US4711768A
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Process for the separation of gadolinium isotopes
Assignee: Westinghouse Electric Corp
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Filing: 1985-06-18
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Granted: 1987-12-08
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Expires: 2005-06-18
Abstract
Abstract An efficient and economical separation of the gadolinium isotopes Gd155, Gd156 and/or Gd157 from mixtures containing the same is effected by a liquid chromatographic column system using an ion exchange resin and an eluant solution. A portion of the eluant solution is used to saturate the columns and a feed solution containing the mixture of gadolinium isotopes is charged to the columns. Further eluant solution is passed through the saturated columns containing the feed solution to form a fraction of eluant solution rich in the desired gadolinium isotopes which is separated from the remainder of the eluant upon discharge from the columns.
Inventors
- 👤 Steven H. Peterson
- 👤 Edward J. Lahoda
- 👤 Sharon L. Weisberg
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-07 18:47
CPC Classifications
B; B01; B01D; B01D59/00; B01D59/28; B01D59/30
Claims Analysis
Total Claims: 19
Claim 1
Independent Claim
165 words
The process for separation of the gadolinium isotopes from a mixture of gadolinium isotopes comprising: providing an eluant solution consisting essentially of aqueous methanol, containing 70-85 percent by volume methanol, and having a concentration of ammonium nitrate of a value of 1.0-2.0 N; saturating a plurality of columns of a strongly basic anion exchange resin with said eluant solution; forming a gadolinium feed solution of said mixture of isotopes; charging said feed solution to said plurality of saturated columns; passing additional said eluant solution through said plurality of columns containing the feed solution so as to form a first fraction of eluant solution richer in at least one of said gadolinium isotopes than a second fraction containing at least one other of said isotopes; separating said first fraction from said second fraction after passage through said columns; recovering the aqueous methanol and ammonium nitrate from the eluant after passage through said columns; and recycling aqueous methanol so recovered for formation of further said eluant solution.
Claim 2
Dependent Claim
165 words
The process for separation of the gadolinium isotopes from a mixture of gadolinium isotopes comprising: providing an eluant solution consisting essentially of aqueous methanol, containing 70-85 percent by volume methanol, and having a concentration of ammonium nitrate of a value of 1.0-2.0 N; saturating a plurality of columns of a strongly basic anion exchange resin with said eluant solution; forming a gadolinium feed solution of said mixture of isotopes; charging said feed solution to said plurality of saturated columns; passing additional said eluant solution through said plurality of columns containing the feed solution so as to form a first fraction of eluant solution richer in at least one of said gadolinium isotopes than a second fraction containing at least one other of said isotopes; separating said first fraction from said second fraction after passage through said columns; recovering the aqueous methanol and ammonium nitrate from the eluant after passage through said columns; and recycling aqueous methanol so recovered for formation of further said eluant solution.
Claim 3
Dependent Claim
28 words
The process for separation of gadolinium isotopes as defined in claim 1 wherein said mixture comprises Gd 155 , Gd 156 , Gd 157 and other gadolinium isotopes.
Claim 4
Dependent Claim
24 words
The process for separation of gadolinium isotopes as defined in claim 2 wherein said mixture comprises said gadolinium isotopes and other rare earth elements.
Claim 5
Dependent Claim
25 words
The process for separation of gadolinium isotopes as defined in claim 1 wherein said eluant solution contains aqueous methanol containing about 80 volume percent methanol.
Claim 6
Dependent Claim
30 words
The process for separation of gadolinium isotopes as defined in claim 1 wherein said plurality of columns comprises 5-30 columns, and each column has a length of about thirteen meters.
Claim 7
Dependent Claim
41 words
The process for separation of gadolinium isotopes as defined in claim 1 wherein at least one of said gadolinium isotopes Gd 155 , Gd 156 and Gd 157 is separated from the others of said fraction after passage through said columns.
Claim 8
Dependent Claim
58 words
The process for separation of gadolinium isotopes as defined in claim 1 wherein said feed solution is in an amount sufficient to form a band in said column of a length of about 0.1 percent to the length of the column and the flow rate of said additional eluant solution is between 0.5-2.0 ml/in 2 of resin column/minute.
Claim 9
Dependent Claim
49 words
The process for separation of gadolinium isotopes as defined in claim 1 wherein, prior to complete passage of said fraction through said columns, a further charging of feed solution to said columns is effected, and further eluant solution passed through said columns to form a second said fraction therein.
Claim 10
Dependent Claim
32 words
The process for separation of gadolinium isotopes as defined in claim 1 wherein said eluant solution and said feed solution have a concentration of nitrates of a value of about 1.5 N.
Claim 11
Dependent Claim
32 words
The process for separation of gadolinium isotopes as defined in claim 1 wherein said additional eluant solution is passed through said plurality of columns at a temperature of between about 40°-70° C.
Claim 12
Dependent Claim
114 words
A process for separation of a gadolinium isotope from a mixture of gadolinium isotopes, said process comprising the steps of: saturating a plurality of columns of a strong acidic cationic exchange resin with an aqueous eluant solution selected from the group consisting of ethylenediaminetetracetic acid, acetonylacetone, and benzoylacetone; passing a solution containing said mixture of gadolinium isotopes and said eluant solution through said plurality of columns; passing additional said eluant solution through said plurality of columns; as said solution containing said gadolinium isotopes exits the last of said plurality of columns, separating a band of solution enriched in at least one of said gadolinium isotope from bands enriched in other of said gadolinium isotopes.
Claim 13
Dependent Claim
114 words
A process for separation of a gadolinium isotope from a mixture of gadolinium isotopes, said process comprising the steps of: saturating a plurality of columns of a strong acidic cationic exchange resin with an aqueous eluant solution selected from the group consisting of ethylenediaminetetracetic acid, acetonylacetone, and benzoylacetone; passing a solution containing said mixture of gadolinium isotopes and said eluant solution through said plurality of columns; passing additional said eluant solution through said plurality of columns; as said solution containing said gadolinium isotopes exits the last of said plurality of columns, separating a band of solution enriched in at least one of said gadolinium isotope from bands enriched in other of said gadolinium isotopes.
Claim 14
Dependent Claim
23 words
The process according to claim 11 further comprising the step of forming gadolinium from said band of solution enriched in said gadolinium isotope.
Claim 15
Dependent Claim
12 words
The process according to claim 11 wherein said eluant is ethylenediaminetetraacetic acid.
Claim 16
Dependent Claim
25 words
The process for separation of gadolinium isotopes as defined in claim 1 wherein the temperature of said eluant solution is about 40° to 70° C.
Claim 17
Dependent Claim
23 words
The process for separation of gadolinium isotopes as defined in claim 1 wherein said strongly basic anion exchange resin has quaternary amine group.
Claim 18
Dependent Claim
18 words
The process according to claim 11 wherein said strongly acidic cationic exchange resin is a styrene gel type.
Claim 19
Dependent Claim
25 words
The process according to claim 11 wherein said eluant has a concentration of 0.5 to 1.0% by weight at a pH between 7 and 9.
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) | 1990-12-07 | 1991-06-08 | 1991-12-08 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1994-12-07 | 1995-06-08 | 1995-12-08 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1998-12-07 | 1999-06-08 | 1999-12-08 | $7700.00 | Window Closed / Lapsed |