Abstract

The organic Rankine cycle (ORC) is a popular technology used in waste heat recovery and low-grade heat utilization, which are two important measures to solve the problems brought by the energy crisis. The economic performance of ORC system is an important factor affecting its application and development. Therefore, the economic analysis of ORC is of great significance. In this study, R123 and R245fa, two frequently-used working fluids during the transition period, were selected for calculating and analyzing the economic performance of an ORC used for recovery of waste heat with a low flow rate and medium-low temperature. Five traditional economic indicators, namely total cost, net earnings, payback period, return on investment, levelized energy cost, and present value of total profit in system service life, which is a relatively new indicator, were used to establish the economic analysis model of ORC. The variation effects of evaporation temperature, condensation temperature of working fluid, flue gas inlet temperature, and mass flow rate of flue gas on the above six economic indicators were analyzed. The results show that the optimal evaporation temperature of R123 is 125 °C, the optimal condensation temperature is 33 °C, and the optimal heat source temperature is 217 °C. For R245fa, the optimal evaporation temperature is 122 °C, the optimal condensation temperature is 27 °C, and the optimal heat source temperature is 177 °C. The economic performance of an ORC demonstration project was reported and used for comparison with the estimation and analysis. It was found that the single screw expander has an excellent economy performance, which greatly reduces the proportion of expander cost in the ORC system.

Highlights

  • Energy consumption has greatly contributed to the promotion of human development and progress

  • The upper limit of the evaporation temperature was set to the temperature corresponding to the maximum entropy value on the saturated vapor curve near critical region of working fluid in T-s diagram

  • Considering traditional and classical indicators mainly focus on the present economic performance evaluation, a relatively new indicator, which is called present value of total profit in system service life, is proposed in this paper

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Summary

Introduction

Energy consumption has greatly contributed to the promotion of human development and progress. Yari et al [42] used capital recovery factor (CRF) as the indicator to conduct an exergoeconomic comparison of TLC (trilateral Rankine cycle), ORC and Kalina cycle using a low-grade heat source They found that, the TLC can achieve a higher net output power compared with ORC and Kalina (KCS11 (Kalina cycle system 11)) systems, its product cost is greatly affected by the expander isentropic efficiency. Purchase cost and payback period [45] were used by Varga and Csaba as the indicators to conduct a techno-economic evaluation of waste heat recovery by organic Rankine cycle using pure light hydrocarbons and their mixtures as working fluid in a crude oil refinery.

Thermodynamic
Typical process of an
Economic Indicators and Calculations
Total Cost of ORC System
Present Value of Total Profit in System Service Life
Results and Discussion
Return
Present
Variation of Condensation on Economic
Variation
Thein condensation temperature was
19. Present
22. Payback
26. Demonstration projectofofORC
Working condition parameters demonstrationORC
29. Proportion of equipmentinvestment investment in system with
Conclusions
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