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Conversion and product distribution affected the heat of reaction.
Temperature also altered the conversion and product ratios as expected.
Quadratic models for CO conversion and product selectivity have been developed based on the experimental results.
The reactor model showed good ability for predicting char conversion and product gas composition.
Temperature, pulse timing, and feed composition were varied to quantify the conversion and product selectivities.
Finite adsorption and axial dispersion have a generally deteriorating effect on overall conversion and product purity.
Model predictions for kerogen conversion and product yield structure agree well with the experimental data.
The conversion and product distribution were also investigated because they affected the heat of reaction.
Turnover frequency (TOF) of propane conversion, and product selectivity were measured in propane oxidation.
(a) CO2 conversion and product selectivity over different combinations of Na Fe3O4 and HZSM-5 catalysts conducted at the same reaction conditions as Fig. 1a; HCs: hydrocarbons.
During reduction, the oxygen carrier donates the required amount of oxygen ions for hydrocarbon conversion and product synthesis.
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