直接甲醇燃料电池中的膜性能比较

制备了磺化聚醚醚酮(SPEEK)和磺化酚酞型聚醚砜(SPES-C)两种质子交换膜,考察了其质子导电和阻醇性能.实验发现,两种新型质子交换膜具有一定的化学稳定性和质子电导率,尤其在高温下两种新膜的质子电导率与Nafion膜接近.两种新膜的甲醇透过系数要比Nafion膜的低1～2个数量级.分别以两种新型膜和Nafion115膜为电解质制备了直接甲醇燃料电池膜电极,讨论了膜材料的性能对直接甲醇燃料电池性能的影响.结果表明,膜材料的阻醇性越好,电池的开路电压越高;膜的电导率越高,在较高电流密度区域内电池的性能越好.     

磺化聚醚醚酮／二氧化硅／磷钨酸复合膜的质子传导率与阻醇性

1引言 由于磺化聚醚醚酮（SPEEK）膜特有的微观结构使其阻醇性能要优于Nafion膜，使其在直接甲醇燃料电池（DMFC）中的应用方面具有良好的应用前景。但随着该材料磺化度的增加，SPEEK膜的抗溶胀性能和机械性能显著下降，而低磺化度的SPEEK的质子传导能力较弱，不能满足DMFC的使用要求。     

SPEEK/PES-C、SPEEK/SPES-C共混质子交换膜研究

通过在磺化聚醚醚酮(SPEEK,DS=61.68%)中分别混入酚酞型聚醚砜(PES-C)、磺化酚酞型聚醚砜(SPES-C,DS=53.7%)制备出SPEEK/PES-C、SPEEK/SPES-C共混质子交换膜.结果表明,共混的两种聚合物之间均具有较好的相容性.PES-C、SPES-C的混入能有效降低膜的溶胀及甲醇透过,且随着共混量的增加,这种作用越趋明显.纯SPEEK膜在75℃左右溶解,而SPEEK/PES-C(30wt%)、SPEEK/SPES-C(30wt%)共混膜在80℃时溶胀度仅为22.5%、26.32%.在室温至80℃范围内,纯SPEEK及共混膜的甲醇透过系数都在10-7cm2.s-1数量级上,远小于Nafion115膜.在饱和湿度下,温度大于90℃时,SPEEK/PES-C(20wt%)共混膜电导率超过Nafion115膜;温度大于110℃时,SPEEK/SPES-C(30wt%)共混膜电导率与Nafion115膜相当,达到0.11S.cm-1.高电导率,低透醇系数以及明显提高了的可使用温度表明该类共混膜有望在DMFC中使用.     

SPEEK/PES-C、SPEEK/SPES-C共混质子交换膜研究

通过在磺化聚醚醚酮(SPEEK,DS=61.68%)中分别混入酚酞型聚醚砜(PES-C)、磺化酚酞型聚醚砜(SPES-C,DS=53.7%)制备出SPEEK/PES-C、SPEEK/SPES-C共混质子交换膜.结果表明,共混的两种聚合物之间均具有较好的相容性.PES-C、SPES-C的混入能有效降低膜的溶胀及甲醇透过,且随着共混量的增加,这种作用越趋明显.纯SPEEK膜在75℃左右溶解,而SPEEK/PES-C(30 wt%)、SPEEK/SPES-C(30 wt%)共混膜在80℃时溶胀度仅为22.5%、26.32%.在室温至80℃范围内,纯SPEEK及共混膜的甲醇透过系数都在10-7 cm2·s-1数量级上,远小于Nation[R]115膜.在饱和湿度下,温度大于90℃时,SPEEK/PES-C(20 wt%)共混膜电导率超过Nation[R]115膜;温度大于110℃时,SPEEK/SPES-C(30 wt%)共混膜电导率与Nafion[R]115膜相当,达到0.11 S·cm-1.高电导率,低透醇系数以及明显提高了的可使用温度表明该类共混膜有望在DMFC中使用.     

磺化聚醚醚酮/二氧化硅/磷钨酸复合膜的质子传导率与阻醇性

1引言 由于磺化聚醚醚酮(SPEEK)膜特有的微观结构使其阻醇性能[1]要优于Nafion膜,使其在直接甲醇燃料电池(DMFC)中的应用方面具有良好的应用前景.但随着该材料磺化度的增加,SPEEK膜的抗溶胀性能[2]和机械性能显著下降,而低磺化度的SPEEK的质子传导能力较弱,不能满足DMFC的使用要求.     

磺化聚醚醚酮／二氧化硅／磷钨酸导电复合膜的制备

1引言 直接甲醇燃料电池（DMFC）被认为是最适合发展可移动电源的选择之一，目前困扰DMFC发展的主要问题之一是所使用的质子交换膜（主要是杜邦公司的Nation膜）的阻醇性能较低。磺化聚醚醚酮膜（SPEEK）特有的微观结构使其阻醇性能明显的优于Nation膜，而较低的质子传导率、较差的机械性能以及溶胀等缺点限制了它的应用；本文通过在其中加入二氧化硅（SiO2）和磷钨酸（PWA）制备磺化聚醚醚酮／二氧化硅／磷钨酸导电复合膜，并考察了二氧化硅及磷钨酸对复合膜溶胀性能、质子传导率及机械性能的影响。     

杂萘联苯聚芳醚质子交换膜材料的研究

质子交换膜是质子交换膜燃料电池的核心部件之一，其性能的优劣直接关系燃料电池的工作性能。目前质子交换膜燃料电池多采用全氟磺酸离子膜，全氟磺酸膜虽然具有较高的质子传导性和良好的化学稳定性，但是也具有价格昂贵、甲醇渗透高和高温下质子传导性能下降等缺点。为了克服全氟磺酸膜的不足，国内外相继开展了非氟质子交换膜的研究，如磺化聚醚醚酮（SPEEK）、磺化聚醚醚酮酮（SPEEKK）、磺化聚砜（SPSU）和磺化聚酰亚胺（SPI）等。     

DMFC用PES/SPEEK共混阻醇质子交换膜

将磺化聚醚醚酮(SPEEK, 磺化度DS为68.3%)和聚醚砜(PES)两种聚合物共混制得PES/SPEEK共混膜. DSC研究表明两种聚合物之间具有较好的相容性, 因而共混膜均匀致密, 未发生大尺度相分离. PES的混入能有效降低膜的溶胀度及甲醇透过系数. 纯SPEEK 膜40 ℃时在1 mol•L−1甲醇水溶液中溶胀度达到160%, 45 ℃时就完全溶解, 而含30%(w)PES的共混膜在80 ℃时的溶胀度仅有15%. 室温下含20%−30%(w)PES的共混膜的甲醇透过系数为1×10−7 cm2•s−1左右, 比Nafion 115膜的透过系数小一个数量级. 尽管80 ℃下30%(w)PES/SPEEK共混膜的电导率与Nafion 115膜相当, 但由于共混膜的厚度比Nafion 115膜小1/3左右, 膜电阻较小, 因而其电池性能比Nafion 115膜的好.     

磺化聚醚醚酮/磷钨酸复合膜的导电和甲醇渗透性能

通过磺化反应制备了磺化聚醚醚酮,1H-NMR测试表明其磺化度分别为0.65和0.73.用共混的方法制备了磺化聚醚醚酮/磷钨酸复合质子交换膜.研究了磺化聚醚醚酮的磺化度和磷钨酸的含量对复合膜的吸水性能?电导率,甲醇渗透性能的影响.随着磺化度和磷钨酸含量的增加,电导率逐渐增大,最高达到1.36×10-2S/cm(20℃),高于相同测试条件下NafionR○117膜的电导率(1.0×10-2S/cm).对复合膜的横向和纵向电导率进行了测试和比较,两者相差接近一个数量级.磷钨酸的掺杂虽然没有降低复合膜的甲醇渗透系数,但是仍然都低于相同条件下测得的NafionR○117膜的甲醇渗透系数.     

磺化聚醚醚酮/二氧化硅/磷钨酸导电复合膜的制备

1引言 直接甲醇燃料电池(DMFC)被认为是最适合发展可移动电源的选择之一,目前困扰DMFC发展的主要问题之一是所使用的质子交换膜(主要是杜邦公司的Nafion膜)的阻醇性能较低.磺化聚醚醚酮膜(SPEEK)[1]特有的微观结构使其阻醇性能明显的优于Nafion膜,而较低的质子传导率、较差的机械性能以及溶胀等缺点限制了它的应用;本文通过在其中加入二氧化硅(SiO2)[2]和磷钨酸(PWA)[3]制备磺化聚醚醚酮/二氧化硅/磷钨酸导电复合膜,并考察了二氧化硅及磷钨酸对复合膜溶胀性能、质子传导率及机械性能的影响.     

Proton and methanol transport behavior of SPEEK/TPA/MCM-41 composite membranes for fuel cell application

This paper reports proton and methanol transport behavior of composite membranes prepared for use in the direct methanol fuel cell (DMFC). The composite membranes were prepared by embedding various proportions (10–30 wt.%) of inorganic proton conducting material (tungstophosphoric acid (TPA)/MCM-41) into sulfonated poly(ether ether ketone) (SPEEK) polymer matrix. The results indicate that the proton conductivity of the membranes increases with increasing loading of solid proton conducting material. The highest conductivity value of 2.75 mS/cm was obtained for the SPEEK composite membrane containing 30 wt.% solid proton conducting material (50 wt.% TPA in MCM-41). The methanol permeability and crossover flux were also found to increase with increasing loading of the solid proton conducting material. Lowest permeability value of 5.7 × 10⁻⁹ cm² s⁻¹ was obtained for composite membrane with 10 wt.% of the solid proton conducting material (40 wt.% TPA in MCM-41). However, all the composite membranes showed higher selectivity (ratio between the proton conductivity and the methanol permeability) compared to the pure SPEEK membrane. In addition, the membranes are thermally stable up to 160 °C. Thus, these membranes have potential to be considered for use in direct methanol fuel cell.     

磺化聚醚醚酮/三羧基丁烷膦酸锆复合质子交换膜的研究

通过在磺化聚醚醚酮(SPEEK)中掺杂1,2,4-三羧基丁烷-2-膦酸锆(Zr(PBTC))制备出SPEEK/Zr(PBTC)复合质子交换膜.结果表明,与纯SPEEK膜相比,Zr(PBTC)的掺杂能降低复合膜的吸液量及甲醇透过系数,且随着Zr(PBTC)含量的增加,这种作用越趋明显.在室温至80℃范围内,复合膜的甲醇透过系数在10-7cm2.s-1数量级上,远小于Nafion115膜.在饱和湿度下,当温度大于90℃时,含40wt%Zr(PBTC)的复合膜电导率超过Nafion115膜,并在160℃时达到0.36S.cm-1.使用温度的提高及在高温下的高电导率表明该复合膜适合在高温DMFC中使用.     

Sulfonated montmorillonite/sulfonated poly(ether ether ketone) (SMMT/SPEEK) nanocomposite membrane for direct methanol fuel cells (DMFCs)

A nanocomposite membrane of sulfonated montmorillonite/sulfonated poly(ether ether ketone) (SMMT/SPEEK) is proposed for direct methanol fuel cells (DMFCs). The SMMT is clay modified with silane of which the structure consists of a sulfonic acid group for proton conductivity improvement. The micro- and nano-scaled morphologies of the membranes perform the increase in inorganic aggregation with SMMT loading content as confirmed by SEM and AFM. The membrane stability, i.e., the liquid uptake in water and in methanol aqueous solution, as well as the mechanical stability increases with the SMMT loading content whereas thermal stability does not improve significantly. The methanol permeability reduction is obtained when the SMMT loading content increases for various methanol concentrations (1.5–4.5 M). A comparative study of the SPEEK nanocomposite membranes with SMMT and with pristine MMT shows fourfold proton conductivity enhancement after sulfonation. The DMFC single cell tests inform us that all nanocomposite membranes give the significant performance revealed by the plot of current density–voltage and power density.     

Preliminary evaluation of sulfonated poly(ether ether ketone)/monoethanolamine/adipic acid composite membranes for direct methanol fuel cell applications

A series of sulfonated poly(ether ether ketone)/monoethanolamine/adipic acid (SPEEK/MEA/AA) composite membranes are prepared and investigated to assess their possibility as proton exchange membranes in direct methanol fuel cells (DMFCs). A preliminary evaluation shows that introducing MEA and AA into SPEEK matrix decreases the thermal stability of membrane. However, the degradation temperatures are still above 260 °C, satisfying the requirement for fuel cell operation. Compared with the pure SPEEK membrane, the composite membranes exhibit not only lower water uptake and swelling ratios but also better mechanical property and oxidative stability. Noticeably, the methanol diffusion coefficient of the composite membranes decrease significantly from 3.15 × 10^?6 to 0.76 × 10^?6 cm²/s with increasing MEA and AA content, accompanied by only a small sacrifice in proton conductivity. Although both the methanol diffusion coefficient and the proton conductivity of composite membranes are lower than those of pure SPEEK and Nafion® 117 membranes, their selectivity (conductivity/methanol diffusion coefficient) are higher. In addition, the composite membranes show excellent stability in aqueous methanol solution. The good thermal and chemical stability, low swelling ratio, excellent mechanical property, low methanol diffusion coefficient, and high selectivity make the use of these composite membranes in DMFCs quite attractive. © 2007 Wiley Periodicals, Inc. J Polym Sci Part B: Polym Phys 45: 2871–2879, 2007     

Hybird Membrane with High Proton Conductivity and Selectivity Based on SPEEK for Direct Methanol Fuel Cells

Composite membranes based on sulfonated silica/sulfonated poly(ether ether ketone)(SPEEK) were prepared by means of sol-gel method so as to gain a high conductivity and reasonable methanol permeability.The sulfonated silica is generated in situ via the hydrolysis of sulfonated 3-anminopropyl triethoxysilane(KH550) synthesized newly from 3-aminopropyl triethoxysilane and 1,4-butane sultone.The membrane with a silica mass fraction of 5% exhibits a conductivity of 0.187 S/cm at 80 °C and a methanol coefficient with 9.72×10-7 cm2/s.The composite membranes show improved condutive ability and better selectivity that can be promisingly used in direct methanol fuel cell.     

Sulfonated poly(ether ether ketone)/polyaniline composite proton-exchange membrane

Sulfonated poly(ether ether ketone) (PEEK) was prepared by sulfonation of commercial Victrex^@ PEEK and degree of sulfonation was found to be about 44.5% by ¹H NMR. Sulfonated PEEK/polyaniline composite membranes, in order to prevent methanol crossover, were prepared by chemical polymerization of a thin layer of polyaniline (PANI) in the presence of a high oxidant concentration on a single face modification. FTIR and PANI coating density studies confirmed the loading of PANI in sulfonated PEEK membrane matrix. PANI composite membranes with different polymerization time were prepared and subjected to thermogravimetric analysis as well as electrochemical and methanol permeability study to compare with sulfonated PEEK and Nafion 117 membrane. Ion-exchange capacity, water uptake, proton transport numbers and proton conductivities for different PANI composite sulfonated PEEK (SPEEK) membranes were found to be dependent on the coating density of the PANI in the membrane matrix and were slightly lower than that of Nafion 117 membrane. Methanol permeability of these membranes (especially SPEEK/PANI-1.5) was about four times lower than Nafion 117 membrane. Among the all SPEEK membranes synthesized in this study, SPEEK-1.5 appears to be more suitable for direct methanol fuel cell (DMFC) application considering optimum physicochemical and electrochemical properties, thermal stability as well as very low methanol permeability. Above all, the cost-effective and simple fabrication technique involved in the synthesis of such composite membranes makes their applicability quite attractive.