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Technology for preparing rareearth cerium silicon and rareearth lanthanum silicon alloy by rareearth enriching material and products thereof

A rare earth silicon alloy and rare earth enrichment technology, which is applied to the process of producing high rare earth silicon alloy by ore thermal method and the field of its products, can solve the problem that the wet method rare earth enrichment cannot be utilized, cannot be adapted to the hydrometallurgical enrichment, high The problem of high cost of rare earth silicon alloys can achieve the effect of short cycle, reduced dosage and stable product quality

Inactive Publication Date: 2002-12-18
PINGLUO FENGHUA METALLURGICAL CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] 1. Rare earth coking agglomerates need to be treated outside the furnace, the process is cumbersome and the cycle is long;
[0006] 2. Wet process rare earth enrichment cannot be used, and most of the raw materials are concentrated ore such as magnetic separation, flotation ore, gravity separation, etc., so the cost of high rare earth silicon alloy is relatively high;
[0007] 3. The potential gradient is set corresponding to the condition of rare earth concentrate, and cannot adapt to the enrichment of hydrometallurgy. If this is copied, it will easily cause the crucible to move up in the high temperature area and the bottom of the furnace to rise

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0040] Example 1 2600 KVA submerged arc furnace to prepare SiRE30

[0041]Among them, REO 40%; CeO / REO 47.5% in self-baking coking agglomerates; 988kg self-baking coking agglomerates, 1470kg silica, 225kg gas coke, and 375kg blue carbon are required for one ton of alloy products; they are smelted in the furnace according to the process briefly described above.

[0042] Control parameters The electrode diameter is 540mm, the potential gradient is 0.95-1.05 V / cm, the primary side current is 150-220A, the secondary side voltage is 80-86V; the alloy is produced once every 1.5-2 hours, and the recovery rate is >95%. Finished product index (%) RE: >30; Ce / RE: 47±0.5; average power consumption 9300 KWh / t; see attached table 1 and table 4 for data.

Embodiment 2

[0043] Example two 2600 KVA submerged arc furnace to prepare SiRE35

[0044] Among them, REO is 40% in self-baked coking agglomerates; CeO / REO>55%; 1 ton of alloy products need self-baking coking agglomerates 1106kg, silica 1450kg, gas coke 223kg, blue carbon 370kg; smelting in the furnace according to the process briefly described above .

[0045] Control parameters The electrode diameter is 540mm, the potential gradient is 1.0-1.15 V / cm, the primary side current is 150-200A, the secondary side voltage is 82-88V; the alloy is produced once every 1.5-2 hours, and the recovery rate is >95%. Finished product index (%) RE: >35; Ce / RE: >55; average power consumption 9700 KWh / t; see attached table 2 and table 5 for data.

Embodiment 3

[0046] Example Three 2600 KVA submerged arc furnace to prepare SiRE40

[0047] Among them, REO is 40% in self-baked coking agglomerates; LeO / REO>40%; 1 ton of alloy products need self-baking coking agglomerates 1290kg, silica 1350kg, gas coke 220kg, blue carbon 360kg; smelting in the furnace according to the process briefly described above .

[0048] Control parameters The diameter of the electrode is 540mm, the potential gradient is 1.0-1.20 V / cm, the primary side current is 150-200A, the secondary side voltage is 82-88V; the alloy is produced once every 1.5-2 hours, and the recovery rate is >95%. Finished product index (%) RE: > 40; Le / RE: > 40; average power consumption 10400 KWh / t; see attached table 3 and table 6 for data.

[0049] Putting into production according to Example 1-3, a total of 3000 heats of rare earth alloys were produced, 8.3 months of continuous production, and 1450 T of alloys were produced; the product quality was stable.

[0050] Stoves

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PUM

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Abstract

The technological process for preparing rare-earth-cerium silicon and rare-earth-lanthanum-silicon alloy by using rare earth enriched material is characterized by that the carbon-added quantity is 2.8-3.5 times carbon quantity required for converting all the rare earth oxides being in wet rare earth enriched material into carbide, the carbonaceous adhesive can be uniformly mixed, extruded and formed, and self-baked and coked in the uniformly mixed, extruded and formed, and self-baked and coked in the ore-smelting furnace to obtain coked briquette, then the silica, gas coal coke and blue carbon are added. The ratio of rate earth metal in the briquette and silicon total quantity in the silica is 1:0.50-1.0; the coke is used as reducing agent, the above-mentioned three materials are uniformly added into ore-smelting furnace for smelting, its potential gradient is 0.90-1.20 V / cm.

Description

technical field [0001] The invention belongs to the field of rare-earth alloy preparation, and in particular relates to a process for preparing high-rare-earth silicon alloy by using a wet-process rare-earth enrichment as a raw material and an ore-thermal method and a product thereof. Background technique [0002] At present, there are four main production methods of rare earth alloys, namely: electrothermal silicon method, carbon reduction method, molten salt electrolysis method or blending method. [0003] The above methods have their own advantages and disadvantages, but there are generally problems such as high energy consumption, low recovery rate of rare earths, short furnace life or long production cycle, which restrict the development of the rare earth alloy industry. [0004] The patent application proposed by the inventor, that is, the application number is: 01107843.X, the application date is February 28, 2001, and the patent application titled "process and produc...

Claims

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Application Information

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IPC IPC(8): C22B59/00C22C1/02C22C28/00
Inventor 袁洪斌王全根岳锋李昌兮王小林袁航
Owner PINGLUO FENGHUA METALLURGICAL CO LTD
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