Conventional and microwave induced pyrolysis of coffee hulls for the production of a hydrogen rich fuel gas

Abstract This paper describes the conventional and microwave-assisted pyrolysis of coffee hulls at 500, 800 and 1000 °C. The influence of the pyrolysis method and temperature on the product yields and on the characteristics of the pyrolysis products is discussed. It was found that the pyrolysis of this particular residue gives rise to a larger yield of the gas fraction compared to the other fractions, even at relatively low temperatures. A comparison of microwave-assisted pyrolysis and conventional pyrolysis showed that microwave treatment produces more gas and less oil than conventional pyrolysis. In addition, the gas from the microwave has much higher H 2 and syngas (H 2  + CO) contents (up to 40 and 72 vol.%, respectively) than those obtained by conventional pyrolysis (up to 30 and 53 vol.%, respectively), in an electric furnace, at similar temperatures. From the pyrolysis fraction yields and their higher heating values it was found that the energy distribution in the pyrolysis products decreases as follows: gas > solid > oil. Moreover, the energy accumulated in the gas increases with the pyrolysis temperature. By contrast, the energy accumulated in the char decreases with the temperature. This effect is enhanced when microwave pyrolysis is used.

[1]  Naim Afgan,et al.  Sustainable Energy Development , 1998 .

[2]  J. A. Menéndez,et al.  On the pyrolysis of sewage sludge: the influence of pyrolysis conditions on solid, liquid and gas fractions , 2002 .

[3]  I. Vasalos,et al.  An investigation of the factors controlling the pyrolysis product yield of greek wood biomass in a fluidized bed , 1990 .

[4]  N. Muradov,et al.  Catalytic activity of carbons for methane decomposition reaction , 2005 .

[5]  W. Tsai,et al.  Fast pyrolysis of rice straw, sugarcane bagasse and coconut shell in an induction-heating reactor , 2006 .

[6]  M. Illán-Gómez,et al.  Effect of potassium content in the activity of K-promoted Ni/Al2O3 catalysts for the dry reforming of methane , 2006 .

[7]  Toyoji Kakuchi,et al.  Rapid pyrolysis of wood block by microwave heating , 2004 .

[8]  J. J. Pis,et al.  Microwave-induced pyrolysis of sewage sludge. , 2002, Water research.

[9]  A. Bridgwater,et al.  Fast pyrolysis processes for biomass , 2000 .

[10]  J. A. Menéndez,et al.  Microwave pyrolysis of sewage sludge: analysis of the gas fraction , 2004 .

[11]  C. Acikgoz,et al.  Fast pyrolysis of linseed: product yields and compositions , 2004 .

[12]  José M. Encinar,et al.  Pyrolysis of maize, sunflower, grape and tobacco residues , 1997 .

[13]  S. Kingman,et al.  Microwave technology for energy-efficient processing of waste , 2005 .

[14]  Don W. Green,et al.  Perry's Chemical Engineers' Handbook , 2007 .

[15]  I. Obernberger Decentralized biomass combustion: state of the art and future development 1 1 Paper to the keynote l , 1998 .

[16]  A. Bridgwater,et al.  An overview of fast pyrolysis of biomass , 1999 .

[17]  S. Yaman Pyrolysis of biomass to produce fuels and chemical feedstocks , 2004 .

[18]  C. Roy,et al.  Hydrocarbon content of liquid products and tar from pyrolysis and gasification of wood , 1991 .

[19]  V. Likholobov,et al.  Iron-containing catalysts of methane decomposition: accumulation of filamentous carbon , 2002 .

[20]  Waichi Iwasaki,et al.  A consideration of the economic efficiency of hydrogen production from biomass , 2003 .

[21]  Paul T. Williams,et al.  Influence of temperature on the products from the flash pyrolysis of biomass , 1996 .

[22]  Kartic C. Khilar,et al.  Pyrolysis characteristics of biomass and biomass components. , 1996 .

[23]  Robert C. Brown,et al.  Biomass-derived hydrogen from an air-blown gasifier , 2005 .

[24]  K. Khilar,et al.  Influence of mineral matter on biomass pyrolysis characteristics , 1995 .

[25]  Ralph P. Overend,et al.  Biomass and renewable fuels , 2001 .

[26]  A. Mujumdar Handbook of Industrial Drying , 2020 .

[27]  K. E. Harfi Pyrolysis of the Moroccan (Tarfaya) oil shales under microwave irradiation , 2000 .

[28]  N. J. Miles,et al.  Microwave heating applications in environmental engineering—a review , 2002 .

[29]  Shaoping Xu,et al.  Fast pyrolysis of biomass in free-fall reactor for hydrogen-rich gas , 2004 .

[30]  G. Mills,et al.  Status and future opportunities for conversion of synthesis gas to liquid fuels , 1994 .

[31]  N. Petrov,et al.  Biomass conversion to carbon adsorbents and gas , 2001 .

[32]  J. J. Pis,et al.  Investigations into the characteristics of oils produced from microwave pyrolysis of sewage sludge , 2005 .

[33]  M. Bradford,et al.  CO2 Reforming of CH4 , 1999 .

[34]  Anuradda Ganesh,et al.  Heating value of biomass and biomass pyrolysis products , 1996 .