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Treatment method for carbon-containing solid waste in aluminum electrolysis industry

A treatment method, the technology of aluminum electrolysis, applied in the field of aluminum electrolysis, can solve problems such as poisoning, HCN is highly toxic, and is not suitable for use in electrolytic cells, and achieves the effects of low temperature and low energy consumption cost

Pending Publication Date: 2022-07-15
ZHENGZHOU UNIV +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] 1) HCN is highly toxic, a small amount can cause poisoning and death in a few seconds (the lethal dose of HCN is 0.05 grams), and HCN can also be poisoned by entering the blood from skin abrasions or inhaling HCN through the respiratory tract
[0005] 2) It is harmful to the growth of animals and plants, causing animal bones / plant tissues to become black and necrotic;
[0006] 3) Affect the balance of agricultural ecology and reduce the yield of crops;
[0008] 5) After long-term storage and weathering, it is easy to form dust and pollute the atmosphere
However, because the electrolyte obtained by flotation also contains about 5% carbon, it is not suitable for use in electrolytic cells; and the carbon powder also contains more than 10% electrolyte, and the scope of use is also affected

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0039] The waste cathode of aluminum electrolytic cell containing 40% carbon is used as the raw material, and crushed to ≤0.5mm; in the initial stage of roasting, 5% PE powder is added as a combustion accelerant, mixed with the raw material, and then added to the boiling furnace; The amount of material is to maintain the height of the boiling layer at 100cm; the boiling layer is equipped with a horizontally arranged tube heat exchanger, and the heat exchange medium is water; the initial intake air temperature is 500 ℃, after the combustion of the combustion accelerant, the intake air temperature is controlled according to the temperature of the boiling layer And the water flow in the heat exchanger, the temperature of the boiling layer is controlled at 500-700 ℃; the roasting time is 8 hours. The carbon content of the calcined product is less than or equal to 0.7%. The calcined product is a cryolite-based electrolyte, and other fluorides or oxides containing elements such as so...

Embodiment 2

[0041] Using carbon-containing 30% aluminum electrolytic carbon residue as raw material, crushed to ≤0.5mm, without adding combustion aid; the boiling gas is 50% air + 50% industrial oxygen, and the intake air volume and the feeding amount are controlled to maintain the boiling layer height of 150cm ; The boiling layer is provided with a horizontally arranged tube heat exchanger with fins, and the heat exchange medium is water; the initial inlet temperature is 700 ℃, after the reaction starts, the inlet temperature is controlled according to the temperature of the boiling layer, and the temperature of the boiling layer is controlled at 600~800℃; calcination time is 3 hours. The carbon content of the calcined product is less than or equal to 0.6%. The calcined product is a cryolite-based electrolyte, and other fluorides or oxides containing elements such as sodium, aluminum, calcium, magnesium, potassium, and lithium can be used as electrolytes for aluminum electrolysis. Raw ma...

Embodiment 3

[0043] Using aluminum electrolysis carbon residue flotation electrolyte powder as raw material, the raw material contains 5% carbon, and in the initial stage of roasting, 3-hydroxycholic acid is added as a combustion-supporting agent, and the addition amount is 10%; The amount of material is to maintain the height of the boiling layer at 30cm; the boiling layer is provided with a horizontally arranged tube-and-tube heat exchanger, and the heat exchange medium is nitrite molten salt; the initial inlet temperature is 700 ℃, and after the reaction starts, it is controlled according to the temperature of the boiling layer The inlet temperature and the boiling layer temperature are controlled at 600-800°C; the roasting time is 1 hour. The carbon content of the calcined product is less than or equal to 0.5%. The calcined product is a cryolite-based electrolyte, and other fluorides or oxides containing elements such as sodium, aluminum, calcium, magnesium, potassium, and lithium can b...

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Abstract

The invention provides a method for treating carbon-containing solid waste in the aluminum electrolysis industry, which comprises the following steps: the carbon-containing solid waste is crushed and then added into a fluidized bed furnace to be roasted, boiling gas in the fluidized bed furnace is at least one of preheated air and industrial oxygen, the height of a boiling layer is 10-300cm, the temperature of the boiling layer is maintained at 500-800 DEG C, the roasting time is 0.1-10 hours, and the carbon-containing solid waste is obtained. The roasted product is electrolyte mainly containing cryolite, and the carbon content is less than or equal to 1%. According to the method, after the waste cathodes of the aluminum electrolysis cell, the aluminum electrolysis carbon residues or the electrolytes obtained through flotation of the waste cathodes and the aluminum electrolysis carbon residues are subjected to boiling oxidation roasting, products are pure electrolytes, the carbon content is reduced to 1% or below, other impurities are not added, the requirements of aluminum electrolysis can be met, and all the electrolytes are subjected to resource utilization.

Description

technical field [0001] The invention relates to the technical field of aluminum electrolysis, in particular to a method for treating carbon-containing solid waste in the aluminum electrolysis industry. Background technique [0002] The service life of the aluminum electrolytic cell is approximately 2000-4000 days. After long-term use, the lining material of the electrolytic cell will be deformed, worn and broken due to physical and chemical effects, which makes the electrolytic cell unable to continue normal production and must be overhauled. The essence of the electrolytic cell overhaul is to replace the lining. The cell lining materials eliminated during the replacement process include: waste cathode carbon blocks, waste refractory materials and anti-seepage materials. These discarded electrolyzer lining materials are also known as overhaul slag. Studies have shown that at present, for every ton of primary aluminum produced, an average of 20-30kg of aluminum electrolysis ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C04B35/52C04B35/622C04B35/64C25C3/12
CPCC04B35/52C04B35/62204C04B35/64C25C3/125
Inventor 杨昇梁学民卢志锋张建勋孔亚鹏陈昱冉王立强
Owner ZHENGZHOU UNIV
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