Abstract

Waste heat recovery (WHR) systems through organic rankine cycles (ORCs) in anaerobic digestion plants may improve cogeneration efficiency. Cogeneration unit power output, flue gas temperature, and mass flow rate are not constant during the day, and the thermal load requested by digesters shows seasonal variations. For this reason, a proper design of the ORC is required. In this study, a design methodology is proposed, based on the clustering of the boundary conditions expected during one year of operation and the anaerobic digestion plant operation. The design has to be a compromise between part-load operation and nominal power rating. In this study, the ORC design boundary conditions were partitioned into four representative clusters with a different population, and the centroid of each cluster was assumed as a potential representative boundary condition for the cycle design. Four different ORC designs, one for each cluster, were defined through an optimization problem that maximized the cycle net power output. ORC designs were compared to those resulting from the seasonal average boundary conditions. The comparison was made based on the ORC off-design performance. Part-load behavior was estimated by implementing a sliding-pressure control strategy and the annual production was therefore calculated. ORC off-design was studied through a detailed Aspen HYSYS simulation. Simulations showed that the power output of each design was directly connected to the cluster population. The design obtained from the most populated cluster generated 10% more energy than that from a system designed by taking into account only the year average conditions.

Highlights

  • Anaerobic digestion plants have been spreading in Europe due to the favorable synergy between energy production and sanitation services [1]

  • Once the design conditions were known, an off-design model was developed in Aspen HYSYS

  • The off-design model of the organic rankine cycles (ORCs) was implemented by considering design data from MATLAB optimization

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Summary

Introduction

Anaerobic digestion plants have been spreading in Europe due to the favorable synergy between energy production and sanitation services [1]. Subsidies related to biogas upgrading into biomethane and its injection in the natural gas network, or its liquefaction, have made anaerobic plants profitable in several European countries [2]. All these issues make anaerobic digestion a promising waste-processing technology from environmental, energy, and economic points of view [3]. Bruno et al [8] proposed mGT inlet air cooling through an absorption chiller that exploits the excess thermal energy in the flue gas. Results showed that for anaerobic digestion plants equipped with a mGT, inlet air cooling is a valid technology from energy and economic points of view. A further study [9] showed that inlet air cooling effectiveness is strongly dependent on the climate conditions

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