Isotope separation methods and systems

Patent metadata

Field	Value
Publication number	US-10556206-B2
Application number	US-201615252805-A
Country	US
Kind code	B2
Filing date	Aug 31, 2016
Priority date	Aug 31, 2016
Publication date	Feb 11, 2020
Grant date	Feb 11, 2020

Abstract

Methods and systems for the separation of isotopes from an aqueous stream are described as can be utilized in one embodiment to remove and recover tritium from contaminated water. Methods include counter-current flow of an aqueous stream on either side of a separation membrane. The separation membrane includes an isotope selective layer (e.g., graphene) and an ion conductive supporting layer (e.g., Nafion®). An electronic driving force encourages passage of isotopes selectively across the membrane to enrich the flow in the isotopes.

First claim

What is claimed is:

1. A system for removal and recovery of an isotope from an aqueous source, the system comprising:
a separation device, the separation device including:
a first flow inlet and a first flow outlet;
a plurality of hollow fiber separation membranes between the first flow inlet and the first flow outlet, each hollow fiber separation membrane including an isotope selective layer and an ion conductive supporting layer, each hollow fiber separation membrane including an exterior surface and an interior surface that surrounds a hollow tubular interior, wherein the first flow inlet is in fluid communication with and upstream of the hollow tubular interior of each of the hollow fiber separation membranes, and the first flow outlet is in fluid communication with and downstream of the hollow tubular interior of each of the hollow fiber separation membranes;
a second flow inlet and a second flow outlet defining a first flow path there between, the first flow path contacting the exterior surface of each of the hollow fiber separation membranes, wherein the separation device is configured such that flow from the first flow inlet to the first flow outlet is counter-current to the first flow path; and

an electric circuit in electrical communication with each of the hollow fiber separation membranes and configured to apply a voltage between the interior surface and the exterior surface of each of the hollow fiber separation membranes.

2. The system of claim 1 , further comprising a second flow path connecting the first flow outlet to the second flow inlet and a third flow path connecting the second flow outlet to the first flow inlet.

3. The system of claim 1 , wherein the isotope selective layer includes from 1 to about 5 atomic or molecular layers of a homogeneous crystalline material.

4. The system of claim 3 , wherein the isotope selective layer includes from 1 to about 5 layers of graphene, hexagonal boron nitride, or a transition metal dichalcogenide.

5. The system of claim 4 , wherein the isotope selective layer comprises from 1 to about 3 graphene layers.

6. The system of claim 1 , wherein the ion conductive supporting layer comprises an ion conductive polymer.

7. The system of claim 6 , wherein the ion conductive supporting layer comprises a sulfonated tetrafluoroethylene based flouropolymer.

8. The system of claim 1 , wherein the ion conductive supporting layer comprises an ion conductive ceramic.

9. The system of claim 1 , the system further comprising one or more electrodes providing electrical communication between the electric circuit and each of the hollow fiber separation membranes.

10. The system of claim 9 , wherein one of the one or more electrodes comprises the isotope selective layer of one or more of the hollow fiber separation membranes.

11. The system of claim 1 , wherein the isotope selective layer of each of the hollow fiber separation membranes is a hydrogen isotope selective layer.

12. The system of claim 1 , wherein the ion conductive supporting layer of each of the hollow fiber separation membranes comprises a perfluorosulfonic acid polymer.

13. The system of claim 1 , wherein the ion conductive supporting layer of each of the hollow fiber separation membranes is a proton conductive supporting layer or an oxygen ion conductive supporting layer.

14. A process for removal and recovery of an isotope from an aqueous source by use of the system of claim 1 , the method comprising:
contacting the interior surfaces of the hollow fiber separation membranes with a first aqueous flow, the first aqueous flow comprising an isotope, the first aqueous flow passing from the first flow inlet to the first flow outlet and through each of the hollow fiber separation membranes;
contacting the exterior surfaces of the hollow fiber separation membranes with a second aqueous flow, the second aqueous flow being counter-current to the first aqueous flow and passing from the second flow inlet to the second flow outlet; and
applying a voltage across each of the hollow fiber separation membranes from the interior surface to the exterior surface, the voltage providing a driving force to selectively conduct the isotope across the hollow fiber separation membranes.

15. The method of claim 14 , further comprising circulating the first aqueous flow to the second aqueous flow and the second aqueous flow to the first aqueous flow in a recirculation path.

16. The method of claim 14 , further comprising feeding a feed stream into the first or second aqueous flow.

17. The method of claim 14 , further comprising pulling at least one product stream off of the first or second aqueous flow.

18. The method of claim 14 , wherein the isotope is a hydrogen isotope.

19. The method of claim 14 , wherein the voltage is about 20 Volts or less.

20. The method of claim 14 , further comprising pre-treating the first or second aqueous stream.

21. The method of claim 20 , wherein the pre-treatment comprises acidifying the stream.

22. The method of claim 14 , wherein the aqueous source comprises tritiated water.

23. A system for removal and recovery of an isotope from an aqueous source, the system comprising:
a separation device, the separation device including
a first flow inlet and a first flow outlet defining a first flow path there between;
a second flow inlet and a second flow outlet defining a second flow path there between, wherein the first flow path and the second flow path are counter-current to one another;
a separation membrane, the separation membrane separating the first flow path and the second flow path, the separation membrane including an isotope selective layer and an ion conductive supporting layer, the separation membrane including a first side and an opposite second side, the first side facing the first flow path and the second side facing the second flow path;
a third flow path connecting the first flow outlet to the second flow inlet;
a fourth flow path connecting the second flow outlet to the first flow inlet; and

an electric circuit in electrical communication with the separation membrane and configured to apply a voltage between the first side of the separation membrane and the second side of the separation membrane.

Assignees

• Savannah River Nuclear Solutions Llc

Inventors

• Xiao Xin
• Sessions Henry T
• Angelette Lucas M
• Beaumont Paul R
• Babineau David W

Classifications

• C02F1/469

  by electrochemical separation, e.g. by electro-osmosis, electrodialysis, electrophoresis · CPC title

• C02F1/66

  by neutralisation; pH adjustment (for degassing C02F1/20; using ion-exchange C02F1/42; for flocculation or precipitation of suspended impurities C02F1/52; for removing dissolved compounds C02F1/58) · CPC title

• C02F1/444

  by ultrafiltration or microfiltration · CPC title

• B01D69/08

  Hollow fibre membranes (manufacture of hollow fibres D01D5/24, D01F1/08) · CPC title

• G21F9/12

  by absorption; by adsorption; by ion-exchange · CPC title