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Defining the Glass Composition Limits for SRS Contaminated Soils (U)
by C. A. Cicero Westinghouse Savannah River Company Savannah River Site Aiken, South Carolina 29808 W. 0. Crews Clemson University SC USA
D. F. Bickford
A document prepared for THIRD BIENNIAL MIXED WASTE SYMPOSIUM at Baltimore from 08/08/95 - 08/11/95.
DOE Contract No. DE-AC09-89SR18035
This paper was prepared in connection with work done under the above contract number with the U. S. Department of Energy. By acceptance of this paper, the publisher and/or recipient acknowiedges the U. S. Government's right to retain a nonexclusive, royalty-free license in and to any copyright covering this paper, along with the right to reproduce and to authorize others to reproduce all or part of the copyrighted paper.
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Keywords: RCRA, low level mixed wastes, vitrification
DEFINING THE GLASS COMPOSITION LIMITS FOR SRS CONTAMINATED SOILS
by
Connie A. Cicero and Dennis F. Bickford Westinghouse Savannah River Company Savannah River Technology Center P.O. Box 616 Aiken, SC 29808
William 0. Crews Clemson University Clemson Research Park Anderson, SC 29634
A paper h P O S e d for Publication in the Proceedings of the Third Biennial Mixed Was& SPPosium, August 8 - 11, 1995, in Baltimore, Maryland.
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Defining the Glass Composition Limits for SRS Contaminated Soils
W.O. Crews, Jr . , C.A. Cicero, and D . F . Bickford
ABSTRACT
Contaminated s o i l resul t ing from t h e excavation, repair , and decommissioning of f a c i l i t i e s located a t t h e Savannah River S i te (SRS) i s current ly being disposed of by shallow land bu r i a l o r i s being s tored when considered only hazardous. Vi t r i f ica t ion of t h i s waste i s being investigated, since it w i l l bind the hazardous and radioactive species i n a s tab le and durable g l a s s matrix, which w i l l reduce t h e r i s k of ground water contamination. However, the composition l i m i t s for producing durable glass have t o be determined before the technology can be applied.
Glass compositions, consisting of SRS s o i l and glass forming additives, were t e s t ed on a crucible-scale i n three ternary phase systems. Nine d i f f e r e n t g l a s s compositions were produced, w i t h waste loadings ranging from 4 3 t o 58 weight percent. These w e r e characterized using various chemical methods and tes ted for durabi l i ty i n both alkaline and acidic environments. All nine performed w e l l i n a l k a l i n e environments, b u t only three met t h e s t r i c t e s t c r i t e r i a fo r t h e ac id ic environment t e s t s . Although t h e glasses did not meet a l l of the l i m i t s f o r t he ac id ic tests, . the t e s t was performed on very conservative s i ze samples, so t h e r e su l t s were also conservative. Therefore, enough evidence was found t o provide proof tha t SRS s o i l can be v i t r i f i e d i n a durable glass matrix.
INTRODUCTION
Contaminated s o i l s and s imilar contaminated concrete wastes resul t ing from the excavation, repair , and decommissioning of Separations, Reactor, and I n t e r i m Waste Storage f a c i l i t i e s located a t the SRS are c u r r e n t l y being disposed of by shallow land burial . These wastes can be contaminated as t h e resul t of hazardous chemical s p i l l s or low levels transuranic (TRU) element or mixed f i ss ion product releases. Vi t r i f ica t ion of these materials, s o i l i n pa r t i cu la r , i s being investigated s i n c e it w i l l destroy the organic contaminants and bind the hazardous (RCRA metals) and radioactive species i n t h e glass mat r ix . T h i s reduces t h e r i s k of ground water contamination with t h e result ing wasteform being a s tab le and durable glass product.
Limited i n - s i t u v i t r i f i c a t i o n s tud ie s with simulated SRS contaminated soil were performed by Campbell and Buelt (1) of Pacif ic Northwest Laboratory. Their findings indicated that v i t r i f i c a t i o n of the s o i l w a s plausible, but suggested t h a t
thorough a d d i t i o n s of a l k a l i n e materials be made so a more homogeneous product would be produced and m e l t i n g would be made easier.
C h e m i c a l ana lyses of uncontaminated SRS s o i l was performed by Looney e t a l . ( 2 ) . The chemical composition of t h e SRS s o i l based on a d ry oxide b a s i s i s given i n Table 1.
P l a c e T a b l e 1 Here
When t h e i n - s i t u t e s t s w e r e b e i n g performed, Campbell and B u e l t chose t o use t y p i c a l contaminants t h a t w e r e found i n SRS s o i l s , s i n c e s e v e r a l SRS s i tes c o n t a i n contaminated s o i l and t h e y wanted t o cove r many waste streams. I n t h e i r s t u d i e s , t h e y used t h e maximum contaminant levels based on l e v e l s found i n t h e i r l i t e r a t u r e s e a r c h and t h e i r equipment d e t e c t i o n l i m i t s . They developed a s i m u l a t e d contaminated s o i l based on t h e d a t a from Looney e t a l . ( 2 ) and these maximum c o n c e n t r a t i o n s . The contaminants selected for t h e i r experimentat ion i s given i n Table 2 .
P l a c e T a b l e 2 Here
I n o r d e r t o more d i r e c t l y app ly v i t r i f i c a t i o n technology t o S R S c o n t a m i n a t e d soils, a b e t t e r d e f i n i t i o n of t h e composi t ion l i m i t s f o r producing d u r a b l e g l a s s e s c o n t a i n i n g SRS s o i l needed t o be determined. Various glass compositions had t o be t e s t e d c o n t a i n i n g S R S s o i l and glass forming a d d i t i v e s , w h i c h c o n s i s t o f f l u x i n g a g e n t s ,and r e a c t i v e chemicals . The i n t e n t of t h e s t u d i e s w e r e t o opt imize w a s t e l o a d i n g without s a c r i f i c i n g l e a c h r e s i s t a n c e and d u r a b i l i t y . The s t u d i e s d i s c u s s e d i n t h i s p a p e r w e r e performed on a c ruc ib l e - sca l e , and r e q u i r e d s e v e r a l glass compositions t o be t e s t e d t o ensure t h a t t h e glass forming r eg ion w a s completely c o v e r e d . S i n c e t h e s t u d i e s w e r e o n l y per formed on a c r u c i b l e - s c a l e , o f f g a s a n a l y s e s were n o t performed because offgas c o l l e c t i o n equipment i s n o t no rma l ly used d u r i n g c r u c i b l e - s c a l e t e s t i n g i n box fu rnaces .
EXPERIMENTAL
The s o i l c h a r a c t e r i z a t i o n performed by Looney e t a l . ( 2 ) and t h e contaminant c o n c e n t r a t i o n s used by Campbell and B u e l t (1) w e r e a l s o u s e d f o r t h i s s t u d y t o make s i m u l a t e d SRS contaminated s o i l . The major d i f f e r e n c e between t h e two s i m u l a n t s used w a s t h e use of cer ium i n these s t u d i e s as a s table s imulan t fo r cesium, c o b a l t , and s t r o n t i u m . (Non- r a d i o a c t i v e cesium, cobalt, and s t r o n t i u m w e r e n o t r e a d i l y a v a i l a b l e , s i n c e cer ium had been used i n other mixed waste s t u d i e s as t h e s table r a d i o a c t i v e s imulan t , cer ium w a s used i n t h e s e s t u d i e s ) . Cyanide w a s n o t added s i n c e it w a s p r e s e n t i n such small amounts, and phenol was used as t h e o r g a n i c m a t e r i a l s u b s t i t u t e b e c a u s e o f t h e s t r i c t h a n d l i n g r e q u i r e m e n t s e n f o r c e d by S R S f o r t h e o r g a n i c s used by
Campbell and Buelt. Table 3 lists the oxide components of the soil. Approximately 500 grams of this simulated soil were made from reagent grade chemicals for the crucible studies.
P l a c e T a b l e 3 Here
The surrogate soil composition was plotted on three different ternary phase diagrams: Calcia-Alumina-Silica (CAS), Soda- Lime-Silica (SLS), and Borosilicate (BOR) . The types and amounts of additives necessary to make homogeneous glasses were determined based on the plots of the soil composition points. Several compositions were selected from each ternary diagram in order to try and maximize waste loading. Approximately 70 gram batches of the compositions shown in Table 4 were fabricated for testing, with the exception of BOR-7 and BOR-8 which were only 45 gram batches. After the batches were thoroughly mixed, they were placed in high purity (99.8%) alumina crucibles and covered. The crucibles were placed in a programmable Lindberg furnace and melted for 4 hours at 130OOC for BOR-4 and the CAS system glasses and 115OoC for the SLS and BOR system glasses. After 4 hours at temperature, the crucibles were removed from the furnace and air-cooled to room temperature.
P l a c e T a b l e 4 Here
After cooling, the glasses were separated from the crucibles and analyzed for chemical composition, phase assemblage, and durability. Standards were submitted with each set of samples to determine the accuracy of the results. The total constituent analysis of the glasses was performed using Inductively Coupled Plasma - Emission Spectroscopy (ICPES) and Atomic Absorption (AA) spectrometry. The organic content of the glass was not analyzed because analytical techniques available at SRS would have destroyed the organics because of the elevated temperatures necessary to digest the glasses. X-ray Diffraction (XRD) analysis was performed to determine the crystalline phase assemblage in the glass and Scanning Electron Microscopy (SEM) was used to confirm the XRD identification and chemical composition of the phases. Durability in an acidic environment was determined by performing the Toxicity Characteristic Leaching Procedure (TCLP), and the results were compared to the TCLP limits, the Resource Conservation and Recovery Act (RCRA) Land Disposal Limits, and the newly established Universal Treatment Standards (UTS), which became effective September 9, 1994.
The durability of the glass in an alkaline environment was determined by using the Product Consistency Test (PCT) per Jantzen et a1 ( 3 ) . This test evaluates the chemical durability of homogeneous and devitrified glasses by measuring the concentrations of the chemical species released from a crushed glass to a test solution. The PCT is only
r e q u i r e d f o r h igh- leve l w a s t e (HLW) g l a s s e s by t h e Department of Energy, b u t t h e r e s u l t s shou ld p rov ide a c o n s e r v a t i v e estimate of g l a s s d u r a b i l i t y f o r low- leve l mixed wastes (LLMW) g lasses . The r e s u l t s w e r e compared t o t h e E n v i r o n m e n t a l Assessment ( E A ) g l a s s P C T r e s u l t s as c h a r a c t e r i z e d by Jan tzen e t a l . (4), which are t h e acceptance c r i t e r i a fo r HLW g l a s s e s .
RESULTS AND DISCUSSION
A l l of t h e s i x t e e n b a t c h composi t ions melted produced dark green glass. H o w e v e r , e i g h t of t h e s i x t e e n w e r e covered wi th a w h i t e , c r u s t y l a y e r r a n g i n g i n t h i c k n e s s f r o m a f e w m i l l i m e t e r s t o several c e n t i m e t e r s . These inc luded b a t c h e s CAS-1,2,3 and BOR-1,2,3,5,6. Of t h e s e e i g h t , chemica l a n a l y s e s w e r e performed only on b a t c h CAS-3, which had t h e t h i n n e s t l a y e r . XRD and SEM showed t h e l a y e r t o be h igh i n s i l i ca , i n d i c a t i n g t h a t it w a s no t comple te ly reacted. I n o r d e r t o p r e v e n t t h e u n r e a c t e d s i l i c a l a y e r f r o m forming, N a 2 C 0 3 w a s s u b s t i t u t e d as an a d d i t i v e f o r a p o r t i o n of t h e CaC03, s i n c e N a acts a b e t t e r f l u x i n g agent for Si02.
The chemical compositions of t h e e i g h t glasses and glass CAS- 3 are g iven i n Table 5. R e s u l t s f o r Hg are no t i n c l u d e d i n t h e a n a l y s e s , s i n c e it was only d e t e c t e d i n trace amounts i n one of t h e glasses. CAS-5 c o n t a i n e d 4 9 pg/l, w h i l e t h e remain ing glasses c o n t a i n e d <30 pg/L. T h i s w a s expec ted s i n c e Hg i s known t o vapor i ze a t h igh t empera tu res . All of t h e measured compositions w e r e r ea sonab ly close t o t h e i r expec ted v a l u e s excep t f o r glasses CAS-3 and SLS-3. These d i f f e r e n c e s w e r e p robably due t o errors i n b a t c h i n g . S ince t h e ana lyzed composi t ions w e r e used fo r a l l of t h e f i n a l ana lyses , these errors w e r e no t of a g r e a t concern and would on ly a f f e c t what t h e a c t u a l waste loading would be. F igures 1 - 3 show t h e l o c a t i o n of t h e glasses on t h e a p p l i c a b l e t e r n a r y phase diagrams.
P l a c e T a b l e 5 Here
Place F i g u r e 1 Here
P l a c e F i g u r e 2 Here
Place F igure 3 Here
XRD a n a l y s i s w a s per formed i n d u p l i c a t e when s u f f i c i e n t q u a n t i t i e s of t h e sample w e r e a v a i l a b l e . The phases detected f o r each glass are shown i n Table 6 . The c r y s t a l l i n e phases p r e s e n t i n glass CAS-3 p robab ly came f r o m t h e u n r e a c t e d s i l i ca l a y e r . The q u a r t z and c r i s t o b a l i t e c r y s t a l s detected i n glasses BOR-4 and BOR-7 w e r e p r e s e n t i n minor amounts and did not seem t o affect d u r a b i l i t y . The SEM performed on t h e samples confirmed t h e f i n d i n g s of t h e XRD a n a l y s e s and did
not reveal the presence of any large peaks of carbon, which would have possibly served a s an indicator of the presence of organics i n the glass .
P l a c e T a b l e 6 Here
TCLP extractions were performed on the glasses according t o USEPA ( 5 ) , and t h e r e s u l t i n g leachates w e r e analyzed by I C P E S . The TCLP was performed on >150 p m crushed glass , w h i l e the standard EPA t e s t s a re u s u a l l y performed on larger s ize glass specimens (1 c m ) . Therefore, the resu l t s provided a conservative estimate of the leach resistance, since more glass surface area was exposed t o the leaching solution. T h e resu l t s for t h e applicable metals are shown i n Table 7 , along w i t h the appropriate l i m i t s .
Place T a b l e 7 Here
TCLP r e su l t s show tha t t h e measured releases were l e s s than the more conservative RCRA l i m i t s only fo r glasses SLS-1, SLS-2, and SLS-3. However, by applying t h e l i m i t s specified i n the TCLP and considering t h e conservative nature of t h i s t e s t , g l a s s e s CAS-5 and BOR-7 were a l s o considered acceptable. When the UTS l i m i t s were considered, a l l glasses m e t the Ag, Ba, and Pb l i m i t s , but on ly glasses SLS-1, SLS-2, and SLS-3 met a l l of the l i m i t s .
After t h e modified TCLP r e s u l t s were received, g l a s s monoliths of the samples were placed i n a c e t i c acid for 2 4 hours t o see how the glass in tegr i ty would be affected. T h i s t e s t simulated t h e TCLP leachant and surface area t o volume r a t i o more closely than t h e modified t e s t . None of t h e glasses showed any signs of degradation a f t e r 2 4 hours and t h e leachates had no de tec tab le amounts of RCRA metals released when analyzed by I C P E S . These observations lend support t o the be l i e f t h a t these glasses may have been acceptable i f t h e standard TCLP conditions were used, since the appropriate s i z e g lass specimen was used and no metals leached from the glass .
To assess the durabi l i ty i n a lkal ine conditions, t h e glasses were subjected t o the PCT as developed by Jantzen e t a l . (31, w h i c h measures the releases of B, Na, S i , and other elements i n ASTM Type I water over a period of seven days a t 90°C. Each glass was run i n t r i p l i c a t e for the PCT, and the resul ts were averaged and then normalized using t h e analyzed elemental compositions. The blanks and standard glasses run simultaneously w i t h t h e o t h e r g l a s ses showed t h a t no significant errors i n the t e s t ing method occurred.
The average normalized releases and the leachate pH are given i n Table 8 fo r each of t h e glasses and the EA glass p e r Jantzen e t a l . ( 4 ) . As can be seen from t h e r e su l t s , t h e normalized releases for a l l of t h e glasses w e r e substantially
less t h a n t h e EA glass . N o l i m i t e x i s t s fo r C e s i n c e it i s n o t a c r i t i ca l component of h igh - l eve l w a s t e glasses, b u t i t s releases are shown s i n c e it w a s t he radioactive s imulan t . C e releases w e r e v e r y s m a l l f o r a l l of t h e glasses. A l s o , though t h e y are n o t l i s t e d , t h e releases for t h e m e t a l s i n t h e glasses were measured and found t o be below o r n e a r d e t e c t i o n l i m i t s (<0.020 ppm Ag, <0.001 ppm B a , <0.001 ppm Cd, <0.004 ppm C r , <0.005 ppm N i , and <0.02 ppm P b ) . P l a c e T a b l e 8 Here
CONCLUSION
C r u c i b l e s t u d i e s w i t h s i m u l a t e d contaminated S R S s o i l have shown t h a t s o i l c a n be c o n v e r t e d t o a d u r a b l e , leach r e s i s t a n t glass wasteform. Three glasses i n t h e Soda-Lime- Si l ica sys t em (SLS-1, SLS-2, SLS-3) and one each i n t h e Calc ia -Alumina-Si l ica and B o r o s i l i c a t e sys t ems (CAS-5 and . BOR-7) passed a l l of t h e t e s t i n g c r i te r ia . Waste load ings o f up t o 58 w t % w e r e o b t a i n e d i n t h e SLS sys tem u s i n g g lass forming additives of CaC03 and N a 2 C 0 3 , up t o 4 8 w t % i n the CAS system u s i n g Al2O3, CaC03, and Na2C03, and up t o 4 3 w t % i n t h e BOR sys t em u s i n g C a C 0 3 , N a 2 C 0 3 , a n d b o r a x . H ighe r w a s t e l o a d i n g s may have b e e n p o s s i b l e i f h i g h e r m e l t i n g t e m p e r a t u r e s w e r e used, b u t t h a t w a s n o t per formed i n t h e scope of these s t u d i e s .
A d d i t i o n a l glass composi t ions may have a l so been accep tab le , b u t because o f t h e c o n s e r v a t i v e sample s i z e used t o perform t h e TCLP, t h e y w e r e n o t c o n s i d e r e d acceptable i n t h e s e s t u d i e s . For t h e modi f ied TCLP performed i n t h e s e s t u d i e s , t h e s u r f a c e area of glass t o volume of l e a c h a n t r a t i o w a s magni tudes greater t h a n it would have been f o r larger s i z e glass specimen. The fac t t h a t t h e s e glasses did n o t l e a c h any detectable amounts of RCRA m e t a l s i n t o t h e acetic acid s o l u t i o n s a f t e r 24 hours l e n d s proof t o t h e n o t i o n t h a t t h e glasses may have been a c c e p t a b l e .
ACKNOWLEDGMENTS
T h i s work w a s sponsored under t h e South C a r o l i n a U n i v e r s i t y Research and Educat ion Foundat ion, w h i c h w a s funded through c o n t r a c t AA009OOT. Funding fo r t h i s c o n t r a c t w a s p rovided by t h e Department of Energy - O f f i c e of Technology Development Mixed Waste I n t e g r a t e d Program under o p e r a t i n g c o n t r a c t N o . DE-ACO9-89SR18035.
REFERENCES
1. Campbell, B . E . ; B u e l t , J . L . I n S i t u V i t r i f i c a t i o n o f S o i l f r o m t h e Savannah R i v e r S i t e . Richland, WA: Pacific Northwest Laboratory, PNL-7421; 1990.
2. Looney, B.B.; Eddy, C.A.; Ramdeen, M.; Pickett, J.; Rogers, V.; Shirley, P.A.; Scott, M.T. Geochemical and Physical Properties of Soils and Shallow Sediments at the Savannah River Site. Aiken, SC: Westinghouse Savannah River Company, WSRC-RP-90-0464; 1990.
3. Jantzen, C.M.; Bibler, N.E.; Beam, D.C.; Ramsey, W . G . Nuclear Waste Glass Product Consistency Test (PCT) Method - Version 7.0. Aiken, SC: Westinghouse Savannah River Company, WSRC-TR-90-539, Revision 3; 1994.
4. Jantzen, C.M.; Bibler, N.E.; Beam, D.C.; Crawford, C.L.; Pickett, M.A. Characterization of the Defense Waste Processing Facility (DWPF) Environmental Assessment (EA) Glass Standard Reference Material. Aiken, SC: Westinghouse Savannah River Company, WSRC-TR-92-346, Rev. 1; 1993.
5. USEPA (United States Environmental Protection Agency) . Method 1131 Toxicity Characteristic Leaching Procedure (TCLP). 40 CFR 261 Appendix 11; 1991.
Table 1 - Composition of
Oxide
CaO
K 2 0 fio2
A 1 2 0 3
Fez03
N a 2 0 p205 Si02 S r O
T i 0 2 Z r 0 2 Total
Uncontaminated SRS Soil
Prv Basis (Wt%I 4 . 8 0.4 0.77 0.13 0.01 0 . 0 5 1.12
92.5 0.001 0.4 Q.09
100.271
Table 2 - Concentrations of Hazardous and Radionuclide Simulant s
Inorganic - As Ba Cd Ce cs c1 Cr co cu CN F Pb Hg Ni Ag Sr NO3 PO4 3 3 4
Bis (2-ethylhexyl) Phthalate
Methylene Chloride1
\
Concentration QQau
5 310 210 2700 450 310 2500 450 190 15 3 320 60 370 40
4500 1700 1800 1100 340
70
Table 3 - Surrogate Soi l Composition
Oxide
A 1 2 0 3 A920
BaO C a O CdO
C e 0 2 C r 2 0 3
CUO Fez03 HgO K 2 0 m02 N a 2 0 NiO p 2 0 5 PbO
S i 0 2 T i 0 2 Z r02
Total
So i l Wt? 0.004 4.696 0.034 0 .391 0.023 1.375 0.357 0.023 0.753 0.006 0.127 0.010 0.049 0.046 1 . 0 9 6 0.034
90.496 0 .391 0.088
99.999
Table 4 - Batch Compositions By Weight Percentages
Batch CAS - 1 CAS-2 CAS-3 CAS-4 CAS - 5 SLS-1 SLS-2 SLS-3 BOR- 1 BOR-2 BOR-3 BOR- 4 BOR-5 BOR- 6 BOR-7 BOR-8
soil 50 58 40 40 48 55 58 55 50 50 45 50 43 52 43 43
U Q 3 10 7 15 15 7 0 0 0
N/A N/A N/A N/A N/A N/A N/A N/A
-3 40 35 45 2 5 30 20 17 15 2 5 20 25 25 17 15 10 15
-2% 0 0 0 20 15 25 25 30 0 0 0 0 0 0 7 1 0
Borax N/A N/A N/A N/A N/A N/A N/A N/A 25 30 30 25 40 33 40 32
Table 5 - Oxide Composition of the Soil Glasses
Oxide A g 2 0
A 1 2 0 3 B 2 0 3 B a O C a O CdO
C e 0 2 C r 2 0 3
CUO F e 2 0 3
K20 m02 Na2O N i O p 2 0 5 P b O Si02 T i 0 2 Z r02 Total
- 0.003 2 - 2 0 1 0.017 0.034
12.926 0.014 0.470 0 .341 0.001 1 .175 0.074 0.010 0 . 1 1 4 0.116 1.154 0 . 0 3 1
81.087 0.194 Q.041
100.003
GA&A 0.002
23.095 0.013 0.029
16.589 0.001 0.378 0.072 0 . 0 0 1 1.518 0.045 0.028
13.620 0.096 1.107 0.023
44.569 0.217 0.057
101 .461
CAS-5 0.002
14.308 0 . 1 0 1 0.057
20.444 0.010 0.404 0.154 0.018 3 . 0 8 1 0.050 0 .051
1 0 . 2 2 1 0.230 1 . 4 1 1 0.074
53.570 0.276 iLcu22
104 .531
sLs-1 0.002 2.140 0 .013 0.019
13.752 0.004 0.586 0.175 0.001 0.585 0.084 0.001
17.300 0.048 0.816 0.024
63.588 0.160 0.032
99.330
515-2 0.002 1.847 0.013 0.025
11 .491 0.013 0 . 3 0 1 0.297 0 .001 1.194 0.090 0.012
1 7 . 1 7 1 0.126 0.912 0.020
66.487 0.159 Q.034
100.203
_Oxide A 9 2 0
A 1 2 0 3 B 2 0 3 BaO C a O CdO
C e 0 2 C r 2 0 3
CUO Fe203
K20 M O 2 Na2O N i O p 2 0 5 P b O S i 0 2 T i 0 2 Z r 0 2 Total
sLs-3 0.002
18.034 0.010 0 .011
25.237 0.001 0.164 0.160 0 . 0 0 1 0.659 0.073 0.005
17.142 0.079 0.488 0.019
37.803 0.087 0.023
99.998
BOR-4 0.006
10.235 12.030
0.026 18.296
0.005 0.634 0.199 0.001 0.823 0.083 0.005 5.350 0.050 1.524 0.023
51.549 0.299 m
101.222
BOR-7 0.002 7.973
1 9 . 4 0 1 0.057 7.618 0.008 0.369 0.104 0.017 2.170 0.047 0.044
13.279 0.143 1.405 0.064
50.300 0.292 0.074
103.367
BOR-8 0 * 002
10.353 1’6.446
0.033 1 2 . 0 1 1
0.008 0.437 0.097 0.010 1.922 0.043 0 .030
14.767 0.122 1 .446 0.062
42.768 0.305 0.073
100.936
F i g u r e 1 - C a O - A l 2 0 3 - S i 0 2 T e r n a r y D i a g r a m
SiO,
1 O O A O Dunreacted Layer
A Did Not Meet TCLP Limits
+ Passed All Limits i3 Expected Position of CAS-:
I Simulated soil
0 Na2 0
Figure 2 - NagO-CaO-Si02 Ternary Diagram
CaO
fJ Expected Pos i t ion of SLS-3
Extended Glass Forming Region
Known Glass Forming Region
Si02 + Also3 100 90 80 70 60 50 40 30 20 10 0
Figure 3 - Borosil icate Ternary Diagram
Si02 0 Unreacted Layer
A Did Not Meet TCLP L i m i t s
+ Passed All L i m i t s Pyrex Glasses
Known Homogeneous 8 Simulated s o i l Waste Glass Regio
Known Region 4 0 of Glass Phase
Separation
Known Glass Forming Regi
+ RO
Table 6 - XRD Phase Assemblage Results
Batch CAS-3
CAS-4 CAS-5 SLS-1 SLS-2 SLS-3 BOR-4
BOR-7 BOR-8
VSlS 1 0.3 wt% Quartz
0.4 wt% Gehlenite
Amorphous Amorphous Amorphous Amorphous Amorphous
1.6 wt% Quartz 0.9 wt% Cristobalite
0.1 wt% Quartz Amorphous
VSlS 2 0.2 wt% Quartz
0.5 wt% Gehlenite 0.1 wt% Anorthite
Amorphous Amorphous Amorphous Amorphous Amorphous
2.0 wt% Quartz 0.8 wt% Cristobalite
N/A N/A
Batch CAS-3 CAS-4 CAS-5 SLS-1 SLS-2 SLS-3 BOR-4 BOR-7 BOR-8
T a b l e 7 - TCLP R e s u l t s (mg/L)
ao: <o. 020 <o -020 <0.020 K O . 020 <o " 020 <o .020 <o .020 <o .020 0.269
Ba 1.540 6.265 3.607 0.549 0.527 0.527 2.441 1.581 4.807
ai 0.720 1.102 0.088
<o. 010 <o. 010 0.012 0.914 0.947 1.700
4x Ki 9.530 1.436 15.777 1.934 1.234 0.113
<O .040 < O . 050 < O . 040 <O. 050 0.103 <0.050 8.440 1.464 3.918 1.104 13.163 1.646
RCRA L i m i t 0.072 TCLP L i m i t 5 UTS L i m i t 0.30
N/A 100 7.6
0.066 1.00 0.19
5.2 5.00 0.86
0.32 N/A 5.00
€ 2 2 1.989 4.694
<o. 200 <o .200 <o . 200 <o . 200 1.770 1.548 2.675
0.51 5.00 0.37
Table 8 - Normalized PCT Results (g/L)
Batch CAS-3 CAS-4 CAS-5 SLS-1 SLS-2 SLS-3 BOR-4 BOR-7 BOR-8
EA
B 0.000 0.000 0.000 8.335 3.612 2.898 0.190 1.905 0.559
H A 0.296 0.321 0.276 3.345 4.346
0.189 1.829 0.643
9.418
16.695 13.346
si 0.033 0.087 0.076 0.589 0.770 3.150 0.050 0.462 0.064
3.922
sh 0.008 0.019 0.010 0.095 0.136 0.247 0.006 0.011 0,009
N/A
PEZ 10.75 10.86 10.73 12.10 12.18 12.45 10.10 9.62 10.14
11.91