Abstract

An optimal load-tracking operation strategy for a grid-connected tubular solid oxide fuel cell (SOFC) is studied based on the steady-state analysis of the system thermodynamics and electrochemistry. Control of the SOFC is achieved by a two-level hierarchical control system. In the upper level, optimal setpoints of output voltage and the current corresponding to unit load demand is obtained through a nonlinear optimization by minimizing the SOFC’s internal power waste. In the lower level, a combined L1-MPC control strategy is designed to achieve fast set point tracking under system nonlinearities, while maintaining a constant fuel utilization factor. To prevent fuel starvation during the transient state resulting from the output power surging, a fuel flow constraint is imposed on the MPC with direct electron balance calculation. The proposed control schemes are testified on the grid-connected SOFC model.

Highlights

  • The globally exploding capacity of renewable energy during the past decade makes a remarkable contribution to the conservation of fossil-fuel energy resources and an increasing number of distributed generations (DGs)

  • This paper proposes a procedure to design a hierarchical control strategy for optimal power tracking operation of grid-connected solid oxide fuel cell (SOFC)

  • The control strategy consists of a set point scheduler in the upper level and a SOFC controller working together with voltage source invertors (VSI) devices in the lower level

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Summary

Introduction

The globally exploding capacity of renewable energy during the past decade makes a remarkable contribution to the conservation of fossil-fuel energy resources and an increasing number of distributed generations (DGs). For grid-connected SOFCs, its output power should track the unit load demand from the dispatching system. With this operation mode, the control problem considered for a grid-connected SOFC lies in: 2. Set points of output voltage and current corresponding to unit load demand are obtained through solving a nonlinear optimization problem for the maximum efficiency of SOFC in steady-state operation. A L1-MPC tracking controller with a combination of MIMO output feedback L1AC and MPC is put forward to steer the output variables to their optimal set points, handling all of the nonlinearities and constraints.

Review of SOFC Structures and Models
Steady-State Analysis
Thermal Balance
The Electrochemical Relations
Control System Design
Set Point Scheduler
Combined L1-MPC Controller
Fuel Starvation Protection
Simulation Results
Conclusions

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