US3382034A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for separating inorganic cations from solution with hydrous oxide cation exchangers
Assignee: Individual
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Filing: 1965-01-28
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Granted: 1968-05-07
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Expires: 1985-01-28
Abstract
No abstract record available.
Inventors
- 👤 Kurt A Kraus
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 20:53
CPC Classifications
B; B01; B01J; B01J39/00; B01J39/02
Claims Analysis
Total Claims: 4
Claim 1
Independent Claim
204 words
A PROCESS FOR SEPARATING INORGANIC CATIONS FROM AN AQUEOUS SOLUTION CONTAINING SUCH CATIONS COMPRISING CONTACTING SAID SOLUTION WITH A NON-SILICEOUS HYDROUS OXIDE CATION EXCHANGER; SAID CATION EXCHANGER CONSISTING ESSENTIALLY OF THE HYDROUS OXIDE OF AT LEAST ONE ELEMENT SELECTED FROM THE GROUP CONSISTING OF TI(IV), ZR(IV), TH(IV), NB(V), TA(V), MO(VI), W(VI) AND SN(IV); THE PH OF SAID SOLUTION BEING SUFFICIENTLY HIGH TO PERMIT SAID CATION EXHCNAGER TO EXHIBIT SUCH CATION EXCHANGE CHARACTERISTICS IN THE PRESENCE OF SAID SOLUTION; SAID CATION EXCHANGER BEING SUBSTANTIALLY INSOLUBLE IN SAID SOLUTION; SAID CATION EXCHANGER, PRIOR TO ITS BEING PLACED IN CONTACT WITH SAID SOLUTION, BEING DRIED INSUFFICIENTLY TO DESTROY ITS HYDROUS CHARACTER INSUFFICIENTLY TO DESTROY ITS CATION EXCHANGE CHARACTERISTICS; SAID CATION EXCHANGER BEING PLACED IN CONTACT WITH A SUFFICIENT QUANTITY OF SAID SOLUTION FOR A SUFFICIENT PERIOD OF TIME TO REMOVE THE DESIRED QUANTITY OF SAID INORGANIC CATIONS FROM SAID SOLUTION, WHEREBY SAID CATION EXCHANGER WILL BECOME ENRICHED WITH SAID INORGANIC CATIONS; SEPARATING THE ENRICHED CATION EXCHANGER FROM SAID AQUEOUS SOLUTION; CONTACTING SAID ENRICHED CATION EXCHANGER WITH AN AQUEOUS SOLUTION CONTAINING A MATERIAL CAPABLE OF SUPPLYING IONS TO DISPLACE SAID INORGANIC CATIONS ON SAID CATION EXCHANGER; AND SEPARATING THE DENUDED CATION EXCHANGER AND SAID LAST MENTIONED AQUEOUS SOLUTION.
Claim 2
Dependent Claim
204 words
A PROCESS FOR SEPARATING INORGANIC CATIONS FROM AN AQUEOUS SOLUTION CONTAINING SUCH CATIONS COMPRISING CONTACTING SAID SOLUTION WITH A NON-SILICEOUS HYDROUS OXIDE CATION EXCHANGER; SAID CATION EXCHANGER CONSISTING ESSENTIALLY OF THE HYDROUS OXIDE OF AT LEAST ONE ELEMENT SELECTED FROM THE GROUP CONSISTING OF TI(IV), ZR(IV), TH(IV), NB(V), TA(V), MO(VI), W(VI) AND SN(IV); THE PH OF SAID SOLUTION BEING SUFFICIENTLY HIGH TO PERMIT SAID CATION EXHCNAGER TO EXHIBIT SUCH CATION EXCHANGE CHARACTERISTICS IN THE PRESENCE OF SAID SOLUTION; SAID CATION EXCHANGER BEING SUBSTANTIALLY INSOLUBLE IN SAID SOLUTION; SAID CATION EXCHANGER, PRIOR TO ITS BEING PLACED IN CONTACT WITH SAID SOLUTION, BEING DRIED INSUFFICIENTLY TO DESTROY ITS HYDROUS CHARACTER INSUFFICIENTLY TO DESTROY ITS CATION EXCHANGE CHARACTERISTICS; SAID CATION EXCHANGER BEING PLACED IN CONTACT WITH A SUFFICIENT QUANTITY OF SAID SOLUTION FOR A SUFFICIENT PERIOD OF TIME TO REMOVE THE DESIRED QUANTITY OF SAID INORGANIC CATIONS FROM SAID SOLUTION, WHEREBY SAID CATION EXCHANGER WILL BECOME ENRICHED WITH SAID INORGANIC CATIONS; SEPARATING THE ENRICHED CATION EXCHANGER FROM SAID AQUEOUS SOLUTION; CONTACTING SAID ENRICHED CATION EXCHANGER WITH AN AQUEOUS SOLUTION CONTAINING A MATERIAL CAPABLE OF SUPPLYING IONS TO DISPLACE SAID INORGANIC CATIONS ON SAID CATION EXCHANGER; AND SEPARATING THE DENUDED CATION EXCHANGER AND SAID LAST MENTIONED AQUEOUS SOLUTION.
Claim 3
Dependent Claim
194 words
A PROCESS FOR SEPARATING INORGANIC CATIONS FROM AN AQUEOUS SOLUTION CONTAINING SUCH CATIONS OTHER THAN THE PROCESSING OF PU(IV)-FISSION PRODUCT SOLUTIONS COMPRISING CONTACTING SAID SOLUTION WITH A NON-SILICEOUIS MIXED HYDROUS OXIDE CATION EXCHANGER CONTAINING AN ACIDIC HYDROUS OXIDE OF P(V) IN COMBINATION WITH A BASIC HYDROUS OXIDE OF ZR(IV); A SUFFICIENT EXCESS OF THE OXIDE OF P(V) BEING PRESENT TO IMPART EFFECTIVE CATION EXCHANGE PROPERTIES TO SAID CATION EXCHANGER IN SAID SOLUTION; SAID CATION EXCHANGER BEING SUBSTANTIALLY INSOLUBLE IN SAID SOLUTION; SAID CATION EXCHANGER, PRIOR TO ITS BEING PLACED IN CONTACT WITH SAID SOLUTION, HAVING BEEN DRIED AT A TEMPERATURE NOT IN EXCESS OF ABOUT 300*C.; SAID CATION EXCHANGER BEING PLACED IN CONTACT WITH A SUFFICIENT QUANTITY OF SAID SOLUTION FOR A SUFFIICIENT PERIOD OF TIME TO REMOVE THE DESIRED QUANTITY OF SAID INORGANIC CATIONS FROM SAID SOLUTION, WHEREBY SAID CATION EXCHANGER WILL BECOME ENRICHED WITH SAID INORGANIC CATIONS; SEPARATING THE ENRICHED CATION EXCHANGER FROM SAID AQUEOUS SOLUTION; CONTACTING SAID ENRICHED CATION EXCHANGER WITH AN AQUEOUS SOLUTION CONTAINING A MATERIAL CAPABLE OF SUPPLYING IONS TO DISPLACE SAID INORGANIC CATIONS ON SAID CATION EXCHANGER; AND SEPARATING THE DENUDED CATION EXCHANGER AND SAID LAST-MENTIONED AQUEOUS SOLUTION.
Claim 4
Dependent Claim
194 words
A PROCESS FOR SEPARATING INORGANIC CATIONS FROM AN AQUEOUS SOLUTION CONTAINING SUCH CATIONS OTHER THAN THE PROCESSING OF PU(IV)-FISSION PRODUCT SOLUTIONS COMPRISING CONTACTING SAID SOLUTION WITH A NON-SILICEOUIS MIXED HYDROUS OXIDE CATION EXCHANGER CONTAINING AN ACIDIC HYDROUS OXIDE OF P(V) IN COMBINATION WITH A BASIC HYDROUS OXIDE OF ZR(IV); A SUFFICIENT EXCESS OF THE OXIDE OF P(V) BEING PRESENT TO IMPART EFFECTIVE CATION EXCHANGE PROPERTIES TO SAID CATION EXCHANGER IN SAID SOLUTION; SAID CATION EXCHANGER BEING SUBSTANTIALLY INSOLUBLE IN SAID SOLUTION; SAID CATION EXCHANGER, PRIOR TO ITS BEING PLACED IN CONTACT WITH SAID SOLUTION, HAVING BEEN DRIED AT A TEMPERATURE NOT IN EXCESS OF ABOUT 300*C.; SAID CATION EXCHANGER BEING PLACED IN CONTACT WITH A SUFFICIENT QUANTITY OF SAID SOLUTION FOR A SUFFIICIENT PERIOD OF TIME TO REMOVE THE DESIRED QUANTITY OF SAID INORGANIC CATIONS FROM SAID SOLUTION, WHEREBY SAID CATION EXCHANGER WILL BECOME ENRICHED WITH SAID INORGANIC CATIONS; SEPARATING THE ENRICHED CATION EXCHANGER FROM SAID AQUEOUS SOLUTION; CONTACTING SAID ENRICHED CATION EXCHANGER WITH AN AQUEOUS SOLUTION CONTAINING A MATERIAL CAPABLE OF SUPPLYING IONS TO DISPLACE SAID INORGANIC CATIONS ON SAID CATION EXCHANGER; AND SEPARATING THE DENUDED CATION EXCHANGER AND SAID LAST-MENTIONED AQUEOUS SOLUTION.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1971-05-07 | 1971-11-06 | 1972-05-07 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1975-05-07 | 1975-11-06 | 1976-05-07 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1979-05-07 | 1979-11-06 | 1980-05-07 | $7700.00 | Window Closed / Lapsed |