Catalytic gasification of lignin with Ni/Al2O3–SiO2 in sub/supercritical water

Abstract Lignin has been gasified with a Ni/Al2O3–SiO2 catalyst in sub/supercritical water (SCW) to produce gaseous fuels. XRD pattern at 6θ angle shows characteristic peaks of crystalline NiO, NiSi, and AlNi3, suggesting that Al2O3–SiO2 not only offers high surface area (122 m2 g) for Ni, but also changes the crystal morphology of the metal. 9 mmol/g of H2 and 3.5 mmol/g of CH4 were produced at the conditions that 5.0 wt% alkaline lignin plus 1 g/g Ni/Al2O3–SiO2 operating for 30 min at 550 °C. A kinetic model was also developed, and the activation energies of gas and char formation were calculated to be 36.68 ± 0.22 and 9.0 ± 2.4 kJ/mol, respectively. Although the loss of activity surface area during reuse caused slight activity reduction in Ni/Al2O3–SiO2, the catalyst system still possessed high catalytic activity in generating H2 and CH4. It is noted that sulfur linkage could be hydrolyzed to hydrogen sulfide in the gasification process of alkaline lignin. The stable chemical states of Ni/Al2O3–SiO2 grants its insensitivity to sulfur, suggesting that Ni/Al2O3–SiO2 should be economically promising for sub/supercritical water gasification of biomass in the presence of sulfur.

[1]  Kunio Arai,et al.  Water density effect on lignin gasification over supported noble metal catalysts in supercritical water , 2006 .

[2]  P. Savage,et al.  Noncatalytic Gasification of Lignin in Supercritical Water , 2008 .

[3]  C. Ballaré,et al.  Dual role of lignin in plant litter decomposition in terrestrial ecosystems , 2010, Proceedings of the National Academy of Sciences.

[4]  E. Dinjus,et al.  Influence of Process Variables on Gasification of Corn Silage in Supercritical Water , 2006 .

[5]  Pooya Azadi,et al.  Review of heterogeneous catalysts for sub- and supercritical water gasification of biomass and wastes , 2011 .

[6]  N. Itoh,et al.  The evaluation of the stability of Ni/MgO catalysts for the gasification of lignin in supercritical water , 2007 .

[7]  Phillip E. Savage,et al.  Gasification of alga Nannochloropsis sp. in supercritical water , 2012 .

[8]  P. Savage,et al.  Expanded and Updated Results for Supercritical Water Gasification of Cellulose and Lignin in Metal-Free Reactors , 2009 .

[9]  Morgan Fröling,et al.  Thermochemical biofuel production in hydrothermal media: A review of sub- and supercritical water technologies , 2008 .

[10]  C. Xu,et al.  Hydrolytic degradation of alkaline lignin in hot-compressed water and ethanol. , 2010, Bioresource technology.

[11]  M. Shirai,et al.  Stability of Supported Ruthenium Catalysts for Lignin Gasification in Supercritical Water , 2006 .

[12]  M. Nachtegaal,et al.  Towards understanding the catalytic reforming of biomass in supercritical water. , 2010, Angewandte Chemie.

[13]  Masaru Watanabe,et al.  Catalytic hydrogen generation from biomass (glucose and cellulose) with ZrO2 in supercritical water , 2002 .

[14]  P. Savage,et al.  Kinetic model for noncatalytic supercritical water gasification of cellulose and lignin , 2010 .

[15]  P. Savage,et al.  Hydrothermal Gasification of Nannochloropsis sp. with Ru/C , 2012 .

[16]  M. Shirai,et al.  Effect of Sulfur on Catalytic Gasification of Lignin in Supercritical Water , 2007 .

[17]  Ki Chul Park,et al.  Gasification reaction of organic compounds catalyzed by RuO2 in supercritical water. , 2003, Chemical communications.

[18]  Phillip E. Savage,et al.  Organic Chemical Reactions in Supercritical Water. , 1999, Chemical reviews.

[19]  Peter McKendry,et al.  Energy production from biomass (Part 1): Overview of biomass. , 2002, Bioresource technology.

[20]  Douglas C. Elliott,et al.  Catalytic hydrothermal gasification of biomass , 2008 .