Next Article in Journal
The Relative Importance of Shear Forces and Surface Hydrophobicity on Biofilm Formation by Coccoid Cyanobacteria
Previous Article in Journal
Tensile Mechanical Behaviour of Multi-Polymer Sandwich Structures via Fused Deposition Modelling
 
 
Font Type:
Arial Georgia Verdana
Font Size:
Aa Aa Aa
Line Spacing:
Column Width:
Background:
Article

Effect of Chemical Structure and Degree of Branching on the Stability of Proton Exchange Membranes Based on Sulfonated Polynaphthylimides

1
College of Chemistry and Environmental Engineering, Shenzhen University, Shenzhen 518060, China
2
Shenzhen Key Laboratory of Polymer Science and Technology, College of Materials Science and Engineering, Shenzhen University, Shenzhen 518060, China
3
Guangdong Research Center for Interfacial Engineering of Functional Materials, Shenzhen University, Shenzhen 518060, China
*
Author to whom correspondence should be addressed.
Polymers 2020, 12(3), 652; https://doi.org/10.3390/polym12030652
Submission received: 12 February 2020 / Revised: 5 March 2020 / Accepted: 5 March 2020 / Published: 12 March 2020
(This article belongs to the Section Polymer Applications)

Abstract

:
Hydrolytic stability and oxidative stability are the core properties of sulfonated polynaphthylimides (SPIs) as proton exchange membranes. The chemical structure of SPIs directly influences the performance. Herein, three different series of branched SPIs were designed and prepared using 1,3,5-tris (2-trifluoromethyl-4-aminophenoxy) benzene as a trifunctional monomer and three non-sulfonated diamine monomers, such as 4,4′-oxydianiline (ODA), 2,2-bis[4-(4-aminophenoxy)phenyl]hexafluoropropane (6FODA), and 4,4′-(9-fluorenylidene)dianiline (BFDA). The effect of the chemical structure and degree of branching on SPIs properties is discussed. The results showed that by controlling the chemical structure and degree of branching, the chemical stability of SPIs changed significantly. SPI-6FODA with two ether linkages and a hydrophobic CF3 group has higher hydrolytic stability than SPI-ODA with only one ether linkage. In addition, with the increase of the introduced B3 monomer, the oxidation stability of SPI-6FODA has been greatly improved. We successfully synthesized SPIs with a high hydrolytic stability and oxidative stability.

Graphical Abstract

1. Introduction

Facing the depletion of oil resources and the increasing environmental pollution caused by fossil fuels, proton exchange membrane fuel cells (PEMFC) have been recognized as one of the clean energy devices in the future [1,2,3,4,5,6,7]. Proton exchange membrane (PEM) is the key part of a PEMFC system, which has been one of the research hotspots in this field in the past few decades [6,8]. Perfluorosulfonic acid polymer membrane, such as Nafion [9,10,11,12], is the universal material for commercial PEM application because of its excellent stability and high ionic conductivity at a fully hydrated condition. However, perfluorosulfonic acid membranes have some drawbacks, such as high cost, high fuel crossover, low operation temperature, and big deformation under fuel cell operation [13,14]. Over the past few decades, hundreds of low-cost sulfonated polymers, such as sulfonated polyether-ether-ketone [15,16,17,18,19,20], sulfonated polyether sulfone [21,22,23,24,25,26,27,28,29,30,31], and sulfonated polynaphthylimides with different chemical structures, have been synthesized for PEMFCs applications [28,29,32]. Among them, sulfonated polynaphthylimides (SPIs) have attracted considerable attention because of their low cost, excellent physical properties, high methanol gas barrier ability, high thermal stability, and easy-to-adjust chemical structure [33,34,35,36]. However, the unsatisfied stability of SPI membrane in a fuel cell under high temperature and high humidity conditions cannot be ignored [37,38,39]. This is because the amide bonds with low electron cloud density on the imide ring are easily attacked by water molecules causing hydrolysis [40]. Studies have shown that the hydrolytic stability of sulfonated polyimide PEM can be improved by changing the monomer structure to increase the electron cloud density of the nitrogen atom and the carbonyl carbon atom. For an aromatic amino monomer, the introduction of an electron donating group, such as an ether bond, can increase the electron cloud density of the nitrogen and carbonyl carbon atoms to achieve higher hydrolytic stability [41]. The SPI synthesized from 4,4′-bis(4-aminophenoxy)biphenyl as a non-sulfonated diamine monomer remains intact after being placed in water at 130 °C for 500 h [42,43]. Nevertheless, the introduced electron donating groups, such as aliphatic and ether linkages, were easily attacked by hydroxyl radicals resulting in poor oxidative stability during the operation of the fuel cell [44,45]. Therefore, it is still a tricky endeavor to put a tradeoff between hydrolytic stability and oxidative stability of polyimide.
In recent years, branching has been widely used in proton exchange membrane modification. Recently, our group found that branching is one of the effective approaches to improve oxidative stability of sulfonated poly(fluorenyl ether ketone sulfone)s, sulfonated block poly(arylene ether)s, etc. [46,47,48,49,50,51,52]. At the same time, the introduction of branched structures also significantly increased the proton conductivity of the membranes.
Based on the above statement, in order to obtain SPI based membranes with a high performance, the effect of the polymer’s scaffold and the degree of branching on the properties was investigated in this study. Firstly, three different non-sulfonated diamine monomers, such as 4,4′-oxydianiline (ODA) with one ether bond, 2,2- bis[4-(4-aminophenoxy)phenyl]hexafluoropropane (6FODA) with two ether bonds and hydrophobic -CF3, and 4,4′-(9-fluorenylidene)dianiline (BFDA) large steric hindrance and 1,3,5-tris (2-trifluoromethyl-4-aminophenoxy) benzene with ether bond and -CF3 group as a trifunctional monomer were selected to synthesize three series of branched SPIs with different degrees of branching. Then, these three series of branched SPIs with different branching degree were fabricated as proton exchange membranes, and their corresponding properties were characterized. The effects of different non-sulfonated diamine monomers and introduced branched structures on the performance of SPIs as a proton exchange membrane were studied.

2. Materials and Methods

2.1. Materials

1,4,5,8-naphthalenetetra-carboxylic dianhydride (NTDA), phloroglucinol, 2-Fluoro-5-Nitrobenzotrifluoride, hydrazine hydrate, 10% palladium on charcoal (Pd/C), m-cresol, triethylamine (TEA), dimethyl sulfoxide (DMSO), dimethylacetamide (DMAC), 4,4′-oxydianiline (ODA), 2,2-bis[4-(4-aminophenoxy)phenyl]hexafluoropropane (6FODA), and 4,4′-(9-fluorenylidene)dianiline (BFDA) were purchased from Energy Chemical Co., Shanghai, China. 4,4′-Diamino-2,2′-biphenyldisulfonic acid (DAPS, 75%) was purchased from Dibo Chemical Reagent Co., Shanghai, China. Unless otherwise noted, all other reagents were used directly. DMSO, DMAC, m-cresol, toluene, and TEA were dried using 4-Å molecular sieves prior to use. DAPS was recrystallized using triethylamine and hydrochloric acid. ODA, 6FODA, and BFDA were dried in a vacuum at 80 °C for 6 h before use, and NTDA was dried in a vacuum at 120 °C for 24 h before use.

2.2. Synthesis of B3 Monomer (TFAPOB)

1,3,5-Tris(2-trifluoromethyl-4-aminophenoxy) benzene (TFAPOB) was synthesized by using the two-step approach. The synthetic route is shown in Scheme 1. The intermediate 1,3,5-tris(2-trifluoromethyl-4-nitrophenoxy) benzene was synthesized in the first step. Phloroglucinol (0.63 g, 5 mmol), 2-fluoro-5-nitrobenzotrifluoride (5.225 g, 25 mmol), and K2CO3 (2.07 g, 15 mmol) were added into a 50 mL three-necked flask equipped with nitrogen inlet, magnetic stirrer, Dean–Stark trap and condenser, and DMAC (25 mL) and toluene (5 mL) were the solvents. The reaction mixture was heated at 140 °C to remove the water. After complete elimination of water, the temperature of the reaction increased to 175 °C and refluxed for 10 h. After cooling to room temperature, the mixture was slowly poured into 500 mL of methanol to obtain the intermediate and was dried in a vacuum.
In the second step, the synthesized 1,3,5-tris(2-trifluoromethyl-4-nitrophenoxy)benzene, ethanol, and palladium carbon were added to a three-necked flask equipped with a constant pressure funnel and condenser. The mixture was stirred and fully dispersed under the protection of nitrogen. After heating to 60 °C, hydrazine monohydrate was slowly added with a constant pressure funnel, refluxed at 60 °C for 8 h, and then filtered. Finally, the filtrate was concentrated to 1/3 and then poured into a 30% NaCl solution and stirred vigorously to obtain a flocculated yellow precipitate. After filtration, the precipitates were vacuum dried at 60 °C for 24 h, and the B3 monomer was obtained with a yield of 64%.

2.3. Synthesis of Sulfonated Polyimide (SPI)

SPI was synthesized by using dianhydride monomer (NTDA), sulfonated monomer (DAPS), B3 monomer (TFAPOB), and three different non-sulfonated diamine monomers (ODA, 6FODA, BFDA). The synthetic route is shown in Scheme 2.

2.3.1. Preparation of Linear SPI-ODA

A total of 0.344 g (1 mmol) of DAPS, 1 mL of triethylamine, and 5 mL of m-cresol were added into a 50 mL three-necked flask. In N2 protection, the reaction mixture was stirred constantly at 80 °C until the DAPS dissolved completely. Next, 0.5 mmol of non-sulfonated diamine monomer (ODA, 0.1 g) was added and stirred continuously until complete dissolution of non-sulfonated diamine monomers. Then, 0.402 g (1.5 mmol) of NTDA and 0.26 g of benzoic acid were added to the above solution. After complete dissolution of NTDA and benzoic acid, the reaction mixture was heated to 80 °C for 4 h and 180 °C for 20 h. After cooling to 80 °C, the mixture was slowly poured into 500 mL methanol to precipitate the polymer. The polymer was washed twice with large amounts of acetone and methanol. The resulting product was dissolved in DMSO and then precipitated in methanol twice and vacuum dried at 120 °C for 24 h. The other liner SPI polymers (SPI-6FODA, SPI-BFDA) were synthesized in a similar manner.

2.3.2. Preparation of Branched SPI

Based on the degree of branching, the required amount of B3 monomer was dissolved in m-cresol. Next, the synthesis process of the linear SPI was repeated. When the viscosity of the solution suddenly increased at 180 °C, the mixture was poured into methanol, and the subsequent processing of the linear SPI was repeated.

2.4. Preparation of Membranes

A total of 1 g of polymer was stirred in 20 g of DMSO containing 0.5 mL of TEA at 80 °C. After obtaining a clear solution, the solution was filtered using absorbent cotton and cast onto a preheated flat glass plate at 80 °C. After drying for 4 h under normal pressure at 80 °C and heated to 120 °C for 12 h, the resulting membrane was immersed in methanol at 40 °C to completely remove the solvent and then soaked in a 1 mol L−1 hydrochloric acid solution for 12 h. Finally, the membranes were washed thoroughly with deionized water. The acidified membrane was fully imidized by immersing it in acetic anhydride:pyridine mixed solution (1:1, v) at 80 °C for 12 h. Finally, the film was immersed in methanol at 50 °C for 12 h to remove the impurities and dried.

2.5. Measurements

The thermal gravimetric analysis (TGA) of SPIs were measured with Q50 (TA Instruments, NewCastle, DE, USA) at a heating rate of 10 °C min−1 under the protection of N2. The Fourier-transform infrared spectra (FTIR) of the SPIs were recorded using a Nicolet 6700 spectrometer (Thermo Scientific, Nicolet, Waltham, MA, USA). 1H NMR of the B3 and SPIs were recorded using a Bruker AVANCE III 500 MHz NMR instrument. The microstructure of the membranes of SPI-BFDA was tested by Field emission scanning electron microscopy (FESEM, S-3400N). The mechanical property of SPIs was measured with an electromechanical universal testing machine (CMT 4204, MTS systems, Jinan, China) at a stretch rate of 5 mm min−1 (the relative humidity was 85%). The SPIs test samples were cut into (15 mm × 4 mm) dumbbell samples.

2.6. Water Uptake and Ion Exchange Capacity

Water uptake of the membranes was measured according to the following procedures. The sample was dried in a vacuum oven at 80 °C for 24 h. The dry membranes were weighed and then soaked in deionized water at different temperatures (20 °C or 25 °C, 40 °C, 50 °C, 60 °C, 70 °C, 80 °C) for 2 h. After that, the wet membranes were taken out, and the excess moisture at their surfaces was absorbed by filter paper. Then, their weights were rapidly measured. Water uptake (WU) of the membranes was measured by
WU ( wt . % ) = W wet - W dry W dry × 100 ,
where Wwet and Wdry are mass (g) of moist and dry membranes, respectively.
Ion-Exchange Capacity (IEC, mmol g–1) was measured by titration. The sample was dried in a vacuum oven at 80 °C for 24 h and weighed. Then, the membrane was immersed in a saturated NaCl solution for 48 h to exchange H+ ions with Na+ ions. The exchanged H+ ions within the solution were titrated with a 0.01 mol L–1 NaOH solution using phenolphthalein as an indicator. We calculated the IEC with Equation (2):
IEC ( mmol   g - 1 )   = M NaOH × V NaOH W dry ,
where MNaOH and VNaOH are the molar concentration (mol L−1) and volume (mL) of the consumed NaOH, and Wdry is the weight of the dried membrane.
The theoretical IEC (IECth) was calculated according to the Equation (3):
IEC th ( mmol   g - 1 )   = n ( - SO 3   H ) W dry ,
where n(-SO3H) represents the mol number of sulfonic groups in reactants, Wdry is the theoretical weight of as-prepared membrane, which is equal to total mass (g) of reactants minus the weight of produced water.

2.7. Proton Conductivity

The proton conductivity (σ, S cm–1) of the membrane was determined by AC impendence spectroscopy (Solartron 1260A) with an oscillating voltage of 10 mV over a frequency range from 100 KHz to 1 Hz. The strip-like film sample (1 cm × 4 cm) was placed in a constant temperature and humidity chamber (98%), and the test temperature ranged from 25 to 80 °C. Proton conductivity of the membrane was calculated by Equation (4)
σ ( S cm 1 ) = L RA ,
where σ (S cm–1) is the proton conductivity, L is the distance (cm) between two electrodes, R is the measured membrane resistance, and A is the cross-sectional area of the membrane.

2.8. Chemical Stability

The oxidation stability of the membrane sample (2 cm × 1 cm) was determined by Fenton’s reagent (30% H2O2 + 20 ppm FeSO4), and the test temperature was 30 °C. The oxidation stability is expressed in terms of its rupture time and complete dissolution time.
The hydrolysis stability of the membrane sample (2 cm × 1 cm) was determined by immersing the deionized water at 80 °C. The hydrolytic stability was expressed as the mass loss of the membrane sample every 24 h.

3. Results and Discussion

3.1. SPIs Synthesis And Characterization

Both the linear and branched SPIs were synthesized using one-step synthesis. Three SPI series with a 66.7% degree of sulfonation and different branching degrees were synthesized by changing the ratio of different monomer additions. The monomer feed ratio, degree of branching, and sulfonated level of the various SPIs are listed in Table 1.
Since the highly branched structure is easily cross-linked during the synthesis, the reaction time of the branched polymer is shortened, and the film is finally soaked in a mixed solution of acetic anhydride and pyridine to completely imidize the film. Figure 1 shows the FT-IR spectra of three series of SPIs. The typical absorption bands of the imido ring are found at 1710, 1670, and 1340 cm−1. The bonds around 1190, 1091, and 1025 cm−1 related to the stretch vibration of the sulfonic acid group. The absorption peak at 1168 cm−1 corresponds to the C-F stretching of -CF3 groups, indicating that the -CF3 groups have been successfully incorporated into the SPIs.
The 1H NMR spectra of three series SPIs are shown in Figure 2. The proton peaks of acid anhydride (corresponding to positions 1 and 2 in Figure 2) are always found at around 8.75–8.8 ppm. Next, the peaks of protons on the benzene ring in biphenyl sulfonic acid (corresponding to positions 3, 4, and 5 in Figure 2) are found at around 7.5–8.0 ppm. These results demonstrate the successful imidization of SPIs membranes. As shown in Figure 2a, the 1H NMR spectra of SPI-ODA has a single peak at 7.3 ppm (corresponding to positions 6 and 7 in Figure 2a), which is identified as the peak of protons on the benzene ring in ODA. At the same time, the proton peak around 6.5 ppm (corresponding to position 8 in Figure 2a) is assignable to the proton peak on the benzene ring in the B3 monomer. As shown in Figure 2b, the 1H NMR spectra of SPI-6FODA have a series of peaks at 7.0–7.5 ppm (corresponding to positions 6, 7, 8 and 9 in Figure 2b), which are assignable to the proton peak on the benzene ring in 6FODA. Moreover, the proton peak around 6.5 ppm (corresponding to position 10 in Figure 2b), may be the peak of the proton on the benzene ring in the B3 monomer. As shown in Figure 2c, the 1H NMR spectra of SPI-BFDA have a series of peaks at 7.0–7.5 ppm (corresponding to positions 6, 7, 8, 9, 10, and 11 in Figure 2c), which belong to the proton peak on the benzene ring in BFDA. Meanwhile, the proton peak around 6.5 ppm (corresponding to position 12 in Figure 2c) may be the proton on the benzene ring in the B3 monomer. All these 1H-NMR spectra results confirmed that three series of SPIs were successfully prepared.
The branched structures in SPIs were determined by 19F NMR (Figure 3). The proton peak of the B3 monomer in all the SPIs is found around 60 ppm, which confirmed the successful synthesis of SPIs with branched structures.
In addition, the microstructure of the representative branched SPI-BFDA-x membranes was evaluated. As shown in Figure 4, as the branching degree increased, the bumps and microcavities increased on the cross-section of the branched membranes because the unique three-dimensional structures increased, which coincided with the results reported in the literature [53].

3.2. Thermal and Mechanical Properties

Thermal properties of the SPIs membranes were investigated via TGA analysis under nitrogen protection. All samples were preheated at 100 °C for 20 min in the TGA furnace to remove the moisture, and the TGA curves of the three series of SPIs membranes are presented in Figure 5. All the SPIs membranes exhibited the two-step degradation pattern. The first weight loss step at about 345 °C was associated with the thermal degradation of the sulfonic acid groups [54]. The second stage weight loss started above 500 °C and was mainly due to the degradation of the polyimide main skeleton. All SPIs membranes exhibited excellent thermal stability, meeting the requirements for fuel cell preparation and application.
The mechanical properties of PEM have important implications for the preparation of membrane electrodes and the durability of fuel cells. The mechanical properties of the SPI membranes are summarized in Table 2 and Figure 6. The test results show that the linear SPIs membrane had excellent mechanical strength. However, the introduction of the branched structure weakened the entanglement and interaction of the macromolecular chains. Therefore, branched SPIs have lower mechanical strength. Young’s Modulus of the typical 6FODA based membranes has been tested, which are higher than those of other proton membranes, indicating the membranes are more brittle than those in the literature [48]. The thickness and viscosity (1 mg/mL in DMSO) of the membranes are shown in Table 2. The viscosity of the branched polymers is lower than that of the linear polymer under the same testing condition, which was in accordance with reference [48].

3.3. Water Uptake (WU) Values and Ion-Exchange Capacity (IEC)

WU is the core property of PEM, which directly affects the proton conductivity, chemical stability, dimensional stability, and mechanical properties. PEMs with high-water-uptake usually have high proton conductivity, but the mechanical properties, chemical stability, and dimensional stability of the membrane will be decreased. The WU of the PEM mainly depends on the content of the sulfonic acid group, at the same time, the molecular structure of the polymer also has a great influence on the WU of the membrane. The WU of the three series of SPIs membranes is presented in Figure 7. The results indicated that the water uptake at room temperature is very low, which can be increased by increasing the temperature. Under the same degree of sulfonation, the WU of the SPIs membranes with different non-sulfonated diamine monomers varies greatly. The SPI-BFDA series membranes introduce a large sterically hindered and kinked fluorenyl on the side chain of the molecule, which facilitates the absorption of water molecules, and thus has the highest water uptake.
Introducing the branched structure in sulfonated polyimide can increase the water absorption of the membrane. However, the increase of SPIs WU is not as obvious as sulfonated block poly(arylene ether)s [46]. This may be due to the strong interaction between the acid anhydride group and the amine group in the polyimide molecular chain, which is not conducive to the absorption of water molecules. In SPI-ODA and SPI-6FDA series membranes, due to the presence of flexible ether bonds the molecular chain is tightly bound and hinder the movement of water molecules in the molecular chain, so the branching structure is not obvious for improving WU. In SPI-BFDA series membranes, due to their larger steric hindrance on the side chain, the branching structure has a little increase in the WU of the membrane.
The theoretical IEC value of the membrane is calculated by the molecular structure, and the actual IEC value is determined by the acid-base titration. The theoretical and experimental IECs of the SPIs are shown in Table 3. The SPI-ODA series of membranes were hydrolyzed during the test, so the IEC value was not measured. The theoretical IEC values of the SPI-6FODA series of membranes are comparable to the experimental IEC values. However, in the case of SPI-BFDA, a little difference between the theoretical IEC value and experimental IEC value occurred, which may be due to the poor hydrolysis stability of SPI-BFDA membranes.

3.4. Chemical Stabilities

When SPIs proton exchange membranes are used in fuel cells, their chemical instability mainly comes from two aspects: (1) hydrolysis of imide rings under high humidity and high temperature conditions; (2) being attacked by peroxide and hydroxyl radicals, generated by crossover or bleeding air reacting with hydrogen in the anode [40]. In order to study the hydrolytic degradation pattern of SPIs, the hydrolytic stability of SPIS membranes was tested in deionized water at 80 °C. The test results of the three series of SPIs membranes are presented in Table 4. The two series of SPI films prepared from ODA and BFDA as non-sulfonated diamine monomers have poor hydrolytic stability and quickly become brittle and broken during testing. The SPIs films prepared with 6FODA as non-sulfonated diamine monomer have good hydrolytic stability, which can still remain intact after soaking in deionized water at 80 °C for 120 h, and retain a certain degree of toughness to bend. This is attributed to the hydrophobic -CF3 group in the 6FODA monomer, which can reduce the contact of the water molecule with the imide ring and effectively protect the polymer backbone at the same degree of sulfonation. In SPI-BFDA series membranes, due to the introduction of a large sterically hindered fluorenyl group in the main chain, high-water uptake was shown, resulting in low hydrolysis stability of the membrane.
In general, the oxidative stability test of PEMs was performed at 30 °C in Fenton’s reagent (30% H2O2 + 20 ppm FeSO4). In this condition, the main degradation pattern of the polymer will be oxidative degradation. The results of the three series of SPIs membranes are presented in Figure 8. It is obvious that the crushing time of all the films was greatly prolonged with the increase of the degree of branching. The results show that the branched structure can effectively improve the oxidative stability of SPI. This is due to the branched structure in the polymer backbone, and the branched film can remain intact even if the molecular chain is attacked by free radicals generated in the electrode.

3.5. Proton Conductivity

PEMs with conductivity higher than 0.01 S cm−1 can be used in fuel cells [6,8]. The proton conductivity results of the three series of SPIs membranes are presented in Figure 9. The three series of synthesized SPIs have enough proton conductivity, meeting the requirement of the fuel cell. The proton conductivity of the membrane rises with temperature increased over the temperature range tested. The membranes of the SPI-ODA and SPI-BFDA series have poor hydrolytic stability and were easily destroyed during the test. Therefore, the conductivity of some membranes cannot be measured at 80 °C. The proton conductivity of PEM depends mainly on the water uptake and the chemical structure of the membrane. In this research, the proton conductivity of the membranes follows the same trend with their water uptake. The high-water absorption of the membranes will lead to high proton conductivity. Therefore, the membranes of the SPI-BFDA series with the highest WU may have the highest conductivity. However, the increase in proton conductivity of the branched membrane is not obvious, and the reason is the same as in the analysis of the effect on WU.

4. Conclusions

In summary, three series of SPIs membranes with different structures and different degrees of branching were successfully synthesized from three non-sulfonated diamine monomers (ODA, 6F0DA, BFDA). The chemical stability, WU, IEC, proton conductivity, and other physical and chemical properties were discussed. The results showed that the chemical structures have a significant effect on the chemical stability of SPIs and further affect the other physical and chemical properties of SPIs. The branched structure can greatly improve the chemical stability of SPIs membranes. Especially the introduction of branched structures in the SPI-6FDA series membranes enhanced the hydrolytic and chemical stability. At the same time, the branched structure can also improve the proton conductivity of the membrane to some extent. Therefore, the selection of chemical structures with electron donating groups and high hydrolytic stability as well as the introduction of branched structures are effective strategies for obtaining high performance SPIs used in PEMFCs.

Author Contributions

Conceptualization, L.W.; methodology, C.G., B.Z., and J.C.; software, B.Z., and J.C.; validation, C.G., B.Z., and J.C.; formal analysis, C.G., B.Z., and J.C.; investigation, C.G., B.Z., and J.C.; resources, L.W.; data curation, C.G., B.Z., and J.C.; writing—original draft preparation, C.G.; writing—review and editing, L.W.; supervision, L.W.; project administration, L.W.; funding acquisition, L.W. All authors have read and agreed to the published version of the manuscript.

Funding

This work was supported by the Natural Science Foundation of Guangdong Province [2015A030313546], Shenzhen Sci & Tech research grant [(JCYJ20180305125204446], and Shenzhen University (2018040).

Acknowledgments

We gratefully acknowledge the supports from the Instrumental Analysis Center of Shenzhen University (Xili Campus).

Conflicts of Interest

The authors declare no conflict of interest.

References

  1. Wang, Y.; Chen, K.S.; Mishler, J.; Cho, S.C.; Adroher, X.C. A review of polymer electrolyte membrane fuel cells: Technology, applications, and needs on fundamental research. Appl. Energy 2011, 88, 981–1007. [Google Scholar] [CrossRef] [Green Version]
  2. Sharma, S.; Pollet, B.G. Support materials for PEMFC and DMFC electrocatalysts-A review. J. Power Sources 2012, 208, 96–119. [Google Scholar] [CrossRef]
  3. Sharaf, O.Z.; Orhan, M.F. An overview of fuel cell technology: Fundamentals and applications. Renew. Sustain. Energy Rev. 2014, 32, 810–853. [Google Scholar] [CrossRef]
  4. Wee, J.H. Applications of proton exchange membrane fuel cell systems. Renew. Sustain. Energy Rev. 2007, 11, 1720–1738. [Google Scholar] [CrossRef]
  5. Higashihara, T.; Matsumoto, K.; Ueda, M. Sulfonated aromatic hydrocarbon polymers as proton exchange membranes for fuel cells. Polymer 2009, 50, 5341–5357. [Google Scholar] [CrossRef] [Green Version]
  6. Steele, B.C.H.; Heinzel, A. Materials for fuel-cell technologies. Nature 2001, 414, 345–352. [Google Scholar] [CrossRef] [PubMed]
  7. Oh, B.H.; Kim, A.R.; Yoo, D.J. Profile of extended chemical stability and mechanical integrity and high hydroxide ion conductivity of poly(ether imide) based membranes for anion exchange membrane fuel cells. Int. J. Hydrogen Energy 2019, 44, 4281–4292. [Google Scholar] [CrossRef]
  8. Hickner, M.A.; Ghassemi, H.; Kim, Y.S.; Einsla, B.R.; McGrath, J.E. Alternative polymer systems for proton exchange membranes (PEMs). Chem. Rev. 2004, 104, 4587–4611. [Google Scholar] [CrossRef]
  9. Alberti, G.; Narducci, R.; Di Vona, M.L.; Giancola, S. Annealing of Nafion 1100 in the Presence of an Annealing Agent: APowerful Method for Increasing Ionomer Working Temperature in PEMFCs. Fuel Cells 2013, 13, 42–47. [Google Scholar] [CrossRef]
  10. Alberti, G.; Narducci, R.; Di Vona, M.L.; Giancola, S. Preparation and Nc/T plots of un-crystallized Nafion 1100 and semi-crystalline Nafion 1000. Int. J. Hydrogen Energy 2017, 42, 15908–15912. [Google Scholar] [CrossRef]
  11. Mauritz, K.A.; Moore, R.B. State of understanding of Nafion. Chem. Rev. 2004, 104, 4535–4585. [Google Scholar] [CrossRef] [PubMed]
  12. Patil, Y.; Kulkarni, S.; Mauritz, K.A. In Situ Grown Titania Composition for Optimal Performance and Durability of Nafion (R) Fuel Cell Membranes. J. Appl. Polym. Sci. 2011, 121, 2344–2353. [Google Scholar] [CrossRef]
  13. Shoesmith, J.P.; Collins, R.D.; Oakley, M.J.; Stevenson, D.K. Status of Solid Polymer Fuel-Cell System-Development. J. Power Sources 1994, 49, 129–142. [Google Scholar] [CrossRef]
  14. Chuang, S.W.; Hsu, S.L.C.; Yang, M.L. Preparation and characterization of fluorine-containing polybenzimidazole/imidazole hybrid membranes for proton exchange membrane fuel cells. Eur. Polym. J. 2008, 44, 2202–2206. [Google Scholar] [CrossRef]
  15. Feng, M.N.; Huang, Y.M.; Cheng, Y.; Liu, J.C.; Liu, X.B. Rational design of sulfonated poly(ether ether ketone) grafted graphene oxide-based composites for proton exchange membranes with enhanced performance. Polymer 2018, 144, 7–17. [Google Scholar] [CrossRef]
  16. Li, C.C.; Yang, Z.H.; Liu, X.P.; Zhang, Y.F.; Dong, J.M.; Zhang, Q.; Cheng, H.S. Enhanced performance of sulfonated poly (ether ether ketone) membranes by blending fully aromatic polyamide for practical application in direct methanol fuel cells (DMFCs). Int. J. Hydrogen Energy 2017, 42, 28567–28577. [Google Scholar] [CrossRef]
  17. Li, X.F.; Zhao, C.J.; Lu, H.; Wang, Z.; Na, H. Direct synthesis of sulfonated poly(ether ether ketone ketone)s (SPEEKKs) proton exchange membranes for fuel cell application. Polymer 2005, 46, 5820–5827. [Google Scholar] [CrossRef]
  18. Lee, C.; Jo, S.M.; Choi, J.; Baek, K.Y.; Truong, Y.B.; Kyratzis, I.L.; Shul, Y.G. SiO2/sulfonated poly ether ether ketone (SPEEK) composite nanofiber mat supported proton exchange membranes for fuel cells. J. Mater. Sci. 2013, 48, 3665–3671. [Google Scholar] [CrossRef]
  19. Anderson, L.J.; Yuan, X.; Fahs, G.B.; Moore, R.B. Blocky lonomers via Sulfonation of Poly(ether ether ketone) in the Semicrystalline Gel State. Macromolecules 2018, 51, 6226–6237. [Google Scholar] [CrossRef]
  20. Kim, A.R.; Vinothkannan, M.; Park, C.J.; Yoo, D.J. Alleviating the Mechanical and Thermal Degradations of Highly Sulfonated Poly(Ether Ether Ketone) Blocks via Copolymerization with Hydrophobic Unit for Intermediate Humidity Fuel Cells. Polymers 2018, 10, 1346. [Google Scholar] [CrossRef] [Green Version]
  21. Lee, K.H.; Chu, J.Y.; Kim, A.R.; Yoo, D.J. Facile Fabrication and Characterization of Improved Proton Conducting Sulfonated Poly(Arylene Biphenylether Sulfone) Blocks Containing Fluorinated Hydrophobic Units for Proton Exchange Membrane Fuel Cell Applications. Polymers 2018, 10, 1367. [Google Scholar] [CrossRef] [PubMed] [Green Version]
  22. Kim, A.R.; Yoo, D.J. A Comparative Study on Physiochemical, Thermomechanical, and Electrochemical Properties of Sulfonated Poly(Ether Ether Ketone) Block Copolymer Membranes with and without Fe3O4 Nanoparticles. Polymers 2019, 11, 536. [Google Scholar] [CrossRef] [PubMed] [Green Version]
  23. Sasikala, S.; Meenakshi, S.; Bhat, S.D.; Sahu, A.K. Functionalized Bentonite clay-sPEEK based composite membranes for direct methanol fuel cells. Electrochim. Acta 2014, 135, 232–241. [Google Scholar] [CrossRef]
  24. Gil, S.C.; Kim, J.C.; Ahn, D.; Jang, J.S.; Kim, H.; Jung, J.C.; Lim, S.; Jung, D.H.; Lee, W. Thermally crosslinked sulfonated polyethersulfone proton exchange membranes for direct methanol fuel cells. J. Membr. Sci. 2012, 417, 2–9. [Google Scholar]
  25. Di Vona, M.L.; Sgreccia, E.; Tamilvanan, M.; Khadhraoui, M.; Chassigneux, C.; Knauth, P. High ionic exchange capacity polyphenylsulfone (SPPSU) and polyethersulfone (SPES) cross-linked by annealing treatment: Thermal stability, hydration level and mechanical properties. J. Membr. Sci. 2010, 354, 134–141. [Google Scholar] [CrossRef] [Green Version]
  26. Prasad, M.; Mohanty, S.; Nayak, S.K. Polymer electrolyte membranes based on sulfonated polysulfone and functionalized layered silicate for direct methanol fuel cell applications. High Perform. Polym. 2015, 27, 714–723. [Google Scholar] [CrossRef]
  27. Yu, J.J.; Dong, C.; Liu, J.H.; Li, C.H.; Fang, J.H.; Guan, R. Crosslinked sulfonated poly (bis-A)-sulfones as proton exchange membrane for PEM fuel cell application. J. Mater. Sci. 2010, 45, 1017–1024. [Google Scholar] [CrossRef]
  28. Zhang, B.P.; Ni, J.P.; Xiang, X.Z.; Wang, L.; Chen, Y.M. Synthesis and properties of reprocessable sulfonated polyimides cross-linked via acid stimulation for use as proton exchange membranes. J. Power Sources 2017, 337, 110–117. [Google Scholar] [CrossRef]
  29. Mistri, E.A.; Banerjee, S.; Komber, H.; Voit, B. Structure-property correlation of semifluorinated 6-membered co-SPIs for proton exchange membrane. Eur. Polym. J. 2015, 73, 466–479. [Google Scholar] [CrossRef]
  30. Kim, A.R.; Vinothkannan, M.; Dong, J.Y. Artificially designed, low humidifying organic–inorganic (SFBC-50/FSiO2 ) composite membrane for electrolyte applications of fuel cells. Compos. Part B Eng. 2017, 130, 103–118. [Google Scholar] [CrossRef]
  31. Kim, A.R.; Park, C.J.; Vinothkannan, M.; Dong, J.Y. Sulfonated poly ether sulfone/heteropoly acid composite membranes as electrolytes for the improved power generation of proton exchange membrane fuel cells. Compos. Part B Eng. 2018, 155, 272–281. [Google Scholar] [CrossRef]
  32. Date, B.; Han, J.; Park, S.; Park, E.J.; Shin, D.; Ryu, C.Y.; Bae, C. Synthesis and Morphology Study of SEBS Triblock Copolymers Functionalized with Sulfonate and Phosphonate Groups for Proton Exchange Membrane Fuel Cells. Macromolecules 2018, 51, 1020–1030. [Google Scholar] [CrossRef]
  33. Marestin, C.; Gebel, G.; Diat, O.; Mercier, R. Sulfonated Polyimides. Adv. Polym. Sci. 2008, 216, 185–258. [Google Scholar]
  34. Arico, A.S.; Srinivasan, S.; Antonucci, V. DMFCs: From Fundamental Aspects to Technology Development. Fuel Cells 2001, 1, 133–161. [Google Scholar] [CrossRef]
  35. Rusanov, A.L.; Komarova, L.G.; Bulycheva, E.G.; Bugaenko, M.G.; Belomoina, N.M. New Sulfonated Polyethers and Polynaphthylimides based on TNT Derivatives. High Perform. Polym. 2009, 21, 508–521. [Google Scholar] [CrossRef]
  36. Rusanov, A.L.; Bulycheva, E.G.; Bugaenko, M.G.; Leikin, A.Y.; Shevelev, S.A.; Dutov, M.D.; Serushkina, O.V.; Voitekunas, V.Y.; Abadi, M.J.P.S. New sulfonated polynaphthylimides: Synthesis and investigation. Polym. Sci. 2009, 51, 3–7. [Google Scholar] [CrossRef]
  37. Zhang, H.W.; Shen, P.K. Recent Development of Polymer Electrolyte Membranes for Fuel Cells. Chem. Rev. 2012, 112, 2780–2832. [Google Scholar] [CrossRef]
  38. Akbarian-Feizi, L.; Mehdipour-Ataei, S.; Yeganeh, H. Survey of sulfonated polyimide membrane as a good candidate for nafion substitution in fuel cell. Int. J. Hydrogen Energy 2010, 35, 9385–9397. [Google Scholar] [CrossRef]
  39. Bao, Y.Y.; Li, Q.B.; Liu, B.; Du, F.F.; Tian, J.; Wang, H.; Wang, Y.X.; Bai, R.K. Conjugated polymers containing a 2,2 -biimidazole moiety-a novel fluorescent sensing platform. Chem. Commun. 2012, 48, 118–120. [Google Scholar] [CrossRef]
  40. Perrot, C.; Gonon, L.; Marestin, C.; Gebel, G. Hydrolytic degradation of sulfonated polyimide membranes for fuel cells. J. Membr. Sci. 2011, 379, 207–214. [Google Scholar] [CrossRef]
  41. Fang, J.H.; Zhai, F.X.; Guo, X.X.; Xu, H.J.; Okamoto, K. A facile approach for the preparation of cross-linked sulfonated polyimide membranes for fuel cell application. J. Mater. Chem. 2007, 17, 1102–1108. [Google Scholar] [CrossRef]
  42. Sutou, Y.; Yin, Y.; Hu, Z.; Chen, S.; Kita, H.; Okamoto, K.; Wang, H.; Kawasato, H. Synthesis and Properties of Sulfonated Polyimides Derived from Bis(sulfophenoxy) Benzidines. J. Polym. Sci. Part A Polym. Chem. 2009, 47, 1463–1477. [Google Scholar] [CrossRef]
  43. Miyatake, K.; Watanabe, M. Emerging membrane materials for high temperature polymer electrolyte fuel cells: Durable hydrocarbon ionomers. J. Mater. Chem. 2006, 16, 4465–4467. [Google Scholar] [CrossRef]
  44. Zhai, F.X.; Guo, X.X.; Fang, J.H.; Xu, H.J. Synthesis and properties of novel sulfonated polyimide membranes for direct methanol fuel cell application. J. Membr. Sci. 2007, 296, 102–109. [Google Scholar] [CrossRef]
  45. Li, N.W.; Cui, Z.M.; Zhang, S.B.; Li, S.H.; Zhang, F. Preparation and evaluation of a proton exchange membrane based on oxidation and water stable sulfonated polyimides. J. Power Sources 2007, 172, 511–519. [Google Scholar] [CrossRef]
  46. Xie, H.X.; Tao, D.; Xiang, X.Z.; Ou, Y.X.; Bai, X.J.; Wang, L. Synthesis and properties of highly branched star-shaped sulfonated block poly(arylene ether)s as proton exchange membranes. J. Membr. Sci. 2015, 473, 226–236. [Google Scholar] [CrossRef]
  47. Xie, H.X.; Wang, D.; Tao, D.; Wang, L. Synthesis of highly branched sulfonated polymers and the effects of degree of branching on properties of branched sulfonated polymers as proton exchange membranes. J. Power Sources 2014, 262, 328–337. [Google Scholar] [CrossRef]
  48. Xie, H.X.; Liu, D.; Xiang, X.Z.; Zhu, C.Z.; Wang, L. Preparation and properties of highly branched sulfonated poly(arylene ether)/polyacrylonitrile composite materials as proton exchange membranes. J. Mater. Sci. 2016, 51, 7119–7129. [Google Scholar] [CrossRef]
  49. Liu, D.; Xu, M.; Fang, M.; Chen, J.; Wang, L. Branched comb-shaped poly(arylene ether sulfone)s containing flexible alkyl imidazolium side chains as anion exchange membranes. J. Mater. Chem. A 2018, 6, 10879–10890. [Google Scholar] [CrossRef]
  50. Neelakandan, S.; Liu, D.; Wang, L.; Hu, M.S.; Wang, L. Highly branched poly(arylene ether)/surface functionalized fullerene-based composite membrane electrolyte for DMFC applications. Int. J. Energy Res. 2019, 43, 3756–3767. [Google Scholar] [CrossRef]
  51. Wang, L.; Liu, Z.R.; Liu, Y.; Wang, L. Crosslinked polybenzimidazole containing branching structure with no sacrifice of effective N-H sites: Towards high-performance high-temperature proton exchange membranes for fuel cells. J. Membr. Sci. 2019, 583, 110–117. [Google Scholar] [CrossRef]
  52. Hu, M.; Li, T.; Neelakandan, S.; Wang, L.; Chen, Y. Cross-linked polybenzimidazoles containing hyperbranched cross-linkers and quaternary ammoniums as high-temperature proton exchange membranes: Enhanced stability and conductivity. J. Membr. Sci. 2020, 593, 117435. [Google Scholar] [CrossRef]
  53. Gao, C.; Liu, Y.; Gao, Y.; Zhou, Y.; Zhou, X.; Yin, X.; Pan, C.; Yang, C.; Wang, H.; Chen, G.; et al. High-performance n-type thermoelectric composites of acridones with tethered tertiary amines and carbon nanotubes. J. Mater. Chem. A 2018, 6, 20161–20169. [Google Scholar] [CrossRef]
  54. Guo, W.; Li, X.; Wang, H.; Pang, J.; Wang, G.; Jiang, Z.; Zhang, S. Synthesis of branched sulfonated poly(aryl ether ketone) copolymers and their proton exchange membrane properties. J. Membr. Sci. 2013, 444, 259–267. [Google Scholar] [CrossRef]
Scheme 1. Synthesis route of B3 monomer.
Scheme 1. Synthesis route of B3 monomer.
Polymers 12 00652 sch001
Scheme 2. Synthesis route of sulfonated polynaphthylimides.
Scheme 2. Synthesis route of sulfonated polynaphthylimides.
Polymers 12 00652 sch002
Figure 1. FT-IR spectra of three series of sulfonated polynaphthylimides (SPIs).
Figure 1. FT-IR spectra of three series of sulfonated polynaphthylimides (SPIs).
Polymers 12 00652 g001
Figure 2. 1H NMR spectra of the (a) SPI-4,4′-oxydianiline (ODA), (b) SPI-2,2-bis[4-(4-aminophenoxy)phenyl]hexafluoropropane (6FODA), and (c) SPI-4,4′-(9-fluorenylidene)dianiline (BFDA).
Figure 2. 1H NMR spectra of the (a) SPI-4,4′-oxydianiline (ODA), (b) SPI-2,2-bis[4-(4-aminophenoxy)phenyl]hexafluoropropane (6FODA), and (c) SPI-4,4′-(9-fluorenylidene)dianiline (BFDA).
Polymers 12 00652 g002
Figure 3. 19F NMR spectra of the (a) SPI-ODA, (b) SPI-6FODA, and (c) SPI-BFDA.
Figure 3. 19F NMR spectra of the (a) SPI-ODA, (b) SPI-6FODA, and (c) SPI-BFDA.
Polymers 12 00652 g003
Figure 4. The cross section FESEM images of (a) SPI-BFDA-1, (b) SPI-BFDA-3, (c) SPI-BFDA-5, and (d) SPI-BFDA-7.
Figure 4. The cross section FESEM images of (a) SPI-BFDA-1, (b) SPI-BFDA-3, (c) SPI-BFDA-5, and (d) SPI-BFDA-7.
Polymers 12 00652 g004
Figure 5. TGA curve of (a) SPI-ODA based membranes, (b) SPI-6FODA based membranes, and (c) SPI-BFDA based membranes.
Figure 5. TGA curve of (a) SPI-ODA based membranes, (b) SPI-6FODA based membranes, and (c) SPI-BFDA based membranes.
Polymers 12 00652 g005
Figure 6. Stress–strain curves of the membranes based on SPI-6FODA.
Figure 6. Stress–strain curves of the membranes based on SPI-6FODA.
Polymers 12 00652 g006
Figure 7. Water uptake of the three SPI based membranes.
Figure 7. Water uptake of the three SPI based membranes.
Polymers 12 00652 g007
Figure 8. Oxidative stability of the three SPI based membranes.
Figure 8. Oxidative stability of the three SPI based membranes.
Polymers 12 00652 g008
Figure 9. Proton conductivity of the three SPI based membranes.
Figure 9. Proton conductivity of the three SPI based membranes.
Polymers 12 00652 g009
Table 1. The feed ratios and degree of branching (DB).
Table 1. The feed ratios and degree of branching (DB).
SPIsMolar RatioDB
NDTANon-Sulfonated Diamine MonomersDAPSB3
ODA6FODABFDA
SPI-ODA-031--200
SPI-ODA-130.97--20.021
SPI-ODA-230.94--20.042
SPI-6FODA-03-1-200
SPI-6FODA-33-0.91-20.063
SPI-6FODA-53-0.85-20.105
SPI-6FODA-73-0.79-20.147
SPI-BFDA-03--0200
SPI-BFDA-13--0.9720.021
SPI-BFDA-33--0.9120.063
SPI-BFDA-53--0.8520.105
SPI-BFDA-73--0.7920.147
Table 2. Tensile strength, thickness, Young’s Modulus, and viscosity of three series of SPIs.
Table 2. Tensile strength, thickness, Young’s Modulus, and viscosity of three series of SPIs.
SampleThickness (μm)Tensile Strength (MPa)Young’s Modulus
(MPa)
Viscosity
(dL g–1)
SPI-ODA-03062.1--
SPI-ODA-13162.0--
SPI-ODA-23350.7--
SPI-6FODA-05271.717200.83
SPI-6FODA-35247.413260.69
SPI-6FODA-55541.712230.72
SPI-6FODA-75332.111450.61
SPI-BFDA-04762.3-0.54
SPI-BFDA-14666.4--
SPI-BFDA-34446.2-0.46
SPI-BFDA-54741.2-0.49
SPI-BFDA-74538.2-0.31
Table 3. Ion-Exchange Capacities (IECs), degree of branching values, and Thickness.
Table 3. Ion-Exchange Capacities (IECs), degree of branching values, and Thickness.
PolymerDegree of BranchingIEC (mmol g−1)
TheoreticalExperimental
SPI-ODA-00%--
SPI-ODA-11%--
SPI-ODA-22%--
SPI-6FODA-00%2.011.98
SPI-6FODA-33%2.011.91
SPI-6FODA-55%1.991.89
SPI-6FODA-77%1.971.90
SPI-BFDA-00%2.381.98
SPI-BFDA-11%2.362.08
SPI-BFDA-33%2.331.82
SPI-BFDA-55%2.311.82
SPI-BFDA-77%2.292.04
Table 4. Hydrolytic stability of sulfonated polyimide membranes.
Table 4. Hydrolytic stability of sulfonated polyimide membranes.
MembraneBroken TimeWeight Residue
after 24 h
Weight residue
after 120 h
SPI-ODA-0140 min--
SPI-ODA-1130 min--
SPI-ODA-2150 min--
SPI-6FODA-0>120 h100%92.8%(Flexible)
SPI-6FODA-3>120 h97.2%89.2%(Flexible)
SPI-6FODA-5>120 h100%90.3%(Flexible)
SPI-6FODA-7>120 h98.2%87.5%(Flexible)
SPI-BFDA-0210 min--
SPI-BFDA-1290 min--
SPI-BFDA-3270 min--
SPI-BFDA-5240 min--
SPI-BFDA-7260 min--

Share and Cite

MDPI and ACS Style

Gao, C.; Chen, J.; Zhang, B.; Wang, L. Effect of Chemical Structure and Degree of Branching on the Stability of Proton Exchange Membranes Based on Sulfonated Polynaphthylimides. Polymers 2020, 12, 652. https://doi.org/10.3390/polym12030652

AMA Style

Gao C, Chen J, Zhang B, Wang L. Effect of Chemical Structure and Degree of Branching on the Stability of Proton Exchange Membranes Based on Sulfonated Polynaphthylimides. Polymers. 2020; 12(3):652. https://doi.org/10.3390/polym12030652

Chicago/Turabian Style

Gao, Chunmei, Jiale Chen, Boping Zhang, and Lei Wang. 2020. "Effect of Chemical Structure and Degree of Branching on the Stability of Proton Exchange Membranes Based on Sulfonated Polynaphthylimides" Polymers 12, no. 3: 652. https://doi.org/10.3390/polym12030652

Note that from the first issue of 2016, this journal uses article numbers instead of page numbers. See further details here.

Article Metrics

Back to TopTop