Home > Research > Publications & Outputs > Thermodynamic analysis of glycerol dry reformin...

Research

Links

Text available via DOI:

View graph of relations

Thermodynamic analysis of glycerol dry reforming for hydrogen and synthesis gas production

Research output: Contribution to Journal/Magazine › Journal article › peer-review

Published

Standard

Thermodynamic analysis of glycerol dry reforming for hydrogen and synthesis gas production. / Wang, Xiaodong; Li, M.; Wang, M. et al.
In: Fuel, Vol. 88, No. 11, 01.11.2009, p. 2148-2153.

Research output: Contribution to Journal/Magazine › Journal article › peer-review

Harvard

Wang, X, Li, M, Wang, M, Wang, H, Li, S, Wang, S & Ma, X 2009, 'Thermodynamic analysis of glycerol dry reforming for hydrogen and synthesis gas production', Fuel, vol. 88, no. 11, pp. 2148-2153. https://doi.org/10.1016/j.fuel.2009.01.015

APA

Wang, X., Li, M., Wang, M., Wang, H., Li, S., Wang, S., & Ma, X. (2009). Thermodynamic analysis of glycerol dry reforming for hydrogen and synthesis gas production. Fuel, 88(11), 2148-2153. https://doi.org/10.1016/j.fuel.2009.01.015

Vancouver

Wang X, Li M, Wang M, Wang H, Li S, Wang S et al. Thermodynamic analysis of glycerol dry reforming for hydrogen and synthesis gas production. Fuel. 2009 Nov 1;88(11):2148-2153. doi: 10.1016/j.fuel.2009.01.015

Author

Wang, Xiaodong ; Li, M. ; Wang, M. et al. / Thermodynamic analysis of glycerol dry reforming for hydrogen and synthesis gas production. In: Fuel. 2009 ; Vol. 88, No. 11. pp. 2148-2153.

Bibtex

@article{6de848b203d34dd5b16518a86ff6512b,
title = "Thermodynamic analysis of glycerol dry reforming for hydrogen and synthesis gas production",
abstract = "A thermodynamic analysis of glycerol dry reforming has been performed by the Gibbs free energy minimization method as a function of CO2 to glycerol ratio, temperature, and pressure. Hydrogen and synthesis gas can be produced by the glycerol dry reforming. The carbon neutral glycerol reforming with greenhouse gas CO2 could convert CO2 into synthesis gas or high value-added inner carbon. Atmospheric pressure is preferable for this system and glycerol conversion keeps 100%. Various of H2/CO ratios can be generated from a flexible operational range. Optimized conditions for hydrogen production are temperatures over 975 K and CO2 to glycerol ratios of 0–1. With a temperature of 1000 K and CO2 to glycerol ratio of 1, the production of synthesis gas reaches a maximum, e.g., 6.4 mol of synthesis gas (H2/CO = 1:1) can be produced per mole of glycerol with CO2 conversion of 33%.",
author = "Xiaodong Wang and M. Li and M. Wang and H. Wang and S. Li and S. Wang and X. Ma",
year = "2009",
month = nov,
day = "1",
doi = "10.1016/j.fuel.2009.01.015",
language = "English",
volume = "88",
pages = "2148--2153",
journal = "Fuel",
issn = "0016-2361",
publisher = "Elsevier BV",
number = "11",

}

RIS

TY - JOUR

T1 - Thermodynamic analysis of glycerol dry reforming for hydrogen and synthesis gas production

AU - Wang, Xiaodong

AU - Li, M.

AU - Wang, M.

AU - Wang, H.

AU - Li, S.

AU - Wang, S.

AU - Ma, X.

PY - 2009/11/1

Y1 - 2009/11/1

N2 - A thermodynamic analysis of glycerol dry reforming has been performed by the Gibbs free energy minimization method as a function of CO2 to glycerol ratio, temperature, and pressure. Hydrogen and synthesis gas can be produced by the glycerol dry reforming. The carbon neutral glycerol reforming with greenhouse gas CO2 could convert CO2 into synthesis gas or high value-added inner carbon. Atmospheric pressure is preferable for this system and glycerol conversion keeps 100%. Various of H2/CO ratios can be generated from a flexible operational range. Optimized conditions for hydrogen production are temperatures over 975 K and CO2 to glycerol ratios of 0–1. With a temperature of 1000 K and CO2 to glycerol ratio of 1, the production of synthesis gas reaches a maximum, e.g., 6.4 mol of synthesis gas (H2/CO = 1:1) can be produced per mole of glycerol with CO2 conversion of 33%.

AB - A thermodynamic analysis of glycerol dry reforming has been performed by the Gibbs free energy minimization method as a function of CO2 to glycerol ratio, temperature, and pressure. Hydrogen and synthesis gas can be produced by the glycerol dry reforming. The carbon neutral glycerol reforming with greenhouse gas CO2 could convert CO2 into synthesis gas or high value-added inner carbon. Atmospheric pressure is preferable for this system and glycerol conversion keeps 100%. Various of H2/CO ratios can be generated from a flexible operational range. Optimized conditions for hydrogen production are temperatures over 975 K and CO2 to glycerol ratios of 0–1. With a temperature of 1000 K and CO2 to glycerol ratio of 1, the production of synthesis gas reaches a maximum, e.g., 6.4 mol of synthesis gas (H2/CO = 1:1) can be produced per mole of glycerol with CO2 conversion of 33%.

U2 - 10.1016/j.fuel.2009.01.015

DO - 10.1016/j.fuel.2009.01.015

M3 - Journal article

VL - 88

SP - 2148

EP - 2153

JO - Fuel

JF - Fuel

SN - 0016-2361

IS - 11

ER -