Steam-reforming of hydrocarbons, especially methane, is one of the main routes for hydrogen production in the world. [1] However, these reactions also cause major emissions of greenhouse gases such as CO 2 , which is generally believed to be responsible for global warming. The separation of H 2 /CO 2 from gaseous streams with subsequent CO 2 sequestration meets demands for significant reductions of CO 2 emissions into the atmosphere. The disadvantages of common H 2 /CO 2 separation technologies (such as amine scrubbing and pressure swing adsorption) include high energy costs, consumption of sorbents, and complicated processing. Consequently, there is a compelling need for the development of more viable and effective H 2 / CO 2 separation technologies.[2] Inorganic membrane-based gas separation offers an environment-friendly alternative to conventional separation technologies owing to its high energy efficiency and high performance, that is, flux and selectivity, at elevated temperatures. [3,4] Such membranes generally consist of a thin separation layer (with a thickness that can range from a few tens of nanometers up to a few micrometers) superimposed onto a mechanically strong porous support. Several materials (e.g., palladium and its alloys, carbon, zeolites, and solgel derived ceramic membranes) have been suggested for hydrogen purification and carbon capture; among these, amorphous silica with pore sizes in the range of 2-5 is one of the most promising materials. [5][6][7][8] However, the modest hydrothermal stability of membranes made from pure silica severely limits their application under humid conditions. Several methods have been put forward to enhance their stability in the presence of hot steam. Imparting excellent hydrothermal stability to microporous membranes while retaining their flux and molecular sieving properties remains one of the main challenges in the field of membrane research. [4,6] Humidity can disrupt the ÀSiÀOÀSiÀ bonds in silica, inducing densification of the micropourous silica network owing to the formation of mobile silica fragments. Different research groups have undertaken numerous attempts to improve the hydrothermal stability of sol-gel derived microporous silica membranes, including (1) modification of the amorphous silica matrix by doping with metal or transition-metal ions (e.g., Ni, Co, Mg, Al, Zr, Ti, Fe, Nb, and others); [4] (2) dispersion of methyl (ÀCH 3 ) functional groups into the silica matrix, so as to make its structure more hydrophobic; [9,10] and (3) use of alternatives to tetraethyl orthosilicate (TEOS) as the source for the alkoxide, such as transition-metal alkoxides or bridged bis-silyl precursors. [11][12][13][14] None of these attempts have succeeded in developing a high-enough membrane performance combined with a sufficient long-term hydrothermal stability to the degree required for application to industrially relevant gas streams and temperatures.Herein, we report on sol-gel derived microporous hybrid inorganic-organic membranes for enhanced CO 2 separatio...