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US4025560A
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Process for the exchange of hydrogen isotopes between streams of gaseous hydrogen and liquid water
Assignee: Atomic Energy of Canada Ltd AECL
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Filing: 1973-12-12
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Granted: 1977-05-24
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Expires: 1993-12-12
Abstract
Abstract A process for the exchange of hydrogen isotopes between streams of gaseous hydrogen and liquid water, wherein the streams are brought into contact with one another and a catalyst assembly at a temperature in the range 0 DEG -300 DEG C. The catalyst is an inherently hydrophobic material such as polytetrafluoroethylene, polyethylene, polystyrene, polymethacrylate, polypropylene or carbon black carrying a catalytically active metal, for example, platinum, rhodium and nickel. The inherently hydrophobic support allows the catalytically active metal to catalyze the hydrogen isotope exchange reaction between hydrogen gas and water vapor in the presence of liquid water while retarding loss of activity of the catalytically active metal by contact of the metal catalyst with liquid water. This catalyzed chemical isotope exchange proceeds simultaneously with isotope exchange from water vapor to liquid water by a non-catalyzed, physical evaporation and condensation exchange reaction to effect an overall rapid catalytic isotopic exchange between streams of hydrogen gas and liquid water.
Inventors
- 👤 John H. Rolston
- 👤 William H. Stevens
- 👤 James Denhartog
- 👤 John P. Butler
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-25 15:00
CPC Classifications
B; B01; B01J; B01J23/00; B01J23/38; B01J23/40; B01J23/42; B01J23/46; B01J23/464; B01J31/00; B01J31/02; B01J31/06; B01J33/00; B01J37/00; B01J37/02; B01J37/0215; B01J37/0219; C; C01; C01B; C01B4/00; B01J35/00; B01J35/50; B01J37/024; B01J37/0244; B01J37/16; B01J37/18
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
264 words
A process for the exchange of hydrogen isotopes between streams of gaseous hydrogen and liquid water, comprising: (a) bringing the streams into contact with one another and a catalyst assembly at an operating temperature in the range 0° to 300° C., with one of the streams containing a concentration of a hydrogen isotope in excess of that which it would contain when the liquid water-gaseous hydrogen streams are in isotopic equilibrium at the operating conditions of temperature and mass flow rates of the streams and the other being a deficient stream and containing a concentration of that hydrogen isotope which is less than that which it would contain when the liquid water-gas system is in equilibrium at said operating conditions, so that the deficient stream is enriched by transfer of the hydrogen isotope in a two-step hydrogen isotope exchange from the other stream, and (b) recovering the said stream enriched in the hydrogen isotope, and wherein the improvement comprises: (c) the catalyst assembly comprises at least one porous, support of polytetrafluoroethylene, with the support surface having exposed catalyst particles of at least one element selected from Group VIII of the Periodic Table, such that the support substantially inhibits the contact of liquid water with the catalyst particles while allowing contact therewith of hydrogen gas and water vapour from the liquid water so that the hydrogen isotope exchange occurs simultaneously between hydrogen gas and water vapour containing the catalyst particles, and between water vapour contacting the liquid water and that liquid water, and whereby submersion of the catalyst particles in liquid water is largely prevented.
Claim 2
Dependent Claim
264 words
A process for the exchange of hydrogen isotopes between streams of gaseous hydrogen and liquid water, comprising: (a) bringing the streams into contact with one another and a catalyst assembly at an operating temperature in the range 0° to 300° C., with one of the streams containing a concentration of a hydrogen isotope in excess of that which it would contain when the liquid water-gaseous hydrogen streams are in isotopic equilibrium at the operating conditions of temperature and mass flow rates of the streams and the other being a deficient stream and containing a concentration of that hydrogen isotope which is less than that which it would contain when the liquid water-gas system is in equilibrium at said operating conditions, so that the deficient stream is enriched by transfer of the hydrogen isotope in a two-step hydrogen isotope exchange from the other stream, and (b) recovering the said stream enriched in the hydrogen isotope, and wherein the improvement comprises: (c) the catalyst assembly comprises at least one porous, support of polytetrafluoroethylene, with the support surface having exposed catalyst particles of at least one element selected from Group VIII of the Periodic Table, such that the support substantially inhibits the contact of liquid water with the catalyst particles while allowing contact therewith of hydrogen gas and water vapour from the liquid water so that the hydrogen isotope exchange occurs simultaneously between hydrogen gas and water vapour containing the catalyst particles, and between water vapour contacting the liquid water and that liquid water, and whereby submersion of the catalyst particles in liquid water is largely prevented.
Claim 3
Dependent Claim
47 words
The process according to claim 1, wherein a solution of a catalyst compound is impregnated into the porous support, and the catalyst compound is deposited from the solution onto the surface of the support and is converted to metallic catalyst particles by chemical reduction at elevated temperatures.
Claim 4
Dependent Claim
20 words
The process according to claim 2, wherein the catalyst is selected from the group consisting of platinum, nickel and rhodium.
Claim 5
Dependent Claim
23 words
The process according to claim 3, wherein the catalytically active metal is between 0.005 and 10.0 percent by weight of the catalyst assembly.
Claim 6
Dependent Claim
24 words
The process according to claim 3, wherein the catalytically active metal is preferably between 0.05 and 1.0 percent by weight of the catalyst assembly.
Claim 7
Dependent Claim
20 words
The process according to claim 1, wherein the catalyst assembly comprises a plurality of discrete bodies disposed as a bed.
Claim 8
Dependent Claim
30 words
The process according to claim 1, wherein the stream of gaseous hydrogen is fed upwardly into contact with the catalyst assembly in counter-current fashion to the stream of liquid water.
Claim 9
Dependent Claim
30 words
The process according to claim 1, wherein the stream of gaseous hydrogen and the stream of liquid water are fed con-currently upwardly or downwardly into contact with the catalyst assembly.
References Cited (Backward Citations)
US2690379A
Cited
US3681021A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1980-05-23 | 1980-11-22 | 1981-05-24 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-05-23 | 1984-11-22 | 1985-05-24 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-05-23 | 1988-11-22 | 1989-05-24 | $7700.00 | Window Closed / Lapsed |