MODERN THERMAL POWER PLANTS

More documents

Recommendations

Info

Copyright Klas Jonshagen Division of Thermal Power Engineering Department of Energy Sciences Lund University Sweden ISBN 978-91-7473-070-8 ISSN 0282-1990 ISRN LUTMDN/TMHP-10/1075-SE Printed in Sweden by E-huset Tryckeri Lund 2010
To Louise
Page 1: MODERN THERMAL POWER PLANTS Aspects
Page 6 and 7: Key words: Combined cycle, CO 2 , c
Page 8 and 9: Metoderna för att minska koldioxid
Page 10 and 11: Paper VI K. Jonshagen, M. Genrup Im
Page 12 and 13: 4.6.1 Dry efficiency ..............
Page 14 and 15: ρ [kg/(m 3 )] Density φ [-] Flang
Page 16 and 17: is higher than it would be if direc
Page 18 and 19: 1.5 Outline of this thesis This the
Page 20 and 21: of two thermodynamic cycles and inc
Page 22 and 23: temperatures of 1400-1500 °C and s
Page 24 and 25: additional evaporators working at l
Page 26 and 27: Figure 3 shows the layout of a trip
Page 31: very low pressure will be beneficia
Page 34 and 35: T-Q diagram in Figure 9. The cycle
Page 36: components should be linked togethe
Page 49: condensational shock does not take
Page 57 and 58:
extracted fluid. A more accurate pa
Page 61 and 62:
5 Post-Combustion Carbon Capture Th
Page 63 and 64:
Equation (37), this results in a sm
Page 65 and 66:
egenerator or stripper. The CO 2 is
Page 67 and 68:
for instance, for enhancing oil rec
Page 69 and 70:
In an attempt to reduce the amount
Page 71 and 72:
If condensing steam, which is extra
Page 73:
MEA carbon capture unit is a dual-p
Page 77 and 78:
educed the pressure ratio will fall
Page 79 and 80:
7 Low Calorific Fuels in CCPPs Reso
Page 81:
7.1 Summary of the results on low c
Page 85 and 86:
9 Summary of papers Paper I K. Jons
Page 87 and 88:
References [1] Le Treut, H., R. Som
Page 89 and 90:
[39] Mimura, T., Shimojo, S., Suda,
Page 93 and 94:
Proceedings of ASME Turbo Expo 2011
Page 95 and 96:
[20] and uses fully dimensionless p
Page 99 and 100:
The dual-pressure chilled ammonia C
Page 101:
[3] Woollatt, G., and Franco, F., 2
Page 106 and 107:
Table 1 Reduction in isentropic exp
Page 108 and 109:
Fig. 1 Schematic figure of the refe
Page 110 and 111:
deaeration is performed in the LP-d
Page 113:
III
Page 116 and 117:
Fig. 1 Schematic figure of the refe
Page 118 and 119:
Table 3 Settings for the CO 2 compr
Page 120 and 121:
Fig. 4 Schematic figure of the sing
Page 122:
Acknowledgment The authors wish to
Page 126:
SCOC-CC Semi-closed oxy-fuel combus
Page 131 and 132:
a given stage loading parameter ψ.
Page 133:
[11] Wennerstrom A. J., 2000, “De
Page 138 and 139:
Mass flow m [kg/s] Pressure p [Pa]
Page 140 and 141:
The inlet pressure drop is simply m
Page 142 and 143:
cannot run on 100% air blown gasifi
Page 144 and 145:
and firing temperature, increase th
Page 146:
[2] Eriksson, P., Genrup, M., Jonsh
Page 150 and 151:
K. Jonshagen, M. Genrup / Energy 35
Page 152 and 153:
Page 154 and 155:
Page 157:
VII
Page 161:
Proceedings of ECOS 2009 Copyright
Page 165:
Proceedings of ECOS 2009 Copyright
show all

MODERN THERMAL POWER PLANTS

Create successful ePaper yourself

Delete template?

Save as template?