Project No: FE0005476
Performer: Virginia Polytechnic Institute and State University
Jenny Tennant Coal and Coal/Biomass to Liquids Technology Manager National Energy Technology Laboratory 3610 Collins Ferry Road P.O. Box 880 Morgantown, WV 26507-0880 304-285-4830 email@example.com Steven Markovich Project Manager National Energy Technology Laboratory 626 Cochrans Mill Road P.O. Box 10940 Pittsburgh, PA 15236-0940 412-386-7537 firstname.lastname@example.org Francine Battaglia Principal Investigator Virginia Polytechnic Institute and State University Mechanical Engineering 100 Randolph Hall Blacksburg, VA 24061 540-231-0077 email@example.com
DOE Share: $999,888.00
Performer Share: $252,504.00
Total Award Value: $1,252,392.00
Performer website: Virginia Polytechnic Institute and State University - http://www.vt.edu
The proposed work is a collaborative effort involving experiments, kinetic modeling, and computational fluid dynamics that incorporates efficient methods for solving complex heterogeneous chemistry. The goal is to determine the key reactive properties for coal-biomass mixed fuels. To achieve this goal, sub-bituminous coal will be mixed with biomass feedstocks of hybrid poplar wood, switchgrass, or corn stover and catalysts added to lower the gasification temperatures, thereby improving the gasification process. The outcome of this research will be characterization of the chemical kinetics and reaction mechanisms of the co-gasification fuels and development of a set of models that can be integrated into other modeling environments. Finally, the reaction kinetics modeling will be implemented into NETL’s multiphase flow code—Multiphase Flow with Interphase Exchange (MFIX)—to efficiently simulate the chemistry and recommendations will be made regarding fluidization characteristics.
SEM photograph of biomass char from pyrolysis of oak wood without catalyst (Source: Virginia Tech).
SEM photograph of biomass char from pyrolysis of pine with catalyst (Source: Virginia Tech).
Program Background and Project Benefits
Project Scope and Technology Readiness Level
Gasification experiments will be conducted in bench-scale (2-inch diameter) and pilot-scale (4-inch diameter) fluidized bed reactors under a range of temperatures and atmospheric pressure. Several acidic catalysts, including nickel, will be used catalysis?ed gasification temperatures a byproduct of the n temperatures?to lower gasification temperatures during the pyrolysis reaction. Slag formation also will be examined. Researchers will analyze the composition of the fuels, which will guide the development of the detailed reaction kinetics models. The molecular kinetic modeling will be used to identify the important reaction pathways and convert the molecules to a set of attributes that provide the molecular detail needed to convert those attributes into a set of equations describing the chemical reaction occurring in the system. A reaction module will be coupled with CHEMKIN, a software tool for solving complex chemical kinetics problems, and built using the equations that describe the co-gasification process. Decoupling the transport and chemical source terms using a fractional step approach will provide an efficient method for solving the complex chemistry. Finally, MFIX will be coupled with an efficient reaction module to provide an excellent computational fluid dynamics tool for analyzing co-gasification, providing valuable information related to fluidization characteristics (including mixing and segregation), and supporting gasifier design.
The Technology Readiness Level (TRL) assessment identifies the current state of readiness of the key technologies being developed under the DOE’s Clean Coal Research Program. In FY 12, this project was assessed a TRL of 3.
The TRL assessment process and its results including definition and description of the levels may be found in the "2012 Technology Readiness Assessment-Analysis of Active Research Portfolio".
The research team has pyrolyzed/gasified biomass under different atmospheres and studied coal/poplar mixtures under different pressures and temperatures in the two-inch fluidized bed reactor. The yields were determined gravimetrically by weighing the coal-biomass mixed fuels used in the reactor before and after each experiment before and after each experiment. Preliminary results indicate that there is a component in the poplar wood that may be increasing the projected gasification yield. Work to determine the effect of CO2 on these reactions is ongoing. Under the modeling task, the reaction kinetics and mechanisms have been determined and researchers are ready to progress to the final phase of model investigation. The MFIX code is being developed for parallel processing of the coal portion of the coal and biomass reaction. The model has been developed and is being validated. Researchers continue to simulate the biomass portion of the reaction.