G. Angelino et C. Invernizzi, PROSPECTS FOR REAL-GAS REVERSED BRAYTON CYCLE HEAT-PUMPS, International journal of refrigeration, 18(4), 1995, pp. 272-280
Ideal-gas reversed Brayton cycles are shown to be intrinsically ineffi
cient owing to the high level of turbomachinery losses. An appropriate
selection of the cycle operating parameters leading to the location o
f the expansion process in the vicinity of the critical point, where s
pecific volumes and turbine works are small, allows the design of rege
nerated gas cycles with efficiencies similar to those of conventional
vapour compression cycles, at least in the generation of high-temperat
ure heat. A number of working fluids are presented (both pure substanc
es and mixtures) yielding a good conversion efficiency at various sour
ce/sink temperatures. Basic optimization rules are given for fluids of
different molecular structure. Fluids with a simple molecule (Xe, CO2
etc.) tend to produce heat at very high temperatures and with an exce
ssive temperature change: compression staging is effective in correcti
ng this trend. Moderate pressure ratios (2 to 4) are sufficient to yie
ld a good cycle efficiency; however, operating pressures are intrinsic
ally high, since a minimum pressure around p(cr) is in general request
ed. The main features of the real-gas heat pump cycle can be summarize
d as the large power density, the ability to operate at high temperatu
re with a small pressure ratio, and non-isothermal heat generation. Wh
enever such characteristics are of particular value, as, for example,
in the production of heat for a long-distance conveyance, as needed fo
r urban heating systems or for industrial heat networks, the real-gas
reversed Brayton cycle should be examined as a possible alternative to
conventional heat pump cycles.