Natural gas comprises a relatively large portion of fossil hydrocarbon resources. The high capital cost of its conversion via synthesis gas, however, leaves much of it unused, i.e., stranded.
Nonoxidative methane dehydro-aromatization (MDA) is a promising way to directly convert natural gas into high-value petrochemicals, such as benzene, toluene, and xylene. The reaction runs at about 700°C in the presence of bifunctional catalysts such as carbided molybdenum nanoclusters dispersed in acidic shape-selective zeolites. Two issues plague this process: The per-pass conversion is limited by thermodynamics, and the catalyst activity decreases quickly because coke accumulates on the external zeolite surface and hinders access to internal active sites.
Scientists from CoorsTek Membrane Sciences, the Univ. of Oslo (Norway), and the Instituto de Tecnología Química (Spain) have figured out a way to circumvent those issues. They have developed a ceramic membrane that can be integrated into the MDA reactor to boost aromatic yields. The new catalytic membrane reactor (CMR) also produces high-purity hydrogen.
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