An experimental and thermodynamic analysis was conducted to explore the match in operating conditions for the heat extraction of supercritical CO 2 and the CO 2 transcritical organic Rankine cycle (CTORC). The results revealed that in the optimal conditions of the experiment, the difference between the pseudocritical temperature and the inlet temperature (ΔT pc − in ) was <10 K and T b /T pc (ratio of the bulk temperature to the pseudocritical temperature) was ≤1 (ideal scenario: T b /T pc = 1). Furthermore, the heat transfer and fluid flow of CO 2 as well as the CTORC system performance at the optimal T b /T pc could be simultaneously improved with respect to those at ΔT pc − in < 10 K.The peak values of system efficiency for the inlet temperature of the expander of 100 C and 150 C were 5.1% at 12.5 MPa and 8.0% at 17 MPa, with the corresponding T b /T pc being 1.24 (T pc of 55.9 C) and 1.45 (T pc of 70 C), respectively. Consequently, to simultaneously improve the heat transfer, fluid flow and system efficiency, T pc of the supercritical CO 2 in the CTORC should be sufficiently high to approach half the inlet temperature of the expander for obtaining an optimal T b /T pc at a low condensing temperature.
K E Y W O R D Sbuoyancy, enhanced geothermal system, heat transfer, pressure drop, supercritical CO 2 , thermodynamic analysis, transcritical organic Rankine cycle