Reformado de etanol con absorción simultánea de CO2 empleando CaO como absorbente

AGUSTIN CUNILL MARTINEZ; ML DIEUZEIDE; N AMADEO

CORDOBA

Congreso; XX CONGRESO ARGENTINO DE CATALISIS; 2017

SOCIEDAD ARGENTINA DE CATALISIS

This paper reports experimental data from laboratory scale fixed bed reactors containing a couple system of reforming catalyst HDL NiMgAl and CaO as sorbent. The distribution of catalyst/adsorbent beds in the reactor has significant effects on reaction/separation performance. The number of catalyst-adsorbent layers has an important impact on the purity of hydrogen. Particularly, the well mixed configuration increases sharply hydrogen purity.The continuous sorption-enhanced steam reforming process would simplify the production of high purity hydrogen since the WGS reactor unit would not be necessary in the purification train.