Intensification of catalytic CO2 methanation mediated by in-situ water removal through a high-temperature polymeric thin-film composite membrane

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作者
Escorihuela, Sara [1 ]
Cerdá-Moreno, Cristina [1 ]
Weigelt, Fynn [2 ]
Remiro-Buenamañana, Sonia [1 ]
Escolástico, Sonia [1 ]
Tena, Alberto [2 ,3 ]
Shishatskiy, Sergey [2 ]
Brinkmann, Torsten [2 ]
Chica, Antonio [1 ]
Serra, Jose M. [1 ]
机构
[1] Instituto de Tecnología Química, Universitat Politècnica de València-Consejo Superior de Investigaciones Científicas, Avda. Los Naranjos, s/n, Valencia,46022, Spain
[2] Helmholtz-Zentrum Hereon, Institute of Membrane Research, Max-Planck-Str.1, Geesthacht,21502, Germany
[3] European Membrane Institute (EMI) Twente, University of Twente, Drienerlolaan 5, Enschede,7522 NB, Netherlands
关键词
Catalytic membrane reactors - CO2 hydrogenation - High energy efficiency - High energy process - Highest temperature - Polymeric thin-films - Process intensification - Selective membranes - Thin film composite membranes - Water removal;
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摘要
Catalytic CO2 methanation technology can be improved by process intensification, i.e. enabling higher energy efficiency and process sustainability. Here, thin-film composite membranes (TFCM) were developed for in-situ water removal in a catalytic membrane reactor (CMR) for the Sabatier process. The selective separation layer (1.4 μm-thick) of the composite membrane is made of the polyimide 6FDA-6FpDA, a glassy polyimide, which exhibits high permeability and selectivity together with stable function at unprecedented high temperatures (>200 °C), compared to polyimides reported until now (90 °C), thus matching the temperature range of Sabatier reactors. Remarkably, TFCM developed in this work, allow to extract an outstanding amount of water up to 1 m3/(m2·h·bar) at 260 °C. TFCM was implemented for the water removal from the methanation reaction in a CMR operated at 260 °C and using Ni-Todorokite as catalyst. The TFCM-mediated water-extraction enabled to raise both catalytic stability and activity during CMR operation. CO2 conversion stability was greatly improved exhibiting a conversion value of 72 % during the course of the reaction (21 % increase in CO2 conversion), with a water removal of 12.5 % and specific flux of ∼100 g·h−1 m−2. © 2021
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