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Selection and optimization of pure and mixed working fluids for low grade heat utilization using organic Rankine cycles

J. G Andreasen ; Ulrik Larsen (Institutionen för sjöfart och marin teknik) ; Thomas Knudsen ; L. Pierobon ; F. Haglind
Energy (0360-5442). Vol. 73 (2014),
[Artikel, refereegranskad vetenskaplig]

We present a generic methodology for organic Rankine cycle optimization, where the working fluid is included as an optimization parameter, in order to maximize the net power output of the cycle. The method is applied on two optimization cases with hot fluid inlet temperatures at 120°C and 90°C. Pure fluids and mixtures are compared to see how mixed working fluids affect performance and important design parameters. The results indicate that mixed working fluids can increase the net power output of the cycle, while reducing the pressure levels. The maximum net power output is obtained by fluids with a critical temperature close to half of the hot fluid inlet temperature. For some mixtures we find the maximum net power when the temperature glide of condensation matches the temperature increase of the cooling water, while for other mixtures there are large differences between these two parameters. Ethane is a fluid that obtains a large net power increase when used in mixtures. Compared to pure ethane, an optimized ethane/propane mixture attains a 12.9% net power increase when the hot fluid inlet temperature is 120_C and a 11.1% net power increase when the hot fluid inlet temperature is 90°C.



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Denna post skapades 2015-09-15.
CPL Pubid: 222535

 

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Institutioner (Chalmers)

Institutionen för sjöfart och marin teknik

Ämnesområden

Energi
Termisk energiteknik

Chalmers infrastruktur