Method and device for rapidly recovering rhenium, copper and lead from copper smelting waste acid
A copper smelting and rapid technology, applied in the field of copper, rapid recovery of rhenium and lead, can solve the problems of long reaction time, large environmental pollution, equipment scale, large investment, etc., and achieves less material handling, good environmental protection, and production small investment
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Patents(China)
- Current Assignee / Owner
- Publication Date
- 2017-12-01
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Abstract
Description
technical field
[0001] The invention relates to a method and a device for recovering rhenium, copper and lead from copper smelting waste acid, in particular to a method and a device for rapidly recovering rhenium, copper and lead from copper smelting waste acid. Background technique
[0002] Rhenium is a rare metal element with a high melting point. It has no independent minerals in nature and is usually associated with copper, molybdenum, uranium and other minerals. During the smelting process of copper, molybdenum, uranium, etc., rhenium is mainly enriched in volatile smoke, flue gas washing liquid or leaching liquid, and this intermediate material can be used as an important raw material for rhenium extraction.
[0003] Copper smelting waste acid is the washing liquid of the flue gas water medium in the copper smelting process. During the copper smelting process, most of the scattered metal rhenium in the copper concentrate volatilizes into the flue gas and then enters t...
Examples
Embodiment 1
[0033] In this example, the sulfuric acid concentration of copper smelting waste acid is 73.48g / L, the rhenium concentration is 17.94mg / L, the copper concentration is 33.48mg / L, and the arsenic concentration is 7.58g / L. The treatment process and effect are as follows:
[0034] (1) The waste acid from copper smelting is filtered by anti-gravity osmosis to remove the lead suspension in the waste acid and send it to the rhenium-copper precipitation tank to obtain the lead slag composition: lead 52.3%, copper 0.1%, bismuth 0.5%, arsenic 0.1%.
[0035] (2) Pump the waste acid after filtering and removing lead to the rhenium-copper precipitation tank, and use a metering pump at a rate of 1m 3 Add 20L of 20% sodium thiosulfate and 15g of sodium sulfide to the waste acid, heat it with steam to 70°C, and stir for 5 minutes; the obtained rhenium-rich slag contains 2.56% rhenium, 32.18% arsenic, and 8.34% copper; the rhenium precipitation rate is 99.8%, The arsenic precipitation rate is ...
Embodiment 2
[0039] In this example, the sulfuric acid concentration of copper smelting waste acid is 73.48g / L, the rhenium concentration is 17.94mg / L, the copper concentration is 33.48mg / L, and the arsenic concentration is 7.58g / L. The treatment process and effect are as follows:
[0040] (1) The waste acid from copper smelting is filtered by anti-gravity osmosis to remove the lead suspension in the waste acid and send it to the rhenium-copper precipitation tank to obtain the lead slag composition: lead 52.3%, copper 0.1%, bismuth 0.5%, arsenic 0.1%. (2) Pump the waste acid after filtering and removing lead to the rhenium-copper precipitation tank, and use a metering pump at a rate of 1m 3 Add 25L of 20% sodium thiosulfate and 20g of sodium sulfide to the waste acid, heat it with steam to 65°C, and stir for 15 minutes; the obtained rhenium-rich slag consists of 2.55% rhenium, 22.18% arsenic, and 8.28% copper; the rhenium precipitation rate is 99.2%, The arsenic precipitation rate is only ...
Embodiment 3
[0044] In this example, the sulfuric acid concentration of copper smelting waste acid is 73.48g / L, the rhenium concentration is 17.94mg / L, the copper concentration is 33.48mg / L, and the arsenic concentration is 7.58g / L. The treatment process and effect are as follows:
[0045] (1) The waste acid from copper smelting is filtered by anti-gravity osmosis to remove the lead suspension in the waste acid and send it to the rhenium-copper precipitation tank to obtain the lead slag composition: lead 52.3%, copper 0.1%, bismuth 0.5%, arsenic 0.1%. (2) Pump the waste acid after filtering and removing lead to the rhenium-copper precipitation tank, and use a metering pump at a rate of 1m 3 Add 10L of 20% sodium thiosulfate and 10g of sodium sulfide to the waste acid, heat it with steam to 50°C, and stir for 15 minutes; the obtained rhenium-rich slag consists of 4.06% rhenium, 30.36% arsenic, and 12.46% copper; the rhenium precipitation rate is 90.5%, The arsenic precipitation rate is only...