Multiple roasting gold extracting method for unmanageable arsenic-containing gold concentrate

A technology of multiple roasting and gold concentrate, which is applied in the improvement of process efficiency, photography technology, instruments, etc., can solve the problem of low recovery of gold and silver from arsenic gold concentrate, and achieve the improvement of resource utilization. The method is simple and easy to implement. Effect

Inactive Publication Date: 2007-11-28
SHANDONG GUODA GOLD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0003] The purpose of the present invention is to provide a simple, economical and practical method for extracting gold by multiple roasting of refractory arsenic-containing gold concentrate, which can recover gold and silver and other products to the maximum extent from refractory arsenic-containing gold concentrate, and solve difficult problems. Solve the problems of low recovery of gold and silver from arsenic-containing gold concentrates, make full use of gold resources, and improve resource utilization

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Example Embodiment

[0015] Example 1

[0016] 1. Ingredients: The tailings after secondary roasting and cyanidation for gold extraction, in which the gold grade is 7.50g / t, and the high-grade sulfide ore containing gold, silver and copper in a ratio of 1:2, are mixed in a slurry tank. , and add water to adjust the slurry concentration to 70%, at room temperature and pressure, and continuously stir to obtain a slurry suitable for roasting conditions with a sulfur content of 25.10%;

[0017] 2. Roasting: The prepared pulp is sent to the boiling furnace for sulfate roasting, and the temperature is controlled at 630°C; the generated sulfur dioxide flue gas enters the acid production system to produce sulfuric acid; the generated slag enters the acid leaching process;

[0018] 3. Acid leaching: in the acid leaching tank, acid leaching the roasting slag with sulfuric acid, control pH=1, the temperature is 85°C, and the liquid-solid ratio is 1.5:1;

[0019] 4. The produced copper-containing acid leachin

Example Embodiment

[0021] Example 2

[0022] 1. Ingredients: Mix the tailings after secondary roasting and cyanidation for gold extraction, in which the gold grade is 8.10g / t, and the ratio of 1:2 with the high-grade sulfide ore containing gold, silver, and copper is carried out in the mixing tank. , and add water to adjust the slurry concentration to 68%, at room temperature and pressure, and continuously stir to obtain a slurry suitable for roasting conditions with a sulfur content of 25.90%;

[0023] 2. Roasting: The prepared pulp is sent to the boiling furnace for sulphation roasting, and the temperature is controlled at 580°C; the generated sulfur dioxide flue gas enters the acid production system to produce sulfuric acid; the generated slag enters the acid leaching process;

[0024] 3. Acid leaching: in the acid leaching tank, acid leaching the roasting slag with sulfuric acid, control pH=1.5, the temperature is 90°C, and the liquid-solid ratio is 1.4:1;

[0025] 4. The produced copper-con

Example Embodiment

[0027] Example 3

[0028] 1. Ingredients: The tailings after secondary roasting and cyanidation for gold extraction, in which the gold grade is 9.28g / t, and the high-grade sulfide ore containing gold, silver and copper in a ratio of 1:2, are mixed in a slurry tank. , and add water to adjust the slurry concentration to 69%, at room temperature and pressure, and continuously stir to obtain a slurry suitable for roasting conditions with a sulfur content of 22.90%;

[0029] 2. Roasting: The prepared pulp is sent to the boiling furnace for sulphation roasting, and the temperature is controlled at 680°C; the generated sulfur dioxide flue gas enters the acid production system to produce sulfuric acid; the generated slag enters the acid leaching process;

[0030] 3. Acid leaching: in the acid leaching tank, acid leaching the roasting slag with sulfuric acid, control pH=2.0, the temperature is 70°C, and the liquid-solid ratio is 1.6:1;

[0031] 4. The produced copper-containing acid le

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Abstract

A kind of method to extract gold by time and time burning with aurin mine containing arsenic difficult to deal with, and it belongs to the mineral pretreatment technology field of gold meltallurgy industry. The following is it' s character: 1.blending: In the paste ark, the high-grade sulfide ore will be added into the ore tailing, which has been extracted gold by secondary burning cyanation, the content of sulfur will increased to more than 22%, the pulp density will be adjusted to 68%-70% by adding water, the temperature will be controlled at 580-680deg.C, the sulfur dioxide smoke gas will enter the acid-making system and produce vitriol, and the burning residue will be delivered into the acid dipping procedure. 3.acid dipping: In the acid dipping ark, the burning residue will be acid dipped by vitriol, and the pH of it will be controlled at 1-2, and the temperature of it is 70-90deg.C, and the liquid to solid is (1.4-1.6): 1. 4.The acid-immersing liquid containing copper will be delivered to electro depositing procedure to reclaim the cathode copper. And the acid-immersing residue will be delivered to cyanating gold extracting procedure to reclaim bullion. The problem that the reclaim of bullion from aurin mine containing arsenic difficult to deal with is low is resolved by this patent, and it fully take advantage of the bullion mineral resource, it does not need new equipments, it is easy to be carried on, and is economic and practical.

Description

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Claims

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Application Information

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Owner SHANDONG GUODA GOLD
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