Fluid extraction of metals of metalloids

A metalloid and metal technology, applied in the field of extraction of metals and metalloids, can solve the problems of unsuitable chemical extraction, difficult extraction, unstable chelating agent, etc.

Inactive Publication Date: 2000-08-30
IDAHO RESARCH FOUNDATION INC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

The technical effect of this patented process described by this inventor relates to an efficient way to recover valuable materials such as copper or nickels during processing industries like mineral production processes that produce large amounts of acute pollution containing harmful chemicals. By utilizing these methods, it becomes possible to recycle them back into their original form without causing environmental concerns due to uncontrolled release thereof.

Problems solved by technology

Technics: Current methods involve treating various types of wastes such as industrial sludge (pollute water), domestic garbage, etc., but they all require expensive equipment and complicated processes involving multiple steps like acid digestion followed by separation/removal procedures. Additionally, these conventional ways cannot effectively remove certain compounds present at low levels due to their high volatility and instability during processing conditions.

Method used

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Examples

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specific example

[0011] Specific examples of the method of the present invention for extracting various heavy metals, noble metals and metalloids from media, especially acidic media, are provided below. The present invention also relates to specific examples of methods for extracting radioactive metals such as uranium from acidic solutions. I. Extraction fluid

[0012] Suitable fluids and / or supercritical fluids for use in the present invention include carbon dioxide, nitrogen, nitrous oxide, methane, ethylene, propane and propylene. It has been found that since carbon dioxide has moderate chemical constants (Tc=31°C, Pc=73atm), and it is chemically inert (i.e., carbon dioxide will not explode even under supercritical conditions, the extraction process is absolutely safe), so regardless of Fluids are particularly useful for both subcritical and supercritical fluid extraction. Carbon dioxide is also the preferred solvent for use due to its abundance and relative cheapness.

[0013] The phase

Embodiment 1

[0052] All experiments in this paper use laboratory-grade supercritical fluid extraction equipment, as described above and shown in Figure 1. This example concerns the extraction of Hg, Cu, Cd, Pb, Zn, As, Sb, Se and U ions from various acidic media. The acidic media tested included 0.1M hydrochloric acid solution, 1.0M hydrochloric acid solution, 0.1M nitric acid solution, 1.0M nitric acid solution, 0.05 sulfuric acid solution and 0.5 sulfuric acid solution. All metal and metalloid ions were extracted from acidic solutions each containing about 10 μg / ml metal or metalloid ions. Uranyl ion U(VI) is prepared from analytical grade uranyl nitrate. All other metal solutions were prepared from AAS standard solutions.

[0053] The extractant fluid used in this example comprised supercritical carbon dioxide. The chelating agent was di-2,4,4-trimethylpentyldithiophosphinic acid supplied by Cytec Industries of New Jersey, which was used without further purification. Supercritical ca

Embodiment II

[0062] This embodiment involves the extraction of Hg, Cu, Cd, Pb, Zn, As, Sb, Se and U ions from acidic medium, using supercritical carbon dioxide and monothiophosphinic acid. The acidic media tested included 0.1M hydrochloric acid solution, 1.0M hydrochloric acid solution, 0.1M nitric acid solution, 1.0M nitric acid solution, 0.05M sulfuric acid solution and 0.5M sulfuric acid solution. All metal and metalloid ions were extracted from acidic solutions each containing about 10 μg / ml metal or metalloid ions. Uranyl ion U(VI) is prepared from analytical grade uranyl nitrate. All other metal solutions were prepared from AAS standard solutions. The extraction method is the same as described in the aforementioned "fluid extraction method".

[0063] The extractant fluid used in this example comprised supercritical carbon dioxide mixed with di-2,4,4-trimethylpentylmonothiophosphinic acid. Di-2,4,4-trimethylpentylmonothiophosphinic acid was supplied by Cytec Industries of New Jersey

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Abstract

Methods for extracting metalloid and metal species from a solid or liquid material by exposing the material to a fluid solvent, particularly supercritical CO2, and a chelating agent are described. The chelating agent forms a chelate with the species, the chelate being soluble in the fluid to allow removal of the species from the material. In preferred embodiments the extraction solvent is supercritical CO2 and the chelating agent comprises an organophosphorous chelating agent, particularly sulfur-containing organophosphorous chelating agents, including mixtures of chelating agents. Examples of chelating agents include monothiophosphinic acid, di-thiophosphinic acid, phosphine sulfite, phosphorothioic acid, and mixtures thereof. The method provides an environmentally benign process for removing metal and metalloids from industrial waste solutions, particularly acidic solutions. Both the chelate and the supercritical fluid can be regenerated and the contaminant species recovered to provide an economic, efficient process.

Description

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Claims

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Application Information

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Owner IDAHO RESARCH FOUNDATION INC
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