Method for using cyaniding barren solution to float, reclaim and cyaniding copper plumbum and zinc in tailings
A technology of cyanidation tailings and cyanidation lean liquid is applied in the field of copper, lead and zinc to achieve the effects of protecting the ecological environment, large economic benefits and saving treatment costs.
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Applications(China)
- Current Assignee / Owner
- Publication Date
- 2008-07-09
- Estimated Expiration
- Not applicable · inactive patent
Smart Images
Figure 1
Abstract
Description
technical field
[0001] The invention belongs to the field of non-ferrous metal beneficiation, and relates to a method for recovering copper, lead and zinc in cyanide tailings by using cyanide barren liquor flotation. Background technique
[0002] Mineral resources are non-renewable and irreplaceable. More than 90% of my country's energy and about 80% of industrial raw materials come from mineral resources. With the massive development and utilization of mineral resources, the demand is increasing day by day, and the resources are becoming increasingly scarce. Tailings, as a secondary resource, have received more and more attention in recent years. Vigorously develop tailings, minimize waste discharge, realize the closed-loop material flow mode of "resource consumption-product-renewable resources", so that secondary resources can be fully developed and utilized, which is in line with the basic principles of circular economy, It also protects and improves the ecological envi...
Examples
Embodiment
[0037] (1) Slurry: Add cyanidation barren solution to cyanidation tailings, and stir to form a slurry.
[0038] The process conditions of pulping:
[0039] Pulp concentration: 38%; stirring time: 25min.
[0040] (2) Priority flotation of lead and zinc: Send the adjusted ore pulp to the flotation unit, add lime, ethion and butyl xanthate, and recover lead and zinc.
[0041] Process conditions for a rough selection:
[0042] Pulp pH value: 12 (adjusted with lime); ethyl disulfide: 125g / t; butyl xanthate: 125g / t;
[0043] Pinitol oil: 50g / t; flotation time: 6min.
[0044] Process conditions for one sweep:
[0045] Ethiazide: 60g / t; Butyl xanthate: 60g / t; Pinitol oil: 25g / t; Flotation time: 5min.
[0046] The process conditions of the second sweep:
[0047] Ethiazide: 30g / t; Butyl xanthate: 30g / t; Pinitol oil: 10g / t; Flotation time: 5min.
[0048] After two rounds of beneficiation, the lead-zinc mixed concentrate with a lead grade of 34.75% and a zinc grade of 32.28% was o...