CN109652823B - 一种高性能质子导体陶瓷膜反应器电解池阳极材料 - Google Patents
一种高性能质子导体陶瓷膜反应器电解池阳极材料 Download PDFInfo
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Abstract
本发明涉及一种高性能质子导体陶瓷膜反应器电解池阳极材料,所述阳极材料由铜和钇共掺杂的BaZr0.2Ce0.8O3‑δ基材料和YBa3Cu2O7‑δ晶相复合组成,所述阳极材料的化学组成式为:Ba1+z Zr0.2Ce0.8‑x‑y Cu x Y y O3‑δ,其中x=0.1~0.5、y=0.1~0.25、z=0.02~0.1。该阳极材料不但具有优异的中低温(400~600℃)催化活性和良好的化学稳定性,而且化学组成、热膨胀性能与BaCeO3基质子导体电解质材料相近。采用本发明提供的阳极材料制备的陶瓷膜反应器电解池具有高的水蒸气电解效率和高的CO2转化及甲醇产率,而且大大提高了电解池在高温长时间电解工作条件下的化学稳定性和结构稳定性,从而提高电解池性能和延长使用寿命。
Description
技术领域
本发明属无机非金属材料(陶瓷)领域,具体是一种高性能质子导体陶瓷膜反应器电解池阳极材料。
背景技术
高温质子导体陶瓷膜电解池可电解水制备氢气,或电解水产生高活性质子并进一步与二氧化碳反应合成碳氢燃料以替代传统的化石燃料,也可用于加氢反应与其他有机气体合成化工原料,其工作过程可采用丰富的可再生能源(风能、太阳能、地热能等)或先进核反应堆及其它工业废热等作为能量来源,对解决当前日益严峻的环境和能源问题、减缓能源危机具有重要意义,显示出了良好的应用前景,因而基于陶瓷膜电解池的陶瓷膜反应器近年来受到越来越多的关注,成为能源材料领域的研究热点之一。但目前关于陶瓷膜电解池的研究多集中于氧离子导体陶瓷膜电解池,而对质子导体陶瓷膜电解池的研究相对较少。对于高温水蒸气电解,质子导体陶瓷膜电解池无疑具有明显的优势,不但可在更低的温度下工作直接获得高纯氢气(无需后续的分离提纯)或高活性质子,还可与其它加氢反应过程耦合合成碳氢燃料或有机化工原料,能改善电池工作条件和长期稳定性及降低电池运行成本。
质子导体陶瓷膜电解池一般由阴极、质子导体电解质膜和阳极构成,其中电解池阳极作为水蒸气催化解离的唯一场所,是影响电解效率的最关键部分。现有的阳极材料一般采用La0.6Sr0.4MnO3-δ(LSM)、La0.6Sr0.4Co0.2Fe0.8O3-δ(LSCF)、Ba0.5Sr0.5Co0.8Fe0.2O3-δ(BSCF)等钙钛矿结构材料,这些材料存在以下致命缺陷:(1)在高温水蒸气电解工作条件下(存在外电场和氢气),化学稳定性差,阳极材料易分解使电解池性能快速衰减;(2)在中低温(400~600℃)条件下电催化性能差、电解效率低,所需工作温度一般要达到700~800℃,这一方面会降低阳极材料稳定性,另一方面对于陶瓷膜反应器,会导致合成碳氢燃料重新分解,影响合成产率;(3)与常用的BaCe0.8-x Zr x Y0.2O3基质子导体电解质材料的化学组成完全不同,在高温工作过程中,阳极材料与电解质膜之间容易产生相互扩散反应,导致阳极和电解质的化学组成改变和性能恶化;(4)LSCF、BSCF这些常用含钴阳极材料的热膨胀系数一般在质子导体电解质材料的2倍以上,导致电解池抗热震性差,阳极/电解质界面易开裂甚至阳极脱落,使电解池结构受到破坏。因此,为改善陶瓷膜电解池性能,亟需开发具有良好化学稳定性和高电催化活性并与电解质材料组成、性能匹配的阳极材料。
发明内容
本发明要解决的技术问题是提供一种具有良好化学稳定性和高电催化活性的高性能质子导体陶瓷膜反应器电解池阳极材料。
本发明的技术方案如下:一种高性能质子导体陶瓷膜反应器电解池阳极材料,其特征在于,所述阳极材料由铜和钇共掺杂的BaZr0.2Ce0.8O3-δ基材料和YBa3Cu2O7-δ晶相复合组成,所述阳极材料的化学组成式为:Ba1+z Zr0.2Ce0.8-x-y Cu x Y y O3-δ,其中x=0.1~0.5、y=0.1~0.25、z=0.02~0.1。
所述阳极材料的化学组成式为:Ba1+z Zr0.2Ce0.8-x-y Cu x Y y O3-δ,其中x=0.2~0.4、y=0.1~0.2、z=0.05~0.1。
所述阳极材料的化学组成式为:Ba1+z Zr0.2Ce0.8-x-y Cu x Y y O3-δ,其中x=0.3~0.4、y=0.1~0.15、z=0.05~0.08。
上述高性能质子导体陶瓷膜反应器电解池阳极材料的制备方法,其特征在于: 通过硝酸盐-柠檬酸络合法予以制备,具体步骤是:
步骤一:首先按照阳极材料的配方组成,将金属离子硝酸盐溶于适量去离子水中,再按总金属离子:柠檬酸=1:1.5的摩尔比加入柠檬酸,充分溶解并搅拌混合均匀后,滴加氨水调节溶液pH=6~8,然后将溶液置于加热板蒸干成深色凝胶直至自燃,得到阳极材料前驱物;
步骤二:将该前驱物在900~1000℃保温3 h煅烧,得到蓬松超细的阳极粉体材料。
与现有技术相比,本发明具有以下技术效果:
(1)在具有高的化学稳定性的铈锆酸钡基质子导体材料中引入少量Cu和Y共掺杂,获得质子/电子混合传导特性(仅钇掺杂的铈锆酸钡无明显电子电导)和提高材料低温电催化活性;
(2)高温反应中原位合成均匀分布、具有高电子电导率和高催化活性的第二相YBa3Cu2O7-δ晶相,提高三相界面面积;
(3)采用本发明采用的阳极材料组成配比,容易形成少量Ba缺位的掺杂铈锆酸钡基材料,可进一步提高阳极材料的催化活性;
(4)本发明提供的复合阳极化学组成与常用的质子导体电解质材料相近,有利于提高陶瓷膜反应器电解池的抗热震性,改善阳极/电解质膜的界面结合,从而提高电解池性能和延长使用寿命。
具体实施方式
下面将结合实施例对本发明作进一步的详细描述。
实施例一:陶瓷膜电解池反应器电解水制氢气
制备阴极支撑的圆片状陶瓷膜电解池,所用复合阳极材料组成可表示为Ba1.08Zr0.2Ce0.3Cu0.35Y0.15O3-δ,电解质膜材料为BaCe0.5Zr0.3Y0.2O3-δ,阴极支撑体材料为NiO-BaCe0.5Zr0.3Y0.2O3-δ (NiO与BaCe0.5Zr0.3Y0.2O3-δ的质量百分比为60:40)。
电解池制备过程:
(1)原料粉体合成
通过硝酸盐-柠檬酸络合法制备Ba1.08Zr0.2Ce0.3Cu0.35Y0.15O3-δ阳极材料粉体,首先按照配方组成,将金属离子硝酸盐溶于适量去离子水中,再按总金属离子:柠檬酸=1:1.5的摩尔比加入柠檬酸,充分溶解并搅拌混合均匀后,滴加氨水调节溶液pH=6,然后将溶液置于加热板蒸干成深色凝胶直至自燃,得到阳极材料前驱物。再将该前驱物在920℃保温3 h煅烧,得到蓬松超细的阳极粉体。采用同样的方法,制备电解质膜和阴极支撑体材料粉体。
(2)电解池制备
先采用共压/一次烧成工艺制备阴极支撑体/电解质膜(NiO-BaCe0.5Zr0.3Y0.2O3-δ/BaCe0.5Zr0.3Y0.2O3-δ)双层结构,共烧条件为1400℃保温10 h,阴极支撑体和电解质膜厚度分别为2 mm和20 μm;将2g阳极粉体与适量乙基纤维素和松油醇一起研磨混合均匀,得到粘稠的阳极浆料。通过丝网印刷法将该阳极浆料涂覆在上述双层结构的电解质膜表面,干燥后,再经过1050℃保温2h 热处理后得到结构为NiO-BaCe0.5Zr0.3Y0.2O3-δ(阴极)/BaCe0.5Zr0.3Y0.2O3-δ(电解质)/Ba1.08Zr0.2Ce0.3Cu0.35Y0.15O3-δ(阳极)的陶瓷膜电解池。
高温水蒸气电解制氢性能:
将电解池密封构建陶瓷膜反应器,工作温度为600℃、阳极侧水蒸气分压40%(Ar气为载气,流速100ml/min)、阴极侧扫气为Ar气(流速100ml/min),运行10h后,电解电压为1.5V 和2.0 V时,氢气产率分别可达到为7.3 ml/(cm2·min)和21.5 ml/(cm2·min)。
实施例二:微管陶瓷膜电解池反应器电解水制氢气
制备微管阴极支撑的陶瓷膜电解池构建膜反应器,所用复合阳极材料组成可表示为Ba1.05Zr0.2Ce0.35Cu0.3Y0.15O3-δ,电解质膜材料为BaCe0.5Zr0.3Y0.16Zn0.04O3-δ,阴极支撑体材料为NiO-BaCe0.5Zr0.3Y0.16Zn0.04O3-δ (NiO与BaCe0.5Zr0.3Y0.16O3-δ的质量百分比为60:40)。
电解池制备过程:
原料粉体的制备方法同实施例1,其中溶液pH=7、前驱物的煅烧温度为960℃。
通过纺丝成型制备微管阴极支撑体:将阴极材料混合粉体、聚醚砜(PES)、N-甲基毗咯烷酮(NMP)按60:8:32 的质量百分比取料。先把PES溶于NMP 中,形成均匀溶液,再外加1%的聚乙烯毗咯烷酮,搅拌均匀。然后加入NiO-BaCe0.5Zr0.3Y0.16Zn0.04O3-δ混合粉体,搅拌5h使之形成均匀的铸膜浆料。最后通过干/湿法纺丝成型和高温预烧结(1350℃保温3h)制备外径为1.5mm的多孔微管阴极支撑体(管壁厚度为0.25mm)。
电解质膜制备:先将适量BaCe0.5Zr0.3Y0.16Zn0.04O3-δ球磨分散于PVB的乙醇溶液制备固含量为10%(质量百分含量)的电解质浆料,再通过浸渍涂敷法在阴极支撑体上形成电解质层,最后经1450℃保温5h共烧后,在阴极支撑体上制备出厚度为20μm电解质膜。
阳极制备:采用与实施例1相同的方法,制备Ba1.05Zr0.2Ce0.35Cu0.3Y0.15O3-δ阳极浆料。然后通过涂刷法在电解质膜表面涂覆阳极层,干燥后,最后经1050℃保温2h 热处理后得到结构为NiO-BaCe0.5Zr0.3Y0.16Zn0.04O3-δ(阴极)/ BaCe0.5Zr0.3Y0.16Zn0.04O3-δ(电解质)/Ba1.05Zr0.2Ce0.35Cu0.3Y0.15O3-δ(阳极)的微管陶瓷膜电解池。
高温水蒸气电解制氢性能:
采用6根长度10cm的微管电解池组装密封构建陶瓷膜反应器,工作温度为600℃、阳极侧水蒸气分压40%(Ar气为载气,流速100ml/min)、阴极侧扫气为Ar气(流速100ml/min),运行10h后,电解电压为1.5 V 和2.0 V时,氢气产率分别可达到为9.5 ml/(cm2·min)和30.4 ml/(cm2·min)。
实施例三:微管陶瓷膜电解池反应器合成甲醇燃料
陶瓷膜反应器电解池材料和制备方法同实施例2,其中溶液pH=7、前驱物的煅烧温度为1000℃。
高温水蒸气电解并与CO2耦合制备甲醇性能:
采用6根长度10cm的微管电解池组装密封构建陶瓷膜反应器,阳极侧水蒸气分压40%(Ar气为载气,流速100ml/min)、阴极侧通入CO2气体(流速40ml/min)、电解电压2.0 V,工作温度为600℃时,运行10h后,合成过程中CO2转化率为58.5%,甲醇产率为32.2%;工作温度为400℃时,合成过程中CO2转化率为31.7%,甲醇产率为40.3%。
Claims (3)
1.一种高性能质子导体陶瓷膜反应器电解池阳极材料,其特征在于,所述阳极材料由铜和钇共掺杂的BaZr0.2Ce0.8O3-δ基材料和YBa3Cu2O7-δ晶相复合组成,所述阳极材料的化学组成式为:Ba1+z Zr0.2Ce0.8-x-y Cu x Y y O3-δ,其中x=0.1~0.5、y=0.1~0.25、z=0.02~0.1;
所述高性能质子导体陶瓷膜反应器电解池阳极材料通过硝酸盐-柠檬酸络合法予以制备,具体步骤是:
步骤一:首先按照阳极材料的配方组成,将金属离子硝酸盐溶于适量去离子水中,再按总金属离子:柠檬酸=1:1.5的摩尔比加入柠檬酸,充分溶解并搅拌混合均匀后,滴加氨水调节溶液pH=6~8,然后将溶液置于加热板蒸干成深色凝胶直至自燃,得到阳极材料前驱物;
步骤二:将该前驱物在900~1000℃保温3 h煅烧,得到蓬松超细的阳极粉体材料。
2.根据权利要求1所述的高性能质子导体陶瓷膜反应器电解池阳极材料,其特征在于,所述阳极材料的化学组成式为:Ba1+z Zr0.2Ce0.8-x-y Cu x Y y O3-δ,其中x=0.2~0.4、y=0.1~0.2、z=0.05~0.1。
3.根据权利要求1所述的高性能质子导体陶瓷膜反应器电解池阳极材料,其特征在于,所述阳极材料的化学组成式为:Ba1+z Zr0.2Ce0.8-x-y Cu x Y y O3-δ,其中x=0.3~0.4、y=0.1~0.15、z=0.05~0.08。
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