CA2759663C - Alkali metal super ionic conducting ceramic - Google Patents
Alkali metal super ionic conducting ceramic Download PDFInfo
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Abstract
Description
FIELD OF THE INVENTION
[0001] The invention relates to metal ion conducting ceramic materials having characteristics of high ion conductivity for certain alkali and monovalent metal ions at low temperatures, high selectivity for the metal ions, good current efficiency and stability in water and corrosive media under static and electrochemical conditions. The metal ion conducting ceramic materials include the type known as MeSICON (Metal Super Ionic CONductor) materials. Where the metal is sodium (NaSICON materials), the invention includes the complete or partial substitution of alkali metal ions such as Lit, K+, Rb+, and Cs + as well as monovalent silver ions, Ag+, into the sodium sites of the disclosed NaSICON
materials. The disclosed metal ion ceramic materials are useful in many applications, but especially in electrolytic systems involving electrolytic reactions of solutions containing alkali metal ions.
BACKGROUND OF THE INVENTION
substituted to maintain charge neutrality. While the Si4+ additions are known to directly substitute into the lattice sites formerly occupied by the P5+ ions, the additional Na + ions are known to occupy one of two or three equivalent lattice sites not fully occupied by sodium ions in any of the NaSICON
compositions for which x<3.
203-220, 1976; J. J. Bentzen et al., in "The preparation and characterization of dense, highly conductive Na5GdSi4012 nasicon (NGS)", Materials Research Bulletin, Vol. 15, pp. 1737-1745, 1980; C. Delmas et al., in "Crystal chemistry of the Nai+xZr2_xLx(PO4)3 (L = Cr, In, Yb) solid solutions", Materials Research Bulletin, Vol. 16, pp. 285-290, 1981; V.
von Alpen et al., in "Compositional dependence of the electrochemical and structural parameters in the NASICON system (Nal+SixZr2P3_x012)", Solid State Ionics, Vol. 3/4, pp. 215-218, 1981; S.
Fujitsu et al., in "Conduction paths in sintered ionic conductive material Nal-FxYxZr2_x(PO4)3", Materials Research Bulletin, Vol. 16, pp. 1299-1309, 1981; Y. Saito et al., in "Ionic conductivity of NASICON-type conductors Nal 5Mo 5Zri 5(PO4)3 (M: Al3+, Ga3+, Cr3+, Sc3+, Fe3+, In3+, Yb3+, Y3+)", Solid State Ionics, Vol. 58, pp. 327-331, 1992; J.
Alamo in "Chemistry and properties of solids with the ll\IZP] skeleton", Solid State Ionics, Vol. 63-65, pp. 547-561, 1993; K. Shimazu in "Electrical conductivity and Ti4+ ion substitution range in NASICON system", Solid State Ionics, Vol. 79, pp. 106-110, 1995; Y. Miyajima in "Ionic conductivity of NASICON-type Nal-FxMxZr2_xP3012 (M: Yb, Er, Dy)", Solid State Ionics, Vol.
84, pp. 61-64, 1996.
Technical papers have claimed this 1) reduces the sintering temperature of the NaSICON; 2) reduces the free Zr02 in the sintered microstructure; 3) increases the stability of the NaSICON (particularly with water); or 4) increases the conductivity of the material. In any case, the more general formula for NaSICON ceramics can be expressed as containing materials can be expressed as Mel-Fx+yMIIIymIV2 ySixP3,012, where Me is the alkali or monovalent metal ion, Mill is a +3 cation and MN is a +4 cation. All materials reported in the literature have the same crystal structure and same basic microstructural characteristics and similar baseline Hong formulations, usually with only minor changes in lattice parameters and ionic conductivities of the ceramic.
materials. These compositions are fundamentally based on the Hong formulation, first reported on in 1976[11, but vary from Hong's chemistries in one important respect ¨ they are made to be metal ion deficient from the baseline formulation Mei x y_zminymb72 3õ..31xr z/2. This distinction appears to be unique to all other literature reported on the subject of NaSICON type materials.
BRIEF SUMMARY OF THE INVENTION
In some embodiments, 2.2 < x < 2.4. In some embodiments, 0.0 < y < 0.12. In some embodiments, 0.05 < z < 0.3.
In one embodiment, x is about 2.4, y is about 0.0, and z is about 0.8 and the metal ion conductive ceramic material has a formula Na26Zr2Si24P0 60116.
These and other features and advantages of the present invention will become more fully apparent from the following figures, description, and appended claims, or may be learned by the practice of the invention as set forth hereinafter.
BRIEF DESCRIPTION OF THE SEVERAL VIEWS OF THE DRAWINGS
Understanding that these drawings depict only typical embodiments of the invention and are not therefore to be considered to be limiting of its scope, the invention will be described and explained with additional specificity and detail through the use of the accompanying drawings in which:
compositions measured as a corrosion rate from exposure to 15 wt% NaOH
solution at 65 C.
compositions measured as a corrosion rate from exposure to 50 wt% NaOH
solution at 65 C.
DETAILED DESCRIPTION OF THE INVENTION
Specifically, compositions made with 0.05-0.9 moles less Na than in Hong's formulation result in a material with the same basic crystal structure and higher electrical properties as materials reported in the literature. In addition, these materials have improved corrosion resistance to highly basic aqueous solutions in the temperature rages of 20-150 C. No such compositions or claims of improved performance have been found thus far in the literature.
metal ion conducting ceramic material having a structure providing high metal cation conductivity within the scope of the present invention has the general formulation:
Me 1 +x+y-zm ym 2-yo ixr 3-0-,12-z/2 (2)
Because the composition may range for x from 2.0-2.4, for y from 0.0-1.0, and for z from 0.05-0.9, and the total Me should be 1+x+y-z, this restricts the value of z to be greater than or equal to x+y-3. That is, z? (x+y-3).
general formulation can be expressed for each specific metal ion. For example, where Me is Na, Mill is Y, and MW is Zr, a general formulation for the sodium deficient materials can be expressed as follows:
This addition and removal of sodium ions is accompanied by the addition and removal of electrons and a change in valence of another cation in the structure (most typically the Zr in the structure substituted for a multivalent metal ion). In contrast, the sodium deficiencies in the metal ion conducting ceramic materials within the scope of the present invention are compensated by vacancies in the oxygen sub-lattice (Ionic substitution), and are not due to the net removal of sodium ions.
Among other advantages, compositions tested have shown an improved chemical stability when exposed to high concentrations of NaOH in water (>15 wt. %) in temperature ranges from 20-65 C over their sodium stoichiometric counterparts.
(Low level radioactively contaminated sodium salt based waste) simulant chemistry and the caustic NaOH solutions without the influence of an electric field. Exposure tests were conducted at about 60 C for 168 hr (1 week) in three different solutions: a 15 wt. % NaOH
aqueous solution (the composition of the baseline catholyte solution), a stock radioactive simulant "AP104" solution with a Na:K ratio of roughly 50:1, and the same "AP104"
solution with enough KOH added to bring the Na:K ratio to 7:1 simulating the highest K
concentration that the membranes may be exposed to in the actual LLW. The results are presented in Table 2 below, in most cases, the corrosion level was notably lower in the 50:1 solution when compared to the 15 wt. % NaOH.
Corrosion Rates (mg/cm2/100hr) NaSICON material 15 wt. %
NaOH "AP104", 50:1 Na:K "AP104", 7:1 Na:K
A-01 0.97 0.10 1.29 0.62 3.11 0.16 A-04 4.64 0.78 0.45 0.07 0.77 0.13 E-04 0.80 0.06 0.19 0.02 0.28 0.03 A-08 2.74 0.11 0.52 0.06 0.38 0.11
The NAS-G
material has been previously tested in exposure experiments for over three months in LLW
simulant without any noticeable impact on chemical stability.
Corrosion Rates (mg/cm2/100hr) NaSICON material 15% NaOH 50% NaOH
A-03 1.85 0.49 13.41 4.53 A-04 4.22 0.77 24.04 0.08 A-05 2.86 1.18 15.02 2.69 A-06 1.62 0.71 44.45 0.00 A-09 3.24 0.95 35.37 0.28 B-02 1.07 0.10 2.16 0.48 B-03 0.88 0.02 3.53 0.25 B-04 0.68 0.17 3.32 0.07 B-05 0.56 0.06 2.47 0.35 C-01 0.66 0.16 1.44 0.28 D-02 0.87 0.07 2.72 0.04 D-03 0.42 0.17 1.83 0.03 E-05 0.54 0.10 2.3 0.19 E-08 0.49 0.08 1.32 0.30 E-09 1.02 0.21 2.87 0.46 F-01 0.57 0.10 1.6 0.23 F-02 0.38 0.11 1.73 0.33 G-02 0.63 0.14 1.68 0.34 G-03 0.64 0.15 3.12 0.10 G-04 0.7 0.07 3.53 0.17 G-05 0.87 0.02 7.73 0.22 G-06 0.55 0.00 2.37 0.11
NaOH
catholyte. The two compartment E-04 membrane electrolytic cell was operated to recycle and synthesize NaOH from an aqueous stream containing mixed sodium salts. The cell voltage (V) and current density (mA/cm2) during operation of the cell over about 2400 hours is presented in Figure 3. The cell voltage was maintained at a constant voltage of 3 volts.
Sodium Ion Conductivity (mS/cm) at 40 C
NaSICON Material 2-probe 4-probe method A-01 2.98 0.10 A-03 3.49 0.28 A-04 4.43 0.14 A-05 5.77 0.22 A-07 8.50 0.49 A-08 8.22 0.26 9.38 B-02 1.44 0.07 B-03 1.53 0.07 B-04 1.78 0.08 B-05 4.07 0.1 C-01 2.02 0.11 D-02 3.76 0.08 D-03 4.44 0.14 E-04 5.49 0.36 7.08 E-05 6.37 0.26 E-06 4.95 0.10 E-08 6.20 0.39 F-01 5.08 0.19 F-02 6.09 0.24 G-01 14.4 G-02 6.26 0.14 G-03 4.85 0.33 G-04 6.83 0.21 G-05 5.65 0.37 A-01 2.98 0.10
membrane compositions will also exhibit sodium ion conductivity of greater than 1x104 S/cm at ambient temperatures to allow operation of cell above 50 mA/cm2 current density and > than 100 mA/cm2 current density.
The invention includes metal ion conductive MeSICON ceramic materials which conduct cations including, but not limited to, Nat, Lit, K+, Rb+, Cs, or Ag+, or mixtures thereof. Such MeSICON ceramic materials are expected to exhibit chemical stability, metal ion conductivity, and current density the same or similar to the NaSICON-type materials disclosed above.
resistant to acid, alkaline, caustic and/or corrosive chemicals.
Supported structures or membranes may comprise dense layers of metal ion conducting ceramic material supported on porous supports. A variety of forms for the supported membranes are known in the art and would be suitable for providing the supported membranes for metal ion conducting ceramic membranes with supported structures, including, but not limited to: ceramic layers sintered to below full density with resultant continuous open porosity, slotted-form layers, perforated-form layers, expanded-form layers including a mesh, or combinations thereof.
In some embodiments, the porosity of the porous supports is substantially continuous open-porosity so that the liquid solutions on either side of the metal ion conducting ceramic membrane may be in intimate contact with a large area of the dense-layers of metal ion conducting ceramic material, and in some, the continuous open-porosity ranges from about 30 volume% to about 90 volume%. In some embodiments of the present invention, the porous supports for the supported structures may be present on one side of the dense layer of metal ion conducting ceramic material. In some embodiments of the present invention, the porous supports for the supported structures may be present on both sides of the dense layer of metal ion conducting ceramic material.
variety of insulative non-conductive materials are also known in the art, as would be understood by one of ordinary skill in the art. In some specific embodiments, the non-conductive materials may include at least one of the following: ceramic materials, polymers, and/or plastics that are substantially stable in the media to which they are exposed.
Such co-joined metal ion conducting ceramic membrane layers could include MeSICON
materials disclosed herein joined to other metal ion conducting ceramic materials, such as, but not limited to, beta-alumina. Such co-joined layers could be joined to each other using a method such as, but not limited to, thermal spraying, plasma spraying, co-firing, joining following sintering, etc. Other suitable joining methods are known by one of ordinary skill in the art and are included herein.
dependent on the composition, followed by milling of the calcined powder with media such as stabilized-zirconia or alumina or another media known to one of ordinary skill in the art to achieve the prerequisite particle size distribution. To achieve the prerequisite particle size distribution, the calcined powder may be milled using a technique such as vibratory milling, attrition milling, jet milling, ball milling, or another technique known to one of ordinary skill in the art, using media (as appropriate) such as stabilized-zirconia or alumina or another media known to one of ordinary skill in the art.
The resulting green form ceramic membrane may then be sintered to form an alkali cation-conductive ceramic membrane using a technique known to one of ordinary skill in the art, such as conventional thermal processing in air, or controlled atmospheres to minimize loss of individual components of the alkali cation-conductive ceramic membranes. In some embodiments of the present invention it may be advantageous to fabricate the ceramic membrane in a green form by die-pressing, optionally followed by isostatic pressing. In other embodiments of the present invention it may potentially be advantageous to fabricate the ceramic membrane as a multi-channel device in a green form using a combination of techniques such as tape casting, punching, laser-cutting, solvent bonding, heat lamination, or other techniques known to one of ordinary skill in the art. Specifically, for NaSICON-type materials, a ceramic membrane in a green-form may be green-formed by pressing in a die, followed by isostatic pressing and then sintering in air in the range of from about 925 C to about 1300 C for up to about 8 hours to make sintered metal ion conductive ceramic membrane structures with dense layers of metal ion conductive ceramic materials. Standard x-ray diffraction analysis techniques may be performed to identify the crystal structure and phase purity of the metal ion conductive ceramic materials in the sintered ceramic membrane.
physical vapor deposition, chemical vapor deposition, sputtering, thermal spraying, or plasma spraying. The thickness of the metal ion conductive ceramic membrane formed by a vapor deposition method onto a porous support is generally from about 1 um to about 100um, but may be varied as is known to one of ordinary skill in the art.
and (5) The membrane provides the added benefits of very low parasitic, losses due to the absence of fouling by precipitants, or electro osmotic transport of H20, which are common with organic or polymer membranes.
30(1): p. 102-105.
Journal of the European Ceramic Society, 2005. 25(4): p. 455-462.
Ionics, 2002. 8(5): p. 383-390.
Materials Research Bulletin, 1985. 20(6): p. 643-651.
28-30(Pt. 1): p. 419-23.
273-277.
Claims (17)
Me1+x+y-z M Ill y M IV2-y Si x P3-x O12-(z/2) wherein Me is Na+, Li+, K+, Rb+, Cs+, Ag+, or mixtures thereof, 2.0<= x <= 2.4, 0.0 <= y <= 1.0, 0.25 <= z <= 0.9, and z >= (x+y-3), where is M III is Al3+, Ga3+, Cr3+, Sc3+, Fe3+, In3+, Yb3+, Y3+, or mixtures thereof and M IV is Ti4+, Zr4+, Hf4+, or mixtures thereof.
0.12, and 0.25 <= z <= 0.9.
Applications Claiming Priority (3)
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| US12/492,834 | 2009-06-26 | ||
| US12/492,834 US8246863B2 (en) | 2009-06-26 | 2009-06-26 | Alkali metal super ionic conducting ceramic |
| PCT/US2010/038877 WO2010151468A2 (en) | 2009-06-26 | 2010-06-16 | Alkali metal super ionic conducting ceramic |
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| CA2759663A1 CA2759663A1 (en) | 2010-12-29 |
| CA2759663C true CA2759663C (en) | 2016-01-12 |
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| CL2004001161A1 (en) * | 2003-05-21 | 2005-04-08 | Boehringer Ingelheim Int | COMPOUNDS DESCRIBES COMPOUNDS DERIVED FROM QUINOLINA; PHARMACEUTICAL COMPOSITION; AND ITS USE TO TREAT AN ILLNESS CAUSED BY THE HEPATITIS C VIRUS. |
| US7941244B2 (en) * | 2007-09-25 | 2011-05-10 | Amazon Technologies, Inc. | Stow and sortation system |
| US9957622B2 (en) | 2009-07-23 | 2018-05-01 | Field Upgrading Limited | Device and method of obtaining diols and other chemicals using decarboxylation |
| US9051656B2 (en) * | 2009-07-23 | 2015-06-09 | Ceramatec, Inc. | Electrochemical synthesis of aryl-alkyl surfacant precursor |
| US8506789B2 (en) * | 2009-07-23 | 2013-08-13 | Ceramatec, Inc. | Method of producing coupled radical products |
| US9206515B2 (en) | 2009-07-23 | 2015-12-08 | Ceramatec, Inc. | Method of producing coupled radical products via desulfoxylation |
| US20110024288A1 (en) * | 2009-07-23 | 2011-02-03 | Sai Bhavaraju | Decarboxylation cell for production of coupled radical products |
| US9493882B2 (en) | 2010-07-21 | 2016-11-15 | Ceramatec, Inc. | Custom ionic liquid electrolytes for electrolytic decarboxylation |
| US9057137B2 (en) | 2010-08-05 | 2015-06-16 | Ceramatec, Inc. | Method and device for carboxylic acid production |
| US8821710B2 (en) | 2011-01-25 | 2014-09-02 | Ceramatec, Inc. | Production of fuel from chemicals derived from biomass |
| US8853463B2 (en) | 2011-01-25 | 2014-10-07 | Ceramatec, Inc. | Decarboxylation of levulinic acid to ketone solvents |
| WO2013031507A1 (en) * | 2011-08-31 | 2013-03-07 | 旭硝子株式会社 | Method for producing lithium-ion conductive solid electrolyte, and lithium-ion secondary battery |
| WO2013109622A1 (en) * | 2012-01-16 | 2013-07-25 | Ceramatec, Inc | Lithium-ion-conducting materials |
| EP2900594B1 (en) * | 2012-09-25 | 2018-01-10 | University of Maryland, College Park | High conductivity nasicon electrolyte for room temperature solid- state sodium ion batteries |
| JPWO2014136650A1 (en) * | 2013-03-05 | 2017-02-09 | 旭硝子株式会社 | Method for producing lithium ion conductive glass ceramics, lithium ion conductive glass ceramics and lithium ion secondary battery |
| US11888149B2 (en) | 2013-03-21 | 2024-01-30 | University Of Maryland | Solid state battery system usable at high temperatures and methods of use and manufacture thereof |
| JP2016517146A (en) | 2013-03-21 | 2016-06-09 | ユニバーシティー オブ メリーランド、カレッジ パーク | Ion conductive battery containing solid electrolyte material |
| JP2015026483A (en) * | 2013-07-25 | 2015-02-05 | トヨタ自動車株式会社 | Positive electrode for sodium batteries, and sodium battery |
| JP6362882B2 (en) * | 2014-03-13 | 2018-07-25 | エナジー・ストレージ・マテリアルズ合同会社 | Solid ion capacitor and manufacturing method thereof |
| JP6362883B2 (en) * | 2014-03-13 | 2018-07-25 | エナジー・ストレージ・マテリアルズ合同会社 | Solid ion capacitor and method of manufacturing solid ion capacitor |
| WO2017053578A1 (en) | 2015-09-22 | 2017-03-30 | Ceramatec, Inc. | Multi-stage sodium heat engine for electricity and heat production |
| DE102015013155A1 (en) * | 2015-10-09 | 2017-04-13 | Forschungszentrum Jülich GmbH | Electrolytic material with NASICON structure for solid sodium ion batteries and process for their preparation |
| WO2018056020A1 (en) * | 2016-09-20 | 2018-03-29 | 株式会社村田製作所 | Solid electrolyte and all-solid-state battery |
| EP3752308A4 (en) | 2018-02-15 | 2021-11-17 | University of Maryland, College Park | ORDERLY, POROUS SOLID ELECTROLYTE STRUCTURES, ELECTROCHEMICAL DEVICES THEREFORE, METHOD FOR MANUFACTURING THEREOF |
| US12154702B1 (en) * | 2018-10-15 | 2024-11-26 | Ampcera Inc. | Methods for manufacturing a freestanding solid state ionic conductive membrane |
| US11569527B2 (en) | 2019-03-26 | 2023-01-31 | University Of Maryland, College Park | Lithium battery |
| CN110038452A (en) * | 2019-04-23 | 2019-07-23 | 东南大学 | Load the ceramic nanofibers base compound purifying film and its preparation method and application of silver |
| US11545723B2 (en) | 2019-11-26 | 2023-01-03 | National Technology & Engineering Solutions Of Sandia, Llc | Sodium electrochemical interfaces with NaSICON-type ceramics |
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| US4097345A (en) * | 1976-10-15 | 1978-06-27 | E. I. Du Pont De Nemours And Company | Na5 GdSi4 O 12 and related rare earth sodium ion conductors and electrolytic cells therefrom |
| IT1115372B (en) * | 1977-07-15 | 1986-02-03 | Oronzio De Nora Impianti | TWO-STAGE CERAMIC MEMBRANES FOR ELECTROLYTIC CELLS |
| US4248715A (en) * | 1979-11-23 | 1981-02-03 | Olivier Paul D | Electrolytic chlorine generator |
| WO1984001829A1 (en) * | 1982-10-29 | 1984-05-10 | Radiometer As | Ion-sensitive measuring electrode device |
| US4990413A (en) * | 1989-01-18 | 1991-02-05 | Mhb Joint Venture | Composite solid electrolytes and electrochemical devices employing the same |
| FR2666520B1 (en) * | 1990-09-06 | 1993-12-31 | Pechiney Recherche | METHOD FOR ACTIVATION OF THE SURFACE OF HEAVY METAL CARBIDES WITH A HIGH SPECIFIC SURFACE FOR CATALYTIC REACTIONS. |
| US5290405A (en) * | 1991-05-24 | 1994-03-01 | Ceramatec, Inc. | NaOH production from ceramic electrolytic cell |
| WO2002097907A2 (en) * | 2001-04-06 | 2002-12-05 | Valence Technology, Inc. | Sodium ion batteries |
| EP1976815B1 (en) * | 2006-01-11 | 2012-06-27 | Ceramatec, Inc. | Synthesis of biodiesel using alkali ion conductive ceramic membranes |
| EP2142277A4 (en) * | 2007-04-03 | 2012-01-04 | Ceramatec Inc | ELECTROCHEMICAL PROCESS FOR RECYCLING AQUEOUS ALKALI CHEMICALS USING ION-CONDUCTING CERAMIC SOLID MEMBRANES |
| US8012621B2 (en) * | 2007-11-26 | 2011-09-06 | Ceramatec, Inc. | Nickel-metal hydride battery using alkali ion conducting separator |
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| US8246863B2 (en) | 2012-08-21 |
| CA2759663A1 (en) | 2010-12-29 |
| JP5701868B2 (en) | 2015-04-15 |
| JP2012531709A (en) | 2012-12-10 |
| EP3760603A1 (en) | 2021-01-06 |
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