This paper presents Aspen Plus (V7.3) simulations of a two-stage organic rankine cycle concept with
internal heat recovery. The proposed system is compared to state-of-the-art processes with four different
working fluids distinguished by the slope of the saturated vapor curve in the corresponding Tes-diagram.
The heat source is defined as exhaust gas (490 C and 1 bar) from an internal combustion engine,
which is fired with biogas from a biomass digestion plant. In a first consideration the exhaust gas outlet is
constrained to 130 C to stay above the acid dew point (study 1). In a second study the pinch point of the
exhaust gas heat exchanger is set to 10 K. For wet and isentropic fluids the thermodynamic efficiencies of
the two-stage cycle exceed the corresponding values of reference processes by up to 2.25%, while the
recuperator design benefits dry fluids compared to the two-stage concept.
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This paper presents Aspen Plus (V7.3) simulations of a two-stage organic rankine cycle concept with
internal heat recovery. The proposed system is compared to state-of-the-art processes with four different
working fluids distinguished by the slope of the saturated vapor curve in the corresponding Tes-diagram.
The heat source is defined as exhaust gas (490 C and 1 bar) from an internal combustion engine,
which is fired with biogas from a biomass digestion plant. In a first consideration the e...
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