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全钒液流电池作为一种电化学储能装置在电网调峰、山区供电、电动车充电电源、应急电源等方面具有很广阔的应用前景。隔膜是全钒液流电池的关键组件之一,其结构和性能决定电池的效能。隔膜的离子传导率和钒离子的渗透率分别影响电池的电压效率和电流效率。隔膜的化学稳定性决定电池的长期运行的稳定性和使用寿命。本文根据隔膜的类别不同,分别阐述了含氟离子膜、非氟离子膜及多孔膜的制备与上述性能的关系,并展望了隔膜的发展方向。 相似文献
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质子交换膜对钒氧化还原液流电池性能的影响 总被引:10,自引:0,他引:10
采用溶液接枝聚合法制备了一种新型的质子交换膜PVDF-g-PSSA, 测定了PVDF-g-PSSA膜、Nafion 117 膜和PE01均相膜的离子交换能力和电导率, 并分别研究了以这3种膜为隔膜的钒电池的电化学性能. 实验结果表明, PVDF-g-PSSA膜具有优良的质子电导率和离子交换能力, 室温下其离子交换能力和质子电导率分别为1.13 mmol/g和3.22×10-2 S/cm, 在不同的充放电电流密度下, 以PVDF-g-PSSA膜为隔膜的钒电池的库仑效率和能量效率明显高于Nafion 117膜和PE01均相膜为隔膜的钒电池; PVDF-g-PSSA膜阻钒离子的渗透性能与PE01均相膜基本一致, 都明显优于Nafion 117膜的阻钒离子渗透能力. 相似文献
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不同磺化度下的磺化聚醚醚酮对全钒储能液流电池性质影响的研究 总被引:2,自引:0,他引:2
本文报道了采用浓硫酸作为磺化剂,成功合成了不同磺化度下的聚醚醚酮(PEEK)膜,并深入研究了磺化条件包括磺化时间和磺化剂的用量对所获薄膜性能的影响,获得了在不同磺化度(DS)下SPPEK膜的离子交换容,含水率,机械性能,质子电导率等参数,特别测定了在全钒液流电池工作条件下钒离子(Ⅳ)渗透率,首次为该类液流储能电池使用价廉质优的质子交换膜提供了基础实验数据。室温条件下的实验结果如下:1)磺化12小时后,膜的磺化度46%,含水量为28%,钒离子(Ⅳ)选择性最佳(钒离子渗透率为1.2×10-7 cm2/min-1,是Nafion117 (2.9×10-6 cm2/min-1)的1/24),其质子电导率只有0.02 S/cm;2)磺化96小时其磺化度达79%的膜,质子电导率达0.16 S/cm,是Nafion117 (0.10S/cm) 的1.6倍, 但其机械性能最差;3)与Nafion117膜相比,磺化在36到48小时的SPPEK膜其机械力学性能好,薄膜的钒离子渗透率、离子交换容IEC、质子导电率和含水率高,且对钒离子的选择性佳,尤其价格仅为Nafion膜的1/13,是理想的Nafion膜的代替物,可望直接应用于全钒氧化还原液流(VRB)电池中。本文还讨论了磺化时间和不同磺化剂量对膜的性质的影响。 相似文献
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将聚苯并咪唑(PBI)与聚乙烯吡咯烷酮(PVP)共混, 制备了一系列PBI/PVP复合质子交换膜, 研究了不同PVP含量对PBI/PVP复合质子交换膜性能的影响. 研究结果表明, PVP的加入可有效提高PBI/PVP复合质子交换膜的吸水率及硫酸吸附量, 从而提高质子电导率, 与PBI原膜相比, PBI-PVP-5复合质子交换膜的结合酸含量可达2.47 mmol/g, 质子电导率达4.81 mS/cm, 选择性(3.12×105 S·min/cm3)远高于原膜(1.12×105 S·min/cm3). 电流密度为120 mA/cm2时, 电池的电压效率(VE)和能量效率(EE)均较PBI原膜提高了10%, 电池自放电时间长达307 h. PVP的加入为PBI系列钒液流电池隔膜提供了一个提高质子电导率的新思路. 相似文献
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锂离子电池作为便携式电子产品、新能源汽车、蓄电设备等产品电源备受关注。锂离子电池由正极、负极、隔膜和电解液四部分组成。隔膜虽然不直接参与锂离子电池中的电化学反应,但是隔膜作为锂离子电池的重要组成部分,其性质在很大程度上影响锂离子电池的性能。目前聚烯烃仍是使用最为广泛和商业化最为成功的锂离子电池隔膜材料,但因其不良的电解液浸润性和热稳定性,降低了锂离子电池的电性能和安全性,因此改性成为改善聚烯烃隔膜材料性能和推广应用的重要途径。本文从聚烯烃材料多层膜结构改性、表面涂覆改性和层层自组装改性三方面总结了近五年聚烯烃隔膜改性研究的最新进展。最后,提出增强聚烯烃隔膜的热稳定性和电化学性能仍是未来研究重点,并对新型隔膜材料进行展望。 相似文献
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质子交换膜燃料电池由于具有能量转换效率高、操作温度低、环境友好等优点而备受人们关注。随着2014年丰田发布燃料电池电动汽车Mirai,带来了新一轮燃料电池及燃料电池汽车的产业化热潮。然而,提升质子交换膜燃料电池的寿命,开发新一代长寿命燃料电池膜电极及燃料电池仍然是本领域的挑战性课题。膜电极(MEA)是质子交换膜燃料电池最核心的部件,其耐久性直接决定着燃料电池的寿命。MEA主要由质子交换膜、催化剂层、气体扩散层三部分组成。本文从质子交换膜、催化剂及载体、气体扩散层三个方面介绍了近年来国内外在提升燃料电池膜电极的寿命(耐久性)方面所做的工作,并对未来的相关研究和发展做了述评及展望。 相似文献
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全钒氧化还原液流电池用Nafion/有机硅复合膜 总被引:1,自引:0,他引:1
采用原位化学反应的方法制备了Nafion/有机硅复合膜, 并对所制备复合膜的离子交换容量(IEC)、电导率和水渗透率等进行了测试. 结果表明, 所制备复合膜具有优异的阻水性能. 以Nafion/有机硅复合膜作为离子交换膜的钒电池的库仑效率(CE)和能量效率(EE)都得到了大幅度提高. 此外, 以所制备复合膜为离子交换膜的VRB单电池充放电80次后性能几乎无衰减, 说明所制备Nafion/有机硅复合膜即使在强酸和强氧化性的钒电池体系中也可以稳定使用, 表明Nafion/有机硅复合膜是一种性能优异的适用于全钒氧化还原液流电池的新型质子交换膜. 相似文献
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荷电膜的膜电位研究进展 总被引:1,自引:0,他引:1
膜电位的测定是表征荷电膜的传递现象的重要参数之一。本文简要介绍了膜电位理论基础,包括T. M. S.理论和不可逆热力学理论。分别阐述了关于离子交换膜、双极膜、两性膜以及复合膜的膜电位的最新进展,并提出今后的发展方向。 相似文献
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Zeolite X membranes were investigated by in-situ hydrothermal synthesis on porous ceramic tubes precoated with zeolite X seeds or precursor amorphous aluminosilicate, and porous α-Al2O3 ceramic tubes with a pore size of 50 200 nm were employed as supports. Zeolite X crystals were synthesized by the classic method and mixed into deionized water as a slurry with a concentration of 0.2 0.5wt%, having a range of crystal sizes from 0.2 to 2μm. Crystal seeds were pressed into the pores near the inner surface of the ceramic tubes, and crystallization took place at 95℃ for 24-96 h. It was also investigated that Boehmite sol added with zeolite X seeds was precoated on ceramic supports to form a layer of γ-Al2O3 by heating, and hydrothermal crystallization could then take place to prepare the zeolite membranes on the composite ceramic tubes. The crystal species were characterized by XRD, and the morphology of the supports subjected to crystallization was characterized by SEM. The composite zeolite membranes have zeolitic top-layers with a thickness of 10-25 μm, and zeolite crystals can be intruded into pores of the supports as deeply as 100μm. The experimental results indicate that the precoating of zeolitic seeds on supports is beneficial to crystallization by shortening the synthesis time and improving the membrane strength. The resulting zeolite X membrane shows permselectivity to tri-n-butylamine((C4H9)3N) over perfluro-tributyl-amine ((C4Fg)3N), and a permeance ratio of 57 for ((C4Hg)3N to (C4F9)3N could be reached at 350℃. Permeances of BZ, EB and TIPB through the zeolite membrane were also measured and were found to slightly increase with temperature. 相似文献
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PREPARATIONOFSILICALITE┐1ANDZSM┐5ZEOLITE/CERAMICCOMPOSITEMEMBRANESZhangLixiong,JiaMengdong,MinEnze(ResearchInstituteofPetrole... 相似文献
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Zhongqiang Xu Qingling Chen Guanzhong LuShanghai Research Institute of Petrochemical Technology Shanghai ChinaInstitute of Industrial Catalysis East China University of Science Technology Shanghai China 《天然气化学杂志》2002,(Z2)
Zeolite X membranes were investigated by in-situ hydrothermal synthesis on porous ceramic tubes precoated with zeolite X seeds or precursor amorphous aluminosilicate, and porous α-Al2O3 ceramic tubes with a pore size of 50-200 nm were employed as supports. Zeolite X crystals were synthesized by the classic method and mixed into deionized water as a slurry with a concentration of 0.2-0.5wt%, having a range of crystal sizes from 0.2 to 2μm. Crystal seeds were pressed into the pores near the inner surface of the ceramic tubes, and crystallization took place at 95℃ for 24-96 h. It was also investigated that Boehmite sol added with zeolite X seeds was precoated on ceramic supports to form a layer of r-Al2O3 by heating, and hydrothermal crystallization could then take place to prepare the zeolite membranes on the composite ceramic tubes. The crystal species were characterized by XRD, and the morphology of the supports subjected to crystallization was characterized by SEM. The composite zeolite membranes hav 相似文献
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A model of the composite membrane consisting of the catalytic layer (CL) and the nanofiltration layer (NFL) is presented. It has been found that applying NFL on the permeate side of CL it is possible to enhance substantially the conversion of substrate into the product. The best performance is obtained for high retention of substrate and low of product. At higher values of volume flow and/or longer catalytic path the retention degree of product becomes negligible. The presence of NFL enhances the influence of distribution of the reaction rate constant, k, on the conversion ratio. Comparing to k = constant the positive effect is obtained if k increases along the catalytic pore, whereas negative—if k decreases. 相似文献