Characterization of products from the pyrolysis of rapeseed oil cake.

The main aim of this study was to investigate the composition of products from the pyrolysis of rapeseed oil cake in a fixed bed reactor at 400, 450, 500, 700 and 900 degrees C. The gas products mainly consisted of CO(2), CO, CH(4) and H(2)S at 500 degrees C. Empirical formula of bio-oil from the pyrolysis of rapeseed oil cake was CH(1.59)O(0.16)N(0.116)S(0.003) for 500 degrees C. Bio-oils mainly contained oleic acid, 1H-indole, 2,3,5-trimethoxy toluene, toluene, (Z)-9-octadecanamide, psoralene, phenol and phenol derivatives at all pyrolysis temperatures. Both non-aromatic and aromatic hydrocarbon compounds were determined in water phase of liquid product by Headspace-GC analysis. The heating values of bio-chars were found to be similar (24MJkg(-1)) at all pyrolysis temperatures.

[1]  E. Çulcuoğlu,et al.  Thermogravimetric analysis of the rapeseed cake , 2001 .

[2]  Filiz Karaosmanoglu,et al.  Production and characterization of bio-oil and biochar from rapeseed cake , 2004 .

[3]  Peter McKendry,et al.  Energy production from biomass (Part 2): Conversion technologies. , 2002, Bioresource technology.

[4]  Aw Drews,et al.  Standard Test Methods for Instrumental Determination of Carbon, Hydrogen, and Nitrogen in Petroleum Products and Lubricants , 1998 .

[5]  Ayşe Eren Pütün,et al.  Fixed-bed catalytic pyrolysis of cotton-seed cake: effects of pyrolysis temperature, natural zeolite content and sweeping gas flow rate. , 2006, Bioresource technology.

[6]  S. Şensöz,et al.  Biooil Production from an Oilseed Crop: Fixed-Bed Pyrolysis of Rapeseed (Brassica napus L.) , 2000 .

[7]  Thallada Bhaskar,et al.  Low-temperature catalytic hydrothermal treatment of wood biomass: analysis of liquid products , 2005 .

[8]  S. Şensöz,et al.  Influence of particle size on the pyrolysis of rapeseed (Brassica napus L.): fuel properties of bio-oil , 2000 .

[9]  S. Küçükbayrak,et al.  Effect of heating rate on the pyrolysis yields of rapeseed , 2006 .

[10]  M. Kujawa FAO Plant Production and Protection Paper, Pesticide Residues in Food; Evaluations 1979, 560 Seiten. Food and Agriculture Organization of the United Nations, Rome 1980. , 1982 .

[11]  F. M. Dean Naturally Occurring Oxygen Ring Compounds , 1963 .

[12]  S. Şensöz,et al.  Flash pyrolysis of sunflower oil cake for production of liquid fuels , 2001 .

[13]  Özlem Onay,et al.  Pyrolysis of rapeseed in a free fall reactor for production of bio-oil , 2006 .

[14]  Filiz Karaosmanoglu,et al.  Biofuel production using slow pyrolysis of the straw and stalk of the rapeseed plant , 1999 .

[15]  S. Şensöz,et al.  Bio-oil production from soybean (Glycine max L.); fuel properties of Bio-oil. , 2006 .

[16]  Ö. Onay,et al.  Slow, fast and flash pyrolysis of rapeseed , 2003 .

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

[18]  E. Çulcuoğlu,et al.  Fixed Bed Pyrolysis of the Rapeseed Cake , 2001 .

[19]  Paul L. Bishop,et al.  Pollution Prevention:Fundamentals and Practice , 1999 .

[20]  Carlos Ricardo Soccol,et al.  Oil cakes and their biotechnological applications--a review. , 2007, Bioresource technology.

[21]  J. Tascón,et al.  Composition of gases released during olive stones pyrolysis , 2002 .

[22]  Ö. Onay,et al.  Fixed-bed pyrolysis of rapeseed (Brassica napus L.). , 2004 .

[23]  Spyros Voutetakis,et al.  Biomass pyrolysis in a circulating fluid bed reactor for the production of fuels and chemicals , 2002 .