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PREVENTION OF RADIOACTIVE AND SOME OTHER CONTAMINANTS PROPAGATION INTO THE GROUNDS BY SHSMETHOD

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Title: PREVENTION OF RADIOACTIVE AND SOME OTHER CONTAMINANTS PROPAGATION INTO THE GROUNDS BY SHSMETHOD


1
PREVENTION OF RADIOACTIVE AND SOME OTHER
CONTAMINANTS PROPAGATION INTO THE GROUNDS BY
SHS-METHOD
  • G. KSANDOPULOa, A. BAIDELDINOVAb,
  • S. KARTKUZHAKOVb
  • G. XANTHOPOULOUc,
  • a. ICP, Almaty - Kazakhstan
  • b. "Floga" company, Almaty - Kazakhstan
  • c. Demokritos Institute - Athens - Greece 

Athens, 8-9 October 2008
2
MAIN PURPOSE
  • Processing of greater amounts of polluted
    components for utilization of radioactive and
    chemically dangerous wastes and neutralization of
    polluted materials, for prevention their
    migration into the soil and to adjacent ambiences
    (atmosphere and hydrosphere)

3
Methods of radioactive and chemically dangerous
wastes isolation
  • Immobilization into phosphate and borosilicate
    glasses (do not prevent radionuclides penetration
    into the environment in the case of long- term
    burial)
  • Obtaining matrix materials (mineral-like
    ceramics analogs rock forming minerals is more
    stable thermodinamically than glasses)
  • Cold pressing with following annealing
  • Hot pressing
  • Synthesizing from melt
  • All this 3 methods connected with complicate
    equipment, heat- and corrosion-resistant
    materials for crucibles, high energy consumption
  • 4. SHS (technological simplicity, absence of
    external heating sources and complicate equipment)

4
MAIN IDEA
  • Agglomeration of the ground in separate matrixes
    by means of a binding agent (10- solution of
    sodium tetraborate (Na2B2O4 4H2O) and 10-
    solution of sodium tetraborate with sodium
    monosilicate (Na2B2O4 4H2O Na2SiO3 9H2O)
  • Packing them into natural reactors (pits,
    trenches)
  • Filling the empty spaces between them with the
    charge of welding mixture (combustible mixture,
    composed of metal oxide and a reducer, for
    example, powdered aluminium)
  • Initiation of combustion in the wave regime.

5
Main components of the soil samples taken in the
Semipalatinsk region of Kazakhstan
Also Al2(Si,Al)4O10(OH)2, chamozit (Fe,
Mg,Mn,Al)6(Si,Al)4O10 , amorphous phase
6
The chemical composition of the model material
7
The optimum diameters of sphere agglomerates for
any welding mixture
  • k is the reactor space factor ( ratio of
    agglomerates volume (4/3 p r3 . n) to total
    volume off reactor),
  • ?a is the density of agglomerates,
  • ?wm is the density of the welding mixture,
  • Ca is the heat capacity of agglomerates,
  • qwm is the heat effect of SHS reaction,
  • Tmt is the ground caking temperature,
  • h is the thickness of recrystallizated layer
    of the agglomerate

8
Agglomerates of ground caked into a block by
SHS-method with the composition on the basis of
Fe3O4 and chromite concentrate
Tcomb1950oC CaO-Al2O3-SiO2 sintering temperature
1300-1540oC
Magnetite Algt Fe3O4, Fe, FeAl2O4
ChromiteAlgt FeCr2O4, (Mg,Fe)(Al0.75Cr0,25)O4
Bulk density of SHS mixture on base Fe3O4 is
2g/cm3
9
Water-stability of caked agglomerates of ground
with different welding mixtures and space factor
of the reactor (from 0.5 to 0. 7)
  • B - Fe3O4Al (k 0.5) C - Fe3O4Al (k 0.6)
    D - Fe3O4Al (k 0.7)
  • E - Fe2O3Al (k 0.5) F - chromite
    concentrate Fe2O3Al (k 0.5)
  • G - chromite concentrate Fe2O3Al (k 0.6)
    H
    - chromite concentrate Fe2O3Al (k 0.7)

740 hours 30 days
10
Change of mass of matrix sample under the
long-term influence of 30 nitric acid
  • B - Fe3O4Al (k 0.5) C - Fe3O4Al (k 0.6)
    D - Fe3O4Al (k 0.7) E - Fe2O3Al (k
    0.5) F - chromite concentrate Fe2O3Al (k
    0.5) G - chromite concentrate Fe2O3Al (k
    0.6)
    H - chromite concentrate Fe2O3Al (k
    0.7)

11
Optimization
  • The soil radioactive components fixing
    optimization in mechanically strong block with
    chemically stable spinel matrix is possible due
    to preparation of sphere soil agglomerates of 2
    sizes. Due to such approach reduced welding
    composition quantity and increased volume of
    roasting soil of one load. This led to economy of
    expensive material and makes cheaper all
    technology.
  • Replacement of reducer, expensive aluminum powder
    with cheaper component. Silicon and its
    alloys(for example, Al-Si alloy silumin) can be
    used as reducer in metallo-thermic processes.
  • First of all thermal effect of silicon reaction
    with iron oxide is enough high. For the
    reaction3Si 2Fe2O3 ? 4Fe 3SiO2 it is
    2462 J/g or 980,2 kJ/mol.
  • Secondary, the main silumin phase is aluminium
    silicon content is 3 and more percent. The most
    approachable piston silumin contains 11-13 of
    silicon.
  • Thirdly, the silumin wastes (cars pistons) are
    cheap raw material.
  • Thermo-physical parameters of SHS process with
    silumin use show, that there is phase
    recrystallization of soil agglomerate surface
    layer in the reactor and formation of minerals
    (quartz, corundum, albite, hercynite) as a result
    of layers combustion. According to the tests this
    composition has satisfactory to requirements
    mechanical and chemical resistance according to
    tests.

12
Conclusion
  • The elaborated method of immobilization of
    radioactive and chemically dangerous components
    spread in grounds uses the peculiarities of
    self-propagating high-temperature synthesis
    combined with agglomeration of polluted
    materials.
  • SHS based on processes of combustion allows
    obtaining refractory minerals which are similar
    to natural ones in the structure and phase
    composition having mechanical strength and high
    chemical stability.
  • Agglomeration provides the possibility for
    treatment and decontamination of greater volumes
    of polluted materials with considerably less
    consumption of welding SHS-mixture and, hence,
    its most expensive component powdered
    aluminium.
  • The proposed technology provides high degree of
    mechanization process that it is important, when
    working with harmful substances. 
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