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T.W.Scholten, C. de Persis, P. Tesi

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Presentation on theme: "T.W.Scholten, C. de Persis, P. Tesi"— Presentation transcript:

1 T.W.Scholten, C. de Persis, P. Tesi
Modeling and Control of Heat Networks with Storage: the Single-Producer Multiple-Consumer Case T.W.Scholten, C. de Persis, P. Tesi

2 Outline District heating Problem description Setup Control goal Flows
Introduction District heating Problem description Model Setup Control goal Control Flows Heat injection Case study Conclusion Conclusions Future work

3 Introduction Model Control conclusion
District heating Introduction Model Control conclusion

4 Introduction Model Control conclusion
Examples Waste incinerators Geothermal energy Industrial users Storage tank Domestic users Greenhouses Introduction Model Control conclusion

5 Introduction Model Control conclusion
Problem description Balance demand and supply Options: Control production Include storage Control demand Dynamic pricing Do optimization over time horizon: Design a controller such that the stored energy converges to the desired setpoints Introduction Model Control conclusion

6 Introduction Model Control conclusion
Setup Heat exchangers Stratified storage Introduction Model Control conclusion

7 Introduction Model Control conclusion
Volume dynamics Hot storage: Cold storage: Constraints both layers: where Introduction Model Control conclusion

8 Introduction Model Control conclusion
Temperature dynamics Introduction Model Control conclusion

9 Introduction Model Control conclusion
Input and disturbance Let: where Introduction Model Control conclusion

10 Introduction Model Control conclusion
Control goal Find controllers and such that: under disturbance Introduction Model Control conclusion

11 Introduction Model Control conclusion
Overall Model Introduction Model Control conclusion

12 Introduction Model Control conclusion
Overall Model Linear if and are constant and exists. Introduction Model Control conclusion

13 Introduction Model Control conclusion
Controller design 1. Design flow controller such that: 2. Design controller for the heat injection assuming 3. Proof boundedness and stability without assuming Introduction Model Control conclusion

14 Introduction Model Control conclusion
1. Flow controller Flow controller: Volume dynamics: exists Recall where Introduction Model Control conclusion

15 Introduction Model Control conclusion
2. Heat injection Let Controller design (Internal model) Always exist! Introduction Model Control conclusion

16 Introduction Model Control conclusion
3. Main result The solutions of system in closed loop with controllers and are bounded and Introduction Model Control conclusion

17 Introduction Model Control conclusion
Remark Where No! Need to know and a priori? IM is robust against parameter uncertainties Introduction Model Control conclusion

18 Case study: time varying demand
Store to 900m³ Drain to 100m³ Saturation applied Setpoint 85°C Extra injection Low injection rate Not in the analysis Introduction Model Control conclusion

19 Case study: time varying demand
Introduction Model Control conclusion

20 Case study: time varying demand; heat exchanger
Introduction Model Control conclusion

21 Introduction Model Control conclusion
Conclusions Model derived and control problem defined Able to reject time varying disturbances Global asymptotic stability proven Some remarks: Flow of the consumer is set constant Simple model: easy to use, but wat about accuracy? What about the time delays? Introduction Model Control conclusion

22 Introduction Model Control conclusion
Future work Extend to multiple consumers and multiple storages Consider optimal production Investigate possibilities of cascading Delays Dissipation Include dynamic pricing Introduction Model Control conclusion

23 Introduction Model Control conclusion
Thank you for your attention! Questions? Introduction Model Control conclusion


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