Thermodynamic Optimization of Recuperative Sub- and Transcritical Organic Rankine Cycle Systems
File(s)ECOS2017_Oyewunmietal-Submitted_2.pdf (914.13 KB)
Accepted version
Author(s)
Oyewunmi, OA
Lecompte, S
De Paepe, M
Markides
Type
Conference Paper
Abstract
There is significant interest in the deployment of organic Rankine cycle (ORC) technology for waste-heat
recovery and power generation in industrial settings. This study considers ORC systems optimized for
maximum power generation using a case study of an exhaust flue-gas stream at a temperature of 380 °C as
the heat source, covering over 30 working fluids and also considering the option of featuring a recuperator.
Systems based on transcritical cycles are found to deliver higher power outputs than subcritical ones, with
optimal evaporation pressures that are 4-5 times the critical pressures of refrigerants and light hydrocarbons,
and 1-2 times those of siloxanes and heavy hydrocarbons. For maximum power production, a recuperator is
necessary for ORC systems with constraints imposed on their evaporation and condensation pressures. This
includes, for example, limiting the minimum condensation pressure to atmospheric pressure to prevent subatmospheric
operation of this component, as is the case when employing heavy hydrocarbon and siloxane
working fluids. For scenarios where such operating constraints are relaxed, the optimal cycles do not feature
a recuperator, providing some capital cost savings, with some cycles showing more than three times the
generated power than with this component, making investments in sub-atmospheric components worthwhile.
recovery and power generation in industrial settings. This study considers ORC systems optimized for
maximum power generation using a case study of an exhaust flue-gas stream at a temperature of 380 °C as
the heat source, covering over 30 working fluids and also considering the option of featuring a recuperator.
Systems based on transcritical cycles are found to deliver higher power outputs than subcritical ones, with
optimal evaporation pressures that are 4-5 times the critical pressures of refrigerants and light hydrocarbons,
and 1-2 times those of siloxanes and heavy hydrocarbons. For maximum power production, a recuperator is
necessary for ORC systems with constraints imposed on their evaporation and condensation pressures. This
includes, for example, limiting the minimum condensation pressure to atmospheric pressure to prevent subatmospheric
operation of this component, as is the case when employing heavy hydrocarbon and siloxane
working fluids. For scenarios where such operating constraints are relaxed, the optimal cycles do not feature
a recuperator, providing some capital cost savings, with some cycles showing more than three times the
generated power than with this component, making investments in sub-atmospheric components worthwhile.
Date Issued
2017-07-02
Date Acceptance
2017-04-20
Publisher
ECOS-2017
Copyright Statement
All publications will be available to the public as well as to the authors free of charge.
Source
30th International Conference on Efficiency, Cost, Optimization, Simulation and Environmental Impact of Energy Systems (ECOS 2017)
Publication Status
Published
Start Date
2017-07-02
Finish Date
2017-07-06
Coverage Spatial
San Diego, California