US20190224642A1 - Methods of use and manufacture of silver-doped, nano-porous hydroxyapatite - Google Patents

Methods of use and manufacture of silver-doped, nano-porous hydroxyapatite Download PDF

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US20190224642A1
US20190224642A1 US16/257,514 US201916257514A US2019224642A1 US 20190224642 A1 US20190224642 A1 US 20190224642A1 US 201916257514 A US201916257514 A US 201916257514A US 2019224642 A1 US2019224642 A1 US 2019224642A1
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silver
microparticles
glass
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Cheol-Woon KIM
Richard K. Brow
Jen-Hsien HSU
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Mo Sci LLC
University of Missouri St Louis
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Mo Sci LLC
University of Missouri St Louis
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Priority to US17/857,388 priority patent/US20220401913A1/en
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/04Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of alkali metals, alkaline earth metals or magnesium
    • B01J20/048Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of alkali metals, alkaline earth metals or magnesium containing phosphorus, e.g. phosphates, apatites, hydroxyapatites
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/28Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
    • B01J20/28002Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their physical properties
    • B01J20/28004Sorbent size or size distribution, e.g. particle size
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/28Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
    • B01J20/28014Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
    • B01J20/28016Particle form
    • B01J20/28019Spherical, ellipsoidal or cylindrical
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/28Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
    • B01J20/28054Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J20/28078Pore diameter
    • B01J20/2808Pore diameter being less than 2 nm, i.e. micropores or nanopores
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/3021Milling, crushing or grinding
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/3078Thermal treatment, e.g. calcining or pyrolizing
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/3085Chemical treatments not covered by groups B01J20/3007 - B01J20/3078
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    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B25/00Phosphorus; Compounds thereof
    • C01B25/16Oxyacids of phosphorus; Salts thereof
    • C01B25/26Phosphates
    • C01B25/32Phosphates of magnesium, calcium, strontium, or barium
    • GPHYSICS
    • G21NUCLEAR PHYSICS; NUCLEAR ENGINEERING
    • G21FPROTECTION AGAINST X-RADIATION, GAMMA RADIATION, CORPUSCULAR RADIATION OR PARTICLE BOMBARDMENT; TREATING RADIOACTIVELY CONTAMINATED MATERIAL; DECONTAMINATION ARRANGEMENTS THEREFOR
    • G21F9/00Treating radioactively contaminated material; Decontamination arrangements therefor
    • G21F9/02Treating gases
    • GPHYSICS
    • G21NUCLEAR PHYSICS; NUCLEAR ENGINEERING
    • G21FPROTECTION AGAINST X-RADIATION, GAMMA RADIATION, CORPUSCULAR RADIATION OR PARTICLE BOMBARDMENT; TREATING RADIOACTIVELY CONTAMINATED MATERIAL; DECONTAMINATION ARRANGEMENTS THEREFOR
    • G21F9/00Treating radioactively contaminated material; Decontamination arrangements therefor
    • G21F9/04Treating liquids
    • G21F9/06Processing
    • G21F9/12Processing by absorption; by adsorption; by ion-exchange
    • GPHYSICS
    • G21NUCLEAR PHYSICS; NUCLEAR ENGINEERING
    • G21FPROTECTION AGAINST X-RADIATION, GAMMA RADIATION, CORPUSCULAR RADIATION OR PARTICLE BOMBARDMENT; TREATING RADIOACTIVELY CONTAMINATED MATERIAL; DECONTAMINATION ARRANGEMENTS THEREFOR
    • G21F9/00Treating radioactively contaminated material; Decontamination arrangements therefor
    • G21F9/04Treating liquids
    • G21F9/06Processing
    • G21F9/16Processing by fixation in stable solid media
    • GPHYSICS
    • G21NUCLEAR PHYSICS; NUCLEAR ENGINEERING
    • G21FPROTECTION AGAINST X-RADIATION, GAMMA RADIATION, CORPUSCULAR RADIATION OR PARTICLE BOMBARDMENT; TREATING RADIOACTIVELY CONTAMINATED MATERIAL; DECONTAMINATION ARRANGEMENTS THEREFOR
    • G21F9/00Treating radioactively contaminated material; Decontamination arrangements therefor
    • G21F9/04Treating liquids
    • G21F9/06Processing
    • G21F9/16Processing by fixation in stable solid media
    • G21F9/162Processing by fixation in stable solid media in an inorganic matrix, e.g. clays, zeolites
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    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2002/00Crystal-structural characteristics
    • C01P2002/50Solid solutions
    • C01P2002/52Solid solutions containing elements as dopants
    • C01P2002/54Solid solutions containing elements as dopants one element only
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    • C01P2002/70Crystal-structural characteristics defined by measured X-ray, neutron or electron diffraction data
    • C01P2002/72Crystal-structural characteristics defined by measured X-ray, neutron or electron diffraction data by d-values or two theta-values, e.g. as X-ray diagram
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    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2004/00Particle morphology
    • C01P2004/01Particle morphology depicted by an image
    • C01P2004/02Particle morphology depicted by an image obtained by optical microscopy
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    • C01P2004/03Particle morphology depicted by an image obtained by SEM
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    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2004/00Particle morphology
    • C01P2004/30Particle morphology extending in three dimensions
    • C01P2004/32Spheres
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2004/00Particle morphology
    • C01P2004/60Particles characterised by their size
    • C01P2004/61Micrometer sized, i.e. from 1-100 micrometer
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
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    • C01P2006/00Physical properties of inorganic compounds
    • C01P2006/16Pore diameter

Definitions

  • the present disclosure relates to nuclear fuel cycle and waste technology. More specifically, the present disclosure relates to methods and materials useful for the removal of harmful waste from the nuclear fuel cycle, methods of using these materials to remove harmful waste, and methods of manufacturing such materials. Even more specifically, the material is a silver-doped nano-porous hydroxyapatite that is useful for removing radioactive iodine from waste streams produced from reprocessed spent nuclear fuel.
  • Nuclear power is particularly useful for large-scale energy production of electricity. Like other energy producing technologies, a certain amount of waste is produced in the generation of this energy. Nuclear power is characterized by the very large amount of energy produced from a very small amount of fuel, and the amount of waste produced during this process is also relatively small. For instance, the amount of waste generated by nuclear power is very small relative to other thermal electricity generating technologies. However, much of the waste produced from nuclear power is radioactive, and therefore must be carefully managed as hazardous material.
  • radioactive waste product is radioactive iodine, 129 I, a noble gas that is a volatile radionuclide generated during used nuclear fuel reprocessing. Because of its long half-life (approximately 15.7 million years) and harmful effects on human health, the long-term disposal of 129 I is particularly important. 129 I, like other radionuclides that tend to form volatile species that evolve into reprocessing facility off-gas systems, poses a greater challenge to efficiently control than radionuclides that remain with the solids or liquids during fuel reprocessing. Unless otherwise managed, 129 I would be released into the environment.
  • the present disclosure generally provides methods and materials useful for the capture and/or removal of harmful waste from the nuclear fuel cycle, methods of using these materials to remove harmful waste, and methods of manufacturing such materials. More specifically, the present disclosure provides a silver-doped, nano-porous hydroxyapatite material that can be utilized to capture and/or remove radionuclides, such as for example, radioactive iodine, 129 I, that are present in spent nuclear fuel. Methods of using the silver-doped, nano-porous hydroxyapatite material and methods of manufacture are also provided.
  • a material for capturing a radioactive product may comprise a plurality of silver-doped microparticles.
  • the microparticles may comprise hydroxyapatite.
  • the microparticles are irregularly shaped, while in other cases, the microparticles may be microspheres that are evenly shaped. These microparticles may be in the range of about 20-800 ⁇ m in diameter, and may include nanopores.
  • the radioactive product may comprise a volatile radionuclide.
  • the volatile radionuclide may be iodine, such as 129 I.
  • the microparticles may have a silver content in the range of about 0.50 to 5.00 wt %, and in some embodiments, may have a silver content in the range of about 1.60 to 1.75% wt % of the microparticles. In one embodiment, the silver content may be about 1.71 wt % of the microparticles.
  • a method of manufacturing a material for capturing a radioactive product involves preparing silver-doped hydroxyapatite from silver-sodium-calcium borate glass in a phosphate solution, melting the glass, quenching the glass melt in air, crushing the glass to a powder, passing the powder through high heat to form glass microparticles, and immersing the glass microparticles in a solution of K 2 HPO 4 for a duration of time.
  • the glass may be melted at a temperature ranging from about 700 to about 1200, or about 1000° C., for a duration of time, such as between 30 minutes and 120 minutes, and in one embodiment for approximately 1 hour.
  • the powder may comprise microparticles having a diameter in the range of about 20-800 ⁇ m. High heat may then be applied to the powder. For example, the powder may be passed through a flame to form a frit.
  • the glass microparticles may be immersed in the K 2 HPO 4 solution for a duration of time, such as for example, between 2 to 6 days, and in one embodiment for about 4 days, at room temperature, after continuously stirring the solution for an initial amount of time, such as the first 24 hours.
  • a method of immobilizing a radioactive product with silver-doped, nano-porous hydroxyapatite material involves providing a silver-doped, nano-porous hydroxyapatite material, capturing the radioactive product within the silver-doped, nano-porous hydroxyapatite material, and cold sintering the silver-doped, nano-porous hydroxyapatite material.
  • the silver-doped, nano-porous hydroxyapatite material comprises microparticles or microspheres.
  • the radioactive product comprises 129 I.
  • the radioactive product may be captured in vapor form, while in other embodiments, the radioactive product may be captured in solution.
  • borosilicate or iron phosphate glass powders may be added to the material.
  • FIG. 1A is a Scanning Electron Microscopy (SEM) micrograph of an Ag-HAp microsphere (30 ⁇ m) transformed from a silver-sodium-calcium borate glass in accordance with a method of the present disclosure.
  • SEM Scanning Electron Microscopy
  • FIG. 1B is a Scanning Electron Microscopy (SEM) micrograph of the external surface of the porous Ag-HAp microsphere of FIG. 1A at high magnification showing 30 nm-100 nm sized HAp crystals.
  • SEM Scanning Electron Microscopy
  • FIG. 2 is an X-ray diffraction (XRD) pattern of Ag-HAp material converted from a silver-sodium-calcium borate glass in accordance with a method of the present disclosure.
  • XRD X-ray diffraction
  • FIG. 3A is a photograph of a pellet comprising cold-sintered (AgI)-HAp material produced in accordance with a method of the present disclosure.
  • FIG. 3B is a cross-sectional Scanning Electron Microscopy (SEM) micrograph of a fracture surface of the pellet of FIG. 3A .
  • FIG. 4A is a photograph of a pellet comprising cold-sintered borosilicate glass produced in accordance with a method of the present disclosure.
  • FIG. 4B is a cross-sectional Scanning Electron Microscopy (SEM) micrograph of a fracture surface of the pellet of FIG. 4A .
  • the present disclosure provides a silver-doped, nano-porous hydroxyapatite material that can be utilized to capture and/or remove radionuclides, such as for example radioactive iodine, 129 I, that are present in spent nuclear fuel.
  • radionuclides such as for example radioactive iodine, 129 I
  • Radioactive iodine, 129 I is generated in the nuclear fuel cycle and so is present in spent nuclear fuel. Because of its long half-life (approximately 15.7 million years) and harmful effects on human health, the long-term disposal of 129 I is particularly important. It has been discovered that 129 I can be immobilized or captured by hollow or solid media composed of silver-doped hydroxyapatite (HAp) nanocrystals as 129 I 2 vapor from the off-gas streams associated with reprocessing spent fuels. Some of the captured 129 I reacts with silver to form silver iodine (AgI), while the rest is adsorbed in the HAp nanopores.
  • HAp silver-doped hydroxyapatite
  • the used (spent) HAp powders in the form of microspheres or microparticles
  • the following describes an exemplary method of manufacturing the silver-doped nano-porous hydroxyapatite material of the present disclosure.
  • High surface area (>150 m 2 /g) powders comprising nano-sized (e.g., 30-100 nm) silver-doped hydroxyapatite (Ca 10 (PO 4 ) 6 (OH) 2 ) designated as Ag-HAp crystals
  • nano-sized (e.g., 30-100 nm) silver-doped hydroxyapatite (Ca 10 (PO 4 ) 6 (OH) 2 ) designated as Ag-HAp crystals may be produced from silver-sodium-calcium borate glass in a phosphate solution using a process such as the transformation process described in the U.S. Pat. No. 6,358,531 (developed by Missouri S&T), the entire contents of which are herein incorporated by reference.
  • Glass e.g., composition of 0.59 mol % Ag 2 O-19.88 mol % Na 2 O-19.88 mol % CaO-59.65 mol % B 2 O 3
  • a high temperate in the range of about 700 to 1200° C., such as for example at about 1000° C., for a duration of time such as for example, between 30 minutes to 120 minutes. In one embodiment, the duration of time may be for about 60 minutes (1 hour).
  • the molten glass can be quenched in air and then crushed to a powder to a desired size or diameter range (e.g., 20-800 ⁇ m) to form a sized frit.
  • Glass microspheres may be produced with the application of high heat, for instance, by passing the sized frit through a flame.
  • the sized glass microparticles (frit) or microspheres can then be immersed in 1M K 2 HPO 4 for a period of time, such as between about 2 to 6 days, for example for about 4 days, at room temperature with continuous stirring for an initial period of time, such as for example, the first 24 hours.
  • the phase ratio between glass and K 2 HPO 4 solution can be 1 kg:10 L.
  • FIGS. 1A, 1B ) and 2 A resultant material produced by the method described above is illustrated in FIGS. 1A, 1B ) and 2 , in which silver-doped glass is fully converted to nano-porous HAp material containing silver (Ag).
  • FIG. 1A is a SEM micrograph showing an Ag-HAp microsphere (30 ⁇ m) transformed from a silver-sodium-calcium borate glass in accordance with the method of the present disclosure.
  • FIG. 1B is a SEM micrograph representing an enlarged view the external surface of the porous Ag-HAp crystalline microsphere of FIG. 1A at high magnification showing 30 nm-100 nm sized HAp crystals.
  • FIG. 1A is a SEM micrograph showing an Ag-HAp microsphere (30 ⁇ m) transformed from a silver-sodium-calcium borate glass in accordance with the method of the present disclosure.
  • FIG. 1B is a SEM micrograph representing an enlarged view the external surface of
  • the specific surface area (SSA) of converted Ag-HAp material is 120-220 m 2 /g as measured by the Brunauer-Emmett-Teller (BET) method.
  • the silver content of converted Ag-HAp material is in the range of about 0.50 to 5.00 wt %, and in one embodiment, is in the range of about 1.60 to 1.75 wt %, and still in another embodiment is about 1.71 wt %, as measured by X-ray fluorescence (XRF).
  • the following describes exemplary methods of using the silver-doped, nano-porous hydroxyapatite material to capture, immobilize, and/or remove, radioactive iodine.
  • Silver-doped, nano-porous hydroxyapatite (Ag-HAp) material in the form of microspheres or irregular shaped microparticles, was placed on a nylon sieve covering a beaker.
  • the beaker contained 100 ml of iodine solution (10% povidone-iodine, equivalent to 1% titratable iodine) on a hot plate and then the iodine solution was boiled using the hot plate until all was evaporated, with the resulting vapor passing through the bed of Ag-HAp particles.
  • the particles were dried at 100° C. overnight, then analyzed.
  • the dried Ag-HAp material contained 1.6 wt % iodine, equivalent to a Ag:I atomic ratio of 1.26.
  • Silver-doped, nano-porous hydroxyapatite (Ag-HAp) material in the form of microspheres or irregular shaped microparticles, was immersed in 25 ml of a five molar sodium hydroxide solution (pH 14) that contained 16.52 ppm of I ⁇ (dissolved KI). The material/solution was agitated on an orbital shaker for 24 hours at room temperature. After 24 hours, the leachate solution was collected using a 0.45 ⁇ m Nalgene syringe filter. The iodine in the solution before and after testing was determined by inductively coupled plasma-mass spectrometry (ICP-MS). The distribution coefficient K d value was calculated from the ICP-MS results per ASTM D4319-93 (Reapproved 2001), as listed below in Table 1.
  • ICP-MS inductively coupled plasma-mass spectrometry
  • the following describes exemplary methods of using the silver-doped, nano-porous hydroxyapatite material to capture radioactive iodine, and then stabilize for storage or disposal.
  • high-level radioactive waste can be immobilized to a chemically stable, solid form by high-temperature ( ⁇ 1150° C.) processes (e.g., vitrification).
  • high-temperature processes e.g., vitrification
  • low-temperature processes are required for the permanent immobilization of radioactive 129 I to avoid volatilization.
  • the cold sintering process which has been reported to densify ceramics (>0.9 relative density) at temperatures lower than 200° C. (see, for example, U.S. Patent Application Publication No. US 2017/0088471 A1), may be applied to waste forms for low-temperature immobilization.
  • the Ag-HAp microparticles (containing 1.6 wt % I) used for filtering iodine vapor was densified for 1 hour at 400 MPa, 120° C. (lower than the AgI decomposition temperature 150° C.), with 20 wt % water.
  • the cold-sintered (Ag,I)-HAp material, shown in the photograph of FIG. 3A , and its cross-sectional SEM micrograph, shown in FIG. 3B shows no significant porosity.
  • the relative density of samples prepared using different times, pressures, and temperatures ranged between 0.88 and 0.93.
  • 3A and 3B was measured to be 1.6 wt % by SEM-EDS (energy dispersive X-ray spectroscopy) and this indicated that there was no measurable iodine loss/volatilization during the low-temperature sintering process.
  • the spent (Ag,I)-HAp material can be combined with chemically durable borosilicate or iron phosphate glass powders, and then densified using the cold sintering process.
  • Borosilicate glass (Pyrex®) powders with d 50 3.8 ⁇ m, were mixed with a sodium silicate aqueous solution in a 75:25 by weight and then pressed at 400 MPa, at 120° C. for 1 hour, to yield pellets that had the same bulk density (2.2 g/cm 3 ) as the starting glass, cold-sintered borosilicate, as shown in the photograph of FIG. 4A .
  • FIG. 4B represents a SEM micrograph of the cross-sectional fracture surface of the glass of FIG. 4A , and shows no significant porosity.
  • the present examples demonstrated that a silver-doped, nano-porous hydroxyapatite (Ag-HAp) material was possible to manufacture into microsphere or irregular shaped microparticle form, and that these Ag-HAp microspheres or microparticles could be effectively used to capture radioactive iodine, 129 I, in vapor form or in solution, and that the microspheres or microparticles could then be further processed for permanent immobilization of the captured iodine, such as by cold sintering, in one embodiment.
  • Ag-HAp nano-porous hydroxyapatite
  • radioactive waste is not unique to the nuclear fuel cycle. Radioactive material exists in other technologies as well. For instance, radioactive materials are extensively used in, and are present in, medicine, agriculture, research, manufacturing, testing, and mineral exploration, to name some examples. Accordingly, the materials and methods of the present disclosure are not limited in their application to the nuclear fuel cycle, but can be equally applicable to these other technologies as well, for the removal and/or permanent immobilization of radioactive waste.

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Abstract

A silver-doped, nano-porous hydroxyapatite material is provided that can be utilized to capture radioactive iodine, 129I. Methods of using the silver-doped, nano-porous hydroxyapatite material to remove radioactive iodine, and methods of manufacturing the material are also provided.

Description

    CROSS-REFERENCE TO RELATED APPLICATIONS
  • This application claims benefit of U.S. Provisional Application No. 62/621,910, filed Jan. 25, 2018, the entire contents of which are incorporated herein by reference.
  • STATEMENT REGARDING FEDERALLY SPONSORED RESEARCH
  • This invention was made with government support under Grant No. DE-SC0011906 awarded by the U.S. Department of Energy (DOE). The Government has certain rights in the invention.
  • TECHNICAL FIELD
  • The present disclosure relates to nuclear fuel cycle and waste technology. More specifically, the present disclosure relates to methods and materials useful for the removal of harmful waste from the nuclear fuel cycle, methods of using these materials to remove harmful waste, and methods of manufacturing such materials. Even more specifically, the material is a silver-doped nano-porous hydroxyapatite that is useful for removing radioactive iodine from waste streams produced from reprocessed spent nuclear fuel.
  • BACKGROUND
  • One of the most consistently reliable and efficient ways of producing energy is with nuclear power. Nuclear power is particularly useful for large-scale energy production of electricity. Like other energy producing technologies, a certain amount of waste is produced in the generation of this energy. Nuclear power is characterized by the very large amount of energy produced from a very small amount of fuel, and the amount of waste produced during this process is also relatively small. For instance, the amount of waste generated by nuclear power is very small relative to other thermal electricity generating technologies. However, much of the waste produced from nuclear power is radioactive, and therefore must be carefully managed as hazardous material.
  • One such radioactive waste product is radioactive iodine, 129I, a noble gas that is a volatile radionuclide generated during used nuclear fuel reprocessing. Because of its long half-life (approximately 15.7 million years) and harmful effects on human health, the long-term disposal of 129I is particularly important. 129I, like other radionuclides that tend to form volatile species that evolve into reprocessing facility off-gas systems, poses a greater challenge to efficiently control than radionuclides that remain with the solids or liquids during fuel reprocessing. Unless otherwise managed, 129I would be released into the environment.
  • Accordingly, it is desirable to provide an effective process for the capture and/or removal of radioactive iodine, 129I, present in spent nuclear fuel and other sources.
  • BRIEF SUMMARY
  • The present disclosure generally provides methods and materials useful for the capture and/or removal of harmful waste from the nuclear fuel cycle, methods of using these materials to remove harmful waste, and methods of manufacturing such materials. More specifically, the present disclosure provides a silver-doped, nano-porous hydroxyapatite material that can be utilized to capture and/or remove radionuclides, such as for example, radioactive iodine, 129I, that are present in spent nuclear fuel. Methods of using the silver-doped, nano-porous hydroxyapatite material and methods of manufacture are also provided.
  • In one exemplary embodiment of the present disclosure, a material for capturing a radioactive product is provided. The material may comprise a plurality of silver-doped microparticles. The microparticles may comprise hydroxyapatite. In some cases, the microparticles are irregularly shaped, while in other cases, the microparticles may be microspheres that are evenly shaped. These microparticles may be in the range of about 20-800 μm in diameter, and may include nanopores. According to one aspect of the disclosure, the radioactive product may comprise a volatile radionuclide. The volatile radionuclide may be iodine, such as 129I. Further, the microparticles may have a silver content in the range of about 0.50 to 5.00 wt %, and in some embodiments, may have a silver content in the range of about 1.60 to 1.75% wt % of the microparticles. In one embodiment, the silver content may be about 1.71 wt % of the microparticles.
  • In another exemplary embodiment of the present disclosure, a method of manufacturing a material for capturing a radioactive product is provided. The method involves preparing silver-doped hydroxyapatite from silver-sodium-calcium borate glass in a phosphate solution, melting the glass, quenching the glass melt in air, crushing the glass to a powder, passing the powder through high heat to form glass microparticles, and immersing the glass microparticles in a solution of K2HPO4 for a duration of time. In some embodiments, the glass may be melted at a temperature ranging from about 700 to about 1200, or about 1000° C., for a duration of time, such as between 30 minutes and 120 minutes, and in one embodiment for approximately 1 hour. The powder may comprise microparticles having a diameter in the range of about 20-800 μm. High heat may then be applied to the powder. For example, the powder may be passed through a flame to form a frit. In some embodiments, the glass microparticles may be immersed in the K2HPO4 solution for a duration of time, such as for example, between 2 to 6 days, and in one embodiment for about 4 days, at room temperature, after continuously stirring the solution for an initial amount of time, such as the first 24 hours.
  • In still another exemplary embodiment of the present disclosure, a method of immobilizing a radioactive product with silver-doped, nano-porous hydroxyapatite material is provided. The method involves providing a silver-doped, nano-porous hydroxyapatite material, capturing the radioactive product within the silver-doped, nano-porous hydroxyapatite material, and cold sintering the silver-doped, nano-porous hydroxyapatite material. According to one aspect, the silver-doped, nano-porous hydroxyapatite material comprises microparticles or microspheres. According to another aspect, the radioactive product comprises 129I. In some embodiments, the radioactive product may be captured in vapor form, while in other embodiments, the radioactive product may be captured in solution. In another embodiment, borosilicate or iron phosphate glass powders may be added to the material.
  • It is to be understood that both the foregoing general description and the following detailed description are exemplary and explanatory only and are not restrictive of the disclosure. Additional features of the disclosure will be set forth in part in the description which follows or may be learned by practice of the disclosure.
  • BRIEF DESCRIPTION OF THE DRAWINGS
  • The accompanying drawings, which are incorporated in and constitute a part of this specification, illustrate several embodiments of the disclosure and together with the description, serve to explain the principles of the disclosure.
  • FIG. 1A is a Scanning Electron Microscopy (SEM) micrograph of an Ag-HAp microsphere (30 μm) transformed from a silver-sodium-calcium borate glass in accordance with a method of the present disclosure.
  • FIG. 1B is a Scanning Electron Microscopy (SEM) micrograph of the external surface of the porous Ag-HAp microsphere of FIG. 1A at high magnification showing 30 nm-100 nm sized HAp crystals.
  • FIG. 2 is an X-ray diffraction (XRD) pattern of Ag-HAp material converted from a silver-sodium-calcium borate glass in accordance with a method of the present disclosure.
  • FIG. 3A is a photograph of a pellet comprising cold-sintered (AgI)-HAp material produced in accordance with a method of the present disclosure.
  • FIG. 3B is a cross-sectional Scanning Electron Microscopy (SEM) micrograph of a fracture surface of the pellet of FIG. 3A.
  • FIG. 4A is a photograph of a pellet comprising cold-sintered borosilicate glass produced in accordance with a method of the present disclosure.
  • FIG. 4B is a cross-sectional Scanning Electron Microscopy (SEM) micrograph of a fracture surface of the pellet of FIG. 4A.
  • DETAILED DESCRIPTION OF THE EMBODIMENTS
  • Methods and materials useful for the capture and/or removal of harmful waste from the nuclear fuel cycle, methods of using these materials to remove harmful waste, and methods of manufacturing such materials, are provided with this disclosure. More specifically, the present disclosure provides a silver-doped, nano-porous hydroxyapatite material that can be utilized to capture and/or remove radionuclides, such as for example radioactive iodine, 129I, that are present in spent nuclear fuel. Methods of using the silver-doped, nano-porous hydroxyapatite material and methods of manufacture are also provided.
  • Radioactive iodine, 129I, is generated in the nuclear fuel cycle and so is present in spent nuclear fuel. Because of its long half-life (approximately 15.7 million years) and harmful effects on human health, the long-term disposal of 129I is particularly important. It has been discovered that 129I can be immobilized or captured by hollow or solid media composed of silver-doped hydroxyapatite (HAp) nanocrystals as 129I2 vapor from the off-gas streams associated with reprocessing spent fuels. Some of the captured 129I reacts with silver to form silver iodine (AgI), while the rest is adsorbed in the HAp nanopores. After capturing 129I, the used (spent) HAp powders (in the form of microspheres or microparticles) can be consolidated into a dense, chemically stable form, typically at low temperatures (<150° C.) to avoid decomposition of AgI and loss of 129I for removal or safe storage.
  • The following describes an exemplary method of manufacturing the silver-doped nano-porous hydroxyapatite material of the present disclosure.
  • Preparation of Silver-Doped Nano-Porous Hydroxyapatite Material
  • High surface area (>150 m2/g) powders (microspheres or irregular shaped microparticles) comprising nano-sized (e.g., 30-100 nm) silver-doped hydroxyapatite (Ca10(PO4)6(OH)2) designated as Ag-HAp crystals may be produced from silver-sodium-calcium borate glass in a phosphate solution using a process such as the transformation process described in the U.S. Pat. No. 6,358,531 (developed by Missouri S&T), the entire contents of which are herein incorporated by reference. Glass (e.g., composition of 0.59 mol % Ag2O-19.88 mol % Na2O-19.88 mol % CaO-59.65 mol % B2O3) may be melted at a high temperate in the range of about 700 to 1200° C., such as for example at about 1000° C., for a duration of time such as for example, between 30 minutes to 120 minutes. In one embodiment, the duration of time may be for about 60 minutes (1 hour). After melting, the molten glass can be quenched in air and then crushed to a powder to a desired size or diameter range (e.g., 20-800 μm) to form a sized frit. Glass microspheres may be produced with the application of high heat, for instance, by passing the sized frit through a flame. The sized glass microparticles (frit) or microspheres can then be immersed in 1M K2HPO4 for a period of time, such as between about 2 to 6 days, for example for about 4 days, at room temperature with continuous stirring for an initial period of time, such as for example, the first 24 hours. The phase ratio between glass and K2HPO4 solution can be 1 kg:10 L.
  • A resultant material produced by the method described above is illustrated in FIGS. 1A, 1B) and 2, in which silver-doped glass is fully converted to nano-porous HAp material containing silver (Ag). FIG. 1A is a SEM micrograph showing an Ag-HAp microsphere (30 μm) transformed from a silver-sodium-calcium borate glass in accordance with the method of the present disclosure. FIG. 1B is a SEM micrograph representing an enlarged view the external surface of the porous Ag-HAp crystalline microsphere of FIG. 1A at high magnification showing 30 nm-100 nm sized HAp crystals. FIG. 2 represents an X-ray diffraction (XRD) pattern of the Ag-HAp material converted from a silver-sodium-calcium borate glass. According to one aspect of the disclosure, the specific surface area (SSA) of converted Ag-HAp material is 120-220 m2/g as measured by the Brunauer-Emmett-Teller (BET) method. According to another aspect of the disclosure, the silver content of converted Ag-HAp material is in the range of about 0.50 to 5.00 wt %, and in one embodiment, is in the range of about 1.60 to 1.75 wt %, and still in another embodiment is about 1.71 wt %, as measured by X-ray fluorescence (XRF).
  • The following describes exemplary methods of using the silver-doped, nano-porous hydroxyapatite material to capture, immobilize, and/or remove, radioactive iodine.
  • Example 1: Iodine Capture from Vapor
  • Silver-doped, nano-porous hydroxyapatite (Ag-HAp) material, in the form of microspheres or irregular shaped microparticles, was placed on a nylon sieve covering a beaker. The beaker contained 100 ml of iodine solution (10% povidone-iodine, equivalent to 1% titratable iodine) on a hot plate and then the iodine solution was boiled using the hot plate until all was evaporated, with the resulting vapor passing through the bed of Ag-HAp particles. The particles were dried at 100° C. overnight, then analyzed. The dried Ag-HAp material contained 1.6 wt % iodine, equivalent to a Ag:I atomic ratio of 1.26.
  • Example 2: Iodine Capture from Solution
  • Silver-doped, nano-porous hydroxyapatite (Ag-HAp) material, in the form of microspheres or irregular shaped microparticles, was immersed in 25 ml of a five molar sodium hydroxide solution (pH 14) that contained 16.52 ppm of I (dissolved KI). The material/solution was agitated on an orbital shaker for 24 hours at room temperature. After 24 hours, the leachate solution was collected using a 0.45 μm Nalgene syringe filter. The iodine in the solution before and after testing was determined by inductively coupled plasma-mass spectrometry (ICP-MS). The distribution coefficient Kd value was calculated from the ICP-MS results per ASTM D4319-93 (Reapproved 2001), as listed below in Table 1.
  • TABLE 1
    Iodine removal from a five molar sodium
    hydroxide solution using Ag-Hap
    Be- Af- Phase Ratio
    SSA fore ter (e.g., 1 g Kd % I
    (m2/ I I Ag-HAp:25 (ml/ Re-
    Media g) (ppm) (ppm) ml solution g) moval
    Ag-HAp 180 16.52 0.005 25 77180 99.97
    sample 1
    Ag-HAp 137 16.52 0.066 25 6225 99.60
    sample 2
  • The following describes exemplary methods of using the silver-doped, nano-porous hydroxyapatite material to capture radioactive iodine, and then stabilize for storage or disposal.
  • Low-Temperature Process for Permanent Immobilization
  • In general, high-level radioactive waste can be immobilized to a chemically stable, solid form by high-temperature (≥1150° C.) processes (e.g., vitrification). However, low-temperature processes are required for the permanent immobilization of radioactive 129I to avoid volatilization. The cold sintering process, which has been reported to densify ceramics (>0.9 relative density) at temperatures lower than 200° C. (see, for example, U.S. Patent Application Publication No. US 2017/0088471 A1), may be applied to waste forms for low-temperature immobilization. In one example, the Ag-HAp microparticles (containing 1.6 wt % I) used for filtering iodine vapor was densified for 1 hour at 400 MPa, 120° C. (lower than the AgI decomposition temperature 150° C.), with 20 wt % water. The cold-sintered (Ag,I)-HAp material, shown in the photograph of FIG. 3A, and its cross-sectional SEM micrograph, shown in FIG. 3B, shows no significant porosity. The relative density of samples prepared using different times, pressures, and temperatures ranged between 0.88 and 0.93. The iodine-content of the sample shown in FIGS. 3A and 3B was measured to be 1.6 wt % by SEM-EDS (energy dispersive X-ray spectroscopy) and this indicated that there was no measurable iodine loss/volatilization during the low-temperature sintering process.
  • Alternatively, the spent (Ag,I)-HAp material can be combined with chemically durable borosilicate or iron phosphate glass powders, and then densified using the cold sintering process. Borosilicate glass (Pyrex®) powders, with d50 3.8 μm, were mixed with a sodium silicate aqueous solution in a 75:25 by weight and then pressed at 400 MPa, at 120° C. for 1 hour, to yield pellets that had the same bulk density (2.2 g/cm3) as the starting glass, cold-sintered borosilicate, as shown in the photograph of FIG. 4A. FIG. 4B represents a SEM micrograph of the cross-sectional fracture surface of the glass of FIG. 4A, and shows no significant porosity.
  • Accordingly, the present examples demonstrated that a silver-doped, nano-porous hydroxyapatite (Ag-HAp) material was possible to manufacture into microsphere or irregular shaped microparticle form, and that these Ag-HAp microspheres or microparticles could be effectively used to capture radioactive iodine, 129I, in vapor form or in solution, and that the microspheres or microparticles could then be further processed for permanent immobilization of the captured iodine, such as by cold sintering, in one embodiment.
  • It is of course understood that radioactive waste is not unique to the nuclear fuel cycle. Radioactive material exists in other technologies as well. For instance, radioactive materials are extensively used in, and are present in, medicine, agriculture, research, manufacturing, testing, and mineral exploration, to name some examples. Accordingly, the materials and methods of the present disclosure are not limited in their application to the nuclear fuel cycle, but can be equally applicable to these other technologies as well, for the removal and/or permanent immobilization of radioactive waste.
  • Other embodiments will be apparent to those skilled in the art from consideration of the specification and practice of the embodiment disclosed herein. It is intended that the specification and examples be considered as exemplary only, with a true scope and spirit of the embodiment being indicated by the following claims.

Claims (25)

What is claimed is:
1. A material for capturing a radioactive product, comprising a plurality of silver-doped microparticles.
2. The material of claim 1, wherein the silver content is in the range of about 0.50 to 5.00 wt % of the microparticles.
3. The material of claim 2, wherein the silver content is in the range of about 1.60 to 1.75 wt % of the microparticles.
4. The material of claim 1, wherein the microparticles comprise microspheres.
5. The material of claim 1, wherein the microparticles are in the range of about 20-800 μm in diameter.
6. The material of claim 1, wherein the microparticles comprise hydroxyapatite.
7. The material of claim 1, wherein the microparticles include nanopores.
8. The material of claim 1, wherein the radioactive product comprises a volatile radionuclide.
9. The material of claim 8, wherein the volatile radionuclide comprises iodine.
10. The material of claim 9, wherein the iodine is 129I.
11. A method of manufacturing the material of claim 1, comprising:
preparing silver-doped hydroxyapatite from silver-sodium-calcium borate glass in a phosphate solution;
melting the glass;
quenching the glass in air;
crushing the glass to a powder;
passing the powder through high heat to form glass microparticles; and
immersing the glass microparticles in a solution of K2HPO4 for a duration of time.
12. The method of claim 11, wherein the glass is melted at a temperature in the range of about 700 to 1200° C. for a duration of time ranging from about 30 minutes to 120 minutes.
13. The method of claim 12, wherein the glass is melted at about 1000° C. for about 1 hour.
14. The method of claim 11, wherein the powder comprises microparticles having a diameter in the range of about 20-800 μm.
15. The method of claim 15, further including the application of heat to the powder.
16. The method of claim 15, wherein the powder is passed through a flame.
17. The method of claim 11, wherein the glass microparticles are immersed in the K2HPO4 solution for about 2 to 6 days at room temperature.
18. The method of claim 11, further including the step of continuously stirring the solution for about 24 hours.
19. A method of immobilizing a radioactive product with silver-doped, nano-porous hydroxyapatite material, comprising:
providing a silver-doped, nano-porous hydroxyapatite material;
capturing the radioactive product within the silver-doped, nano-porous hydroxyapatite material; and
cold sintering the silver-doped, nano-porous hydroxyapatite material.
20. The method of claim 19, wherein the silver-doped, nano-porous hydroxyapatite material comprises microparticles or microspheres.
21. The method of claim 19, wherein the silver content of the material is in the range of about 1.25 to 2.00 wt % of the microparticles.
22. The method of claim 19, wherein the radioactive product comprises 129I.
23. The method of claim 19, wherein the radioactive product is captured in vapor form.
24. The method of claim 19, wherein the radioactive product is captured in solution.
25. The method of claim 19, further including the step of adding borosilicate or iron phosphate glass powders.
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