2012
DOI: 10.3390/en5125111
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Linear Active Disturbance Rejection Control of Waste Heat Recovery Systems with Organic Rankine Cycles

Abstract: Abstract:In this paper, a linear active disturbance rejection controller is proposed for a waste heat recovery system using an organic Rankine cycle process, whose model is obtained by applying the system identification technique. The disturbances imposed on the waste heat recovery system are estimated through an extended linear state observer and then compensated by a linear feedback control strategy. The proposed control strategy is applied to a 100 kW waste heat recovery system to handle the power demand va… Show more

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Cited by 28 publications
(26 citation statements)
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“…Similarly, disturbance rejection scenarios were investigated associated with hot gas stream velocity variation and throttle valve dynamics. Zhang et al [99] extended the previous work by developing an extended observer that aims to provide accurate state estimates for the system.…”
Section: Control Approachesmentioning
confidence: 99%
“…Similarly, disturbance rejection scenarios were investigated associated with hot gas stream velocity variation and throttle valve dynamics. Zhang et al [99] extended the previous work by developing an extended observer that aims to provide accurate state estimates for the system.…”
Section: Control Approachesmentioning
confidence: 99%
“…PPTD between the diesel engine exhaust and zeotropic mixture R416A is set to 10 K. The PPTD occurrence position is first assumed to appear at the inlet of the evaporator of the zeotropic mixture side (State Point 3 in Figure 2), which indicates that the difference between T exh_out and T 3 is 10 K. T 4 is the temperature of the zeotropic mixture R416A at the outlet of the evaporator of the zeotropic mixture side, T exh_in can be measured during the engine test, and T 4 can be determined when the evaporating pressure and degree of superheat are certain (in this paper, "certain" means "be held constant", the same as below), such that the difference between T exh_in and T 4 can be calculated. T exh_e can be calculated using Equation (1), where T b is the bubble temperature of the zeotropic mixture R416A in the saturated liquid state, such that the difference between T exh_e and T b can be calculated. The occurrence position of PPTD between diesel engine exhaust and zeotropic mixture R416A can be determined by comparing the values of the above-mentioned three temperature difference: The evaporator and condenser are mainly responsible for the exergy destruction rate ( I  ) of the ORC waste heat recovery system; exergy destruction rate is mainly caused by the temperature difference of the heat transfer between the hot and cold fluids.…”
Section: Description and Modeling Of The Orc Waste Heat Recovery Systemmentioning
confidence: 99%
“…The organic Rankine cycle (ORC) system is an effective and promising method for converting waste heat into useful work, and has been widely studied and applied in many domains [1][2][3][4][5]. Li et al [6] analyzed the performance of ORC in recovering low-temperature waste heat from flue gas.…”
Section: Introductionmentioning
confidence: 99%
“…The organic Rankine cycle (ORC) system is considered effective in converting low-grade waste heat to useful work and has recently been widely studied and applied in many domains [4][5][6][7]. Wang et al [8] established an off-design model of an ORC system driven by solar energy.…”
Section: Introductionmentioning
confidence: 99%