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ENCLOSUE 2 ARGONNE NATIONAL LABORATORY - tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert Browning Division of High Level Waste Management Nuclear Regulatory Commission 'c Mall Stop 4H3 Washington, DC 20555 Dear Mr. Browning: I would greatly appreciate the opportunity to discuss the treatment and disposal of fuel reprocessing wastes from an Integral Fast Reactor (IFR) with representatives of your Division as well as the Division of Low Level Waste Management. The IFR is being developed by the Department of Energy as one of their advanced concepts for commercial power reactors. It is a sodium-cooled, fast reactor with metal alloy fuel. This reactor concept has a close-coupled fuel cycle that employs a pyrochemical electrorefining process to separate fission products from actinides. Reactor licensing aspects of the IFR are being discussed on an informal basis with other Divisions of the NRC. Work is under way at Argonne to develop methods for treating process wastes and converting them to disposable waste forms. The principal radioactive wastes from the electrorefining process are (1)a metallic mixture with the stainless steel cladding and noble metal and rare earth fission products; and (2)a chloride salt containing alkali metal, alkaline earth and halide fission products. We are assuming that the IFR would be a commercial power reactor and, consequently, the high-level wastes would be sent to a deep geologic repository and low-level wastes would be sent to a near-surface disposal facility. The IFR process wastes are considerably different from the wastes produced by the conventional Purex process, and for that reason, we feel that informal discussions with the staff of the Nuclear Regulatory Commission would be useful. We would like to obtain background information f on current regulations relevant to the disposal of both high- and low-level wastes. The analyses that led to these regulations are of particular interest. If these analyses were made with more conventional wastes in mind, we would need advice on how to apply the analyses to the IFR situation. These discussions will help to get the development of IFR waste treatment methods started in the right direction. When I first talked with you, I had asked for a meeting during the last half of May. We would now prefer coming to your office sometime between June 1 and June 10 in the early afternoon, if possible. About two hours should be sufficient-time for Les Burris and me to present background information on the IFR fuel cycle and waste handling concepts, and to obtain initial reactions from your people. A suggested agenda is: 8806300388 80628 NMSS SUBJ 407 DCD USDwP"dEKRqy ThE Wmshy d CWwp
Transcript
Page 1: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

ENCLOSUE 2

ARGONNE NATIONAL LABORATORY - tu"g--9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9

Telephone: (312) S488

May 2, 1988

Mr. Robert BrowningDivision of High Level Waste ManagementNuclear Regulatory Commission 'cMall Stop 4H3Washington, DC 20555

Dear Mr. Browning:

I would greatly appreciate the opportunity to discuss the treatmentand disposal of fuel reprocessing wastes from an Integral Fast Reactor(IFR) with representatives of your Division as well as the Division of LowLevel Waste Management. The IFR is being developed by the Department ofEnergy as one of their advanced concepts for commercial power reactors. Itis a sodium-cooled, fast reactor with metal alloy fuel. This reactorconcept has a close-coupled fuel cycle that employs a pyrochemicalelectrorefining process to separate fission products from actinides.Reactor licensing aspects of the IFR are being discussed on an informalbasis with other Divisions of the NRC.

Work is under way at Argonne to develop methods for treating processwastes and converting them to disposable waste forms. The principalradioactive wastes from the electrorefining process are (1) a metallicmixture with the stainless steel cladding and noble metal and rare earthfission products; and (2) a chloride salt containing alkali metal, alkalineearth and halide fission products. We are assuming that the IFR would be acommercial power reactor and, consequently, the high-level wastes would besent to a deep geologic repository and low-level wastes would be sent to anear-surface disposal facility.

The IFR process wastes are considerably different from the wastesproduced by the conventional Purex process, and for that reason, we feelthat informal discussions with the staff of the Nuclear RegulatoryCommission would be useful. We would like to obtain background information fon current regulations relevant to the disposal of both high- and low-levelwastes. The analyses that led to these regulations are of particularinterest. If these analyses were made with more conventional wastes inmind, we would need advice on how to apply the analyses to the IFRsituation. These discussions will help to get the development of IFR wastetreatment methods started in the right direction.

When I first talked with you, I had asked for a meeting during thelast half of May. We would now prefer coming to your office sometimebetween June 1 and June 10 in the early afternoon, if possible. About twohours should be sufficient-time for Les Burris and me to present backgroundinformation on the IFR fuel cycle and waste handling concepts, and toobtain initial reactions from your people. A suggested agenda is:

8806300388 80628NMSS SUBJ407 DCD

USDwP"dEKRqy ThE Wmshy d CWwp

Page 2: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

. * 4

Mr. R. Browning 2 May 2, 1988

L. BurrnsR. JohnsonR. JohnsonR. Johnson

Overview of IFR Fuel Cycle ......................Description-of IFR Process Wastes ........... T.Proposed Waste Treatment Methods ............ T.Proposed Waste Forms for Disposal ........... T.Comments and Discussion

We would also like to establish contacts with both the High-Level and Low-Level Waste Management Divisions to facilitate on-going discussions.

Sincerely,

1,ei,4 -'IO

Terr6 R. JohnsonNuclear Fuel Reprocessingand Waste Management Section

Chemical Technology Division

TRJ : sc

Page 3: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

ENCLOSURE 3

IFR FUEL CYCLE- 1 -

Mr. Terry R. JohnsonNuclear Fuel Reprocessing

and Waste Management SectionChemical Technology DivisionArgonne National Laboratory9700 South Cass AvenueArgonne, Illinois 60439

MAY 2 7 192

tweller9 gTR

Dear Mr. Johnson:

I am responding to your letter of May 2, 1988, regarding your interest indiscussing with the Nuclear Regulatory Commission (NRC) staff the plannedDepartment of Energy Integral Fast Reactor (IFR) and its closely coupled fuelcycle. Specifically, you expressed interest in discussing the treatmentand disposal of both high-level and low-level wastes resulting from thereprocessing of IFR spent fuel. The staff of the NRC would be pleased toparticipate in discussions with you and Les Burris on the IFR fuel cycle andwaste handling concepts and arrangements have been made for an initial meetinghere at NRC Headquarters for the early afternoon (1:0 PM) of June 9, 1988. Wewill have a representative from the Division of High-Level Wasteila-nagement,the Division of Low-Level Waste Management and Decommissioning, and the Officeof Nuclear Regulatory Research (Waste Management Branch) for these discussions.

In your letter, you also expressed interest in establishing contacts with boththe High-Level and Low-Level Waste Management Divisions to facilitate ongoingdiscussions related to waste management issues. The contact for theDivision of High-Level Waste Management is Rick Weller (301-492-3458),Materials Engineering Section Leader, Technical Review Branch. Thecontact for the Division of Low-Level Waste Management and Decommissioning isMike Tokar (301-492-0961), Engineering Section Leader, Technical Branch.

We look forward to meeting with you and Les Barris.

Sincerely,

c.a dt1e of

£&6°05

A ed ° eo4' Robert E. Browning, DirectorDivision of High-Level Waste ManagementOffice of Nuclear Material Safety

and Safeguards

DISTRIBUTION

Central Files REBrowning, HLWMBYoungblood, HLOB HLTR r/fRCunningham, FC MKnapp, LLWMJSurmeier, LLTB/LLWM

RLBallard, HLTRRWeller, HLTRJGreeves, LLWM

JOBunting, HLSEFCostanzi, RESMTokar, LLTB/LLWM

-

OFC : HLTR - :…NAME :RWeller/cj : RBal

k : J__ eier- :-xkar : JSurmeier : E

DATE : 5/:7/88 : 5/,/88 : 5/88 : 5/2 88 :

TW ning: : :

5 7 88 :

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ENCLOSURE 4

TREATMENT AND DISPOSAL OFFUEL CYCLE WASTES

FROM ANINTEGRAL FAST REACTOR

(IFR)

Terry JohnsonLes Burris

ChemicalArgonne

Technology DivisionNational Laboratory

* IFR and Its Fuel Cycle

* Process Wastes and Their Treatment

* Concepts for Waste Packaging and Disposal

Page 5: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

ASSUMPTIONS

* Commercial IFR

* Discharged

* Recoveredto Reactor

- Fuels Are Reprocessed

U and Pu Are Returned

* TRU, HL WastesRepository

Go to Geologic

* LLW Go to Engineered,Surface Repository

Near-

Page 6: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

a

A~

PURPOSE OF MEETING

* Introduce IFR Fuel Cycle

* EstablishContacts

Ongoing Informal

* Obtain Guidance inProposed MethodsDisposal

Assessingfor Waste

Page 7: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

. . a

ENCLOSURE 5

Overview of theIFR Pyrochemical Process

by

Leslie Burris

Presented to theNuclear Regulatory Commission

Washington, DC

June 9 1988

Page 8: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

WHAT IS THE IFR?

An Advanced Fast Reactor Concept

Key Features

* Pool Primary Coolant System

Integral with* CompleteReactor

Fuel Cycle

* Metallic Alloy Fuel

Page 9: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

PUMP W,,,, I H X

POOL (

(

LOOP

Page 10: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

.

20 I I I I

IT I I I I I I

EBR-II DRIVER FUEL BURNUPCAPABILITY

E

0o

a:

zc:co

15

10

5

ExpectedBurnup Limit

MARK-11A

xIIIIIIII

(

C

MARK-II Iv

(75% Sdensil

MARK-IA

'mear\ -jty) x

x ?(85% Smear

density)

0_0�-_yI I

J

I I I Il I0o I

1964 1968 1972 1976 1980 1984

DATE BURNUP LIMIT ACHIEVED

Page 11: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

EFFECT OF LOSS OF FLOW WITHOUTSODIUM TEMPERATURE FOR METAL50 0 I I I I I I I III I I I .

SCRAM ONAND OXIDE

OUTLETFUELS

.

co

C,zwcc-

ccwa.Li6Fp

400

300

200

100

(

(

01 10 100 1000

TIME (Seconds)

Page 12: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

LOSS-OF-FLOW WITHOUT SCRAM(EBR-II TEST)

ISOc

o - --, PREDICTION

1400 * MEASURED DATA

M4(

'fLoo-

o 1 1000~~~~~~~~~~~~~~~~~~

.100 a 200

TIME INTO TRANSIENT, S

Page 13: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

IFR Concept

SUBASSEMBLY DISMANTLINGAND REMANUFACTURE (AIR CELL)

(

(

FUEL TRANSFER CORRIDOR

EBR-H REACTOR VESSEL

FUEL ELEMENTAND FABRICATION

REPROCESSING( ARGON CELL)

Page 14: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

Fuel Cycle for the Integral Fast Reactor

REACTOR

- Fresh Fuel 4--Discharged Fuel(

Assembly of FuelSubassembiles I Dismantling of

Subassembiles IClad FuelElements

I NChoppedFuel Pins

Fuel Fabricationby Inject. Casting

Recovery of Fuelby Pyroprocess (.Processed Fuel

I PIn 14- _

Molds

Fisslon-- Product

WastesI11 WASTE PROCESSING 1 I

To Waste StorageMOFucNr E N^ArI 0NA L L AEDO AATO RY,J,

Page 15: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

qmlm.." ..... a

Injection Casting at ANL

Melting

00CDO-

s u

Casting

K000000

Q000Olo

0

.0000.

0.

0000O0

- AR QCAN N m N ATI ON AL LA^ 30O rATO RY_

Page 16: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

IFR PROCESS OBJECTIVES

Core Fuel

* Removal of Fission Products

* Reenrichment

* High Recovery -> 98%

Blanket Fuel

* Provide Plutonium for Reenrichmentof Core Fuel

* Adequate-> 95%

Recovery of Plutonium

Page 17: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

HOW DOES THE PYROPROCESS WORK?PYROPROCESS STEPS

Core Fuel Uranium Blanket Cathode Metal Product

(

Recycle U-Pu Recycle UProduct to Core Product to Blanket

Page 18: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

ELECTROREFINING IS THEKEY STEP OF THE PROCESS

H HCATHODE-

HEAVY-METAL

DEPOSIT(U-Pu)

A ~~& A A, AL AL AL ,

_ _ ~~0

-ANODE

-ELECTROLYTE

-CADMIUM_. .wn

Electrolytic Transport of Pu and Ufrom Liquid Metal Anode to LiquidMetal Cathode through a Molten SaltElectrolyte Provides the NecessarySeparations.

^ Fuels (Core and Blanket) AreSeparated from Cladding Material

* Plutonium and Uranium AreTransported bgether for Recoveryof Core Fuel

* Uranium Is Selectively Depositedon a Solid Steel Mandrel forRecovery of Blanket Fuel

* Fission Products Are Removed inSalt and Metal (Cadmium) WasteStreams

C

(kp

I

ELECTROREFINER (U-Pu)

Page 19: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

0

ELECTROREFINING FOR RECOVERYOF PLUTONIUM AND URANIUM

Metal Waste(Clad, Cd, N.M. FPs)

(

Xe, Kr

P Uranium CathodeI Deposit to Product

+ - Consolidation

4 -CathodeCell

El ectrolyte -(

r� I

-- oSalt Waste(Atk., Alk. Earth,R. Earth FPs,and Na as NaCl)Anode Basket- If WIb

.

Blanket orCcre Fuel

4 500CIV I Cadmiuml. J Anode

Page 20: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

DOD EQnwfOO9 Off FwmmA'n OfhO0de a 773"K9 =AG" , kc/gm-qDw. C

BaC12 87.9 CmCI3 64.0 CdCD2 32.3 (Cs¢C 87.8 PuC13 62.4 FoCI2 29.2RbCD 87.0 MgCD2 62.1 MbCD5 26.7KCI 86.7 IpCD3 685. 1 MOC12 16.8CrC° 2 84.7 UCD 665.2 TCCD3 11.oUCO 82.5 ZrCD 2 46.6 RhCO 10. 0MaCI 81. PdCD2 9.0CaCD 2 80.7 RuC13 . 0

LaCB3 70.2PrCi 3 69.0 (CeCD3 68.65HdC13 67,. C 3 S6. Estimated VaDue

Argonne NatlonaO Laboratory

Page 21: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert
Page 22: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

MAJOR REASON FOR CHOOSINGCADMIUM CATHODE

UCI3 + (Pu)__ '-cathode

PuCI 3 + (U)cathode

(

SOLID CATHODE

XPuC13

XUC13= 8.8 X lol

LIQUID CADMIUM CATHODEXPUCI p

fuc 2.0X UCI3

(

Artcmhommw Lmmcpr L%^T _

Page 23: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

SCHEMATIC REPRESENTATION OFELECTROREFINING OPERATION

Metal Waste(Clad, Cd, N.m. FPs)

I Xe, Kr

Low-CarbonSteel Vessel

Anode Basket -

Core and/or Blanket -

Fuel, Clad, andNa Bond

-s-fl r

CelnElectrolyte

+

Cathode Deposit toProduct Consolidation

(U, Pu, Cd)

CadmiumCathode

- Salt WasteElectroposItive

FPs, as rand Na as NaCI

(

III I1-4-1, _..

CadmiumAnode(600C)

C

.41% RIC Alan qr--p M rig = F'IO A rqT O _ N r

Page 24: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

1 4..~~~

% . . 4-1K. .q

a-; - me, .

'. ,

PI� .

.. 10

-

Page 25: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert
Page 26: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

PRODUCT REMOVAL METHODS

Product Constituent Removal Method (

Uranium Solid Cathode MandrelLiquid Cadmium Cathode

I 'lutonium Liquid Cadmium Cathode(Accompanied by Uranium)

Page 27: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

i.

- V

p..

-p.

A

pp.

�,,�.,

.dt�. 411

i'�.

i

C

Page 28: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

OPERATIONAL SEQUENCE FORPROCESSING CORE AND BLANKET MATERIALS

- ~ ~- -,

Amounts (kg Material Fate f ICharge U Pu Removed Cathode PlutoniGImn I

Blanket 9.5 0.5 m8 kg U Solid mandrel Retained insystem

Core 8 1.5 P6.5 kg U Solid mandrel Retained insystem

2 kg Pu Liquid cadmium 1 Removed in3 kg U J U-Pu Produc

Blanket 9.5 0.5Cycle repeated

Core 8 1.5

Page 29: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

K-

<.i;1 1i<jII AS~f ?1lMHi Y

* -I)MIuM S II4lImh f'& tjf l y . L. )C 1 V

E.Lf ('Tt, CY r I.0I l t S I t 1I : R._ ASS iMllt yFLf Tis i 8 .f

CO0Vf*tI ....

i .1 SIlfI I -)

(;HUCFit r-

HFAVY MFTAt

IMPELI-Ff4

IA ,

U PPLF.I HI' A TI 3 FAF IIAND iit:'F

1:1 } TR t Y I F

.IMI'F I [1t k

L 0W 1 H f T A f: l ffAND ClDE

1'1 Iii.

I FN H E L E C T , n r- .r n i

Page 30: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

I

' -w--

-

I

-1 -I.'

(

*'*I'.

1'

I

I ,>+t, ̂ !

: I . II

I'i

V'

r

Page 31: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

A &tejt

: . ..L., ..

,;. i,7 .

tL%._,

MItd

rOK j v; f -

V': {H+

',

f.Z;-

H

I i,-I

I

If

1' NE I I,

.ir1 FA I

I WI

I-IIt

R -2-I._P"_ W-1:11"2':-4~ U

C0 I.q I

M.-0'lkw -uo -A

I FfI

r

I'

42t -~

I-

,v ;ZSw1 Ij'44s'- '

Page 32: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

low,

v t l

-- I ^ s

*

"'--V-'S

.;i:�

I -�

Large (10-kg) Uranium Deposit

Page 33: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

7

. . .I

Consolidated Ingot

Page 34: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

TREATMENT OF SOLID PYROPROCESS WASTES

cd-Qa% U +| A S

<"X IIA TO DWPOSAL

ASSEMYDWHARD WARE

SALT 'I7i

Cd+

ACflNIS+

RARE EA h

cu

(

Aptt4^ N ArscuoM4 L. L _

Page 35: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

K>

Summary

* Electrorefining of IFR FuelCathode is Promising

- Thermodynamics Well Es,- U and Pu Have Been Tr- Adequate Purification Acl

Using a Cadmiurn

ded Together

tablishe-ansport[ievable

* Good Progress Has Been Made in DevelopingMethods for Processing Waste Streams

- Thermodynamics Are Reasonably WellHand

- Waste Forms Are Being Evolved andCharacterized

in

* Equipment Operation Has Been VerySatisfactory

* Proceeding with Engineering-ScaleDemonstration of Electrorefining (Initially,Depc- ion on Solid Cathode)

U

Page 36: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

<-/,! ENCLOSURE 6

IFRPROCESS WASTES

* Description

* Treatment

* Disposal of

of Principal

and Handling

Wastes

I of Wastes

' Solid Wastes

* Future Development

Page 37: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

IFR ELECTROREFINING PROCESSFOR IFR CORE AND BLANKET

(Cd Vaporaand Prod.Consol.

U-Pu Product

Xe,Kr

tL Cd Recycle i _U-Pu Cathode Deposit

CoreBlanket

,

HeadendMechanicalOperations

PinDissolution

andElectroref.

1 I

Halide Salt WasteCd-Metal Waste

Segmentsi

I

I

Cd Recycle I1 U Cathode Deposit

TI Blanket U

(I-I

Cd Vapsand ProcConsoL

'L

Page 38: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

IFR Fission Gas Handling

Process Cell

ImpureAr-5%N2 C

Purified Ar-N2

8500L/mIn.

DE-OXO

Condenser 130K

LLN2

DistillationColumn v

To On-Site Storage(100 cylinders/y)

Gas Cylinders(2000 Cis 35 atm)

Reboller 200K

__________________________A - _ -RGONNE "IATrIONAL LABORFTR.ATr ORm

Page 39: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

FISSION GAS HANDLING

Tritium

* Collected in Small Volume of Water

* 30 Y, 1100 MWe = < 20,000 L

* Stored '100 y in Monitored, On-Site Facility

Krypton-Xenon

* Collected in Cylinders at 30 atm

* 30 y, 1100 MWe = 1200 Cylinders

(180 std ft3 at 3000 psi)

* Stored -'100 y in Monitored, On-Site Facility

Page 40: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

IFR PYROPROCESS SOLID WASTES

Basis: Reactor:Process Plant:

1100 MWy(e)/y; 4 y in reactor; 1 y cooling250 operating days/y; 65 kg HM fed/d

(Activities

Waste Weight Composition P-7 aStream (kg/d) (kCi/d) (Cu/d)

ER Salt 20 LiCl-KCl-NaCl 150 10

ER Metal 25 Cd- Zr 150 30

Cladding 40 SST 10 Ml

Hardware 120 SST + B4C <10 <<1

Ceramic 5 BeO + Y20 3 <1 ow

(

Page 41: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

nonTRU,LL METAL WASTES

* Primarily Fuel Assembly Hardware

* 30 y, 1100 MWe = 800 T SST

= 130 T B 4 C

* Decontaminated and Na Removed

* Compacted and Contained

* Disposal in On-Site, Near-Surface Repository

Page 42: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

TREATMENT OF SO10 PYROPROCES WASTES

FLY AS:HA WATER

Cd-LI | CEMENT

WASTE ALT _ XTRACTNOfTRU SALT _ ENCAP- TO

(ELECTROLYTE) CTINIDES SULATION DISPOSAL (Cd &

_ ACTINIDES

PLENUM CLAD DISPE-RSE ASSEMBLYSOLIDS HARDWAREIN METAL..

METAL WASTES ENCAP- INTERIM SECONDARY TOENCAP-

(ANODE RASKETS) ULAT ON -TORAGE DISPOSAL

.-.. ---.- -- --..- � -. - .. ..-- -..

Page 43: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

-t

TRUMETAL-CERAMIC WASTE

* Sources

- Anodes from Electrorefiner

- Cadmium from Waste Salt Extraction

- Broken Ceramic Crucibles

* Composition (wt %)

Cd 25Cladding 50Zr 10Ceramics 6Anodes (Steel) 5Fission Products 4

100

* Fission Products

- Noble Metals (including Tc)

- Rare Earths (except Sm. Eu)

* Alpha Activity 0.5 mCi/g

Page 44: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

TRUMETAL-CERAMIC WASTE

* Treatment

- Distill Excess Cd from Metals

- Crush Ceramics

- Disperse in Cu Matrix(Cu/Waste Weight Ratio 3)

- Seal in Cu Container

* 30 y 1100 MWe = 2000 T( 9 L/MWy (e) )

* Disposal in Civilian Repository

Page 45: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

PERFORMANCE OFCOPPER CONTAINMENT

* Cu Container Should Last >1000 y

- Stable in Some Groundwaters

- Resistant to Pitting

- Resistant to Stress Corrosion

* Radiation Has Small or No Effect

- Embrittlement

- Aqueous Radiolysis

* Fabrication/inspection

- Feasible

- Practical

* Swedish Program

- Expect 106 y Container Lifetime

- Developed HIP for Containing LWR FuelAssemblies

Page 46: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

COPPER CONTAINMENTOF HLW

ASSESSMENT ISSUES

* Quality of Copper - Waste Matrix

- Uniformity

- Effects of Waste Components Dissolved inCu

* How Long Will It

* Effect of Cu on Forms

Really Last in Repository?

repository and Other Waste

Page 47: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

A -I I - - - -- - - ww�

ACTINIDE EXTRACTION FROM SALT* REQUIRED DF: - 1000* MEASURED DISTRIBUTION COEFFICIENTS

U < aooiPu < OOlAm 01- 0.02Cm 0.005- ao.,RE -. 0.0 - .1ICs, Sr>100I

. TYPICAL PROCESSCd-al Z Li

IV1=a3

(

SAtY

c.c =ImC,. STAGE

XTRACIN

An+

fCod-Ql Z L~il1e/s!= 3

! SECOND IT aE IRCTONI = 00 XXo

I 8; A= 3 Cs trut+

(

* INSOLUBLES IN SALT?�WwrwcwcMwwMw Nbe.A a.o. L .n m _

Page 48: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

CHARACTERISTICSTREATED SALT

OF

* Composition (wt %)

LiCIKCINaCIRb, Cs) ClSr, Ba)Cl 2RE) Cl3

384810

220.2

1-129a

2 Ci/g (Sr, Cs, Sm)300 nCi/g<1000 nCi/g (Cm)

* Heat Rate: 7 mW/g3 mW/g 3I0y)

* 30 y, 1100 MWe = 150 T salt

Page 49: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

---

vI

PACKAGING OFTREATED SALT

* Dispersed in Mortar

Portland Cement (Type I)Fly Ash (Class F)Blast Furnace SlagWaterSalt

20 wt %20203010

* Activity after 3 Years

Sr-Y-90Cs- Ba-1371-129

a

"100,000 Ci/mr3-- 260,000 C/m 3

"0.05 Cl/m<100 nCi/gm (90 wt % Cm-242)

* Mortar-Salt Properties

Strength (3(128

d)d)

>10>40

MPaMPa

Leach. Index (128 d) 9 (for C)

Radiation Effects

Page 50: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

DISPOSAL OFWASTE SALT

* Store Treated Salt for 10-30 Y

* Disperse in Mortar

* Seal in Corrosion-Resistant Containers

* Store Contained Waste Forms for 30 Y

* Dispose of in On-Site Repository(Engineered, Near-Surface)

Page 51: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

SALT DISPOSAL

APPROACH

* 10CFR61.58

"The Commission mayauthorize other provisions for theclassification and characteristics ofwastes on a specific basis, if, afterevaluation, it findsreasonable assurance of compliance withthe performance objectives in Subpart C

',* s6e68

* Analysis to Determine if IFR SaltMeets Performance Objectives?

Page 52: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

SUMMARY

* " Nuisance" Fission Products Are Easily Handled

Tritium - in a small volume of water

Krypton - easily concentrated and stored

C-14 - forms stable carbides

Iodine - forms stable iodides

Ruthenium - contained in Cd as metal

* Radioactivity Is Easily Contained in ReprocessingFacility

* Few Waste Streams

* Wastes Contain <1% of Np, Pu, Am, and Cm

Page 53: ENCLOSUE 2 ARGONNE NATIONAL LABORATORY tug-- · ENCLOSUE 2 ARGONNE NATIONAL LABORATORY -tu"g-- 9W~J SOUffk CASS AV&C AMQMW tbrOS 6O4N 9 Telephone: (312) S488 May 2, 1988 Mr. Robert

SUMMARY

IFR Results in Low Potential Dose to Public

* Less U Mining

* Lower Releases from Reactor

* Low Doses from Fuel Reprocessing

* Lower Releases from Waste Repositories

Total Potential Dose is Lower than Dose from LWRCycle without Fuel Reprocessing


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