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Catalytic surface activation of ceramic oxygen transport membranes based on BSFC and LSFC

机译:基于BSFC和LSFC的陶瓷输氧膜的催化表面活化。

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摘要

Oxygen transport membranes based on mixed oxides allow the selective O_2 separation at high temperature. The development of highly permeable materials and membranes would make possible their integration in oxyfuel power plants, which can readily apply CCS technologies. For mixed ionic-electronic conducting (MIEC) membrane, the bulk oxygen ionic diffusion and surface exchange kinetics steps are particularly important for the oxygen transporting process. Oxygen permeation shows Arrhenius behaviour and, the apparent activation energies for oxygen transport often change as a function of the temperature, so the rate limiting step changes according to the temperature range investigated:rn(a) At higher temperatures, the bulk oxygen-ion diffusion is the limiting step for oxygen permeation across the disk membrane, and hence the oxygen permeation flux (J_(O2)) should be given by Wagner equationrn(b) At temperatures below the characteristic thickness, the permeation of oxygen is limited by surface steps, i.e., the rate of oxygen exchange between the gas and the membrane surface. Bouwmeester et al. proposed an empirical power equation.rnOxygen permeation studies and catalytic membrane tests were carried out in the same experimental set-up. The disk-shaped planar membrane (diameter 15 mm, thickness ~ 0.5 - 0.7 mm) was sealed using gold gaskets. Synthetic air was fed to the oxygen-rich membrane compartment, while argon was used as a sweep gas on the permeate (reaction) side. Gas chromatography and mass spectrometry allowed complete analysis of gases at both sides of the membrane.rnPreparation of membranes samples was performed using Ba_(0.5)Sr_(0.5)Fe_(0.8)Co_(0.2)O_(δ_3) (BSFC) and La_(0.58)Sr_(0.4)Fe_(0.8)Co_(0.2)O_(δ-3) (LSFC) powders, respectively. The catalyst formulation of the active layer was based on MIEC (perovskites). Different catalyst formulations were considered, varying the element in the A-site of perovskite structure (ABO_(3-δ)). The perovskite-based compounds were synthesized by EDTA-citrate complexation route. The modification of the membrane surface was done on the permeate side of the membranes by screen-printing and subsequent sintering.
机译:基于混合氧化物的氧气传输膜可以在高温下选择性地分离O_2。高渗透性材料和膜的开发将使其整合到氧燃料​​发电厂中成为可能,碳氧发电厂可以很容易地应用CCS技术。对于混合离子电子导电(MIEC)膜,本体氧离子扩散和表面交换动力学步骤对于氧传输过程特别重要。氧气渗透表现出阿累尼乌斯行为,并且氧气输送的表观活化能通常随温度而变化,因此限速步骤根据所研究的温度范围而变化:rn(a)在较高温度下,大量氧离子扩散是氧气透过圆盘膜的限制步骤,因此氧气透过量(J_(O2))应由Wagner方程rn(b)给出。在低于特征厚度的温度下,氧气的透过受到表面台阶的限制,即,气体与膜表面之间的氧气交换速率。 Bouwmeester等。在同一实验装置中进行了氧渗透研究和催化膜测试。盘状平面膜(直径15 mm,厚度〜0.5-0.7 mm)用金垫圈密封。将合成空气送入富氧膜隔室,同时将氩气用作渗透物(反应)侧的吹扫气。气相色谱法和质谱法可以完全分析膜两侧的气体。rn使用Ba_(0.5)Sr_(0.5)Fe_(0.8)Co_(0.2)O_(δ_3)(BSFC)和La_( 0.58)Sr_(0.4)Fe_(0.8)Co_(0.2)O_(δ-3)(LSFC)粉末。活性层的催化剂配方基于MIEC(钙钛矿)。考虑了不同的催化剂配方,改变了钙钛矿结构(ABO_(3-δ))的A位元素。钙钛矿基化合物是通过EDTA-柠檬酸盐络合路线合成的。通过丝网印刷和随后的烧结在膜的渗透侧上完成膜表面的改性。

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  • 来源
  • 会议地点 Washington DC(US);Washington DC(US);Washington DC(US);Washington DC(US);Washington DC(US)
  • 作者单位

    Instituto de Tecnologia Quimica (Universidad Politecnica de Valencia - Consejo Superior de Investigaciones Cientificas). Avenida de los Naranjos s.46022 Valencia,Spain;

    rnInstituto de Tecnologia Quimica (Universidad Politecnica de Valencia - Consejo Superior de Investigaciones Cientificas). Avenida de los Naranjos s.46022 Valencia,Spain;

    rnForschungszentrum Juelich GmbH, Institute of Energy Research, Leo-Brandt-Str, 52425 Juelich, Germany;

    rnForschungszentrum Juelich GmbH, Institute of Energy Research, Leo-Brandt-Str, 52425 Juelich, Germany;

    rnForschungszentrum Juelich GmbH, Institute of Energy Research, Leo-Brandt-Str, 52425 Juelich, Germany;

    rnInstituto de Tecnologia Quimica (Universidad Politecnica de Valencia - Consejo Superior de Investigaciones Cientificas). Avenida de los Naranjos s/;

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  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类 薄膜技术;
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