Fuel Processing Technology

Caculation method for this paper.

Data processing of infrared thermal images

This provides the experimental data for synthesis of methyl lactate from cellulose catalyzed by mixed Lewis acid systems, including original data of the yield of methyl lactate, particle distribution formed by ball-milling treatment, and FT-IR spectra of ball-milled cellulose.

data in beief, contains: 1.Carbon conversion rate and CO2 selectivity at different No. of cycle; 2.CO2 concentrations evolution with No. of cycles; 3.The change in mechanical strength of the OC before and during cycled testing;4.The evolution on attrition rates of the OC as a function of operation time; 5.XRD patterns of OC after different cycles of carbon oxidation.

These data is a complete description of the methodology to determine the uncertainties in the research. The determination of the uncertainties is important since the reliability of the experimental results is the most important characteristic of any research.

Supplementary material of the manuscript "Dearomatization of pyrolysis gasoline by extractive distillation with 1-ethyl-3-methylimidazolium tricyanomethanide" Tables Table S1 Experimental VLLE or VLE dataa for pyrolysis gasoline model dearomatization using [emim][TCM] with S/F = 5 Table S2 Experimental VLLE or VLE dataa for pyrolysis gasoline model dearomatization using [emim][TCM] with S/F = 10 Table S3 FUGK simulations of the EDC to separate BTX from pyrolysis gasoline by extractive distillation Table S4 Experimental VLE dataa for the BTX/[emim][TCM] separation in the residue stream Table S5. Residue and distillate temperature and composition by FUGK and COSMO-based/Aspen Plus methodologies at 101.3 kPa Table S6. Aromatic purities (Puarom) and recoveries (Rarom) by Navarro et al. algorithm and COSMO-based/Aspen Plus methodologies at 452 K and 5 kPa Table S7. Benzene, toluene and p-xylene solubilities in [emim][TCM] at 363.2 K Table S8. Battery limits for extractive distillation and liquid-liquid extraction processes for S/F = 5 and 15 equilibrium stages for comparison purposes Table S9. Costs for the utilities used from Aspen Economics Figures Figure S1. Extractive distillation process scheme evaluated in the operating cost calculation. Figure S2. Liquid-liquid extraction process scheme evaluated in the operating cost calculation.

The uploaded file including the tar conversion efficiency, yields of each gas component and the standard deviation.

It is a comprehensive high temperature model developed for the mixed alcohols (methanol, n-hexanol, n-heptanol and n-octanol). This model performs well in predicting the laminar flame speeds of the blends of methanol and n-hexanol/n-heptanol/n-octanol at 433 K and 0.1 MPa.

The data are experimental laminar flame speeds and Markstein lengths of the blends of methanol and n-hexanol/n-heptanol/n-octanol at 433 K and 0.1 MPa. The uncertainties of the experimental data are also included.

1. Types of biomass feedstocks, 2. Typical measurements during a solar gasification experiment, 3. Typical evolution of syngas production rates during continuous biomass injection, 4. Operating conditions and solar reactor performances assessment, 5. Steam mass flow-rate chart for a stoichiometric H2O/biomass molar ratio, 6. Window deposit due to the presence of smoke at low temperature, 7. Effect of temperature on syngas yield and energy upgrade factor, 8. Kinetic study, 9. Ashes remaining in the reactor cavity, 10. Effect of biomass feeding rate for each biomass type at 1200 °C, 11. Effect of biomass feeding rate for each biomass type at 1300 °C, 12. Influence of biomass feeding rate on syngas production rates evolution, 13. Energy balance, 14. Comparison of the carbon consumption rate at different temperatures as a function of biomass feeding rate