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US4051230A
Expired / Lapsed
US
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Liquid-liquid extraction process of metals
Assignee: Gore Enterprise Holdings Inc
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Filing: 1974-12-17
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Granted: 1977-09-27
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Expires: 1994-12-17
Abstract
Abstract In this process metal ions such as Ag + , Pb 2+ , Co 2+ , Cu.sup. 2+, Fe 3+ , etc., are extracted through a porous membrane impregnated with the first extractant containing chelating agents. The membrane contacts with an extraction feed on one side, and with the second extractant on the other side, and the objective metal ions are transferred from the feed to the second extractant. Throughout the extraction process, the pH values of the extraction feed, the impregnated extractant solution, and the second extractant are kept in decreasing order. An apparatus used for the above objective is also provided by this invention.
Inventors
- 👤 Terukatsu Miyauchi
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-29 13:30
CPC Classifications
C; C22; C22B; C22B3/00; C22B3/02; B; B01; B01D; B01D61/00; B01D61/38; B01D71/00; B01D71/06; B01D71/30; B01D71/32; B01D71/36; B01J; B01J45/00; Y; Y02; Y02P; Y02P10/00; Y02P10/20
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
144 words
A continuous liquid-liquid extraction process of extracting heavy metal cations from an aqueous solution extraction feed containing said cations, which process comprises bringing said aqueous solution into contact with one side of a chemically resistant membrane, said membrane having continuous fine pores impregnated and filled with a first organic extractant containing a chelating agent, and bringing a second aqueous extractant in contact with the other side of said membrane, while maintaining the pH value of the extraction feed greater than that of the second extractant, whereby said heavy metal cations dissolved in said feed solution are transferred from said extraction feed to said first extractant supported in said fine pores with complexing, through said membrane, due to the decreasing concentration of the metal chelate and into said second extractant from said membrane with regeneration of the chelating agent and release of said metal cation.
Claim 2
Dependent Claim
144 words
A continuous liquid-liquid extraction process of extracting heavy metal cations from an aqueous solution extraction feed containing said cations, which process comprises bringing said aqueous solution into contact with one side of a chemically resistant membrane, said membrane having continuous fine pores impregnated and filled with a first organic extractant containing a chelating agent, and bringing a second aqueous extractant in contact with the other side of said membrane, while maintaining the pH value of the extraction feed greater than that of the second extractant, whereby said heavy metal cations dissolved in said feed solution are transferred from said extraction feed to said first extractant supported in said fine pores with complexing, through said membrane, due to the decreasing concentration of the metal chelate and into said second extractant from said membrane with regeneration of the chelating agent and release of said metal cation.
Claim 3
Dependent Claim
25 words
The process of claim 1 in which the pH values of the extraction feed, the first extractant, and the second extractant are in decreasing order.
Claim 4
Dependent Claim
26 words
The process of claim 1 in which said chelating agent is one selected from the group consisting of β-diketones, quinolines, oximes, dioximes, dithizones and mixtures thereof.
Claim 5
Dependent Claim
29 words
The process of claim 1 in which said chelating agent is one selected from the group consisting of acetylacetone, trifluoroacetylacetone, dibenzoylmethane, thenoyltrifluoroacetone, 8-hydroxyquinoline, N-nitroso-phenylhydroxylamine, N-furoylphenylhydroxylamine, dithizone, and mixtures thereof.
Claim 6
Dependent Claim
35 words
The process of claim 1 in which said organic extractant is one selected from the group consisting of benzene, toluene, xylene, carbon tetrachloride, chloroform, methylethylketone, acetone, methylisobutylketone, kerosene, silicone oil, chlorinated hydrocarbons and mixtures thereof.
Claim 7
Dependent Claim
27 words
The process of claim 1 in which said membrane is one selected from the group consisting of porous polymeric film, paper filter, non-woven cloth and fibrous filter.
Claim 8
Dependent Claim
13 words
The process of claim 1 in which said membrane is expanded porous polytetrafluoroethylene.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1980-09-26 | 1981-03-28 | 1981-09-27 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-09-26 | 1985-03-28 | 1985-09-27 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-09-26 | 1989-03-28 | 1989-09-27 | $7700.00 | Window Closed / Lapsed |