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Working fluid mass flow rate [kg/s] ORC net electric power [W] ➮ Phase‐change and saturation degree affect 300 the numerical simulation leading to 200 unsteadiness during the integration process of the balance equations under phase‐ 100 change conditions. Similar to Quoilin et al. Power (Single ramp) 0.03 Power (Double ramp) 0.02 Mass flow rate (Single ramp) Mass flow rate (Double ramp) 0.01 ORC-System Analysis and Optimization: Unsteady-State Analysis (1/2) ORC system driven by residential user electricity demand The dynamic behavior of the ORC is evaluated by an increased request of the electrical power demand. ➮ The ORC system response to the double ramp is clearly faster; ➮ Similarities on signal response behavior can be observed. ➮ In the double ramp case, the final steady 700 0.07 0.06 0.05 0.04 state condition is reached in a shorter period of time, because the system is already running from a previous quasi‐ stationary condition. 600 500 400 ➮ Different time‐step solver and simulation error control required. 0 10 20 30 40 50 Quoilin, S., 2011, “Sustainable Energy Conversion Through the Use of Organic Rankine Cycles for Waste Heat Recovery and Solar Applications”, PhD Thesis in Applied Sciences, University of Liège (Belgium), October 2011. 0 0.00 Time [min]PDF Image | Application of Micro CHP ORC Heat Recovery
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