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RESEARCH PRODUCT

CO2 to Liquid Fuels: Photocatalytic Conversion in a Continuous Membrane Reactor

Elisa I. García-lópezFrancesca Rita PomillaFrancesca Rita PomillaGiuseppe MarcìAdele BrunettiGiuseppe BarbieriEnrica FontananovaLeonardo Palmisano

subject

Materials scienceContinuous operationDiffuse reflectance infrared fourier transformContact timeCarbon nitrideGeneral Chemical Engineering2Renewable Energy Sustainability and Environment02 engineering and technology010402 general chemistryPhotocatalytic membrane reactor01 natural sciencesCatalysisMatrix (chemical analysis)chemistry.chemical_compoundNafionEnvironmental ChemistryMembrane reactorRenewable Energy Sustainability and the EnvironmentGeneral Chemistry021001 nanoscience & nanotechnologyphotoreduction0104 chemical sciencesCOchemistryChemical engineeringCO2 photoreductionPhotocatalysisSettore CHIM/07 - Fondamenti Chimici Delle Tecnologie0210 nano-technologySelectivityCarbon nitride CO2 photoreduction Continuous operation Photocatalytic membrane reactor

description

The photocatalytic reduction of CO, into value-added chemicals using sunlight is a promising approach to promote energy-bearing products, mitigating the adverse effects of anthropogenic CO2 emissions. In this work, exfoliated C3N4 was incorporated into Nafion matrix and used in a continuous photocatalytic reactor for converting CO2 into liquid fuels. Comprehensive structural and morphological diffuse reflectance spectroscopy (DRS), FT-IR, ATR-IR, and SEM measurements were performed for C3N4-loaded Nafion membrane and then compared with those of a Nafion membrane without any catalyst. The synergic effect of C3N4 organic catalyst embedded in a Nafion dense matrix and a continuous operating mode of the photoreactor was successfully accomplished for the first time, as yet absent in the literature, analyzing the reactor performance as a function of key parameters such as contact time and H2O/CO2 feed molar ratio. The reactor performance was analyzed under UV-vis light in terms of productivity, selectivity, and converted carbon. Alcohol (MeOH + EtOH) production was 32.8 mu mol g(catlyst)(-1) h(-1) corresponding to 47.6 mu mol g(catalyst)(-1) h(-1) of total converted carbon per gram of catalyst at the best operating conditions. So far, this value results as higher than most of the literature values reported up to date. Moreover, the membrane reactor converted at least 10 times more carbon than the batch system, as a result of the catalyst embedding in a Nafion matrix.

10.1021/acssuschemeng.8b01073http://hdl.handle.net/10281/280274