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
. * 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
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 :
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
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-
a
A~
PURPOSE OF MEETING
* Introduce IFR Fuel Cycle
* EstablishContacts
Ongoing Informal
* Obtain Guidance inProposed MethodsDisposal
Assessingfor Waste
. . a
ENCLOSURE 5
Overview of theIFR Pyrochemical Process
by
Leslie Burris
Presented to theNuclear Regulatory Commission
Washington, DC
June 9 1988
WHAT IS THE IFR?
An Advanced Fast Reactor Concept
Key Features
* Pool Primary Coolant System
Integral with* CompleteReactor
Fuel Cycle
* Metallic Alloy Fuel
PUMP W,,,, I H X
POOL (
(
LOOP
.
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
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)
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
IFR Concept
SUBASSEMBLY DISMANTLINGAND REMANUFACTURE (AIR CELL)
(
(
FUEL TRANSFER CORRIDOR
EBR-H REACTOR VESSEL
FUEL ELEMENTAND FABRICATION
REPROCESSING( ARGON CELL)
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,
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_
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
HOW DOES THE PYROPROCESS WORK?PYROPROCESS STEPS
Core Fuel Uranium Blanket Cathode Metal Product
(
Recycle U-Pu Recycle UProduct to Core Product to Blanket
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)
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
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
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 _
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
1 4..~~~
% . . 4-1K. .q
a-; - me, .
'. ,
PI� .
.. 10
-
PRODUCT REMOVAL METHODS
Product Constituent Removal Method (
Uranium Solid Cathode MandrelLiquid Cadmium Cathode
I 'lutonium Liquid Cadmium Cathode(Accompanied by Uranium)
i.
- V
p..
-p.
A
pp.
�,,�.,
.dt�. 411
i'�.
i
C
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
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
I
' -w--
-
I
-1 -I.'
(
*'*I'.
1'
I
I ,>+t, ̂ !
: I . II
I'i
V'
r
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'- '
low,
v t l
-- I ^ s
*
"'--V-'S
.;i:�
I -�
Large (10-kg) Uranium Deposit
7
. . .I
Consolidated Ingot
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 _
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
<-/,! ENCLOSURE 6
IFRPROCESS WASTES
* Description
* Treatment
* Disposal of
of Principal
and Handling
Wastes
I of Wastes
' Solid Wastes
* Future Development
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
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
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
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
(
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
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
.-.. ---.- -- --..- � -. - .. ..-- -..
-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
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
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
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
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 _
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
---
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
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)
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?
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
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