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ADSORPTION, CO-CRYSTALLIZATION AND ION EXCHANGE
   AS MECHANISMS FOR TECHNETIUM DISPOSITION
  IN SEVERAL SAVANNAH RIVER SITE WASTE TANKS

                           •   K.Guerman, C. Delegard*, D. Hobbs**
                           •   A. Ananiev, N. Budantseva,
                           •   A. Fedoseev, S.Nikitenko,
                           •   N. Popova, V. Shilov,
                           •   V. Silin, V. Tarasov

Institute of Physical Chemistry of Russian Academy of Sciences
               (Moscow, Leninsky pr.31, 119991,Russia)
          * - Pacific Northwest National Laboratory,
                 (Richland, Washington 99352 U.S.A.)
                   **- Savannah River Site,
Institute of Physical Chemistry
              Russian Academy of Sciences
                                                              D ir e c t io n
                                              ( E le c t io n s N o v e m b . 2 0 0 1 )

   D e p a rtm e n t         D e p a rtm e n t          D e p a rtm e n t             D e p a rtm e n t        D e p a rtm e n t
   S u r f a c e S c i.       C o llo id S c i.       R a d io c h e m is t r y      P o ly m e r S c i.      C o r r o s io n S c i.
           250                  2 5 0 re s .                3 5 0 re s                      300                        300

Lab.               Lab.           Lab.               Lab.                Lab.               Lab.            Lab.                 Lab.
TUE                 EX            RCH                 IX                IN J - 1          R A D -1         C a t a l.          S O L ID

Lab.           G RO UP        G RO UP             G RO UP                Lab.               Lab.             Lab.               Lab.
TP uE           E L .C H .    RCH&EC                 Tc                 IN J - 2          R A D -2         F IL T R .          ANAL.

                Collaboration with US/DOE (Hanford, Savannah River and other
                      sites) was very important for IPC RAS in 1993-2001
Tc concentrations found in
     99

     various tank sludges at SRS

                                                [Tc-99],
The discovery of relatively high    Tank       mCi/g dried      Reference
      99
         Tc concentrations in      Number        solids
inorganic mineral sludge heels       17          0.462       d'Entremont et
 taken from some tanks at the                                al. 1997
US-DOE Savannah River Site         20, white      0.34       d'Entremont and
       (SRS) has prompted            solids                  Hester 1996
  investigations of Tc uptake      20, brown      0.94       d'Entremont and
   from alkaline highly active       solids                  Hester 1996
      waste (HAW) by solid             42         0.22       Hay 1999
             adsorbents
                                      51          0.21       Hay 1999
                                      8           0.22       Hay 1999
                                      11          0.34       Hay 1999
The SRS waste volumes (Table 2.4 of "Integrated Database Report - 1993:
   S.Spent Fuel and Radioactive Waste Inventories, Projections, and
         Characteristics,”] Tc-99 quantities (Table 2.11), and
           Tc-99 concentrations calculated from these data


                Volume,    Tc-99, Ci   [Tc-99],       [Tc], 106 Kd
                 liters                 Ci/liter       g/liter   total


Liquid          61.4      1.68E+04     2.74E-03       0.162          -
Sludge           13.9      1.14E+04    8.20E-03       0.483          3
Salt Cake        53.8      2.78E+03    5.17E-04       0.0305         0.2
Overall waste   129.1     3.098E+04    2.40E-03       0.141           -

Question to be studied : Which components absorb Tc with Kd
  higher than 3 and are resistant to leaching?
Sludge components as carriers
     for Tc(VII) and Tc(IV)
             S O L ID S L U D G E C O M P O N E N T S

            W H IT E S O L ID S                  B R O W N S O L ID S


      A L U M IN O S IL IC A T E S            M E T A L H Y D R O X ID E S
            C A N C R IN IT E                   (F e , C r, M n )(O )(O H )
             S O D A L IT E


        .     C R Y O L IT E      .       .     P L A T IN U M G R O U P      .
                N a 3 A lF 6                           M E T A L S
                                                      R h, R u, P d


  .    S O D IU M O X A L A T E       .
             N a 2C 2O 4

      TiO2 was also tested
Experimental conditions for
     precipitation and leaching tests:
        Precipitation tests:                     Leaching modes:
    Wastes are alkaline                  Surface leaching.
    Tc is redox sensitive                Complete dissolution.
    Sharp differences in the                     Leaching agents
     redox potential within the           all precipitates : 0.1N NaOH
     tanks are observed,
                                          aluminosilicates - NaHF2
              So, both:
     oxidizing [Tc(VII)]                 Na oxalate - 0.1N NaOH, NaNO2
     and reducing [Tc(IV)]               FeOOH - 0.1N NaOH, H2O2
    conditions were tested in            MnOOH - 0.1N NaOH, H2O2
     0.1- 5 N NaOH + 0-5 N NaOH.
                                          TiO2 - 0.1- 3N NaOH
    Methods: Liquid scintillation counting (LSC) of solutions, XRD, NMR, IR
Study of Tc uptake with Aluminosilicates
  under oxidizing conditions at 70-130oC
 Literature data have demonstrated the possibility of
ClO4- and MnO4- co-crystallisaton with aluminosilicates :
purple Na8[AlSiO4]6(MnO4)2 (Weller,1999 etc.)

OUR EXPERIMENTS on TcO4- (reaction: NaAlO2+Na2SiO3+NaOH)
   Solution      Formed solid        Kd
                                                 TcO4- is too large
 10-3-10-5M Tc                                  and therefore it is
 0.2-5M NaOH      Cancrinite        less 1
0.5-5 M NaNO3
                                                excluded from the
                                                 aluminosilicate
 10-3-10-5M Tc                                  structure in both
 0.2-5M NaOH       Sodalite         less 1
  NaNO3 free
                                                  cancrinite and
                                                     sodalite
Case of Aluminosilicates formed
    in concentrated Tc(VII) solution
   [Tc] = 0.2 M                            Fig. 1. NMR-99Tc spectrum of the aluminosilicate containing

   in NaNO3 solutions - cancrinite         57 mg-Tc/kg. Tc spectrum presents evidence for -30 ppm shift

                                                     characteristic of coordinated pertechnetate
   in NaNO3-free solutions - sodalite
   Although NMR spectrum presented
    shift typical for coordinated Tc(VII)
    its concentration is very low

   Dissolution in NaHF2 and LSC has
    shown : [Tc] in solid cancrinite was
    57 mg/kg ~ 100 times less than in
    initial solution

   Tc is excluded from the
    aluminosilicate structure
Study of Tc uptake with Aluminosilicates under
               reducing conditions
     (0.2M N2H5Cl, 1M NaNO3, T = 800С, t = 3 d)

 Precipitation of                   Leaching conditions:
   cancrinite↓
                       Leaching      T,         Leaching yield , Tc, %
NaOH      Tc yield,     agent:       o
                                      C
                                                3      1 day      10 days
 M           %
                                              hour
 2.0        18.9       1M NaOH       20        0.8          1       3.7
 4.0         32        2M NaOH       20        0.8         1.2      2.0
 2.0        25.2      0.1M NaOH +    60        25          26.9     27
                      0.25 M H2O2
 2.0        18.9      0.1M NaOH +    18        4           6.9       7
                         0.5 H2O2
 4.0         32       0.1M NaOH +    18        6.5         6.9      11
                         0.5 H2O2
Under reducing conditions Tc uptake is important
Tc(IV) in aluminosilicates is resistant to leaching
Study of Tc(VII) sorption
           by crystalline TiO2
        under oxidizing conditions

   Tc(VII) was sorbed by TiO2
    from neutral solution
    with Kd = 30 ml/g.
   However, the Kd at pH=10
    was only 3.3 ml/g                     Among the
   No affinity to Tc(VII) was     minerals tested for
    noted for TiO2 at pH=12            Tc(VII) uptake,
    and higher .                     high-density TiO2
         MST and Silicotitanates        was the most
         yet not tested ..?                  efficient
Study of Tc uptake with
         Na oxalate under
 oxidizing and reducing conditions

NaOH + H2C2O4 = Na2C2O4
  X-ray diffraction tests :
        the precipitate is
 sodium oxalate Na2C2O4
           (PDF#20-1149)

   Tc(VII) is excluded from the Na oxalate structure
    under oxidizing conditions (Kd = 1-2)
   Under reducing conditions Tc(IV) forms a separate
    TcO2*1.6H2O phase - no interaction between Tc
    hydroxide and Na oxalate were detected
   Tc precipitate is not resistant to leaching with 0.1 N
    NaNO2
Study of Tc uptake with
          Cryolite Na3AlF6 under
    oxidizing and reducing conditions

           6F-+NaAlO2+Na2CO3
                X-ray diffraction tests :
    the precipitate is cryolite Na3AlF6

   Reduced Tc :                               Oxidizing
                                                conditions:
   17-35% of Tc(IV) as
    TcCl62- is co-                             Kd is less 1
    precipitated with
    cryolite                                   Tc(VII) is excluded
   N2H5NO3 inhibits co-                        from cryolite
                                                structure
    precipitation
Study of Tc(IV) uptake
           with Cryolite Na3AlF6
         under reducing conditions
          [NH4F]      [Na2CO3] in      [N2H5NO3], in      Tc(IV)
    No    initial,   final solution,   final solution,   uptake,
            M               M                 M             %

     1      2,0           0,6                -             20
     2      2.5           0.6                -             23
     3      3.0           0,6                -             26
     4      4,0           0.6                -             28
     5      6,0           0,6                -             35
     8      2,0           0,4                -             25
     9      2,0           0,8                -             17
    10      2,0           0,6               0,1             0

• Tc(IV) is added as Na2TcCl6 to (NH4F+NaAlO2) solution
• No additional reducing agent in exp. No 1-9
• Leaching test were impossible to quantify relative to
real cryolite in tanks as complete peptization occurred.
Study of Tc(IV) uptake with
  FeOOH under reducing conditions
  Reducing agent: 0.02M FeSO4, T = 600С, time = 3 h
  Precipitate : FeOOH/Fe2O3
         Precipitation test:      Leaching test (t=18 oC, d = days):
       NaOH      Tc in solid    Leaching      Leaching yield ,Tc, %
        M         phase, %       agent:       1 d 10 d 29 d 105d
        0.6           97       0.1M NaOH      1.0    9.8 14.9          24
        2.0          88.0      1M NaOH        2.9 16.5 40.2            58
        4.0           90       2M NaOH        0.8     2      3         8.2
  Though Tc adsorbed better on iron hydroxides from 0.5–2.0 M NaOH
   than from 3.0-4.0 M NaOH, the precipitates formed at lower NaOH
      concentration were more easily leached by the NaOH leachant
Tc leaching with H2O2 was 20 % and with Na2S2O8 was70-100% in 100 days
Study of Tc(IV) uptake with
MnOOH under reducing conditions
     Reaction NaOH + Na2MnO4+ N2H5OH= MnOOH
    X-ray diffraction tests : the freshly precipitated
         solid was Mn2O3 , the aged precipitate was
                   manganite MnOOH (PDF#18-805)
                                                   MnOOH precipitation                   MnOOH leaching to 0.1 NaOH (1,3,4) and Na2S2O8(2)
                                                                                                           12
                                                                                                                    1) Mn/Al=1/10
                                      90                                                                            2) Mn/Al=1/40
                                                                                                           10
                                                                                                                    3)Mn/Al=1/10
                                      75
        Tc uptake by precipitate, %




                                                                                                            8       4) Mn/Al=1/40




                                                                                           Leached Tc, %
                                      60
                                                                       Mn/Al=1/10                           6
                                      45

                                      30                               Mn/Al=1/40                           4

                                      15                                                                    2

                                       0
                                                                                                            0
                                           0   5    10    15      20        25      30
                                                                                                                0     2        4       6      8   10   12
                                                         Time,d                                                                     Time. d




 Manganese(III) oxides were effective Tc carriers and underwent
chemical transformations on ageing that increased leaching resistance
to most agents.
What additional work is necessary to clarify
      results obtained in the present work
   It is still possible that some polymeric inorganics involving larger ions
    (like titanium, forming hydroxides, complex titanates and Silicotitanates)
    could be better sorbents for TcO4-, - additional tests of different (Ti?)
    compounds could explain some cases of Tc presence in sludge, and
    possibly result in efficient inorganic Tc(VII)-sorbent for long-term storage.
   Tests of the Tc/Fe hydroxide co-precipitate formed at 4M NaOH could be
    continued aiming to demonstrate the nature of the precipitate and its
    stability domain. EXAFS/XANES, Tc-NMR and γ -resonance spectroscopy
    could be useful for Tc speciation under these conditions.
   Co-precipitation tests could be continued with the transition metal
    hydroxide mixtures (Fe/Ti, Mn/Al, Ti/Cr, Ti/Zr and others) as these could
    provide higher affinity to reduced technetium, or even Tc(VII) and higher
    resistance to leaching. Tc speciation experiments in these cases are
    desirable.
Acknowledgements
• This work was supported by the U.S. Department of Energy Under a
  contract to the Institute of Physical Chemistry RAS by the Office of
  Environmental Management, Efficient Separations and Processing
  Cross cutting Program.

• We recognize the organizational skill of Dr. M. Khankhasaev in
  contract implementation, Liliya Petrachenkova (SAIC), Dr. V.
  Polyanichko, IPC financial manager Edouard German and RAS corr.-
  member A.K. Pikaev for administrative assistance.


• We are thankful to Dr.D. Hobbs for his encouraging attention to this
  work, useful discussions and elaboration of the experimental program

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Doklad usa-tc

  • 1. ADSORPTION, CO-CRYSTALLIZATION AND ION EXCHANGE AS MECHANISMS FOR TECHNETIUM DISPOSITION IN SEVERAL SAVANNAH RIVER SITE WASTE TANKS • K.Guerman, C. Delegard*, D. Hobbs** • A. Ananiev, N. Budantseva, • A. Fedoseev, S.Nikitenko, • N. Popova, V. Shilov, • V. Silin, V. Tarasov Institute of Physical Chemistry of Russian Academy of Sciences (Moscow, Leninsky pr.31, 119991,Russia) * - Pacific Northwest National Laboratory, (Richland, Washington 99352 U.S.A.) **- Savannah River Site,
  • 2. Institute of Physical Chemistry Russian Academy of Sciences D ir e c t io n ( E le c t io n s N o v e m b . 2 0 0 1 ) D e p a rtm e n t D e p a rtm e n t D e p a rtm e n t D e p a rtm e n t D e p a rtm e n t S u r f a c e S c i. C o llo id S c i. R a d io c h e m is t r y P o ly m e r S c i. C o r r o s io n S c i. 250 2 5 0 re s . 3 5 0 re s 300 300 Lab. Lab. Lab. Lab. Lab. Lab. Lab. Lab. TUE EX RCH IX IN J - 1 R A D -1 C a t a l. S O L ID Lab. G RO UP G RO UP G RO UP Lab. Lab. Lab. Lab. TP uE E L .C H . RCH&EC Tc IN J - 2 R A D -2 F IL T R . ANAL.  Collaboration with US/DOE (Hanford, Savannah River and other sites) was very important for IPC RAS in 1993-2001
  • 3. Tc concentrations found in 99 various tank sludges at SRS [Tc-99], The discovery of relatively high Tank mCi/g dried Reference 99 Tc concentrations in Number solids inorganic mineral sludge heels 17 0.462 d'Entremont et taken from some tanks at the al. 1997 US-DOE Savannah River Site 20, white 0.34 d'Entremont and (SRS) has prompted solids Hester 1996 investigations of Tc uptake 20, brown 0.94 d'Entremont and from alkaline highly active solids Hester 1996 waste (HAW) by solid 42 0.22 Hay 1999 adsorbents 51 0.21 Hay 1999 8 0.22 Hay 1999 11 0.34 Hay 1999
  • 4. The SRS waste volumes (Table 2.4 of "Integrated Database Report - 1993: S.Spent Fuel and Radioactive Waste Inventories, Projections, and Characteristics,”] Tc-99 quantities (Table 2.11), and Tc-99 concentrations calculated from these data Volume, Tc-99, Ci [Tc-99], [Tc], 106 Kd liters Ci/liter g/liter total Liquid 61.4 1.68E+04 2.74E-03 0.162 - Sludge 13.9 1.14E+04 8.20E-03 0.483 3 Salt Cake 53.8 2.78E+03 5.17E-04 0.0305 0.2 Overall waste 129.1 3.098E+04 2.40E-03 0.141 - Question to be studied : Which components absorb Tc with Kd higher than 3 and are resistant to leaching?
  • 5. Sludge components as carriers for Tc(VII) and Tc(IV) S O L ID S L U D G E C O M P O N E N T S W H IT E S O L ID S B R O W N S O L ID S A L U M IN O S IL IC A T E S M E T A L H Y D R O X ID E S C A N C R IN IT E (F e , C r, M n )(O )(O H ) S O D A L IT E . C R Y O L IT E . . P L A T IN U M G R O U P . N a 3 A lF 6 M E T A L S R h, R u, P d . S O D IU M O X A L A T E . N a 2C 2O 4 TiO2 was also tested
  • 6. Experimental conditions for precipitation and leaching tests: Precipitation tests: Leaching modes:  Wastes are alkaline  Surface leaching.  Tc is redox sensitive  Complete dissolution.  Sharp differences in the Leaching agents redox potential within the  all precipitates : 0.1N NaOH tanks are observed,  aluminosilicates - NaHF2 So, both:  oxidizing [Tc(VII)]  Na oxalate - 0.1N NaOH, NaNO2  and reducing [Tc(IV)]  FeOOH - 0.1N NaOH, H2O2  conditions were tested in  MnOOH - 0.1N NaOH, H2O2 0.1- 5 N NaOH + 0-5 N NaOH.  TiO2 - 0.1- 3N NaOH Methods: Liquid scintillation counting (LSC) of solutions, XRD, NMR, IR
  • 7. Study of Tc uptake with Aluminosilicates under oxidizing conditions at 70-130oC  Literature data have demonstrated the possibility of ClO4- and MnO4- co-crystallisaton with aluminosilicates : purple Na8[AlSiO4]6(MnO4)2 (Weller,1999 etc.) OUR EXPERIMENTS on TcO4- (reaction: NaAlO2+Na2SiO3+NaOH) Solution Formed solid Kd  TcO4- is too large 10-3-10-5M Tc and therefore it is 0.2-5M NaOH Cancrinite less 1 0.5-5 M NaNO3 excluded from the aluminosilicate 10-3-10-5M Tc structure in both 0.2-5M NaOH Sodalite less 1 NaNO3 free cancrinite and sodalite
  • 8. Case of Aluminosilicates formed in concentrated Tc(VII) solution  [Tc] = 0.2 M Fig. 1. NMR-99Tc spectrum of the aluminosilicate containing  in NaNO3 solutions - cancrinite 57 mg-Tc/kg. Tc spectrum presents evidence for -30 ppm shift characteristic of coordinated pertechnetate  in NaNO3-free solutions - sodalite  Although NMR spectrum presented shift typical for coordinated Tc(VII) its concentration is very low  Dissolution in NaHF2 and LSC has shown : [Tc] in solid cancrinite was 57 mg/kg ~ 100 times less than in initial solution  Tc is excluded from the aluminosilicate structure
  • 9. Study of Tc uptake with Aluminosilicates under reducing conditions (0.2M N2H5Cl, 1M NaNO3, T = 800С, t = 3 d) Precipitation of Leaching conditions: cancrinite↓ Leaching T, Leaching yield , Tc, % NaOH Tc yield, agent: o C 3 1 day 10 days M % hour 2.0 18.9 1M NaOH 20 0.8 1 3.7 4.0 32 2M NaOH 20 0.8 1.2 2.0 2.0 25.2 0.1M NaOH + 60 25 26.9 27 0.25 M H2O2 2.0 18.9 0.1M NaOH + 18 4 6.9 7 0.5 H2O2 4.0 32 0.1M NaOH + 18 6.5 6.9 11 0.5 H2O2 Under reducing conditions Tc uptake is important Tc(IV) in aluminosilicates is resistant to leaching
  • 10. Study of Tc(VII) sorption by crystalline TiO2 under oxidizing conditions  Tc(VII) was sorbed by TiO2 from neutral solution with Kd = 30 ml/g.  However, the Kd at pH=10 was only 3.3 ml/g  Among the  No affinity to Tc(VII) was minerals tested for noted for TiO2 at pH=12 Tc(VII) uptake, and higher . high-density TiO2 MST and Silicotitanates was the most yet not tested ..? efficient
  • 11. Study of Tc uptake with Na oxalate under oxidizing and reducing conditions NaOH + H2C2O4 = Na2C2O4 X-ray diffraction tests : the precipitate is sodium oxalate Na2C2O4 (PDF#20-1149)  Tc(VII) is excluded from the Na oxalate structure under oxidizing conditions (Kd = 1-2)  Under reducing conditions Tc(IV) forms a separate TcO2*1.6H2O phase - no interaction between Tc hydroxide and Na oxalate were detected  Tc precipitate is not resistant to leaching with 0.1 N NaNO2
  • 12. Study of Tc uptake with Cryolite Na3AlF6 under oxidizing and reducing conditions 6F-+NaAlO2+Na2CO3 X-ray diffraction tests : the precipitate is cryolite Na3AlF6  Reduced Tc :  Oxidizing conditions:  17-35% of Tc(IV) as TcCl62- is co-  Kd is less 1 precipitated with cryolite  Tc(VII) is excluded  N2H5NO3 inhibits co- from cryolite structure precipitation
  • 13. Study of Tc(IV) uptake with Cryolite Na3AlF6 under reducing conditions [NH4F] [Na2CO3] in [N2H5NO3], in Tc(IV) No initial, final solution, final solution, uptake, M M M % 1 2,0 0,6 - 20 2 2.5 0.6 - 23 3 3.0 0,6 - 26 4 4,0 0.6 - 28 5 6,0 0,6 - 35 8 2,0 0,4 - 25 9 2,0 0,8 - 17 10 2,0 0,6 0,1 0 • Tc(IV) is added as Na2TcCl6 to (NH4F+NaAlO2) solution • No additional reducing agent in exp. No 1-9 • Leaching test were impossible to quantify relative to real cryolite in tanks as complete peptization occurred.
  • 14. Study of Tc(IV) uptake with FeOOH under reducing conditions  Reducing agent: 0.02M FeSO4, T = 600С, time = 3 h  Precipitate : FeOOH/Fe2O3 Precipitation test: Leaching test (t=18 oC, d = days): NaOH Tc in solid Leaching Leaching yield ,Tc, % M phase, % agent: 1 d 10 d 29 d 105d 0.6 97 0.1M NaOH 1.0 9.8 14.9 24 2.0 88.0 1M NaOH 2.9 16.5 40.2 58 4.0 90 2M NaOH 0.8 2 3 8.2 Though Tc adsorbed better on iron hydroxides from 0.5–2.0 M NaOH than from 3.0-4.0 M NaOH, the precipitates formed at lower NaOH concentration were more easily leached by the NaOH leachant Tc leaching with H2O2 was 20 % and with Na2S2O8 was70-100% in 100 days
  • 15. Study of Tc(IV) uptake with MnOOH under reducing conditions  Reaction NaOH + Na2MnO4+ N2H5OH= MnOOH X-ray diffraction tests : the freshly precipitated solid was Mn2O3 , the aged precipitate was manganite MnOOH (PDF#18-805) MnOOH precipitation MnOOH leaching to 0.1 NaOH (1,3,4) and Na2S2O8(2) 12 1) Mn/Al=1/10 90 2) Mn/Al=1/40 10 3)Mn/Al=1/10 75 Tc uptake by precipitate, % 8 4) Mn/Al=1/40 Leached Tc, % 60 Mn/Al=1/10 6 45 30 Mn/Al=1/40 4 15 2 0 0 0 5 10 15 20 25 30 0 2 4 6 8 10 12 Time,d Time. d  Manganese(III) oxides were effective Tc carriers and underwent chemical transformations on ageing that increased leaching resistance to most agents.
  • 16. What additional work is necessary to clarify results obtained in the present work  It is still possible that some polymeric inorganics involving larger ions (like titanium, forming hydroxides, complex titanates and Silicotitanates) could be better sorbents for TcO4-, - additional tests of different (Ti?) compounds could explain some cases of Tc presence in sludge, and possibly result in efficient inorganic Tc(VII)-sorbent for long-term storage.  Tests of the Tc/Fe hydroxide co-precipitate formed at 4M NaOH could be continued aiming to demonstrate the nature of the precipitate and its stability domain. EXAFS/XANES, Tc-NMR and γ -resonance spectroscopy could be useful for Tc speciation under these conditions.  Co-precipitation tests could be continued with the transition metal hydroxide mixtures (Fe/Ti, Mn/Al, Ti/Cr, Ti/Zr and others) as these could provide higher affinity to reduced technetium, or even Tc(VII) and higher resistance to leaching. Tc speciation experiments in these cases are desirable.
  • 17. Acknowledgements • This work was supported by the U.S. Department of Energy Under a contract to the Institute of Physical Chemistry RAS by the Office of Environmental Management, Efficient Separations and Processing Cross cutting Program. • We recognize the organizational skill of Dr. M. Khankhasaev in contract implementation, Liliya Petrachenkova (SAIC), Dr. V. Polyanichko, IPC financial manager Edouard German and RAS corr.- member A.K. Pikaev for administrative assistance. • We are thankful to Dr.D. Hobbs for his encouraging attention to this work, useful discussions and elaboration of the experimental program