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To recuperate or not to recuperate -To recuperate or not to recuperate -ORC cycles compared to ideal
cyclesPall Valdimarsson
University of Iceland, Reykjavik, IcelandUniversity of Iceland, Reykjavik, Iceland
The performance of real power cycles for heat source in the temperature range from 100C to source in the temperature range from 100C to 300C is studied in this paper.
A reference is made to three ideal power production cycles: Carnot Triangular Triangular Lorenz.
The source fluid flow is 1 kg/s for all calculations
The real cycles are assumed to have infinite heat exchanger area
Pumps and turbines are isentropic The cooling fluid is produced by external
means, without being a parasite of the power means, without being a parasite of the power plant.
The binary cycles studied are: ORC with a single high pressure level ORC with two pressure high levels ORC with two pressure high levels Saturated Kalina cycle Transcritical cycle Single and double flash geothermal power cycles
are included as well A few different working fluids are considered for the ORC A few different working fluids are considered for the ORC
cycles A few different ammonia concentrations for the Kalina cycle.
The results are presented as:
The produced power for these cycles from the same source is then compared and a range of superiority for each cycle presented.
The effect of recuperation on the produced The effect of recuperation on the produced power as well as on the calculated efficiency is shown.
Finally the influence of finite heat exchanger area is analyzed and an estimate of the cooling fluid generation parasitic power made both for air and wet cooling tower system.
Source properties the denominator
Optimistic Carnot
Pessimistic Carnot
Triangular
Lorenz
Lorenz
600600600600
Carnot
100
200
300
400
500
600
100
200
300
400
500
600
100
200
300
400
500
600
100
200
300
400
500
600
Lorenz
Triangular
100150
200250
300
0
50
100
1500
100150
200250
300
0
50
100
1500
100150
200250
300
0
50
100
1500
100150
200250
300
0
50
100
1500
Ideal cycles
ORCs1
5
12
3 4
s2c2
7
c1
6
8
Saturated Isopentane
150200250
Isopentane
50
100
150
50
100
150
200
50
100
150
200
250
R134a
R245fa
100150
200250
300
0
50
100
1500
100150
200250
300
0
50
100
1500
100150
200250
300
0
50
100
1500
Saturated comparison
Recuperated Isopentane
Superheated Isopentane
140
160
Superheated
80
100
120
Recuperated
100 120 140 160 180 200 220 240 260 280 30040
60
Superiority ranges
Saturated
Transcritical Isopentane
250
Superheated
Transcritical
50
100
150
200
250
100150
200250
300
0
50
100
1500
Recuperated
Saturated
Superiority
Double pressure
Kalina4s1
5
12
3
c2
9
12
1110
7
s2
c1
c2
6
8
Kalina 80% ammonia
250250
50
100
150
200
250
50
100
150
200
250
100150
200250
300
0
50
100
1500
100150
200250
300
0
50
100
1500
Kalina compared
42
1
6
c1
c2
5
3
0
Single flash
250
Saturated IsopentaneSingle flash
50
100
150
200
250
100150
200250
300
0
50
100
1500
Sf compared
Source
SinkSink
n-butane
Isopentane
R134a
IP superheat
IP transctitical
Kalina
Source
SinkSink
n-butane
Isopentane
R134a
IP superheat
IP transctitical
Kalina
Dank U wel !!