, but the rare earths will lose 2%-5% during the beneficiation process
The process of decomposing Baotou rare earth concentrate by sodium hydroxide method is relatively mature, but it is rarely used in domestic large-scale factories because of the disadvantages of high grade rare earth concentrate, impurity removal treatment before decomposition and low recovery rate of rare earth.

Method used

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  • Method for decomposing bastnaesite through calcification transformation-leaching

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Experimental program
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Effect test

Embodiment 1

[0032] (1) Activation pretreatment of rare earth concentrate

[0033] Roast bastnaesite concentrate at 430°C for 3 hours to obtain activated ore;

[0034] (2) Activated ore calcification transition pretreatment

[0035] Mix the activated ore obtained in step (1) with CaO evenly at a mass ratio of 100:70, then mix the mixture with 0.5mol / L NaOH solution according to the solid-to-liquid ratio of 1kg:20L for calcification and fluorine-fixing transition pretreatment, and the transition temperature is 150°C, the transformation time is 3 hours, and then solid-liquid separation is carried out to obtain transformation slag and lye, and the lye is directly recycled;

[0036] (3) Transformation slag acid leaching

[0037] (a) The transformation slag obtained in step (2) and 1 mol / L hydrochloric acid solution are subjected to acid leaching treatment according to the solid-to-liquid ratio of 1 kg : 20L, the leaching temperature is 30°C, the leaching time is 120min, and the mass fraction...

Embodiment 2

[0043] (1) Activation pretreatment of rare earth concentrate

[0044] Roast bastnaesite concentrate at 480°C for 2 hours to obtain activated ore;

[0045] (2) Activated ore calcification transition pretreatment

[0046] Mix the activated ore obtained in step (1) with CaO evenly at a mass ratio of 100:80, then mix the mixture with 0.5mol / L NaOH solution according to the solid-to-liquid ratio of 1kg:15L for calcification and fluorine-fixing transition pretreatment, and the transition temperature is 180°C, the transformation time is 2 hours, and then the solid-liquid separation is carried out to obtain the transformation slag and lye, and the lye is directly recycled;

[0047] (3) Transformation slag acid leaching

[0048] (a) The transformation slag obtained in step (2) and 1.5mol / L hydrochloric acid solution are subjected to acid leaching treatment according to the solid-to-liquid ratio of 1 kg: 20L, the leaching temperature is 50°C, the leaching time is 90min, and the mass f...

Embodiment 3

[0054] (1) Activation pretreatment of rare earth concentrate

[0055] Roast bastnaesite concentrate at 500°C for 1 hour to obtain activated ore;

[0056] (2) Activated ore calcification transition pretreatment

[0057] Mix the activated ore obtained in step (1) with CaO evenly at a mass ratio of 100:100, then mix the mixture with 1.0mol / L NaOH solution according to the solid-to-liquid ratio of 1kg:10L for calcification and fluorine-fixing transition pretreatment, and the transition temperature is 300°C, the transformation time is 2 hours, and then solid-liquid separation is carried out to obtain transformation slag and lye, and the lye is directly recycled;

[0058] (3) Transformation slag acid leaching

[0059] (a) The transformation slag obtained in step (2) and 1.5mol / L hydrochloric acid solution are subjected to acid leaching treatment according to the solid-to-liquid ratio of 1 kg: 20L, the leaching temperature is 90°C, the leaching time is 30min, and the mass fraction ...

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Abstract

The invention belongs to the technical field of rare earth metallurgy, and particularly relates to a method for decomposing bastnaesite through calcification transformation-leaching. The method comprises the following the steps of: carrying out activation pretreatment on rare earth ore concentrate, carrying out calcification transformation pretreatment on the activated ore, carrying out acid leaching on transformed slag, extracting rare earth chloride fine liquid to finally obtain a solution with thorium-iron slag and cerium chloride or lanthanum chloride or praseodymium chloride or neodymium trichloride, and efficiently separating valuable elements such as a rare earth element, a fluorine element and a thorium element. According to the method, energy consumption and fuel consumption are reduced, and when the low-temperature baking is carried out below 500 DEG C, only carbonates are decomposed, so that the reaction activity of the rare earth ore concentrate is supplied, and simultaneously the waste of fluorine resources and the emission pollution are avoided; and therefore, the method belongs to a green clean technology.

Description

[0001] technical field [0002] The invention belongs to the technical field of rare earth metallurgy, in particular to a method for decomposing bastnaesite by calcification transformation-leaching. Background technique [0003] Bastnaesite is an important rare earth resource in the world. The mineral is mainly produced in Sichuan and Shandong in China and Mountain Pass in the United States. Bastnaesite, which is rich in Sichuan, Shandong and other places, is the second largest rare earth resource in my country, and rare earths exist in the form of fluorocarbonates. After beneficiation, the concentrate grade can reach 50% to 70%, and the concentrate generally contains 8% to 9% fluorine. At present, the industrial processes for decomposing bastnaesite to extract rare earths include acid method and alkali method. [0004] Among them, the acid leaching method includes hydrochloric acid and sulfuric acid decomposition methods. In the 1990s, bastnaesite in Sichuan area of...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B59/00C22B1/02
Inventor 张廷安豆志河吕国志牛丽萍刘燕赫冀成
Owner NORTHEASTERN UNIV
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