(389c) Solar Gasification in a Molten Salt Reactor for Continuous Production of Syngas
AIChE Annual Meeting
2017
2017 Annual Meeting
2017 International Congress on Energy
Symposium on Solar Power and Chemical Systems in Honor of Prof. Edward A. Fletcher II
Tuesday, October 31, 2017 - 1:20pm to 1:40pm
In the present study, we present a model of an improved volumetric pumping feed system and provide operational data for gasification of cellulose in the improved reactor. The feed system consists of a single fluted screw within a straight barrel, similar to that used for polymer extrusion systems. The feed enters the reactor as a densified cylinder rather than as loose powder, encouraging the formation of larger char particles which have a reduced tendency to be entrained by the product gases leaving the reactor. The design of the feed delivery system is based in part on a numerical model of the transient heat transfer and kinetics of pyrolysis and gasification of the feedstock material during transport.
The reactor was operated for CO2 gasification of cellulose in the University of Minnesotaâs high flux solar simulator. The simulator consists of seven radiation units, each composed of a 6.5 kW xenon short arc lamp close-coupled to a custom reflector in the shape of a truncated ellipsoid of revolution. The total power delivered to the aperture of the reactor was measured using a water-cooled black body calorimeter of the same aperture diameter. The feedstock is ash-free microcrystalline cellulose (C6H10O5) sieved to a particle size of 0.5 mm. Temperatures of the solar cavity and within the salt melt are measured using Type-K thermocouples. The product gas composition is measured using a Raman Laser Gas Analyzer. The downstream gas lines and HEPA filter are analyzed for residual secondary products. Tars are separated from solids using a solvent wash and the particle size distribution of the solid material is measured using laser diffraction.
The reactor performance is quantified by the solar to fuel efficiency defined in rate form as the ratio of the lower heating value of the useful products and the sum of the solar input and the LHV of the carbonaceous feedstock. Carbon conversion is given by the ratio of the net gaseous carbon released from the reactor to the feedstock carbon delivered to the reactor. The measured species flow rates are compared to the equilibrium flow rates predicted using Gibbs free energy minimization. The data demonstrate the improvements in performance for the reactor with the new feed system in terms of longer operation without blockage, and higher solar efficiency.