Partial Oxidation of Methane over CaO Decorated TiO2 Nanocatalyst for Syngas Production in a Fixed Bed Reactor

Abstract

Syngas is a valuable entity for downstream liquid fuel production and chemical industries. The efficient production of syngas via catalytic partial oxidation of methane (CPOM) is an important process. In this study, partial oxidation of methane (POM) was carried out using CaO decorated TiO2 catalysts. The catalysts were synthesized employing the sol-gel method, while the decoration of TiO2 with CaO was achieved in an aqueous solution by wetness impregnation method. The prepared catalysts were characterized by employing XRD, Raman, TG-DTG, and SEM-EDX for structural and morphological analysis. On testing for POM, at 750 °C the catalysts demonstrate excellent CH4 conversion of 83.6 and 79.5% for 2% and 3% CaO loaded TiO2, respectively. While the average H2/CO ratio for both 2% and 3% CaO loaded TiO2, 2.25 and 2.28, respectively, remained slightly above the theoretical value (H2/CO = 2.0) of POM. The improved POM performance is attributed to the optimally loaded CaO on the TiO2 surface that promotes the reaction where TiO2 support ensure less agglomerated particles, resulting into a fine distribution of the active catalytic sites.

Promoter Impact on 5Ni/SAPO-5 Catalyst for H2 Production via Methane Partial Oxidation

“…However, CO can oxidize into CO 2 , but it can easily dissociate again into CO. It has also been explained in the literature that low energy barriers are required for CO 2 dissociation into CO [60]. As a result of increased oxygen consumption, more active sites are exposed to CH 4 adsorption and increased H 2 generation, as shown in Figure 14.…”

“…Ni [60]. As a result of increased oxygen consumption, more active sites are exposed to CH4 adsorption and increased H2 generation, as shown in Figure 14.…”

Current and Future Role of Natural Gas Supply Chains in the Transition to a Low-Carbon Hydrogen Economy: A Comprehensive Review on Integrated Natural Gas Supply Chain Optimisation Models

“…The commercialisation of ATR is still not comparable to that of SMR [182]. In recent years, research on ATR and POM technologies has become a common area of research to satisfy the need for cost-effective and less pollutant-high conversions in mild reaction environments [183][184][185]. The main characteristics of three hydrogen production processes from natural gas are summarised in Table 4, adapted from [176].…”