(212d) Assessment of Looping Combustion and Gasification of Carbon (CarboLoop) in a Twin Fluidized Bed Reactor
AIChE Annual Meeting
2017
2017 Annual Meeting
Topical Conference: Innovations of Green Process Engineering for Sustainable Energy and Environment
Chemical Looping Processes II
Monday, October 30, 2017 - 4:19pm to 4:40pm
An experimental campaign based on discontinuous experiments in a thermogravimetric analyzer (Salatino and Senneca, 2009, Salatino et al., 2010) has been directed to provide the proof-of-concept of the process. An extensive experimental campaign based on the combined use of TGA and DSC (Senneca et al., 2013) complemented by microstructural characterization by XPS (Levi et al., 2015) contributed to shed light on important and non trivial mechanistic and thermochemical features of the cyclic oxidation-desorption reactions, and on the chemical nature of surface oxides involved.
In this study the CarboLoop concept is tested under conditions that approach those of a realistic looping setup, consisting of a dual interconnected fluidized bed reactor. The âTwin Bedâ test reactor (Coppola et al., 2016) has been purposely developed for the characterization of looping processes at the bench scale while preserving the time-temperature history that particles experience in a realistic looping conditions. It consists of two lab-scale bubbling beds of an inert bed, acting as thermal ballast, operated batchwise, connected to each other by a rapid solids transfer line. Carbon samples are fed to the system and undergo sequential steps of Oxidization and Desorption of pre-set duration by rapid transfer from one reactor to the other. The fuel tested is a bituminous coal char with size range of 400-1000µm. The Oxidizer was operated in air at different temperatures in the range 200-300°C with a holding time of 20 min. The desorption stage was carried out at 700-800°C with the same holding time of 20 min in N2. The progress of char oxidation has been monitored following the profiles of CO and CO2concentration at the exhaust of the Desorber over iterated cycles. The effect of multiple cycles on char oxidation/desorption propensity has been investigated. A systematic characterization of the influence of the operating conditions holding in the oxidation and in the desorption steps has been performed, and analyzed in the light of a simple semi-lumped kinetic scheme. Results are relevant to the development of a tentative process layout for the implementation of the CarboLoop concept.
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