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A kind of boiling chlorination extraction method of niobium and tantalum concentrate

A technology of boiling chlorination and extraction method, which is applied in the field of metallurgy, can solve the problems of low added value of products, low attention, high pollution, etc., and achieve the effects of reducing the discharge of three wastes, significant environmental benefits, and short process flow

Inactive Publication Date: 2020-12-04
内蒙古扎鲁特旗鲁安矿业有限公司 +3
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0003] my country's niobium and tantalum smelting still has a large gap compared with the international advanced level in terms of production technology and product quality. The main factors hindering the development of niobium and tantalum smelting are: high product development costs, high consumption of raw materials and auxiliary materials, Pollution is heavy, product quality is low, product added value is low, benefit is low, and there are not many enterprises in China that have mastered niobium and tantalum hydrometallurgy technology
At present, my country's niobium and tantalum smelting mainly relies on imported high-grade niobium and tantalum concentrates. The smelting methods only include hydrofluoric acid leaching and sulfuric acid hydrofluoric acid mixed acid leaching. There is nothing to do with ore with complex grades, and these two methods are high pollution, high material consumption, and high energy consumption processes. Compared with the bulk nonferrous metallurgy industry, there are serious problems such as backward technology and equipment. Small industry, so the general public does not pay much attention to it

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  • A kind of boiling chlorination extraction method of niobium and tantalum concentrate

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0028] The mass fractions of the oxides of the niobium-tantalum concentrate of the present embodiment are respectively: Nb 2 o 5 17.08%, Ta 2 o 5 40.0%, TiO 2 7.45%, SiO 2 10.45%, the boiling chlorination extraction method of the niobium-tantalum concentrate of the present embodiment comprises the following steps:

[0029] Mix niobium and tantalum concentrate with coke and metal silicon, add it to the boiling chlorination furnace and pass chlorine gas to react, the mass ratio of niobium tantalum concentrate, coke, metal silicon and chlorine gas is 1:0.1:0.1:1.5, tantalum niobium The adding speed of concentrate is 1000g / min, the adding speed of coke is 260g / min, the adding speed of metal silicon is 240g / min, the adding speed of chlorine gas is 2800g / min, the reaction temperature is 700-900℃, the reaction product overflows the boiling chlorination furnace The overflow, the overflow is subjected to continuous five-stage cooling and separation, and the refractory slag in t...

Embodiment 2

[0037] The mass fractions of the oxides of the niobium-tantalum concentrate of the present embodiment are respectively: Nb 2 o 5 50.12%, Ta 2 o 5 11.56%, TiO 2 10.87%, SiO 2 8.21%, the boiling chlorination extraction method of the niobium-tantalum concentrate of the present embodiment comprises the following steps:

[0038] Mix niobium and tantalum concentrate with coal powder, petroleum coke and silicon carbide, add it to a fluidized chlorination furnace and feed chlorine gas for reaction, the mass ratio of niobium and tantalum concentrate, coal powder, petroleum coke, silicon carbide and chlorine gas is 1: 0.1:0.2:0.3:3, the addition rate of tantalum and niobium concentrate is 1000g / min, the addition rate of coal powder is 260g / min, the addition rate of petroleum coke is 60g / min, the addition rate of silicon carbide is 390g / min, the addition rate of chlorine gas The reaction temperature is 2800g / min, and the reaction temperature is 900-1180°C. The reaction generates ov...

Embodiment 3

[0046] The mass fractions of the oxides of the niobium-tantalum concentrate of the present embodiment are respectively: Nb 2 o 5 3.45%, Ta 2 o 5 0.58%, TiO 2 28.51%, REO16.12%, SiO 2 10.17%, the boiling chlorination extraction method of the niobium-tantalum concentrate of the present embodiment comprises the following steps:

[0047] Mix niobium and tantalum concentrate with petroleum coke and metal silicon, add chlorine gas into the boiling chlorination furnace for reaction, the mass ratio of niobium and tantalum concentrate, petroleum coke, metal silicon and chlorine gas is 1:0.4:0.4:5, The addition rate of tantalum and niobium concentrate is 1000g / min, the addition rate of petroleum coke is 400g / min, the addition rate of metal silicon is 400g / min, the addition rate of chlorine gas is 4800g / min, the reaction temperature is 900-1200°C, and the reaction produces overflowing boiling chlorine For the spill outside the chlorination furnace, the overflow is subjected to co...

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Abstract

The invention discloses a fluidizing chlorination extraction method of niobium tantalum concentrates. The method comprises the following steps: the niobium tantalum concentrates are mixed with reducing agents and stabilizing agents to add in a fluidizing chlorination furnace; chlorine is introduced for reaction to generate overflowing matters overflowing outside the fluidizing chlorination furnace; and the overflowing matters are continuously cooled and separated by five stages. The method can solve the current situation of high pollution, high energy consumption and high material consumptionin the niobium tantalum smelting process, can solve the awkward situation of incapability of realizing metallurgical extraction caused by difficult extraction of niobium tantalum resources due to lowgrade, and can realize high-additional-value recovery of multiple resources when niobium tantalum is extracted; the niobium tantalum concentrates with high or low grades can be extracted by adopting the method; the method is short in process flow, and meets the atomic economy; and obtained niobium chloride can be directly electrolyzed to prepare metal niobium, so that the prominent environmental benefit is achieved, the three-waste emission is reduced, and the green extraction of niobium tantalum can be realized.

Description

technical field [0001] The invention belongs to the technical field of metallurgy, and in particular relates to a boiling chlorination extraction method of niobium and tantalum concentrate. Background technique [0002] my country's consumption of niobium and tantalum accounts for 26% of the world's total, and it is the world's largest consumer of niobium and tantalum resources. However, almost all the concentrate products needed by my country's niobium and tantalum industry rely on imports, and the domestic production of niobium concentrate is less than the global output. 0.1%, and until the middle of this century, my country's demand for niobium may reach saturation. [0003] my country's niobium and tantalum smelting still has a large gap compared with the international advanced level in terms of production technology and product quality. The main factors hindering the development of niobium and tantalum smelting are: high product development costs, high consumption of raw...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C22B34/24C22B1/08C01G35/02C01G23/02C01B33/107
CPCC01B33/10721C01G23/022C01G35/02C22B1/08C22B34/24
Inventor 李梅张栋梁高凯
Owner 内蒙古扎鲁特旗鲁安矿业有限公司
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