# US 4,399,108 A · Method for reprocessing and separating spent nuclear fuels

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- Number: US 4,399,108 A
- Document ID: US4399108A
- Status: Granted
- Kind: A
- Application number: 06/340,591
- Filed: 1982-01-19
- Granted: 1983-08-16
- Earliest claimed: 1982-01-19
- Inventors: Oscar H. Krikorian; John Z. Grens; William H. Parrish, Sr.
- Web page: https://patentgrep.com/patent/US4399108A

## CPC

- G21C 19/48: Non-aqueous processes
- C01B 21/063: {with one or more actinides, e.g. UN, PuN}
- Y02E 30/30: Nuclear fission reactors
- Y02W 30/50: Reuse, recycling or recovery technologies
- Y10S 423/12: Molten media
- G21C: NUCLEAR REACTORS (fusion reactors, hybrid fission-fusion reactors G21B; nuclear explosives G21J)
- C01B: NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; {METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C}
- Y02E: REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02W: CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y10S: TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS

## Abstract

Spent nuclear fuels, including actinide fuels, volatile and non-volatile fission products, are reprocessed and separated in a molten metal solvent housed in a separation vessel made of a carbon-containing material. A first catalyst, which promotes the solubility and permeability of carbon in the metal solvent, is included. By increasing the solubility and permeability of the carbon in the solvent, the rate at which actinide oxides are reduced (carbothermic reduction) is greatly increased. A second catalyst, included to increase the affinity for nitrogen in the metal solvent, is added to increase the rate at which actinide nitrides form after carbothermic reduction is complete.

## Claims

### Claim 1

A method for reprocessing and separating spent nuclear fuels comprising actinide fuels, volatile and non-volatile fission products, comprising:
providing a separation vessel formed of a carbon-containing material, and a molten metal solvent disposed within said separation vessel, said separation vessel including an aperture disposed within a vessel wall member;
adding a first catalyst to said metal solvent which increases the solubility of carbon in said solvent;
introducing spent nuclear fuels into said separation vessel; and
forming CO within said molten metal solvent from actinide fuels which are oxides.

### Claim 2 (depends on 1)

The method according to claim 1, further comprising removing said volatile fission products and CO from said separation vessel.

### Claim 3 (depends on 2)

The method according to claim 2, further comprising:
introducing a non-oxidizing nitrogen-containing atmosphere into said separation vessel after said volatile fission products and CO have been removed therefrom;
forming solid nitrides from said actinide fuels within said molten metal solvent; and
separating said solid actinide nitrides from said molten metal solvent and non-volatile fission products.

### Claim 4 (depends on 1, 2, 3)

The method according to claims 1, 2 or 3, wherein said first catalyst is selected from Co, Ni, Fe, and mixtures thereof.

### Claim 5 (depends on 1, 2, 3)

The method according to claims 1, 2 or 3, wherein said first catalyst is Co.

### Claim 6 (depends on 1, 2, 3)

The method according to claims 1, 2 or 3, wherein said molten metal solvent is tin.

### Claim 7 (depends on 1, 2, 3)

The method according to claims 1, 2 or 3, wherein said carbon-containing material is graphite.

### Claim 8 (depends on 1, 2, 3)

The method according to claims 1, 2 or 3, wherein the weight percentage of said first catalyst in molten metal solvent is about 5.0 to 10.0.

### Claim 9

A method for reprocessing and separating spent nuclear fuels comprising actinide fuels, volatile and non-volatile fission products, in a molten tin solvent, comprising:
providing a separation vessel formed of a carbon-containing material, said separation vessel defining a reaction region housing said molten tin solvent and a reflux region positioned adjacent to and above said reaction region, said separation vessel including an aperture disposed within a vessel wall member in a position adjacent said reflux region;
adding a first catalyst to said tin solvent which increases the solubility of carbon in said solvent;
maintaining said reaction region at a temperature sufficient to convert said actinide fuels to a solubilized state;
maintaining said reflux region at a temperature sufficient to reflux said tin solvent, said reflux temperature being lower than said reaction region temperature;
introducing spent nuclear fuels into said tin solvent;
forming CO within said molten tin solvent from actinide fuels which are oxides;
allowing CO and volatile fission products within said molten tin solvent, along with some molten tin, to evaporate and flow into said reflux region;
removing CO and volatile fission products which are not condensable at said reflux temperature from said reflux region through said vessel aperture, leaving evaporated tin and condensable fission products in said reflux region; and
allowing evaporated tin and condensable fission products disposed within said reflux region which are condensable at said reflux temperature to cool sufficiently and return to said molten tin solvent in said reaction region.

### Claim 10 (depends on 9)

The method according to claim 9, further comprising:
raising said reflux temperature to said reaction region temperature after CO and said non-condensable volatile fission products have been removed from said reflux region;
distilling said condensable volatile fission products and some tin from said molten tin solvent;
removing said distilled volatile fission products and some tin from said reflux and reactive region of said separation vessel; and
lowering the temperature of said reflux region to said reflux temperature.

### Claim 11 (depends on 10)

The method according to claim 10, further comprising:
introducing a non-oxidizing nitrogen-containing atmosphere into said separation vessel; and
forming solid actinide nitrides from actinide fuels within said molten tin solvent, while substantially leaving non-volatile fission products in solution.

### Claim 12 (depends on 11)

The method according to claim 11, further comprising: separating said actinide nitrides from said molten tin solvent and non-volatile fission products.

### Claim 13 (depends on 9, 10, 11, 12)

The method according to claims 9, 10, 11 or 12, wherein said first catalyst is selected from Co, Ni, Fe, and mixtures thereof.

### Claim 14 (depends on 9, 10, 11, 12)

The method according to claims 9, 10, 11 or 12, wherein said first catalyst is Co.

### Claim 15 (depends on 9, 10, 11, 12)

The method according to claims 9, 10, 11 or 12, wherein said carbon-containing material is graphite.

### Claim 16 (depends on 9, 10, 11, 12)

The method according to claims 9, 10, 11 or 12, wherein the weight percentage of first catalyst in molten tin solvent is about 5.0 to 10.0.

### Claim 17 (depends on 9, 10, 11, 12)

The method according to claims 9, 10, 11 or 12, wherein said reaction region temperature is about 1500.degree. to 1700.degree. C.

### Claim 18 (depends on 9, 10, 11, 12)

The method according to claims 9, 10, 11 or 12, wherein said reflux temperature is about 950.degree. to 1050.degree. C.

### Claim 19 (depends on 11)

The method according to claim 11, further comprising adding a nitriding catalyst to said molten metal solvent prior to introducing said non-oxidizing nitrogen-containing gas into said separation vessel, said nitriding catalyst increasing the affinity of nitrogen in said molten metal solvent.

### Claim 20 (depends on 19)

The method according to claim 19, wherein said nitriding catalyst is selected from magnesium, calcium, strontium, barium, aluminum, manganese, vanadium, chromium, and mixtures thereof.

### Claim 21 (depends on 19)

The method according to claim 19, wherein said nitriding catalyst is calcium.

### Claim 22 (depends on 19)

The method according to claim 19, wherein the weight percentage of said nitriding catalyst to metal solvent is about 1.8 to 2.5.

### Claim 23

A method for reprocessing and separating spent nuclear fuels comprising actinide fuels, volatile and non-volatile fission products, comprising:
providing a separation vessel formed from a carbon-containing material housing a molten metal solvent, said separation vessel including an aperture disposed within a vessel wall member;
introducing spent nuclear fuels into said separation vessel;
forming CO within said molten metal solvent from actinide fuels which are oxides;
removing CO and volatile fission products from said separation vessel;
introducing a nitriding catalyst into said vessel which increases the affinity for nitrogen in said molten metal solvent;
introducing a non-oxidizing nitrogen-containing atmosphere into said separation vessel;
forming solid nitrides from said actinide fuels within said molten metal solvent; and
separating said solid actinide nitrides from said molten metal solvent and non-volatile fission products.

### Claim 24 (depends on 23)

The method according to claim 23, wherein said molten metal solvent is tin.

### Claim 25 (depends on 23)

The method according to claim 23, wherein said nitriding catalyst is selected from magnesium, calcium, strontium, barium, aluminum, manganese, vanadium, chromium, and mixtures thereof.

### Claim 26 (depends on 23)

The method according to claim 23, wherein said nitriding catalyst is calcium.

### Claim 27 (depends on 23)

The method according to claim 23, wherein the weight percentage of said nitriding catalyst to metal solvent is about 1.8 to 2.5.

### Claim 28 (depends on 23)

The method according to claim 23, further comprising including a another and different catalyst to said molten metal solvent which increases the solubility of carbon in said molten metal solvent.

### Claim 29 (depends on 28)

The method according to claim 28, wherein said another and different catalyst is selected from cobalt, nickel, iron, and mixtures thereof.

### Claim 30 (depends on 28)

The method according to claim 28, wherein said another and different catalyst is cobalt.