<style face="normal" font="default" size="100%">Influence of hydrothermal pretreatment on acidity and activity of H-GaAlMFI zeolite for the propane aromatization reaction</style>

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<style face="normal" font="default" size="100%">Influence of hydrothermal pretreatment on acidity and activity of H-GaAlMFI zeolite for the propane aromatization reaction</style>

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<style face="normal" font="default" size="100%">Influence of PdO content and pathway of its formation on methane combustion activity</style>

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<style face="normal" font="default" size="100%">CO2 reforming of methane to syngas over CoOx/MgO supported on low surface area macroporous catalyst carrier: Influence of Co loading and process conditions</style>

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<style face="normal" font="default" size="100%">Direct oxidation of H-2 to H2O2 over Pd-based catalysts: influence of oxidation state, support and metal additives</style>

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<style face="normal" font="default" size="100%">Factors influencing decomposition of H2O2 over supported Pd catalyst in aqueous medium</style>

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<style face="normal" font="default" size="100%">Methane reforming over a high temperature stable-NiCoMgOx supported on zirconia-hafnia catalyst</style>

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<style face="normal" font="default" size="100%">Oxy-CO2 reforming of methane to syngas over CoOx/CeO2/SA-5205 catalyst</style>

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<style face="normal" font="default" size="100%">Oxy-CO2 reforming of methane to syngas over CoOx/MgO/SA-5205 catalyst</style>

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<style face="normal" font="default" size="100%">Partial oxidation of methane to syngas with or without simultaneous steam or CO2 reforming over a high-temperature stable-NiCoMgCeOx supported on zirconia-hafnia catalyst</style>

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<style face="normal" font="default" size="100%">Propane conversion to aromatics on highly active H-GaAlMFI: effect of thermal pretreatment</style>

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<style face="normal" font="default" size="100%">Oxy-methane reforming over high temperature stable NiCoMgCeOx and NiCoMgOx supported on zirconia-haffnia catalysts: accelerated sulfur deactivation and regeneration</style>

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<style face="normal" font="default" size="100%">Energy-efficient syngas production through, catalytic oxy-methane reforming reactions</style>