A method for extracting metals from fly ash by molten salt electrolysis

A technology for metal extraction and molten salt electrolysis, applied in the field of metallurgy, can solve the problems of non-recyclable alkali reactant, equipment corrosion, low purification rate, etc., and achieve the effects of green and efficient comprehensive utilization, short process and simple process

Active Publication Date: 2016-06-22
NORTHEASTERN UNIV LIAONING
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

Among them, the alkali method mainly includes soda lime sintering method and limestone sintering method. The alkali reactant of the alkali method process cannot be recycled, the energy consumption is high, the production cost is high, and the amount of residue generated is large; the acid leaching method mainly adopts sulfuric acid or hydrochloric acid leaching Fly ash, Fe, K, Mg, Ca and other elements can also be leached during acid leaching, which increases the difficulty of alumina extraction, and the equipment is severely corroded, and the production cost is high; the quality of the alumina product produced by the acid-base method Higher, but there are many production processes and equipment, large energy consumption, and high production costs; the ammonium sulfate roasting method uses fly ash and ammonium sulfate to mix and roast, but there are still problems such as high energy consumption and low purification rate
In these research works, only the recycling of aluminum resources is reflected, and the comprehensive utilization of silica and alumina in fly ash has not yet been truly reflected.

Method used

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  • A method for extracting metals from fly ash by molten salt electrolysis
  • A method for extracting metals from fly ash by molten salt electrolysis

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0034] Na 3 AlF 6 and AlF 3 Mix evenly to make cryolite-based molten salt, the mixing ratio is NaF and AlF in cryolite-based molten salt 3 The molar ratio is 2;

[0035] Put the metal aluminum in the electrolytic cell; then place the cryolite-based molten salt in the electrolytic cell, and then add fly ash, the amount of fly ash added is 5% of the total weight of the cryolite-based molten salt and fly ash; The composition of fly ash contains Al by weight percentage 2 o 3 52.75%, SiO 238.05%, CaO3.88%, TiO 2 1.97%, Fe 2 o 3 1.86%, MgO0.51%, K 2 0.10%, the balance is impurities;

[0036] Heating cryolite-based molten salt and fly ash to 910°C, metal aluminum is melted into liquid aluminum, the liquid aluminum is used as the cathode, and the carbon anode is used as the anode; electrolysis is carried out by electrification, and the current density between the cathode and the anode is controlled to be 0.4A / cm 2 , the electrolysis time is 8h. After starting the electrol...

Embodiment 2

[0039] The method that molten salt electrolysis extracts metal from fly ash is the same as embodiment 1, and difference is:

[0040] (1) NaF and AlF in cryolite-based molten salt 3 The molar ratio is 2.2;

[0041] (2) The amount of fly ash added to the electrolytic cell is 3% of the total weight of cryolite-based molten salt and fly ash; the composition of fly ash contains Al 2 o 3 39.04%, SiO 2 55.24%, CaO0.25%, TiO 2 0.77%, Fe 2 o 3 3.76%, MgO0.10%, K 2 0.01%, the remainder is impurities;

[0042] (3) Heat cryolite-based molten salt and fly ash to 955°C, use an inert anode as the anode, and the inert anode is a metal-based aluminum electrolytic inert anode; electrify for electrolysis, and the current density between the cathode and the anode is 0.6A / cm 2 , the electrolysis time is 7h; the amount of fly ash added each time is 30% of the total weight of fly ash in the electrolytic cell when electrolysis is started;

[0043] (4) The composition of the aluminum-based a...

Embodiment 3

[0045] The method that molten salt electrolysis extracts metal from fly ash is the same as embodiment 1, and difference is:

[0046] (1) NaF and AlF in cryolite-based molten salt 3 The molar ratio is 2.4;

[0047] (2) The amount of fly ash added to the electrolytic cell is 10% of the total weight of cryolite-based molten salt and fly ash; the composition of fly ash contains Al by weight percentage 2 o 3 47.11%, SiO 2 34.30%, CaO3.90%, TiO 2 1.86%, Fe 2 o 3 6.20%, MgO3.70%, K 2 O2.10%, the balance is impurities;

[0048] (3) Heat cryolite-based molten salt and fly ash to 965°C; electrify for electrolysis, and the current density between the cathode and anode is 0.7A / cm 2 , the electrolysis time is 6h; the amount of fly ash added each time is 40% of the total weight of fly ash in the electrolytic cell when the electrolysis is started;

[0049] (4) The composition of the aluminum-based alloy contains Al67.9%, Si17.9%, Fe5.4%, Ti8.4% by weight percentage, and the rest is ...

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Abstract

The method for extracting metals from fly ash by molten salt electrolysis belongs to the field of metallurgy technology. The first method is: (1) Na 3 AlF 6 and AlF 3 Mix to make cryolite-based molten salt; (2) put fly ash into the electrolytic cell; (3) heat to 910~985°C, then electrify for electrolysis, and deposit aluminum-based alloy on the cathode. The second method is: (1) Na 3 AlF 6 and AlF 3 Mix evenly to make cryolite-based molten salt; (2) add fly ash and alumina to the electrolytic tank; (3) heat to 930~985°C, then turn on electricity for electrolysis, and deposit aluminum on the cathode after electrolysis base alloy. The invention treats fly ash by molten salt electrolysis, and prepares alloys by direct electrodeposition of oxides such as aluminum, silicon, titanium and iron, so as to realize the green and efficient comprehensive utilization of fly ash. The process is simple and can be used in existing industrial aluminum electrolytic cells Production, and the process is short, the advantages of continuous production.

Description

technical field [0001] The invention belongs to the technical field of metallurgy, in particular to a method for extracting metal from fly ash by molten salt electrolysis. Background technique [0002] Fly ash, commonly known as fly ash, refers to the dust and bottom slag collected from the flue gas of coal-fired (including gangue and coal slime) boilers, as well as the desulfurization and denitrification ash produced in the production process of coal-fired power plants. The output and discharge of fly ash are increasing year by year, and the accumulation of fly ash has obviously become a public hazard. The chemical composition of fly ash mainly includes silicon oxide, aluminum oxide, iron oxide, calcium oxide, magnesium oxide, potassium oxide, sodium oxide, sulfur trioxide, loss on ignition, etc. [0003] At present, the utilization of fly ash is mainly concentrated in building materials and road construction projects, etc., which basically belongs to the extensive utiliza...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C25C3/36
Inventor 石忠宁刘爱民陈功胡宪伟高炳亮王兆文于江玉徐君莉
Owner NORTHEASTERN UNIV LIAONING
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