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Catalytic Membrane Reactors based on Mixed Ionic-Electronic Conductors

机译:基于混合离子电子导体的催化膜反应器

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摘要

The present work focused on the application of oxygen permeable membranes to the alkane activation at high temperatures. The employed membranes are based on mixed oxides with the perovskite crystalline structure and present mixed ionic-electronic conductivity. The synthesized and characterized membranes consist of ferrite-cobaltites with different alkali-earth and lanthanide metals. The oxygen separation from air was studied using argon and methane as sweep gas in the temperature range from 700 to 1000℃. It was possible to distinguish two different permeation regimes: (ⅰ) bulk diffusion limited at high temperatures; and (ⅱ) surface exchange limited at lower temperatures. The membranes were used as catalytic membrane reactor for the conversion of alkanes and two different reactions were studied: (ⅰ) oxidative methane coupling and (ⅱ) oxidative dehydrogenation of ethane.rnIn this context, dense ionic oxygen conducting membrane reactors are highly attractive solutions for syngas production, oxidative dehydrogenation of ethane (ODHE) and oxidative coupling of methane (OCM), where both, separation and reaction are integrated in the same unit [1-5].rnThe oxygen permeation experiments and the catalytic test were performed in the same experimental set-up. Synthetic air was fed to the oxygen-rich membrane compartment, while argon was used as sweep gas on the permeate side. Permeate was analyzed by on-line gas chromatography using micro-GC Varian CP-4900 equipped with Molsieve5A, Pora-Plot-Q glass capillary, and CP-Sil modules. Membrane gas leak free conditions were ensured by monitoring nitrogen concentration on the products gas stream. The membrane formulation was base on MIEC (perovskites). Different catalyst formulations were considered, varying the element in the A-site of perovskite structure (A_(0.58)Sr_(0.4)Fe_(0.8)Co_(0.2)O_(3-δ) [6]. The perovskite-based compounds were synthesized by EDTA-citrate complexation route [7]. The structural characterization of the perovskite powders and MIEC membrane was performed by XRD and SEM.rnOxygen permeation from the air to the reaction side is a key aspect in oxidation reactions, determining the performance of the catalytic membrane reactor. From the oxygen content measured in the argon sweep side of the permeation assemble and the argon flow rate, the total oxygen permeation rate (mL min~(-1) cm~(-2)) was calculated.
机译:目前的工作集中于将透氧膜应用于高温下的烷烃活化。所使用的膜基于具有钙钛矿晶体结构的混合氧化物,并具有混合的离子-电子传导性。合成和表征的膜由具有不同碱土金属和镧系元素金属的铁氧体-钴酸盐组成。以氩气和甲烷为吹扫气,在700至1000℃的温度范围内,研究了从空气中分离氧气的方法。可以区分两种不同的渗透方式:(ⅰ)高温下的本体扩散受限; (ⅱ)在较低温度下的表面交换受到限制。该膜被用作催化膜反应器以转化烷烃,并研究了两个不同的反应:(ⅰ)氧化甲烷偶联和(ⅱ)乙烷的氧化脱氢。合成气的生产,乙烷的氧化脱氢(ODHE)和甲烷的氧化偶联(OCM),其中分离和反应都集成在同一单元中[1-5]。rn氧气渗透实验和催化实验在同一单元中进行实验装置。将合成空气送入富氧膜室,同时将氩气用作渗透侧的吹扫气。使用配备Molsieve5A,Pora-Plot-Q玻璃毛细管和CP-Sil模块的micro-GC Varian CP-4900,通过在线气相色谱分析渗透液。通过监测产品气流中的氮浓度,确保无膜气泄漏条件。膜配方基于MIEC(钙钛矿)。考虑了不同的催化剂配方,改变了钙钛矿结构A位的元素(A_(0.58)Sr_(0.4)Fe_(0.8)Co_(0.2)O_(3-δ)[6]。 EDTA-柠檬酸盐络合路线合成[7],钙钛矿粉和MIEC膜的结构表征通过XRD和SEM进行。根据在渗透组件的氩吹扫侧测得的氧气含量和氩气流量,计算出总的氧气渗透率(mL min〜(-1)cm〜(-2))。

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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 Superiorde Investigaciones Cientificas). Av. de los Naranjos s.Valencia, Spain.46022;

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

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

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

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