A method of suspending, magnetizing and roasting high ferricyanide tailings to break cyanide and extract iron by magnetic separation

A technology of cyanide tailings and magnetization roasting, which is applied in the field of suspension magnetization roasting of ferricyanide tailings for cyanide breaking-magnetic separation and iron extraction, which can solve the problems of environmental pollution, waste of resources, large amount of waste water, etc., and achieve heat transfer High mass transfer efficiency and full contact effect

Active Publication Date: 2021-08-17
NORTHEASTERN UNIV LIAONING
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Problems solved by technology

[0002] Gold smelting enterprises discharge a large amount of cyanide tailings every year, and their long-term storage not only occupies land, but also pollutes the environment
Cyanide tailings contain valuable metals such as gold, silver, copper, iron, zinc, etc. Among them, the high-ferricyanide tailings TFe grade reaches 30-40%, which is a valuable secondary iron resource. If it cannot be obtained effectively Utilization will cause a waste of resources; but due to the highly toxic cyanide remaining in the cyanide tailings, it is easy to produce cyanide-containing wastewater or waste residues when extracting valuable metals, making it difficult to obtain large-scale utilization; therefore , to develop a new technology for the harmless and efficient utilization of ferricyanide tailings, which can not only solve the serious environmental pollution caused by its large amount of stockpiling, but also obtain iron ore resources
[0003] Patent CN201610618637.6 discloses a method for cleaning and converting roasted cyanidation tailings, and proposes to obtain TFe through the method of "first-stage acidification cyanide removal-first-stage dehydration-secondary acidification cyanide removal-secondary dehydration-magnetic separation-wastewater treatment" The iron concentrate with a grade of 55% has realized the clean conversion of roasting cyanidation tailings; but this method consumes a large amount of additives such as sulfuric acid, sodium sulfite, hydrogen peroxide and copper sulfate, as well as a large amount of clean water, and the acidification and oxidation time is as long as 11 More than one hour, there are problems such as high cost, low efficiency, low grade of iron concentrate, and large amount of waste water.
[0004] Patent CN201610129549.X discloses a method for recovering gold, iron, and lead in cyanide tailings, and proposes to use hydrochloric acid to leach iron, lead, and gold in cyanide tailings, and adopts a step-by-step separation method to gradually recover gold, iron, and lead , to realize the recovery of valuable metals; but this method does not point out how to remove the cyanide in the cyanide tailings, and needs to use a large amount of concentrated hydrochloric acid, which takes 1 to 2 hours in the leaching process, and the removal of cyanide is not complete. Concentrated hydrochloric acid is volatile and causes air pollution, and the separation process of gold, iron and lead in the leaching solution is complicated, etc.

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  • A method of suspending, magnetizing and roasting high ferricyanide tailings to break cyanide and extract iron by magnetic separation

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Experimental program
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Effect test

Embodiment 1

[0031] Ferricyanide tailings by mass percentage TFe 38.61%, SiO 2 27.49%, CN - Content 350mg / L;

[0032] Process such as figure 1 shown;

[0033] The ferricyanide tailings are crushed and ground to a particle size of -0.038mm, accounting for 65% of the total mass, to obtain tailings powder;

[0034] The tailings powder is passed into the pre-oxidation suspension roaster with a burner at the bottom, and the top of the pre-oxidation suspension roaster is connected with the induced draft fan through a pipe; under the condition of the induced draft fan, the gas and air are ignited through the burner High-temperature flue gas is generated, and the high-temperature flue gas enters the pre-oxidation suspension roaster, and the tailings powder is in a suspended state under the action of airflow and negative pressure, and is heated to 650°C for cyanide-breaking roasting, so that the CN in the tailings powder - converted to N 2 and CO 2 , the remaining solid material after cyanide...

Embodiment 2

[0041]Ferricyanide tailings by mass percentage TFe 31.97%, SiO 2 30.62%, CN - Content 400mg / L;

[0042] Method is with embodiment 1, and difference is:

[0043] (1) The part of ferricyanide tailings that is crushed and ground to a particle size of -0.038mm accounts for 70% of the total mass;

[0044] (2) The cyanide breaking roasting temperature is 700°C, and the residence time of the tailings powder in the pre-oxidation roasting furnace is 10 minutes;

[0045] (3) The reduction roasting temperature is 550°C, and the amount of gas introduced is based on the amount of H in the gas. 2 / CO and Fe in oxide slag powder 2 o 3 1.2 times of the amount required for the complete reaction theory is introduced; the volume concentration of the gas in the reduction roaster is 20%; the residence time of the oxidized slag powder in the reduction roaster is 40 minutes;

[0046] (4) The first section of grinding to particle size -0.038mm accounts for 85% of the total mass, and the magnet...

Embodiment 3

[0050] Ferricyanide tailings by mass percentage TFe 33.42%, SiO 2 25.33%, CN - Content 386mg / L;

[0051] Method is with embodiment 1, and difference is:

[0052] (1) The part of ferricyanide tailings that is crushed and ground to a particle size of -0.038mm accounts for 75% of the total mass;

[0053] (2) The cyanide breaking roasting temperature is 750°C, and the residence time of the tailings powder in the pre-oxidation roasting furnace is 5 minutes;

[0054] (3) The reduction roasting temperature is 600°C, and the amount of gas introduced is based on the amount of H in the gas. 2 / CO and Fe in oxide slag powder 2 o 3 1.3 times of the amount required for the complete reaction theory is introduced; the volume concentration of gas in the reduction roaster is 15%; the residence time of the oxidized slag powder in the reduction roaster is 20 minutes;

[0055] (4) The first stage of grinding to particle size -0.038mm accounts for 90% of the total mass, and the magnetic fiel...

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Abstract

A method for suspending, magnetizing and roasting ferricyanide tailings to break cyanide-magnetic separation and extract iron, which is carried out in the following steps: (1) breaking and grinding the ferricyanide tailings; (2) passing it into a pre-oxidation suspension roaster , the high-temperature flue gas enters the pre-oxidation suspension roaster, and the tailings powder is heated to 650-750°C in a suspension state to break the cyanide and roast, and the remaining solid material is the oxide slag powder; (3) The oxide slag powder is passed into the reduction roaster, and the reduction roasting The bottom of the furnace is fed with coal gas and nitrogen, and the oxidized slag powder is in a suspended state and reduced and roasted at 500-600°C, leaving the remaining reduced slag powder; (4) After the reduced slag powder is cooled, a stage of grinding and a stage of weak magnetic separation are carried out; (5) a stage of refining The ore undergoes secondary grinding and secondary weak magnetic separation, and the concentrate of the second stage is iron concentrate. The invention adopts the iron-extracting and cyanide-breaking process by suspending magnetization roasting, which can eliminate the threat of toxic waste water produced by wet cyanide breaking to environmental safety.

Description

technical field [0001] The invention belongs to the technical field of mineral processing, and in particular relates to a method for suspending, magnetizing and roasting ferricyanide tailings to break cyanide and extract iron by magnetic separation. Background technique [0002] Gold smelting enterprises discharge a large amount of cyanide tailings every year, and their long-term stockpiling not only occupies land, but also pollutes the environment. Cyanide tailings contain valuable metals such as gold, silver, copper, iron, zinc, etc. Among them, the high-ferricyanide tailings TFe grade reaches 30-40%, which is a valuable secondary iron resource. If it cannot be obtained effectively Utilization will cause a waste of resources; but due to the highly toxic cyanide remaining in the cyanide tailings, it is easy to produce cyanide-containing wastewater or waste residues when extracting valuable metals, making it difficult to obtain large-scale utilization; therefore , to develo...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C22B1/02C21B13/00B03B9/06
CPCB03B9/06C21B13/0046C21B13/0073C22B1/02Y02W30/52
Inventor 高鹏韩跃新肖汉新袁帅李艳军孙永升
Owner NORTHEASTERN UNIV LIAONING
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