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Method for recycling gold from cyaniding tailings through grading and shunting flotation

A technology for cyanidation tailings and gold recovery, which is applied in chemical instruments and methods, flotation, solid separation, etc., can solve the problems of reduced gold mineral floatability, difficulty in recovery, waste of resources, etc. The effect of improving the comprehensive utilization rate of resources, improving the comprehensive recovery rate and improving the recovery efficiency

Inactive Publication Date: 2020-05-15
COLLEGE OF APPLIED SCI JIANGXI UNIV OF SCI & TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Traditionally, the treatment of cyanide tailings is mainly landfill, which wastes resources and pollutes the environment. At present, some mines use the flotation method to recover gold and silver. There are two main methods: one is through the cyanide tailings Carry out full-grain flotation to obtain flotation gold concentrate, and then go through two steps of cyanidation leaching and deposition extraction to obtain gold; the other is to enrich gold and silver to non-ferrous metals (such as copper, lead, etc.) through flotation In the concentrate, after pyro-smelting, gold, silver, copper and lead metals are obtained
[0003] Due to the high proportion of fine particles in cyanide tailings (-0.074mm content generally accounts for more than 80%), the silicate mineral mud is serious, and the pH value of the zero-electric point of various minerals is different. In the same slurry environment, the surface is charged The particles interfere with each other and affect each other, the non-selective adsorption of flotation reagents increases, and the viscosity of the pulp increases during the flotation process; the surface of valuable minerals adsorbs other ions to form an electric double layer, and a thicker hydration film will also appear on the surface. The flotation agent has a weak ability to collect it; the properties of different particle sizes vary greatly, and the coarse and fine particles are mixed with each other during the flotation process, and the useful minerals and gangue minerals interact with each other; The properties have changed significantly, and even many gold-encapsulated minerals are inhibited by cyanide and are difficult to float. The above reasons will greatly reduce the floatability of gold minerals in cyanide tailings, and recovery becomes very difficult.
[0004] The existing patent "Method for recovering gold from cyanide tailings" (Patent No. 2017112413846) includes the steps of raw ore pretreatment, roughing operation, sweeping operation, and beneficiation operation. The patent uses combined collectors Y-89 and YP -35, adding combined inhibitor sodium silicate and Linx385 at the same time, the flotation effect on gold wrapped in sulfide ore is good, but it does not grasp the characteristic that different particle sizes have different properties, and it is difficult to use the whole particle size flotation method. Guarantee the recovery effect of valuable minerals in cyanidation tailings with large interaction between coarse and fine particle size flotation or serious sludge

Method used

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  • Method for recycling gold from cyaniding tailings through grading and shunting flotation
  • Method for recycling gold from cyaniding tailings through grading and shunting flotation
  • Method for recycling gold from cyaniding tailings through grading and shunting flotation

Examples

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Embodiment 1

[0031] ① Step: screen classification, the raw ore 1 is mixed with water according to the pulp mass concentration of 36.58%, and the sieve classification is carried out through a Taylor standard sieve with an aperture of 0.038mm to obtain coarse grains (+0.038mm grain size) and fine grains (-0.038mm mm particle size) two products;

[0032] ②Steps: coarse-grained roughing, adding water to the coarse-grained product according to the pulp mass concentration of 33.26% to make pulp, and then adding dispersant (water glass: 500g / t), activator (copper sulfate: 100g / t), Combining collector (MA-1: 30g / t, butyl ammonium black drug: 15g / t), foaming agent (pine alcohol oil: 10g / t), conduct coarse separation 3 to obtain coarse separation concentrate 8 and coarse-grained roughing tailings;

[0033] ③Step: the first coarse-grain sweeping, add combined collector (MA-1: 15g / t, butyl ammonium black medicine: 10g / t), foaming agent (terpineol oil : 5g / t), carry out coarse scavenging 4 for the fi...

Embodiment 2

[0046] Embodiment 2 is the same as Embodiment 1 except for the following differences.

[0047] ②, ③, ④, ⑤, ⑦, ⑧, ⑨, The medicament consumption used in the step is different from Example 1, and is respectively 2. step: coarse grain selection 3 adds dispersant (water glass: 700g / t), activator (copper sulfate: 120g / t), combined collector ( MA-1: 40g / t, butyl ammonium black drug: 20g / t); ③Step: first coarse-grained sweeping 4 Add combined collector (MA-1: 20g / t, butyl ammonium black drug: 15g / t t); ④ Step: Add combined collector (MA-1: 10g / t, butyl ammonium black medicine: 8g / t) for the second coarse-grained screening 5; ⑤ Step: Add 6 for the first coarse-grained selection Dispersant (water glass: 300g / t); ⑦Step: rough selection of fine particles 15 Add dispersant (water glass: 1200g / t), activator (copper sulfate: 120g / t), combined collector (MOS-2 : 40g / t, MA-1: 16g / t), foaming agent (terpineol oil: 30g / t); ⑧ step: the first fine particle sweeping 16 add dispersant (water glas...

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Abstract

The invention relates to a method for recycling gold from cyaniding tailings through grading and shunting flotation, which comprises the following steps: grading the cyaniding tailings by using a screen to divide the cyaniding tailings into a coarse product and a fine product, and preparing for grading and shunting flotation; selecting targeted process parameters and reagent systems for flotationof the coarse and fine fraction products; and selecting proper coarse fraction flotation middlings as carriers for fine fraction flotation, so as to improve the recovery efficiency of fine fraction tothe maximum extent. Finally, the comprehensive recovery rate of gold is integrally improved through coarse and fine particle grading and shunting flotation, series flow-carrier flotation, combined reagent enhanced flotation and the like. The method is advanced in process, good in separation effect and capable of effectively recycling the gold with the micro-fine particle size fraction in the cyaniding tailings. The Au grade of the final gold concentrate is larger than or equal to 16.03g / t, and the Au recycling rate is larger than or equal to 76.81%. The comprehensive resource utilization rateof the cyaniding tailings is increased, and economic benefits are brought to enterprises.

Description

technical field [0001] The invention belongs to the technical field of mineral processing, and in particular relates to a method for recovering gold by fractional flow flotation of cyanide tailings, and is particularly suitable for resource recovery of gold in cyanide tailings with uneven particle size distribution. Background technique [0002] Cyanide gold extraction method is an important technology for gold extraction in gold mines. During the process of cyanide gold extraction, a large amount of cyanide tailings will be produced, and the gold grade in the tailings can reach 1-8g / t. Traditionally, the treatment of cyanide tailings is mainly landfill, which wastes resources and pollutes the environment. At present, some mines use the flotation method to recover gold and silver. There are two main methods: one is through the cyanide tailings Carry out full-grain flotation to obtain flotation gold concentrate, and then go through two steps of cyanidation leaching and deposi...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B03D1/018B03D101/00B03D101/02B03D101/04B03D103/02
CPCB03D1/018B03D2201/00B03D2201/005B03D2201/02B03D2201/04B03D2203/025B03D1/014B03D1/012B03D1/008B03D1/011B03D1/02B03D1/025B03D1/082B03D2201/007C01G7/00
Inventor 胡海祥
Owner COLLEGE OF APPLIED SCI JIANGXI UNIV OF SCI & TECH