Patent Description:
The following description relates a fuel cell with polymer electrolyte.

Recently, the depletion of existing fossil energy resources such as oil and coal is predicted, and various limitations such as thermal power generation that causes a large amount of greenhouse gases and environmental pollution problems using the fossil energy resources, or nuclear power generation that has problems of stability of the facility itself or waste treatment have been revealed, and interests in alternative energy sources which are more eco-friendly and have high efficiency are being increased. As one of such alternative energy sources, a fuel cell is particularly attracting attention due to advantages such as high efficiency, no emission of pollutants such as NOx and SOx, and abundant fuel to be used.

Among the fuel cells, polymer electrolyte fuel cells have been developed in various ways since proposed in the <NUM> for the purpose of supplying energy to a spacecraft, and include a proton exchange membrane fuel cell (PEMFC) using a hydrogen gas as fuel and a direct methanol fuel cell (DMFC) using liquid methanol as direct fuel supplied to a positive electrode. The supplied fuels, hydrogen and methanol, are almost permanent and produce only water as by-products through electrochemical reactions.

The fuel cell includes a membrane electrode assembly including an anode, a cathode and a hydrogen ion conductive polymer electrolyte membrane located therebetween, and hydrogen or methanol supplied to the anode (oxidation electrode, positive electrode) forms hydrogen ions through a catalytic reaction, the formed hydrogen ions move to the cathode (reduction electrode, negative electrode) through the hydrogen ion conductive polymer electrolyte membrane, and meet electrons, which are moved through an external circuit, and air or oxygen, which is supplied to the cathode, so that water, electric energy, and heat are generated through the reduction reaction.

Numerous types of sulfonated polymers and polymer compositions have been tested as a hydrogen ion conductive polymer electrolyte membrane. However, the sulfonated polymer has a hydrogen ion transfer function in the hydrated state, and accordingly, there are problems in that when the fuel cell is operated at a high temperature of <NUM> or higher, the moisture in the polymer electrolyte membrane decreases and the proton conductivity decreases rapidly due to decomposition of the sulfonic acid group at a high temperature. Various methods have been studied to solve these problems, and typically, there are a method for solving the reduction of proton conductivity at a high temperature of <NUM> or higher by introducing an inorganic oxide such as TiO<NUM>, SiO<NUM>, Al<NUM>O<NUM>, ZrO<NUM>, tetraethoxysilane (TEOS), montmorillonite, or mordenite to a perfluorinated sulfonated ionomer such as Nafion to improve the moisture carrying capacity at a high temperature, and a method for offsetting the reduction of the moisture carrying capacity at a high temperature and the consequent reduction of proton conductivity by introducing heteropolyacid (HPA) such as zirconium phosphoric acid (ZrP), phosphotungstic acid, silicotungstic acid, phospho molybdic acid, and silico molybdic acid having proton conductivity. However, the introduction of the inorganic oxide has a limitation in securing balanced physical properties such as mechanical properties and chemical durability because the inorganic oxide is not uniformly dispersed, and there is a limitation in that the mechanical properties are deteriorated, or basic performances of the polymer electrolyte membrane, such as proton conductivity, thermal stability, and hydration stability, are deteriorated.

Accordingly, there is a need to develop an additive for a polymer electrolyte membrane that can harmoniously improve performances such as mechanical properties, chemical durability, thermal stability, and proton conductivity of the polymer electrolyte membrane. <CIT> discloses a sulfonate-based compound and a polymer electrolyte membrane using the same, a membrane electrode assembly including the same, and a fuel cell including the same.

In one general aspect, a compound is represented by Formula <NUM> below:
<CHM>
wherein R<NUM> to R<NUM> are each independently a hydrogen atom, an alkyl group having <NUM> to <NUM> carbon atoms, a fluoro-substituted alkyl group having <NUM> to <NUM> carbon atoms, or a fluorine atom, wherein at least one among R<NUM> to R<NUM> is a fluorine atom, A is a divalent linking group selected from -O- and -S-, M<NUM> and M<NUM> are each independently potassium or sodium, and n and m are each independently an integer of <NUM> to <NUM>.

R<NUM> to R<NUM> may each independently be the hydrogen atom, where at least one among R<NUM> to R<NUM> is the fluorine atom.

The alkyl group may have <NUM> to <NUM> carbon atoms, where at least one among R<NUM> to R<NUM> is the fluorine atom.

The fluoro-substituted alkyl group may have <NUM> to <NUM> carbon atoms, where at least one among R<NUM> to R<NUM> is the fluorine atom.

R<NUM> to R<NUM> may be the fluorine atom.

In Formula <NUM>, A is -O- or -S- as defined in the claims.

In Formula <NUM>, M<NUM> and M<NUM> may each independently be potassium.

R<NUM> to R<NUM> may all be fluorine atoms, A may be -O-, M<NUM> and M<NUM> may be sodium, and n and m may each independently be an integer of <NUM> to <NUM>.

The compound represented by Formula <NUM> may be represented by Formula <NUM>-<NUM> below:
<CHM>.

A polymer electrolyte membrane may include the compound disclosed.

The polymer electrolyte membrane may have a proton conductivity of <NUM>/cm to <NUM>/cm under the conditions of <NUM> and <NUM>% relative humidity (RH).

The polymer electrolyte membrane may include a polymer support and the compound is comprised in an amount of <NUM> wt% to <NUM> wt% based on a weight of the polymer support.

In another general aspect, a membrane electrode assembly includes an anode, a cathode, and the polymer electrolyte membrane disclosed disposed between the anode and the cathode.

In another general aspect, a fuel cell includes a stack including the at least two membrane electrode assemblies disclosed, and a separator disposed between the membrane electrode assemblies, a fuel supplier configured to supply fuel to the stack, and an oxidizer supplier configured to supply an oxidizer to the stack.

Also, descriptions of features that are known after understanding of the disclosure of this application may be omitted for increased clarity and conciseness.

Spatially relative terms such as "above," "upper," "below," and "lower" may be used herein for ease of description to describe one element's relationship to another element as shown in the figures. Such spatially relative terms are intended to encompass different orientations of the device in use or operation in addition to the orientation depicted in the figures. For example, if the device in the figures is turned over, an element described as being "above" or "upper" relative to another element will then be "below" or "lower" relative to the other element. Thus, the term "above" encompasses both the above and below orientations depending on the spatial orientation of the device. The device may also be oriented in other ways (for example, rotated <NUM> degrees or at other orientations), and the spatially relative terms used herein are to be interpreted accordingly.

Due to manufacturing techniques and/or tolerances, variations of the shapes shown in the drawings may occur. Thus, the examples described herein are not limited to the specific shapes shown in the drawings, but include changes in shape that occur during manufacturing.

It will be further understood that the words or terms should be interpreted as having meanings that are consistent with their meanings in the context of the relevant art and the technical idea of the disclosure, based on the principle that an inventor may properly define the meaning of the words or terms to best explain the disclosure.

As used herein, the term "antioxidant functional group" refers to a functional group that plays a role in suppressing oxidation by having a property of preventing and suppressing a function of active oxygen under conditions such as light and heat with respect to an oxidizing material, and for example, a functional group that serves as an antioxidant by reacting with oxygen radicals of reactive oxygen species (ROS) instead of a polymer electrolyte membrane in an environment in which the polymer electrolyte membrane is attacked by radicals.

As used herein, the term "ion conductive functional group" refers to a functional group that increases ion conductivity, particularly proton conductivity, and for example, a functional group that does not form an ion bond with an anionic functional group of a polymer electrolyte membrane or suppresses the formation thereof, thereby suppressing a decrease in ion conductivity.

As used herein, the term "membrane electrode assembly (MEA)" refers to an assembly of an electrode (anode and cathode) in which an electrochemical catalyst reaction between fuel and air occurs and a polymer electrolyte membrane in which hydrogen ions are transferred, and refers to a single integral unit in which the electrode (anode and cathode) and the polymer electrolyte membrane are bonded.

It will be further understood that the terms "comprising," "including," and "having" and the derivatives thereof as used herein, though these terms are particularly disclosed or not, are not intended to preclude the presence or addition of optional components, steps, or processes. In order to avoid any uncertainty, all materials and methods claimed by using the term "comprising" may include optional additional additives, auxiliaries, or compounds, unless otherwise described. In contrast, the term "consisting essentially of" excludes unnecessary ones for operation and precludes optional other components, steps or processes from the scope of optional continuous description. The term "consisting of" precludes optional components, steps or processes, which are not particularly described or listed.

In the present specification, the "proton conductivity" is measured by cutting a polymer electrolyte membrane into a specimen having a size of <NUM>×<NUM>, engaging the specimen with a four-probe cell, maintaining a temperature/humidity equilibrium for <NUM> hours under conditions of <NUM> and <NUM>% relative humidity (RH) before measurement, and measuring the proton conductivity by dropping the humidity from <NUM>% RH to <NUM>% RH, and then measuring the proton conductivity by increasing the humidity from <NUM>% RH to <NUM>% RH by using BekkTech BT-552MX equipment.

The present disclosure provides a compound with a novel structure which is applied as an additive for a polymer electrolyte membrane, thereby improving the chemical durability, thermal stability, and mechanical stability of the polymer electrolyte membrane and simultaneously improving performance such as proton conductivity.

The compound according to an embodiment of the present disclosure is represented by Formula <NUM> below:
<CHM>.

The compound represented by Formula <NUM> above according to an embodiment of the present disclosure includes both an antioxidant functional group and an ion conductive functional group in the molecule, and thus is applied as an organic additive for the polymer electrolyte membrane, thereby preventing the oxidation of the polymer electrolyte membrane and improving ion conductivity.

Specifically, as the polymer electrolyte membrane, for example, a sulfonated polymer electrolyte membrane is widely used, which is prepared by preparing a membrane from a polymer support and an additive mixture solution as necessary, and dipping the membrane in a reagent such as sulfuric acid to be subjected to a sulfonation reaction. The compound represented by Formula <NUM> above includes a butylbenzene group to which an -OM<NUM> group is bonded in the molecule, and is applied during the preparation of a polymer electrolyte membrane such that the -OM<NUM> group of the butylbenzene group to which the -OM<NUM> group is bonded is exchanged with a —OH group by an ion exchange reaction to form a hindered phenol group (<NUM>,<NUM>-di-tert-butyl-<NUM>-hydroxyphenyl group) as an antioxidant group in the polymer electrolyte membrane, and the hindered phenol group reacts with oxygen radicals of ROS instead of the polymer electrolyte membrane by a reduction reaction of the —OH group thereof to prevent oxidation, thereby improving the chemical durability of the polymer electrolyte membrane.

In addition, since the compound represented by Formula <NUM> has a structure in which the -OM<NUM> group is bonded at position <NUM> of the benzene group and a t-butyl group, which is capable of providing a large amount of electrons, at positions <NUM> and <NUM> adjacent thereto, the —OH group (derived from the -OM<NUM> group) at the position <NUM> by the t-butyl group at positions <NUM> and <NUM> smoothly generates radicals such as -O- and reacts with radicals generated during the driving of the fuel cell, thereby more effectively preventing oxidation.

In addition, an additive, such as an inorganic-based antioxidant, commonly used to improve the durability of the polymer electrolyte membrane suppresses decomposition of the polymer electrolyte membrane by the ROS, thereby improving the durability, but there is a limitation that the proton conductivity is reduced by forming an ionic bond with a cation exchange group (-SOs-) introduced into the polymer electrolyte membrane to block a proton exchange channel. However, the compound represented by Formula <NUM> above according to the present disclosure includes a perfluorinated sulfonate group (e.g., -CF<NUM>SO<NUM>Na) as an ion conductive functional group in conjunction with an -OM<NUM> group-bonded butylbenzene group forming the antioxidant functional group in the molecule, thereby improving the chemical durability of the polymer electrolyte membrane and simultaneously improving the proton conductivity.

Meanwhile, as shown in Reaction Scheme <NUM>, which will be described below, the compound represented by Formula <NUM> above is synthesized by reacting a compound providing an ion conductive functional group to a hindered phenol, and a reaction may occur only at position <NUM> of the phenol group due to reaction activity, and thus the compound represented by Formula <NUM> above according to an embodiment of the present disclosure has a structure in which an -OM<NUM> group is bonded at position <NUM> of the benzene group, a t-butyl group is bonded at positions <NUM> and <NUM> adjacent thereto, and an ion conductive functional group is bonded at position <NUM>.

Specifically, in Formula <NUM> above, R<NUM> to R<NUM> may be each independently a hydrogen atom, an alkyl group having <NUM> to <NUM> carbon atoms, a fluoro-substituted alkyl group having <NUM> to <NUM> carbon atoms, or a fluorine atom, wherein at least one among R<NUM> to R<NUM> may be a fluorine atom.

In addition, in Formula <NUM> above, A is -O- or -S- as defined in the claims.

In addition, in Formula <NUM> above, M<NUM> and M<NUM> may be each independently potassium or sodium.

As another example, in Formula <NUM> above, R<NUM> to R<NUM> may all be fluorine atoms, A may be -O-, M<NUM> and M<NUM> may be sodium, and n and m may be each independently an integer of <NUM> to <NUM>.

More specifically, the compound represented by Formula <NUM> may be a compound represented by Formula <NUM>-<NUM> below:
<CHM>.

Meanwhile, the compound represented by Formula <NUM> above according to an embodiment of the present disclosure may be prepared by reacting a compound represented by Formula a and a compound represented by Formula b to prepare a compound represented by Formula c, which is a precursor compound, and reacting the compound represented by Formula c with an alkali metal hydroxide, as shown in Reaction Scheme <NUM> below:
<CHM>.

In Reaction Scheme <NUM> above, R<NUM> to R<NUM>, A, M<NUM>, M<NUM>, n and m may be the same as defined in Formula <NUM>, and B<NUM> and B<NUM> may be each independently F, Cl, Br or I. B<NUM> and B<NUM> above may be each independently F, Cl, Br or I, and may be different from each other, and more specifically, B<NUM> may be I and B<NUM> may be F.

In addition, the present disclosure provides a polymer electrolyte membrane including a unit derived from the compound.

The polymer electrolyte membrane according to an embodiment of the present disclosure includes a unit derived from the compound represented by Formula <NUM> above, and the unit derived from the compound represented by Formula <NUM> above may be included as a monomer polymerized in a polymer constituting the polymer electrolyte membrane or may be included as an additive, and specifically, may be included as an additive.

Here, the unit derived from the compound represented by Formula <NUM> may be a compound represented by Formula <NUM> below:
<CHM>.

In Formula <NUM> above, R<NUM> to R<NUM>, A, M<NUM>, n and m are the same as defined in Formula <NUM>.

The compound represented by Formula <NUM> according to an embodiment of the present disclosure may be present in the same structure as the compound represented by Formula <NUM> in the polymer electrolyte membrane because the -OM<NUM> group forms a —OH group by ion exchange during the sulfonation reaction for forming the polymer electrolyte membrane when applied to the polymer electrolyte membrane.

When the compound represented by Formula <NUM> above is included as an additive of the polymer electrolyte membrane, the polymer electrolyte membrane may include a polymer support and a unit derived from the compound represented by Formula <NUM> above, and the unit derived from the compound represented by Formula <NUM> above may be included in an amount of <NUM> wt% to <NUM> wt% with respect to <NUM> wt% of the polymer.

In addition, the polymer support is not particularly limited as long as it is commonly known, but may be, for example, at least one among a perfluorosulfonic acid polymer, a hydrocarbon-based polymer, polyimide, polyvinylidene fluoride, polyethersulfone, polyphenylene sulfide, polyphenylene oxide, polyphosphazine, polyethylene naphthalate, polyester, doped polybenzimidazole, polyetherketone, polysulfone, or an acid or a base thereof.

In addition, the polymer electrolyte membrane according to an embodiment of the present disclosure may be prepared by a material or method commonly known in the art except for including the unit derived from the compound represented by Formula <NUM>, and may also have a thickness of several microns to several hundred microns.

Meanwhile, the polymer electrolyte membrane according to the present disclosure includes the unit derived from the compound represented by Formula <NUM>, and thus may have excellent chemical durability, thermal stability, and mechanical properties, and also may have excellent proton conductivity.

For example, the polymer electrolyte membrane may have a proton conductivity of <NUM>/cm to <NUM>/cm under the conditions of <NUM> and <NUM>% relative humidity (RH).

In addition, the polymer electrolyte membrane may have a proton conductivity of <NUM>/cm to <NUM>/cm under the conditions of <NUM> and <NUM>% relative humidity (RH).

In addition, the polymer electrolyte membrane may have an ion exchange capacity (IEC) of <NUM> mEq/g to <NUM> mEq/g.

Also, the present disclosure provides a membrane electrode assembly including the polymer electrolyte membrane.

The membrane electrode assembly according to an embodiment of the present disclosure includes: an anode; a cathode; and the polymer electrolyte membrane provided between the anode and the cathode.

As another example, the membrane electrode assembly may include the polymer electrolyte membrane and the anode and the cathode facing each other with the polymer electrolyte membrane located therebetween.

The anode may include an anode catalyst layer and an anode gas diffusion layer, and the anode gas diffusion layer may also include an anode micropore layer and an anode electrode substrate. In this case, the anode gas diffusion layer is provided between the anode catalyst layer and the polymer electrolyte membrane.

In addition, the cathode may include a cathode catalyst layer and a cathode gas diffusion layer, and the cathode gas diffusion layer may also include a cathode micropore layer and a cathode electrode substrate. In this case, the cathode gas diffusion layer is provided between the cathode catalyst layer and the polymer electrolyte membrane.

The anode catalyst layer is a place where the oxidation reaction of the fuel occurs, and a catalyst selected from the group consisting of platinum, ruthenium, osmium, a platinum-ruthenium alloy, a platinum-osmium alloy, a platinum-palladium alloy, and a platinum-transition metal alloy may be used, and the cathode catalyst layer is a place where the reduction reaction of the oxidizer occurs, and platinum or a platinum-transition metal alloy may be used as a catalyst. Here, the catalyst may be used by itself or may be used by being supported on a carbon-based carrier.

In addition, the catalyst layer of each electrode may be introduced into an electrode by a method commonly known in the art, and for example, a catalyst layer may be formed by directly coating a polymer electrolyte membrane with a catalyst ink or by coating a gas diffusion layer with a catalyst ink. In this case, the coating method of the catalyst ink is not particularly limited, but for example, spray coating, tape casting, screen printing, blade coating, die coating, or spin coating may be used. In addition, the catalyst ink may include a catalyst, a polymer ionomer, and a solvent.

The gas diffusion layer of each electrode serves as a current conductor and becomes a passage for the movement of the reaction gas and water, and may have a porous structure. Accordingly, the gas diffusion layer may include a conductive substrate, and as the conductive substrate, for example, carbon paper, carbon cloth, or carbon felt may be used. In addition, the gas diffusion layer may further include a micropore layer between the catalyst layer and the electrode substrate, and the micropore layer may serve to reduce an amount of water flowing out of the gas diffusion layer to maintain a sufficient wet state of the polymer electrolyte membrane, thereby improving the performance of the fuel cell under low-humidity conditions.

Furthermore, the present disclosure provides a fuel cell including the membrane electrode assembly.

The fuel cell according to an embodiment of the present disclosure includes: a stack including the at least two membrane electrode assemblies and a separator provided between the membrane electrode assemblies; a fuel supplier configured to supply fuel to the stack; and an oxidizer supplier configured to supply an oxidizer to the stack.

The stack may include the at least two membrane electrode assemblies, and may be provided with the separator between the membrane electrode assemblies. The separator may serve to prevent the membrane electrode assemblies from being electrically connected, and transfer the fuel and oxidizer supplied from the outside to the membrane electrode assemblies.

The oxidizer supplier serves to supply the oxidizer to the stack, and oxygen may be typically used as the oxidizer, and oxygen or air may be injected with a pump.

In addition, the fuel supplier serves to supply the fuel to the stack, and may include a fuel tank configured to store the fuel and a pump configured to supply the fuel stored in the fuel tank to the stack. In addition, as the fuel, hydrogen or hydrocarbon in a gaseous or liquid state may be used, and the hydrocarbon may include methanol, ethanol, propanol, butanol, or natural gas.

Hereinafter, the present disclosure will be described in more detail according to examples. However, the example according to the present disclosure may be modified in many different forms, and the scope of the present disclosure should not be interpreted to be limited to the examples described below. Rather, the example of the present disclosure is provided so that this description will be thorough and complete, and will fully convey the scope of the present disclosure to those skilled in the art.

<NUM>,<NUM>-di-tert-butylphenol (<NUM>, <NUM> mmol) and tetrafluoro-<NUM>-(tetrafluoro-<NUM>-iodoethoxy)ethanesulfonyl fluoride (<NUM>, <NUM> mmol) were stirred and reacted at <NUM> for <NUM> hours in <NUM> of a solvent (CHCl<NUM>:H<NUM>O=<NUM>:<NUM>) using a catalyst composed of Na<NUM>S<NUM>O<NUM> (<NUM>, <NUM> mmol), NaHCO<NUM> (<NUM>, <NUM> mmol), and hexadecyltrimethylammonium bromide (<NUM>, <NUM> mmol). After the reaction, <NUM> HCl (<NUM>) was added to adjust the pH to <NUM>-<NUM>, the mixture was diluted with <NUM> of distilled water, and extracted using diethylether (3x10 mL) and brine (2x10 mL), and purified by column chromatography (<NUM>% hexane) to prepare <NUM>-(<NUM>-(<NUM>,<NUM>-di-tert-butyl-<NUM>-hydro>cyphenyl)-<NUM>,<NUM>,<NUM>,<NUM>-tetrafl uoroetho>cy)-<NUM>,<NUM>,<NUM>,<NUM>-tetrafl uoroethanesulfonyl fluoride, which is a precursor compound, and the synthesis was confirmed through <NUM>H NMR (CDCl<NUM>) and <NUM>F NMR (CDCl<NUM>) analyses, and the results are shown in <FIG>.

As shown in <FIG>, a phenyl ring peak (peak <NUM>), a methyl group partial peak (peak <NUM>), and a —OH peak (peak <NUM>) of the phenol group were identified in the <NUM>H NMR result. In addition, -CF<NUM> peaks (peaks <NUM>, <NUM>, <NUM>, and <NUM>) and a sulfonyl fluoride peak (peak <NUM>) were identified from the results of 19F NMR.

<NUM>-(<NUM>-(<NUM>,<NUM>-di-tert-butyl-<NUM>-hydroxyphenyl)-<NUM>,<NUM>,<NUM>,<NUM>-tetrafluoroethoxy)-<NUM>,<NUM>,<NUM>,<NUM>-tetrafluoroethanesulfonyl fluoride (<NUM>, <NUM> mmol) and NaOH (<NUM>, <NUM> mmol) prepared in <NUM> of distilled water were reacted at <NUM> for <NUM> hours. Then, the solvent was removed using an evaporator, the organic layer was dissolved by adding ethanol and then vacuum-filtered to remove the salt, and dried in a <NUM>-vacuum oven for <NUM> hours to prepare sodium <NUM>-(<NUM>-(<NUM>,<NUM>-di-tert-butyl-<NUM>-oxidophenyl)-<NUM>,<NUM>,<NUM>,<NUM>-tetrafluoroethoxy)-<NUM>,<NUM>,<NUM>,<NUM>-tetrafluoroethanesulfonate, which is a compound represented by Formula <NUM>-<NUM>, and the synthesis was confirmed through <NUM>H NMR (DMSO-d<NUM>) and <NUM>F NMR (DMSO-d<NUM>) analyses, and the results are shown in <FIG>. In addition, the synthesis of the compound was confirmed through FT-IR analysis, and the result is shown in <FIG>.

As shown in <FIG>, in the <NUM>H NMR result, it was confirmed that the phenyl ring peak (peak <NUM>) was shifted and changed, and the -OH peak (peak <NUM>) of the phenol group disappeared as compared with <FIG>. In addition, in the <NUM>F NMR result, it was confirmed that the -CF<NUM> peaks (peaks <NUM>, <NUM>, <NUM>, and <NUM>) were slightly shifted and the sulfonyl fluoride peak (peak <NUM>) disappeared as compared with <FIG>.

As shown in <FIG>, a hydrogen bond peak may be identified around <NUM>-<NUM>, and thus it was confirmed that the peak of -OH of the phenol group is substituted with -O-Na+, and a C-H peak was identified around <NUM>-<NUM>, and a C-F bond around <NUM>-<NUM>.

Thermal stability and solubility of the compound of Example <NUM> were compared and analyzed.

The thermal stability was confirmed through thermogravimetric analysis (TGA), and specifically, each compound sample was put into a heating furnace of the thermogravimetric analyzer, and the temperature was elevated from room temperature to <NUM> at <NUM>/min and maintained for <NUM> minutes, thereby removing the remaining water and performing stabilization. Thereafter, the weight change of the sample was measured while cooling to <NUM> at <NUM>/min and heating from <NUM> to <NUM> at <NUM>/min in a nitrogen atmosphere, and the results are shown in Table <NUM> below.

The solubility of each compound sample was observed by dissolving the same amount in a total of six solvents, including water, dimethylacetamide (DMAc), methanol, ethanol, <NUM>-propanol and <NUM>-propanol, and the results are shown in Table <NUM> and <FIG>. In the results, if the phase separation is not visible with the naked eye and the sample is dissolved well, it is indicated as ∘, and if the phase separation is visible or the sample is not dissolved, it is indicated as ×.

Referring to Table <NUM> above, it was confirmed that the compound of Example <NUM> is not dissolved in water and the decomposition occurs when the temperature reaches a very high temperature.

A polymer electrolyte membrane including the compound prepared in Example <NUM> as an additive was prepared.

<NUM> wt% of the compound prepared in Example <NUM> with respect to Nafion was added to <NUM> of <NUM> wt% Nafion solution, stirred at room temperature for <NUM> hour to prepare a solution, and the solution was cast on a glass plate and dried in a <NUM>-oven for <NUM> hours to prepare a membrane. Thereafter, the membrane was separated from the glass plate using a moisture penetration method, impregnated with <NUM> sulfuric acid solution at <NUM> for <NUM> hours, and then washed until neutral. Then, the membrane was dried at <NUM> for <NUM> hours using a gel dryer to prepare a polymer electrolyte membrane having a thickness of <NUM>.

A polymer electrolyte membrane was prepared in the same manner as in Example <NUM>, except that the compound prepared in Example <NUM> was added in an amount of <NUM> wt% with respect to the Nafion.

A polymer electrolyte membrane was prepared in the same manner as in Example <NUM>, except that the compound prepared in Example <NUM> was not added.

The thermal stability, chemical durability, mechanical properties, ion exchange capacity, and proton conductivity of each of the polymer electrolyte membranes prepared in Examples <NUM> to <NUM> and Comparative Example were compared and analyzed.

The thermal stability was confirmed through thermogravimetric analysis (TGA) and glass transition temperature (Tg) measurement, and the results are shown in Table <NUM>, <FIG>, and <FIG>.

In the thermogravimetric analysis, each polymer electrolyte membrane sample was put into a heating furnace of the thermogravimetric analyzer, and the temperature was elevated from room temperature to <NUM> at <NUM>/min and maintained for <NUM> minutes, thereby removing the remaining water and performing stabilization. Thereafter, the weight change of the sample was measured while cooling to <NUM> at <NUM>/min and heating from <NUM> to <NUM> at <NUM>/min in a nitrogen atmosphere.

The glass transition temperature was analyzed through a dynamic mechanical analyzer, and each polymer electrolyte membrane was cut into a size of <NUM>×<NUM> and used as a sample, and the conditions were set as the frequency of <NUM> and the amplitude of <NUM>, tan δ was measured while raising the temperature from <NUM> to <NUM> at <NUM>/min, and the maximum point of tan δ was recorded as the glass transition temperature.

From the results of Table <NUM>, <FIG>, and <FIG>, it was confirmed that the polymer electrolyte membranes of Examples <NUM> to <NUM> including the compound of Example <NUM> as an additive have higher glass transition temperature and decomposition temperature than the polymer electrolyte membrane of Comparative Example, and thus it may be confirmed that the polymer electrolyte membranes of Examples <NUM> to <NUM> have excellent thermal stability.

The chemical durability of the polymer electrolyte membrane was confirmed through water uptake and dimensional change. Three measurements were performed per sample, the measurement results are shown as an average value, and the results are shown in Table <NUM> and <FIG>.

Each polymer electrolyte membrane dried through a desiccator was cut into a size of <NUM>×<NUM>, and the thickness and weight thereof were measured. Thereafter, the cut polymer electrolyte membrane was put into a vial, filled with distilled water, stored in a <NUM>-drying oven for <NUM> hours, and the swollen polymer electrolyte membrane was taken out, and the area, thickness, and weight thereof were measured to confirm the water uptake and dimensional change through Equations <NUM> and <NUM> below. <MAT> <MAT>.

In Equations <NUM> and <NUM>, Wdry and Wwet respectively represent the weights of the dried polymer electrolyte membrane and the swollen polymer electrolyte membrane, Adry and Awet respectively represent the areas of the dried polymer electrolyte membrane and the swollen polymer electrolyte membrane, and Tdry and Twet respectively represent the thicknesses of the dried polymer electrolyte membrane and the swollen polymer electrolyte membrane.

Referring to Table <NUM> and <FIG>, it may be confirmed that the polymer electrolyte membranes of Examples <NUM> to <NUM> have significantly less water absorption and dimensional change than the polymer electrolyte membrane of Comparative Example, and thus it may be confirmed that the polymer electrolyte membranes of Examples <NUM> to <NUM> have excellent chemical durability.

The mechanical properties of each polymer electrolyte membrane were confirmed through tensile strength, elastic modulus, and elongation.

Specifically, <NUM> N of Load cell was coupled to the LLOYD UTM LSI device, each polymer electrolyte membrane specimen prepared according to ASTM D638 type V was engaged, and then tensile strength, elastic modulus, and elongation thereof were measured at an extension rate of <NUM>/min. In this case, each specimen was measured seven times, the measurement results were shown as an average value thereof, and the results are shown in Table <NUM> below:.

Referring to Table <NUM>, it was confirmed that the polymer electrolyte membranes of Examples <NUM> to <NUM> have mechanical properties remarkably superior to the polymer electrolyte membrane of Comparative Example.

The proton conductivity was measured in two states: a state in which oxidation was not induced and a state in which oxidation was induced.

The proton conductivity was measured by cutting each polymer electrolyte membrane into a specimen having a size of <NUM>×<NUM>, engaging the specimen with a four-probe cell, maintaining a temperature/humidity equilibrium for <NUM> hours under conditions of <NUM> and <NUM>% relative humidity (RH) before measurement, and measuring the proton conductivity by dropping the humidity from <NUM>% RH to <NUM>% RH, and then measuring the proton conductivity by increasing the humidity from <NUM>% RH to <NUM>% RH by using BekkTech BT-552MX equipment. Each polymer electrolyte membrane was measured three times, and the results are shown in Table <NUM> and <FIG> as an average value thereof.

Referring to Table <NUM> and <FIG>, it was confirmed that the polymer electrolyte membranes of Examples <NUM> to <NUM> have significantly improved proton conductivity as compared with the polymer electrolyte membrane of Comparative Example.

Each of the polymer electrolyte membranes of Example <NUM> and Comparative Example <NUM> was cut into a specimen having a size of <NUM>×<NUM>, the weight thereof was measured, and then put into a <NUM>-vial, and then, <NUM> of Fenton's reagent (<NUM> wt% hydrogen peroxide, <NUM> ppm iron sulfate aqueous solution) was added into the vial, and the specimen was impregnated with the reagent at <NUM> for <NUM> hours. Thereafter, each specimen, which has been impregnated, was washed several times with distilled water and dried, and then the proton conductivity was measured in the same manner as in the method of <NUM>) above. The results are shown in Table <NUM> below:.

Referring to Table <NUM>, in the case of Example <NUM>, the proton conductivity was not significantly changed before and after the oxidation induction, and the proton conductivity was superior to that of the Comparative Example, but in the case of the Comparative Example, the proton conductivity after oxidation was significantly decreased as compared with that before oxidation. This means that the polymer electrolyte membrane of Example <NUM> is prevented from being oxidized, and thus the compound of the present disclosure has excellent antioxidant effects.

Each dried polymer electrolyte membrane was weighed, and then put into a <NUM>-vial, <NUM> of <NUM> NaCl solution was added to the vial, and then stirred at <NUM> for <NUM> hours or more to prepare a specimen for measuring the ion exchange capacity. A <NUM> NaOH solution was added to the vial containing the polymer electrolyte membrane using a potentiometric titrator (TITRANDO <NUM>) until the pH of the vial internal solution reached <NUM> to check the total input NaOH volume, and then the ion exchange capacity was calculated with Equation <NUM> below, and the results are shown in Table <NUM> below.

In Equation <NUM>, CNaOH represents the concentration of NaOH (<NUM>), ΔVNaOH represents the total volume of the injected NaOH, and Ws represents the weight of the dried polymer electrolyte membrane.

Referring to Table <NUM>, it was confirmed that the polymer electrolyte membranes of Examples <NUM> to <NUM> exhibited excellent ion exchange capacity equal to or higher than that of the Comparative Example.

From the results shown in Tables <NUM> to <NUM> and <FIG>, it was confirmed that the compound represented by Formula <NUM> according to an embodiment of the present disclosure has excellent antioxidant and ion conducting effects, and also the polymer electrolyte membrane of the present disclosure includes the compound as an additive, thereby having excellent chemical durability, thermal stability, and mechanical stability and significantly improving the proton conductivity.

The compound according to the present disclosure includes both an antioxidant functional group and an ion conductive functional group in the molecule, and thus is applied as an additive for the polymer electrolyte membrane, thereby improving the chemical durability, thermal stability, and mechanical stability of the polymer electrolyte membrane and simultaneously improving performance such as proton conductivity.

The polymer electrolyte membrane according to the present disclosure includes the compound represented by Formula <NUM> as an additive, and thus has improved chemical durability, thermal stability, and mechanical stability, and also has excellent performance such as proton conductivity.

Claim 1:
A compound represented by Formula <NUM> below:
<CHM>
wherein R<NUM> to R<NUM> are each independently a hydrogen atom, an alkyl group having <NUM> to <NUM> carbon atoms, a fluoro-substituted alkyl group having <NUM> to <NUM> carbon atoms, or a fluorine atom, wherein at least one among R<NUM> to R<NUM> is a fluorine atom,
A is a divalent linking group selected from -O- and -S-,
M<NUM> and M<NUM> are each independently potassium or sodium, and
n and m are each independently an integer of <NUM> to <NUM>.