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A laboratory scale dry gas cleaning unit has been developed and tested at CSIRO to address some of these challenges.
The experimental system consists of the downdraft gasifier and the gas cleaning unit made up by a cyclone, a scrubber and a filter box.
The section Thermal Power Engineering of Delft University of Technology operates a 1.5 MW pressurised fluidised bed gasification rig, including a hot gas cleaning unit and a pressurised downscaled Alstom gas turbines combustor.
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In addition, other important parameters such as FGR rate and FGR ratio, flue gas compositions, and load of flue gas cleaning units are analyzed based on coal properties and plant operational conditions.
This is needed to obtain detailed information on contaminant tolerance of SOFCs, and to arrive at detailed designs of gas cleaning units that are economically viable for biomass gasifier-SOFC systems.
Examples are CHP units that serve heat as well as electricity grids or biogas units that either serve CHP (in themselves already grid overarching) or may even serve gas grids when coupled with gas cleaning units.
The proposed plant consists of air separation unit, gasification unit, gas cooling and cleaning unit, pressure swing absorption (PSA) for hydrogen production, high temperature electrolyzer for hydrogen production, Brayton cycle, steam Rankine cycle and organic Rankine cycle (ORC) system for power generation.
Stack concentrations appeared to be influenced by the design and process configuration of flue gas cleaning systems, with most significant effects related to the presence of wet scrubbing units and the baghouse operating temperature of dry removal processes.
The evaluated gas cleaning technologies are low temperature gas cleaning and high temperature gas cleaning and the two scales are 100 kWe and 30 MWe.
Spray towers offer great advantages over other gas cleaning devices.
High temperature gas cleaning results in a slightly higher performance (0.5%) compared to low temperature gas cleaning.
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