Patent Application
20190126589
The present invention relates to a functional layer including a layered double hydroxide, and a composite material.
A layered double hydroxide (hereafter also referred to LDH) is a material having an exchangeable anions and H2O as intermediate layers between stacked basic hydroxide layers, and is used as, for example, catalysts, adsorbents and dispersants in polymers for improving heat resistance to take its advantage.
The LDH has also been attractive as a material that conducts hydroxide ions; hence, addition of the LDH to an electrolyte of an alkaline fuel cell and a catalytic layer of a zinc air battery has been studied. In particular, the use of a LDH as a solid electrolyte separator for alkaline secondary batteries such as nickel-zinc secondary batteries and zinc-air secondary batteries has been recently proposed, and composite materials with a LDH containing functional layer suitable for such a separator application are known. For example, Patent Document 1 (WO2015/098610) discloses a composite material comprising a porous substrate and a LDH containing functional layer having no water permeability formed on and/or in the porous substrate. The LDH containing functional layer is represented by the general formula: M2+1-xM3+x(OH)2An-x/n.mH2O, wherein M2+ is a divalent cation such as Mg2+, M3+ is a trivalent cation such as Al3+, An- is an n-valent anion such as OH−, CO32-, n is an integer of 1 or more, x is 0.1 to 0.4, and m is 0 or above 0. The LDH containing functional layer disclosed in PLT 1 is densified to such an extent that it has no water permeability. When the LDH is used as a separator, it can prevent deposition of dendritic zinc and penetration of carbon dioxide from an air electrode in zinc air batteries that are obstacles to practical use of alkaline zinc secondary batteries.
Unfortunately, high hydroxide ion conductivity is required for electrolytic solutions of alkaline secondary batteries (for example, metal air batteries and nickel zinc batteries) including LDHs, and thus the use of strong alkaline aqueous potassium hydroxide solution at pH of about 14 is desired. For this purpose, it is desirable for LDH to have high alkaline resistance such that it is barely deteriorated even in such a strong alkaline electrolytic solution. In this regard, Patent Document 2 (WO2016/051934) discloses a LDH containing battery that contains a metallic compound containing a metallic element (for example, Al) corresponding to M2+ and/or M3+ in the general formula described above dissolved in the electrolytic solution to suppress erosion of the LDH.
Patent Document 1: WO2015/098610
Patent Document 2: WO2016/051934
The present inventors have now found that it is possible to provide a LDH containing functional layer having not only high ionic conductivity but also high alkaline resistance by employing a LDH whose basic hydroxide layers are composed of predetermined elements and/or ions including Ni, Al, Ti and OH groups.
Accordingly, an object of the present invention is to provide a LDH containing functional layer having not only high ionic conductivity but also high alkaline resistance, and a composite material with the LDH containing functional layer.
According to one embodiment of the present invention, a functional layer comprising a layered double hydroxide is provided, wherein the layered double hydroxide is composed of: a plurality of basic hydroxide layers comprising Ni, Al, Ti, and OH groups; and intermediate layers composed of anions and H2O, each intermediate layer being interposed between two adjacent basic hydroxide layers.
Another embodiment of the present invention provides a composite material that comprises:
Another embodiment of the present invention provides a battery including the functional layer or the composite material as a separator.
The functional layer of the present invention includes a layered double hydroxide (LDH), and the LDH is composed of: a plurality of basic hydroxide layers; and intermediate layers, each of which is interposed between two adjacent basic hydroxide layers. The basic hydroxide layers include Ni, Al, Ti, and OH groups. The intermediate layers are composed of the intermediate layer composed of anions and H2O. Although the alternately stacked structure itself of basic hydroxide layers and intermediate layers is basically the same as the commonly known alternately stacked structure of LDH, it is possible in the present invention to provide a LDH containing functional layer having not only high ionic conductivity but also high alkaline resistance by employing a LDH whose basic hydroxide layers are composed of predetermined elements and/or ions including Ni, Al, Ti and OH groups.
As described above, high alkaline resistance that barely exhibits the deterioration even in a strong alkaline electrolytic solution is desired for the LDH in alkaline secondary batteries. In this respect, the functional layer of the present invention, a LDH whose basic hydroxide layers are composed of predetermined elements and/or ions including Ni, Al, Ti and OH groups can exhibit high alkaline resistance. Although the reason is not clear, it is believed that Al, which has been considered to be easily dissolved in an alkaline solution, is hard to elute into the alkaline solution due to some interaction with Ni and Ti. Nevertheless, the functional layer of the present invention can also exhibit high ionic conductivity suitable for separators for alkaline secondary batteries.
Ni in the LDH can have the form of nickel ions. Although nickel ions in the LDH are typically believed to be Ni2+, they may be present in any other valence, for example, Ni3+. Ti in the LDH can have the form of titanium ions. Although titanium ions in the LDH are typically believed to be Ti4+, they may be present in any other valence, for example, Ti3+. Each of the incidental impurities is any element which may be inevitably mixed in a manufacturing process, and it may be mixed into the LDH from, for example, a raw material or a substrate. The intermediate layers of the LDH contained in the functional layer are composed of anions and H2O. The anions are monovalent or multivalent anions, preferably monovalent or divalent ions. Preferably, the anions in the LDH include OH and/or CO32-. As described above, it is impractical or impossible to strictly specify the LDH with a general formula since valences of Ni and Ti are not necessarily confirmed. Assuming that the basic hydroxide layers are mainly composed of Ni2+, Ti4+ and OH groups, the basic composition of the corresponding LDH can be represented by the general formula: Ni2+1-xTi4+x(OH)2An-2x/n.mH2O, wherein An- is an n-valent anion, n is an integer of 1 or more, preferably 1 or 2, x is above 0 to below 1, preferably 0.01 to 0.5, and m is a real number of 0 or more, typically a real number above 0 or 1 or more. However, it should be understood that the general formula indicates merely the “basic composition”, and it may be replaced with other elements or ions (including elements with other valences of the same element, or elements or ions that may be unavoidably mixed in the manufacturing process) to such an extent that the elements such as Ni2+, and Ti4+ do not impair the basic properties of LDH.
In the functional layer, the atomic ratio Ti/(Ni+Ti+Al) determined by energy dispersive X-ray analysis (EDS), is preferably 0.10 to 0.90, more preferably 0.20 to 0.80, further preferably 0.25 to 0.70, particularly preferably 0.30 to 0.61. Within these ranges, both the alkaline resistance and the ion conductivity can be improved. Accordingly, the functional layer may contain not only LDH but also Ti in an amount large enough to produce titania as a by-product. That is, the functional layer may further include titania. Inclusion of titania leads to high hydrophilicity, which is expected to improve wettability with an electrolytic solution (namely to improve conductivity).
The LDH contained in the functional layer preferably undergoes no changes in the surface microstructure and crystalline structure when immersed in a 5 mol/L aqueous potassium hydroxide solution containing zinc oxide in a concentration of 0.4 mol/L at 70° C. for three weeks or 504 hours because such an LDH has high alkaline resistance. The presence of a change in the surface microstructure can be preferably determined by SEM (Scanning Electron Microscopy), and the presence of a change in the crystalline structure can be preferably determined by crystalline structural analysis (for example, a shift in (003) peak) by XRD (X-ray diffractometry).
The functional layer (in particular, the LDH contained in the functional layer) has preferably hydroxide ion conductivity. The functional layer has preferably an ionic conductivity of at least 0.1 mS/cm, more preferably at least 0.5 mS/cm, and most preferably at least 1.0 mS/cm. Higher ionic conductivity is preferred. The upper limit thereof is for example, 10 mS/cm, which should not be construed as limiting. Such high ionic conductivity is particularly suitable for battery application. For example, it is preferred to lower the resistance by thinning in order to put the LDH into practical use, and providing the LDH containing functional layers with desirably low resistance according to the embodiment is particularly advantageous in the application of LDH as a solid electrolyte separator for alkaline secondary batteries such as zinc air batteries or nickel zinc batteries.
Preferably, the functional layer is disposed on the porous substrate and/or embedded into the porous substrate. That is, a preferred embodiment of the present invention provides a composite material comprising a porous substrate and a functional layer disposed on the porous substrate and/or embedded into the porous substrate. For example, as in the composite material 10 shown in
The porous substrate in the composite material of the present invention can preferably form the LDH containing functional layer thereon and/or therein. The substrate may be composed of any material and have any porous structure. Although it is typical to form the LDH containing functional layer on and/or in the porous substrate, the LDH containing functional layer may be formed on a non-porous substrate and then the non-porous substrate may be modified into a porous form by any known method. In any case, the porous substrate has preferably a porous structure having good water permeability and it can deliver electrolytic solution to the functional layer when incorporated into a battery as a separator for the battery.
The porous substrate is composed of, preferably, at least one selected from the group consisting of ceramic materials, metallic materials, and polymeric materials, more preferably, at least one selected from the group consisting of ceramic materials and polymeric materials. More preferably, the porous substrate is composed of ceramic materials. In this case, preferred examples of the ceramic material include alumina, zirconia, titania, magnesia, spinel, calcia, cordierite, zeolite, mullite, ferrite, zinc oxide, silicon carbide, and any combination thereof. More preferred examples include alumina, zirconia, titania, and any combination thereof. Particularly preferred examples include alumina, zirconia (for example, yttria-stabilized zirconia (YSZ)), and combination thereof. Using these porous ceramics, a LDH containing functional layer with high density can be readily formed. Preferred examples of the metallic material include aluminum, zinc, and nickel. Preferred examples of the polymeric material include polystyrene, polyethersulfone, polypropylene, epoxy resin, poly(phenylene sulfide), hydrophilized fluororesin (such as tetrafluoro resin: PTFE), cellulose, nylon, polyethylene and any combination thereof. All these preferred materials have high resistance to the alkaline electrolytic solution of the battery.
Further preferably, the porous substrate is composed of the polymeric material. The polymeric porous substrate has the following advantageous properties; (1) high flexibility (hard to crack even if thinned), (2) high porosity, (3) high conductivity (thin thickness with high porosity), and (4) good manufacturability and handling ability. Further preferred polymeric materials are polyolefins such as, for example, polypropylene, polyethylene, and most preferably polypropylene from the viewpoint of high resistance to hot water, high acid resistance and high alkaline resistance, as well as low cost. When the porous substrate is composed of the polymeric material, it is more preferred that the functional layer is embedded into the entire porous substrate over the thickness (for example, most or substantially all of the pores inside the porous substrate are filled with the LDH). The preferred thickness of the polymeric porous substrate in this case is 5 to 200 μm, more preferably 5 to 100 μm, most preferably 5 to 30 μm. Usable polymer porous substrates are microporous membranes commercially available as separators for lithium batteries.
The porous substrate has preferably a mean pore diameter of at most 100 μm, more preferably at most 50 μm, for example, typically 0.001 to 1.5 μm, more typically 0.001 to 1.25 μm, further more typically 0.001 to 1.0 μm, particularly typically 0.001 to 0.75 μm, most typically 0.001 to 0.5 μm. Within these ranges, a dense LDH containing functional layer having no water permeability can be formed while keeping desirable water permeability and strength as a support for the porous substrate. In the present invention, the mean pore size can be determined by measuring the largest dimension of each pore based on the electron microscopic image of the surface of the porous substrate. The electron microscopic image is measured at 20,000-fold magnification or more. All the measured pore sizes are listed in order of size to calculate the average, from which the subsequent 15 larger sizes and the subsequent 15 smaller sizes, i.e., 30 diameters in total, are selected in one field of view. The selected sizes of two fields of view are then averaged to yield the average pore size. In the measurement, a dimension measuring function in software of SEM or image analyzing software (for example, Photoshop manufactured by Adobe) can be used.
The porous substrate has a porosity of preferably 10 to 60%, more preferably 15 to 55%, most preferably 20 to 50%. Within these ranges, the resulting dense LDH containing functional layer has no water permeability while the porous substrate keeps desirable water permeability and required strength as a support. The porosity of the porous substrate can be preferably measured by Archimedes' method. In the case where the porous substrate is composed of the polymeric material and the functional layer is embedded over the region of the porous substrate in the thickness direction, the porosity of the porous substrate is preferably 30 to 60%, more preferably 40 to 60%.
The functional layer preferably has no air permeability. That is, it is preferred that the functional layer be densified with the LDH to such an extent that it has no air permeability. In the present specification, the phrase “having no air permeability” has the following meaning: In the case of evaluation of air permeability by the “density determination test” adopted in the examples described later or a similar method, no bubbling of helium gas is observed at one side of the measured object, i.e., the functional layer and/or the porous substrate even if helium gas is brought into contact with the other side in water at a differential pressure of 0.5 atm across the thickness. By this densification, the functional layer or the composite material as a whole selectively allows only the hydroxide ion due to its hydroxide ion conductivity to pass through, and can function as separators for batteries. In the case of the application of LDH as solid electrolyte separators for batteries, although the bulk LDH dense body has high resistance, the LDH containing functional layer in a preferred embodiment of the present invention can be thinned to reduce the resistance because the porous substrate has high strength. In addition, the porous substrate can have high water permeability and air permeability; hence, the electrolytic solution can reach the LDH containing functional layer when used as solid electrolyte separators of batteries. In summary, the LDH containing functional layer and the composite material of the present invention are very useful materials for solid electrolyte separators applicable to various batteries, such as metal air batteries (for example, zinc air batteries) and various other zinc secondary batteries (for example, nickel zinc batteries).
In the functional layer or the composite material including the functional layer, a helium permeability per unit area is preferably 10 cm/min·atm or less, more preferably 5.0 cm/min·atm or less, most preferably 1.0 cm/min·atm or less. The functional layer having such a range of helium permeability has extremely high density. When the functional layer having a helium permeability of 10 cm/min·atm or less is applied as a separator in an alkaline secondary battery, passage of substances other than hydroxide ions can be effectively prevented. For example, zinc secondary batteries can significantly effectively suppress penetration of Zn in the electrolytic solution. Since penetration of Zn is remarkably suppressed in this way, it can be believed in principle that deposition of dendritic zinc can be effectively suppressed in zinc secondary batteries. The helium permeability is measured through supplying helium gas to one surface of the functional layer to allow helium gas to pass through the functional layer and calculating the helium permeability to evaluate density of the functional layer. The helium permeability is calculated from the expression of F/(P×S) where F is the volume of permeated helium gas per unit time, P is the differential pressure applied to the functional layer when helium gas permeates through, and S is the area of the membrane through which helium gas permeates. Evaluation of the permeability of helium gas in this manner can extremely precisely determine the density. As a result, a high degree of density that does not permeate as much as possible (or permeate only a trace amount) substances other than hydroxide ions (in particular, zinc that causes deposition of dendritic zinc) can be effectively evaluated. Helium gas is suitable for this evaluation because the helium gas has the smallest constitutional unit among various atoms or molecules which can constitute the gas and its reactivity is extremely low. That is, helium does not form a molecule, and helium gas is present in the atomic form. In this respect, since hydrogen gas is present in the molecular form (H2), atomic helium is smaller than molecular H2 in a gaseous state. Basically, H2 gas is combustible and dangerous. By using the helium gas permeability defined by the above expression as an index, the density can be objectively and readily evaluated regardless of differences in sample size and measurement condition. Thus, whether the functional layer has sufficiently high density suitable for separators of zinc secondary batteries can be evaluated readily, safely and effectively. The helium permeability can be preferably measured in accordance with the procedure shown in Evaluation 5 in Examples described later.
The LDH includes agglomerates of platy particles (that is, LDH platy particles), and surfaces of platy particles are preferably oriented perpendicular or oblique to the surface of the functional layer (the surface when macroscopically observed to such an extent that the fine irregularities of the functional layer can be ignored). In the case that the functional layer is provided on the porous substrate, the functional layer has a membrane portion provided above the porous substrate. In this case, the LDH constituting the membrane portion includes agglomerates of platy particles (that is, LDH platy particles), and surfaces of platy particles are preferably oriented perpendicular or oblique to the surface of the porous substrate (the surface of the porous substrate when macroscopically observed to such an extent that the fine irregularities due to the porous structure can be ignored). In the case that the functional layer has a composite portion to be embedded in the porous substrate, the LDH platy particles may also be present in the pores of the porous substrate. Also, the membrane portion may further contain ceramic particles such as alumina particles as a filler to increase the adhesive strength between the LDH in the membrane portion and the substrate.
It is known that LDH crystals have the form of platy particles including a layered structure as shown in
The functional layer has preferably a thickness of 100 μm or less, more preferably 75 μm or less, further preferably 50 μm or less, particularly preferably 25 μm or less, most preferably 5 μm or less. Such thinning can reduce the resistance of the functional layer. In the case where the functional layer is formed as the LDH membrane on the porous substrate, the thickness of the functional layer corresponds to the thickness of the membrane portion composed of the LDH membrane. In the case where the functional layer is formed to be embedded into the porous substrate, the thickness of the functional layer corresponds to the thickness of the composite potion composed of the porous substrate and the LDH. In the case where the functional layer is formed on and in the porous substrate, the thickness of the functional layer corresponds to the total thickness of the membrane portion (the LDH membrane) and the composite portion (the porous substrate and the LDH). In any case, the above thickness leads to a low resistance suitable for practical use in, for example, battery application. Although the lower limit of the thickness of the LDH membrane is not limited because it depends on the application, the thickness is preferably 1 μm or more, more preferably 2 μm or more in order to assure a certain degree of rigidity suitable for a functional membrane such as a separator.
The LDH containing functional layer and the composite material can be produced by any method. They can be produced by appropriately modifying conditions of a known method for producing LDH containing functional layers and composite materials (see, for example, PLT 1 and 2). For example, the LDH containing functional layer and the composite material can be produced by (1) providing a porous substrate, (2) applying a mixed sol of alumina and titania onto the porous substrate and then heating the sol to form an alumina/titania layer, (3) immersing the porous substrate into an aqueous raw material solution containing nickel ions (Ni2+) and urea, and (4) hydrothermally treating the porous substrate in the aqueous raw material solution to form the LDH containing functional layer on the porous substrate and/or in a porous substrate. In particular, in Step (2), forming the alumina/titania layer on the porous substrate can not only produce a raw material for the LDH, but also serve as a seed of LDH crystalline growth and uniformly form the LDH containing functional layer that is highly densified on the surface of the porous substrate. In addition, in Step (3), the presence of urea raises the pH value through generation of ammonia in the solution through the hydrolysis of urea, and gives the LDH by formation of hydroxide with coexisting metal ions. Also, generation of carbon dioxide in hydrolysis gives the LDH of a carbonate anion type.
In particular, a composite material in which the porous substrate is composed of a polymeric material and the functional layer is embedded over the porous substrate in the thickness direction is produced by applying the mixed sol of alumina and titania to the substrate in Step (2) in such that the mixed sol permeates into all or most area of the interior pores of the substrate. By this manner, most or substantially all pores inside the porous substrate can be embedded with the LDH. Examples of preferred application include dip coating and filtration coating. Particularly preferred is dip coating. The amount of the deposited mixed sol can be varied by adjusting the number of times of coating such as dip coating. The substrate coated with the mixed sol by, for example, dip coating may be dried and then subjected to Steps (3) and (4).
The present invention will be described in more detail by the following examples. The functional layers and the composite materials produced in the following examples were evaluated as follows:
The crystalline phase of the functional layer was measured with an X-ray diffractometer (RINT TTR III manufactured by Rigaku Corporation) at a voltage of 50 kV, a current of 300 mA, and a measuring range of 10° to 70° to give an XRD profile. The resultant XRD profile was identified with the diffraction peaks of LDH (hydrotalcite compound) described in JCPDS card NO. 35-0964.
The surface microstructure of the functional layer was observed at an accelerating voltage of 10 to 20 kV with a scanning electron microscope (SEM, JSM-6610LV, manufactured by JEOL Ltd.). After preparation of a cross-sectional polished surface of the functional layer (a membrane portion composed of a LDH membrane and a composite portion composed of the LDH and the substrate) with an ionic milling system (IM4000, manufactured by Hitachi High-Technologies Corporation), the microstructure of the cross-sectional polished surface was observed with the SEM under the same conditions.
The functional layer (the membrane portion composed of the LDH membrane and the composite portion composed of the LDH and the substrate) was polished across the thickness for observation with a cross-sectional polisher (CP). A field of cross-sectional image of the functional layer (the membrane portion composed of the LDH membrane and the composite portion composed of the LDH and the substrate) was observed with a 10,000-fold magnification with FE-SEM (ULTRA 55, manufactured by Carl Zeiss). The LDH membrane on the substrate surface and the LDH portion (by point analysis) inside the substrate in this cross-sectional image was subjected to elemental analysis at an accelerating voltage of 15 kV with an EDS analyzer (NORAN System SIX, manufactured by Thermo Fisher Scientific Inc.).
Compositional analysis was performed on the surface of the functional layer with an EDS analyzer (a brand name of the analyzer: X-act, manufactured by Oxford Instruments plc) to calculate an atomic ratio Ti/(Ni+Ti+Al). This analysis comprises 1) taking an image at an acceleration voltage of 20 kV with 5,000-fold magnification, 2) analysis in a point analytic mode at three points spaced with about 5 μm each other, 3) repeating Steps 1) and 2) further two times, and 4) calculation of the average value of nine points in total.
Zinc oxide was dissolved in 6 mol/L of aqueous potassium hydroxide solution to yield 5 mol/L of aqueous potassium hydroxide solution that contained 0.4 mol/L of zinc oxide. In the next stage, 15 mL of the resultant aqueous potassium hydroxide solution was placed in a hermetic container made of Teflon™. A composite material having dimensions of 1 cm×0.6 cm was placed on the bottom of the hermetic container such that the functional layer faced upward, and the lid was closed. The composite material was held at 70° C. (Examples 1 to 5) or 30° C. (Example 6) for one week (168 hours), three weeks (504 hours) or 7 weeks (1176 hours) and then removed from the hermetic container. The composite material was dried overnight at room temperature. The microstructure of the resultant sample was observed with SEM and the crystalline structure was analyzed with XRD. In the analysis of crystalline structure by XRD, if a shift of the peak (26) beyond 0.25° with respect to the (003) peak of LDH occurs after immersion in the aqueous potassium hydroxide solution, the crystalline structure was determined to be significantly changed.
The conductivity of the functional layer in the electrolytic solution was measured with an electrochemical measurement system shown in
The density was determined to confirm that the functional layer had density having no air permeability. As shown in
A helium permeation test was conducted to evaluate the density of the functional layer from the viewpoint of helium permeability. The helium permeability measurement system 310 shown in
The sample holder 316 had a structure including a gas supply port 316a, a sealed space 316b and a gas discharge port 316c, and was assembled as follows: An adhesive 322 was applied along the outer periphery of the functional layer 318 and bonded to a jig 324 (made of ABS resin) having a central opening. Gaskets or sealing members 326a, 326b made of butyl rubber were disposed at the upper end and the lower end, respectively, of the jig 324, and then the outer sides of the members 326a, 326b were held with supporting members 328a, 328b (made of PTFE) each including a flange having an opening. Thus, the sealed space 316b was partitioned by the functional layer 318, the jig 324, the sealing member 326a, and the supporting member 328a. The functional layer 318 was in the form of a composite material formed on the porous substrate 320, and was disposed such that the functional layer 318 faced the gas supply port 316a. The supporting members 328a and 328b were tightly fastened to each other with fastening means 330 with screws not to cause leakage of helium gas from portions other than the gas discharge port 316c. A gas supply pipe 34 was connected to the gas supply port 316a of the sample holder 316 assembled as above through a joint 332.
Helium gas was then supplied to the helium permeability measurement system 310 via the gas supply pipe 334, and the gas was permeated through the functional layer 318 held in the sample holder 316. A gas supply pressure and a flow rate were then monitored with a pressure gauge 312 and a flow meter 314. After permeation of helium gas for one to thirty minutes, the helium permeability was calculated. The helium permeability was calculated from the expression of F/(P×S) where F (cm3/min) was the volume of permeated helium gas per unit time, P (atm) was the differential pressure applied to the functional layer when helium gas permeated through, and S (cm2) was the area of the membrane through which helium gas permeates. The permeation rate F (cm3/min) of helium gas was read directly from the flow meter 314. The gauge pressure read from the pressure gauge 312 was used for the differential pressure P. Helium gas was supplied such that the differential pressure P was within the range of 0.05 to 0.90 atm.
A BF-STEM image of the functional layer was taken with a scanning transmission electron microscope (STEM) (a brand name: JEM-ARM200F, manufactured by JEOL). The BF-STEM image was subjected to Fast Fourier Transform (FFT) analysis to give an analytical pattern after FFT. The resultant analytical pattern was compared with the result of the electron analysis simulation of the anatase titanium oxide and it was then confirmed whether the lattice constant read from the analytical pattern after FFT roughly corresponds to the anatase titanium oxide.
A functional layer including Ni/Al/Ti-containing LDH and a composite material were prepared and evaluated by a following procedure.
One hundred parts by weight of zirconia powder (TZ-8YS manufactured by Tosoh Corporation), 70 parts by weight of a dispersing medium (xylene:butanol=1:1), 11.1 parts by weight of a binder (polyvinyl butyral: BM-2 manufactured by Sekisui Chemical Co., Ltd.), 5.5 parts by weight of a plasticizer (DOP manufactured by Kurogane Kasei Co., Ltd.), and 2.9 parts by weight of a dispersant (Rheodol SP-030 manufactured by Kao Corporation) were mixed, and the mixture was stirred to be deformed under reduced pressure to yield a slurry. The slurry was shaped into a sheet on a PET film with a tape shaping machine to yield a green sheet having the membrane thickness of 220 μm after drying. The green sheet was cut into 2.0 cm×2.0 cm×0.022 cm and fired at 1100° C. for two hours to yield a porous substrate made of zirconia.
The porosity of the porous substrate was measured to be 40% by Archimedes' method.
The observed mean pore size of the porous substrate was 0.2 μm. In the present invention, the mean pore size was determined by measuring the longest dimension of each pore based on the scanning electron microscopic (SEM) image of the surface of the porous substrate. The SEM image was observed at 20,000-fold magnification. All the measured pore sizes are listed in order of size to calculate the average, from which the subsequent 15 larger sizes and the subsequent 15 smaller sizes, i.e., 30 diameters in total, are selected in one field of view. The selected sizes of two fields of view are then averaged to yield the average pore size. In the measurement, a dimension measuring function in software of SEM was used.
An amorphous alumina solution (AI-ML15 manufactured by Taki Chemical Co., Ltd.) and a titanium oxide sol solution (M6 manufactured by Taki Chemical Co., Ltd.) (weight ratio of 1:1) were mixed at Ti/AI molar ratios shown in Table 1 to prepare a mixed sol. The zirconia porous substrate prepared in Procedure (1) was coated with 0.2 mL of the mixed sol by spin coating. In the spin coating, the mixed sol was dropwise added to the substrate spinning at a rotation rate of 8,000 rpm, then the spin was stopped after five seconds. The substrate was placed on a hot plate heated to 100° C. and dried for one minute. The substrate was heated at 300° C. in an electric furnace. The thickness of the layer formed by this procedure was about 1 μm.
Nickel nitrate hexahydrate (Ni (NO3)2.6H2O, manufactured by Kanto Chemical CO., Inc.), and urea ((NH2)2CO, manufactured by Sigma-Aldrich Corporation) were provided as raw materials. Nickel nitrate hexahydrate was weighed to be 0.015 mol/L and placed in a beaker, and ion-exchanged water was added thereto into a total amount of 75 mL. After stirring the solution, the urea weighed at a urea/NO3− molar ratio of 16 was added, and further stirred to give an aqueous raw material solution.
The aqueous raw material solution prepared in Procedure (3) and the substrate prepared in Procedure (2) were placed in a Teflon™ hermetic container (autoclave, the internal volume: 100 mL, and covered with stainless steel jacket). The substrate was horizontally fixed away from the bottom of Teflon™ hermetic container such that the solution was in contact with the two surfaces of the substrate. A LDH was then formed on the surface and the interior of the substrate by a hydrothermal treatment at a temperature of 150° C. for 72 hours (Example 1) or 120° C. for 24 hours (Example 2 to 5). After a predetermined period, the substrate was removed from the hermetic container, washed with ion-exchanged water, and dried at 70° C. for ten hours to yield a LDH containing functional layer partly embedded in the porous substrate. The thickness of the functional layer was about 5 μm (including the thickness of the portion embedded in the porous substrate).
Evaluations 1 to 8 were performed on the resultant functional layer or composite material. Evaluation 9 was performed on Example 4 only. The results were as follows.
Table 1 shows the results of SEM observation in Examples 1 to 5.
A functional layer including Mg/Al-containing LDH and a composite material were prepared and evaluated by a following procedure.
One hundred parts by weight of alumina powder (AES-12 manufactured by Sumitomo Chemical Co., Ltd.), 70 parts by weight of a dispersing medium (xylene:butanol=1:1), 11.1 parts by weight of a binder (polyvinyl butyral: BM-2 manufactured by Sekisui Chemical Co., Ltd.), 5.5 parts by weight of a plasticizer (DOP manufactured by Kurogane Kasei Co., Ltd.), and 2.9 parts by weight of a dispersant (Rheodol SP-O30 manufactured by Kao Corporation) were mixed, and the mixture was stirred to be deformed under vacuum to yield a slurry. The slurry was shaped into a sheet on a PET film with a tape shaping machine to yield a green sheet having the film thickness of 220 μm after drying. The green sheet was cut into dimensions of 2.0 cm×2.0 cm×0.022 cm and fired at 1300° C. for two hours to yield a porous substrate made of alumina.
The porosity of the porous substrate was determined to be 40% by Archimedes' method.
The mean pore size of the porous substrate was also determined to be 0.3 μm. In the present invention, the mean pore size was determined by measuring the longest dimension of each pore based on the scanning electron microscopic (SEM) image of the surface of the porous substrate. The SEM image was observed at 20,000-fold magnification. All the measured pore sizes are listed in order of size to calculate the average, from which the subsequent 15 larger sizes and the subsequent 15 smaller sizes, i.e., 30 diameters in total, are selected in one field of view. The selected sizes of two fields of view are then averaged to yield the average pore size. In the measurement, a dimension measuring function in software of SEM was used.
A polystyrene substrate (0.6 g) was dissolved in a xylene solution (10 mL) to prepare a spin coating solution having a polystyrene concentration of 0.06 g/mL. The resulting spin coat solution (0.1 mL) was dropwise applied and spin-coated on the 8YSZ porous substrate at a rotation rate of 8,000 rpm. The spin coating was continued for 200 seconds including the dropwise application and drying. The porous substrate coated with the spin coating solution was sulfonated in 95% sulfuric acid at 25° C. for four days.
(3) Preparation of Aqueous Raw Material Solution Magnesium nitrate hexahydrate (Mg(NO3)2.6H2O, manufactured by Kanto Chemical CO., Inc.), aluminum nitrate nonahydrate (Al(NO3)3.9H2O, manufactured by Kanto Chemical CO., Inc.), and urea ((NH2)2CO, manufactured by Sigma-Aldrich Corporation) were provided as raw materials. Magnesium nitrate hexahydrate and aluminum nitrate nonahydrate were weighed such that a cation ratio (Mg2+/Al3+) was 2 and a molar concentration of the total metal ions (Mg2++Al3+) was 0.320 mol/L to be placed in a beaker. Ion-exchanged water was added thereto into a total amount of 70 mL. After stirring the solution, the urea weighed at a urea/NO3− molar ratio of 4 was added, and further stirred to yield an aqueous raw material solution.
The aqueous raw material solution prepared in Procedure (3) and the substrate prepared in Procedure (2) were placed in a Teflon™ hermetic container (autoclave, the internal volume: 100 mL, and covered with stainless steel jacket). The substrate was horizontally fixed away from the bottom of Teflon™ hermetic container such that the solution was in contact with the two surfaces of the substrate. A LDH oriented membrane was then formed on the surface of the substrate by a hydrothermal treatment at a temperature of 70° C. for 168 hours (or seven days). After a predetermined period, the substrate was removed from the hermetic container, washed with ion-exchanged water, and dried at 70° C. for ten hours to give a LDH containing functional layer partly embedded in the porous substrate. The thickness of the functional layer was about 3 μm (including the thickness of the portion embedded in the porous substrate).
Evaluations 1 to 3 and 5 to 8 were performed on the resultant functional layer or composite material. The results were as follows.
A functional layer containing a Ni/Al/Ti-containing LDH and a composite material were prepared with a polymeric porous substrate and evaluated by a following procedure.
A commercially available polypropylene porous substrate having a porosity of 50%, a mean pore size of 0.1 μm and a thickness of 20 μm was cut out into a size of 2.0 cm×2.0 cm.
An amorphous alumina solution (AI-ML15, manufactured by Taki Chemical Co., Ltd.) and a titanium oxide sol solution (M6, manufactured by Taki Chemical Co., Ltd.) were mixed at Ti/Al molar ratio of 2 to yield a mixed sol. The mixed sol was applied onto the substrate prepared in Procedure (1) by dip coating. In dip coating, the substrate was immersed in 100 mL of the mixed sol, pulled up vertically and dried in a dryer at 90° C. for five minutes.
An aqueous raw material solution was prepared as Procedure (3) in Example 1.
The aqueous raw material solution and the dip-coated substrate were placed in a Teflon™ hermetic container (autoclave, the internal volume: 100 mL, and covered with stainless steel jacket). The substrate was horizontally fixed away from the bottom of a Teflon™ hermetic container such that the solution was in contact with the two surfaces of the substrate. The LDH was then formed on the surface of the substrate and in the substrate by a hydrothermal treatment at a temperature of 120° C. for 24 hours. After a predetermined period, the substrate was removed from the hermetic container, washed with ion-exchanged water, and dried at 70° C. for ten hours to give a LDH containing functional layer embedded into the porous substrate.
Evaluations 1 to 8 were performed on the resultant functional layer or the composite material. The results were as follows.
Evaluation 7: The functional layer and the composite material were confirmed to have high density with no air permeability.
Evaluation 8: Helium permeability through the functional layer and the composite material was 0.0 cm/min·atm.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2016-125531 | Jun 2016 | JP | national |
| 2016-125554 | Jun 2016 | JP | national |
| 2016-125562 | Jun 2016 | JP | national |
| PCT/JP2017/003333 | Jan 2017 | JP | national |
This application is a continuation application of PCT/JP2017/022906 filed Jun. 21, 2017, which claims priority to PCT/JP2017/003333 filed Jan. 31, 2017, Japanese Patent Application No. 2016-125531 filed Jun. 24, 2016, Japanese Patent Application No. 2016-125554 filed Jun. 24, 2016, and Japanese Patent Application No. 2016-125562 filed Jun. 24, 2016, the entire contents all of which are incorporated herein by reference.
| Number | Date | Country | |
|---|---|---|---|
| Parent | PCT/JP2017/022906 | Jun 2017 | US |
| Child | 16227612 | US |
