Process simulation of sorption enhanced chemical-looping reforming for hydrogen production
from biomass was investigated. Corn stover was converted to bio-oil via pyrolysis prior to …

The effect of catalyst calcination temperature (450C, 600C, and 750C) on catalytic performance
of synthesized and commercial grade sulfated zirconia catalysts towards isosynthesis …

This paper investigates the isosynthesis via CO hydrogenation over zirconia and ceria catalysts.
Various techniques including XRD, NH 3 -TPD, CO 2 -TPD and BET surface area were …

Intensified process of sorption enhanced chemical-looping reforming (SECLR) for hydrogen
production was studied. This process was modified by recycling a portion of solid NiO and …

The present study revealed the isosynthesis via CO hydrogenation over ZrO 2 –CeO 2 mixed
oxide catalysts. The catalysts were synthesized by coprecipitation and the physical mixing …

This paper studied the effect of temperature ramping rate during calcination on characteristics
of nanoscale zirconia and its catalytic performance for isosynthesis. The physical …

Catalytic performances of sulfated zirconia catalysts with various contents of sulfur (from 0.1
to 0.75%) on isosynthesis were studied. It was firstly found that undoped-zirconia …

This research investigated the mass transfer performance of the extraction of benzoic acid
in water/n-heptane system in a spinning disc reactor (SDR). The effects of rotational disc …

This paper reports a thermodynamic-based study into the production of hydrogen via biogas
decomposition for use in polymer electrolyte membrane fuel cells (PEMFC) and solid oxide …

A compact heat integrated reactor system (CHIRS) of a steam reformer, a water gas shift
reactor, and a combustor were designed for stationary hydrogen production from ethanol. …