← Back to Patent Explorer
US3382034A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for separating inorganic cations from solution with hydrous oxide cation exchangers

Assignee: Individual
•
Filing: 1965-01-28
•
Granted: 1968-05-07
•
Expires: 1985-01-28
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

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.

References Cited (Backward Citations)

US2298464A Cited
US2369270A Cited
US2859093A Cited
US2855269A Cited
US2970035A Cited
US2671712A Cited
US2993000A Cited
US3056647A Cited
US2990376A Cited
US3180741A Cited
US3193346A Cited

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

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag