This paper presents a new heat upgrading method that utilizes waste heat from nuclear reactors for thermochemical water splitting with a copper-chlorine (Cu–Cl) cycle. Through combined power, hydrogen, and oxygen generation, the exergy efficiency of a power plant can be significantly augmented. The heat rejected to the environment for moderator cooling, a relatively small amount of low pressure superheated steam and a small fraction of generated power, are extracted from the nuclear reactor and used to drive a Cu–Cl hydrogen plant. More specifically, the moderator heat transfer at 80°C is used as a source to a newly proposed vapor compression heat pump with a cascaded cycle, operating with retrograde fluids of cyclohexane (bottoming cycle) and biphenyl (topping supercritical cycle). Additionally, the heat pump uses as input the heat recovered from within the Cu–Cl cycle itself. This heat is recovered at two levels: 80130°C and 250485°C. This heat input is upgraded up to 600°C by work-to-heat conversion and then used to supply the endothermic water splitting process. The extracted steam is fed into the Cu–Cl cycle and split into hydrogen and oxygen as overall products. Electricity is partly used for an electrochemical process within the Cu–Cl cycle, and also partly for the heat pump compressors. This paper analyses the performance of the proposed heat pump and reports the exergy efficiency of the overall system. The proposed system is about 4% more efficient than generating electricity alone from the nuclear reactor.

1.
Orhan
,
M. F.
,
Dincer
,
I.
, and
Rosen
,
M. A.
, 2008, “
Energy and Exergy Assessments of a Hydrogen Production Step of a Copper-Chloride Thermochemical Water Splitting Cycle Driven by Nuclear-Based Heat
,”
Int. J. Hydrogen Energy
0360-3199,
33
, pp.
6456
6466
.
2.
Orhan
,
M. F.
,
Dincer
,
I.
, and
Rosen
,
M. A.
, 2008, “
Thermodynamic Analysis of the Copper Production Step in a Copper-Chlorine Cycle for Hydrogen Production
,”
Thermochim. Acta
0040-6031,
480
, pp.
22
29
.
3.
Naterer
,
G. F.
, 2008, “
Second Law Viability of Upgrading Industrial Waste Heat for Thermochemical Hydrogen Production
,”
Int. J. Hydrogen Energy
0360-3199,
33
, pp.
6037
6045
.
4.
Abanades
,
S.
,
Charvin
,
P.
,
Flamant
,
G.
, and
Neveu
,
P.
, 2006, “
Screening of Water-Splitting Thermochemical Cycles Potentially Attractive for Hydrogen Production by Concentrated Solar Energy
,”
Energy
0360-5442,
31
, pp.
2805
2822
.
5.
Lewis
,
M. A.
,
Serban
,
M.
, and
Basco
,
J. K.
, 2003, “
Hydrogen Production at <550°C
Using a Low Temperature Thermochemical Cycle,”
Proceedings of the Nuclear Production of Hydrogen: Second Information Exchange Meeting
, Argonne, IL, Oct. 2–3, pp.
145
156
.
6.
Granovskii
,
M.
,
Dincer
,
I.
,
Rosen
,
M. A.
, and
Pioro
,
I.
, 2008, “
Thermodynamic Analysis of the Use a Chemical Heat Pump to Link a Supercritical Water-Cooled Nuclear Reactor and a Thermochemical Water-Splitting Cycle for Hydrogen Production
,”
Int. J. Electr. Power Energy Syst.
0142-0615,
2
, pp.
756
767
.
7.
Granovskii
,
M.
,
Dincer
,
I.
,
Rosen
,
M. A.
, and
Pioro
,
I.
, 2008, “
Performance Assessment of a Combined System to Link a Supercritical Water-Cooled Nuclear Reactor and a Thermochemical Water Splitting Cycle For Hydrogen Production
,”
Energy Convers. Manage.
0196-8904,
49
, pp.
1873
1881
.
8.
Matsumura
,
Y.
,
Nakahara
,
Y.
,
Morita
,
H.
, and
Yoshida
,
K.
, 1995, “
A Chemical Heat Pump Using Hydration of MgO Particles in Three-Phase Reactor
,”
Int. J. Energy Res.
0363-907X,
19
, pp.
263
273
.
9.
Kato
,
Y.
, and
Yoshizawa
,
Y.
, 2001, “
Application of a Chemical Heat Pump to a Cogeneration System
,”
Int. J. Energy Res.
0363-907X,
25
, pp.
129
140
.
10.
Kim
,
T. G.
,
Yeo
,
Y. K.
, and
Song
,
H. K.
, 1992, “
Chemical Heat Pump Based on Dehydrogenation and Hydrogenation of I-Propanol and Acetone
,”
Int. J. Energy Res.
0363-907X,
16
, pp.
897
916
.
11.
Aristov
,
Y. I.
,
Parmon
,
V. N.
,
Cacciola
,
G.
, and
Girodano
,
N.
, 1993, “
High-Temperature Chemical Heat Pump Based on Reversible Catalytic Reactions of Cyclohexane-Dehydrogenation/Benzene-Hydrogenation: Comparison of the Potentialities of Different Flow Diagrams
,”
Int. J. Energy Res.
0363-907X,
17
, pp.
293
303
.
12.
Tahat
,
M. A.
,
Babushaq
,
R. F.
,
O’Callaghan
,
P. W.
, and
Probert
,
S. D.
, 1995, “
Integrated Thermochemical Heat-Pump/Energy-Store
,”
Int. J. Energy Res.
0363-907X,
19
, pp.
603
613
.
13.
Altinişik
,
K.
, and
Veziroğlu
,
T. N.
, 1991, “
Metal Hydride Heat Pumps
,”
Int. J. Energy Res.
0363-907X,
15
, pp.
549
560
.
14.
Lide
,
D. R.
, 2006,
CRC Handbook of Chemistry and Physics
, 87th ed.,
CRC
,
Boca Raton, FL
.
15.
Rowley
,
R. L.
,
Wilding
,
W. V.
,
Oscarson
,
J. L.
,
Yang
,
Y.
,
Zundeland
,
N. A.
,
Daubert
,
T. P.
, and
Danner
,
R. P.
, 2004,
DIPPR Data Compilation of Pure Chemical Properties
,
Taylor & Francis
,
New York
.
16.
Colonna
,
P.
, and
van der Stelt
,
T. P.
, 2004, “
FluidProp: A Program for the Estimation of Thermo Physical Properties Of Fluids
,” Energy Technology Section, Delft University of Technology, The Netherlands, www.FluidProp.comwww.FluidProp.com
17.
Stryjek
,
R.
, and
Vera
,
J. H.
, 1986, “
PRSV, An Improved Peng-Robinson Equation of State for Pure Compounds and Mixtures
,”
Can. J. Chem. Eng.
0008-4034,
64
, pp.
323
333
.
18.
Angelino
,
G.
, and
Invernizzi
,
C.
, 1993, “
Cyclic Methylsiloxanes as Working Fluids for Space Power Cycles
,”
ASME J. Sol. Energy Eng.
0199-6231,
115
, pp.
130
137
.
19.
Calderazzi
,
L.
, and
di Paliano
,
P. C.
, 1997, “
Thermal Stability of R-134a, R-141b, R-1311, R-7146, R-125 Associated With Stainless Steel as a Containing Material
,”
Int. J. Refrig.
0140-7007,
20
, pp.
381
389
.
20.
Zamfirescu
,
C.
, and
Dincer
,
I.
, 2008, “
Thermodynamic Analysis of a Novel Ammonia-Water Trilateral Rankine Cycle
,”
Thermochim. Acta
0040-6031,
477
, pp.
7
15
.
21.
Armstrong
,
A.
,
Haseen
,
F.
,
Marnoch
,
I.
,
Weston
,
J.
,
Naterer
,
G. F.
,
Lu
,
L.
,
Rosen
,
M. A.
, and
Dincer
,
I.
, 2007, “
Thermodynamic Optimization and Control of a Marnoch Thermal Energy Conversion Device
,”
21st Canadian Congress of Applied Mechanics
, Toronto, Ontario, Jun. 3–7.
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