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L. Guillaumea, A. Legrosa, V. Lemorta
Introduce your company logo here THERMO-ECONOMIC OPTIMIZATION OF ORAGNIC RANKINE CYCLE SYSTEMS FOR WASTE HEAT RECOVERY FROM EXHAUST AND RECIRCULATED GASES OF HEAVY DUTY TRUCKS L. Guillaumea, A. Legrosa, V. Lemorta aDepartment of A&M, Thermodynamics laboratory, University of Liege, Belgium
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Introduction ORC waste heat recovery Design:
Fuel consumption and CO2 emissions Design: Essential part of the design process Library of steady-state models Numerous steady-state models of different candidate ORCs Design in three steps Selection of the design conditions Design (Optimization) Evaluation of the off design performance Thermodynamic vs thermo-economic optimization Cost relations for all components 3rd EORC workshop, Belfast, 2016
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Introduction Context 3rd EORC workshop, Belfast, 2016
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Heat sources and heat sink
Temperature Capacity flow rate Exhaust gases mid to high high EGR gases low Charge Air low to mid Coolant Oil 3rd EORC workshop, Belfast, 2016
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Expansion machines and working fluids
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Topologies 3rd EORC workshop, Belfast, 2016
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Models of components Pump Model Expansion machine Model:
Semi empirical model Fixed efficiencies Expansion machine Model: semi empirical model Heat exchanger on the hot side Tube and tube Shell and tube Plates Heat exchanger on the cold side Tube and tube Shell and tube Plates 3rd EORC workshop, Belfast, 2016
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Validation of the models Heat exchangers
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Constraints and optimization variables
Economic constraints Evaporating pressure Mass of the heat exchangers Pinch of the heat exchangers Constraints for WHR Built-in volume ratio Temperature of the EGR Heat rejection capacity Technical constraints Expander speed Limited speed Overheating degree Limited inlet temperature Gas mass fraction 3rd EORC workshop, Belfast, 2016
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Selection of the design conditions
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Validation of the models Expansion machines
Simulation models for the volumetric expanders: Calibration of the models on existing machines using experimental data. References Scaling of the parameters to adapt the models to the machine being currently designed (efficiencies). Scaling relations applied to the model parameters Model calibrated on a existing machine (reference) Model of the machine being designed for the truck application 3rd EORC workshop, Belfast, 2016
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Design Additional constraints
Expander technology Scroll Screw Piston Vane Rotational speed [RPM] <10000 <25000 <4000 Max. Inlet temperature [°C] 250 [2] 490 [3] >500 [4] <165 Built-in volume ratio [-] 4-5 6-14 2-4.5 Pressure ratio [-] 25 [5] 50 [6] Same as in ICE 3rd EORC workshop, Belfast, 2016
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Design Costs relations
Example for a piston expander Assumptions Swashplate 5 cylinders Constant L/D ratio 3rd EORC workshop, Belfast, 2016
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Design Thermo-economic optimization
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Design Thermo-economic optimization
Screw expander, topology 5 and ethanol Net power output: 10.9 kW Evaporating pressure: 19 bar Condensing pressure: 1 bar Rotational speed: 25 krpm (6.25 cm³) Overheating degree: 48 °C Built-in volume ratio: 6 3rd EORC workshop, Belfast, 2016
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Off-Design Optimization
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Conclusion and perspectives
Help ORC designers to best select the expansion machine and working fluid for truck applications. Preliminary design Performance is not the only criteria Decision array to select the components Results are not general Future work Mixtures water/ethanol Simulation of driving cycles 3rd EORC workshop, Belfast, 2016
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Questions Thank you 3rd EORC workshop, Belfast, 2016
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Bibliography Technico-economicsurveyofOrganicRankineCycle(ORC) systems S. Quoilin, M.VanDenBroek, S. Declaye, PierreDewallef, V.Lemort. Experimental study and modeling of an Organic Rankine Cycle using scroll expander, S. Quoilin, V. Lemort, J. Lebrun. Multi-objective optimization of organic Rankine cycles for waste heat recovery: Application in an offshore platform L. Pierobon, T. Van Nguyen, U. Larsen, F. Haglind, Brian Elmegaard. European comission, Energy 2020, en-ergy2020/energy2020.htm 2013. 3rd EORC workshop, Belfast, 2016
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Appendix Limit on the EGR temperature
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