Breadcrumb
- Home
- Publications
- Proceedings
- 2012 AIChE Annual Meeting
- Catalysis and Reaction Engineering Division
- Reaction Engineering for Biomass Conversion
- (50e) Kinetic Modeling & Simulation of Thermo-Chemical Conversion of Jatropha De-Oiled Cake
Kinetics of thermal decomposition of biomass material is complicated, as it involves a large number of reactions in parallel and series. Different classes of mechanisms are reported for the pyrolysis of wood and other ligno-cellulosic materials. The models are classified into three categories: one-step global models; one-stage multi-reaction models; and two-stage semi-global models. The second category of models discuss those mechanisms, which consider simultaneous and competing first order reactions in which virgin biomass decomposes into different constitutes of pyrolysis products, namely, tar, char, and volatile gases. The third class of models consider pyrolysis to be a two-stage reaction, in which the products of the first stage break up further in the presence of each other to produce secondary pyrolysis products (Babu, 2008). These reported kinetic studies are limited to use for certain species of biomass only for which kinetic data are available. In this work, the pyrolysis process is described by the independent parallel first order reactions model.
In the present study, a kinetic model is developed to represent the pyrolysis process that is described by independent parallel first order reactions. The kinetic model is simulated using finite forward difference method to predict the pyrolysis rate. The corresponding kinetic parameters of the model are estimated by minimizing the square of the error between the experimental data of thermo-gravimetry and simulated model predicted values of residual weight fraction using Differential Evolution (Price and Storn, 1997, Gujrathi and Babu, 2011), a population based search algorithm. Thermo-gravimetric experimental runs are carried out using Thermo-gravimetric analyzer (TGA 4000, Perkin Elmer) of Jatropha cake waste. TGA study is performed in a nitrogen atmosphere under non-isothermal conditions at different heating rates and the thermal decomposition profiles are used to find the kinetic parameters.
References
Babu, B.V., 2008. Biomass pyrolysis: a state-of-the-art review. Biofuels, Bioproducts and Biorefining 2, 393-414.
Gujarathi, A.M., Babu, B.V., 2011. Multi-objective optimization of industrial processes using Elitist Multi-Objective Differential Evolution (Elitist-MODE). Materials and Manufacturing Processes 26, 455-463.
Price, K., Storn, R., 1997. Differential evolution - a simple evolution strategy for fast optimization, Dr. Dobb's Journal 264, 18-24 & 78.
Sheth, P.N., Babu, B.V., 2009. Experimental studies on producer gas generation from wood waste in a downdraft biomass gasifier. Bioresource Technology 100, 3127-3133.
Sheth, P.N., Babu, B.V., 2010. Production of hydrogen energy through biomass (waste wood) gasification. International Journal of Hydrogen Energy 35, 10803-10810.
Sricharoenchaikul, V., Atong, D., 2009. Thermal decomposition study on Jatropha curcas L. waste using TGA and fixed bed reactor. Journal of Analytical and Applied Pyrolysis 85, 155-162.