Featured Project

Integrated SOFC/GT System

World-Class Power Generation Efficiency

Solid Oxide Fuel Cell/ Gas Turbine (SOFC/GT) hybrid systems have the potential for world-class fuel to electrical conversion efficiencies. Czero has partnered with Nexceris and Brayton Energy to develop the next generation SOFC/GT Hybrid Power Generation Pilot System which is funded in part through the United States’ Department of Energy’s ARPA-E INTEGRATE Phase II program.

Nexceris is the prime contractor and leading the development of a novel planar SOFC chemistry and overall stack design, Brayton Energy is leading the turbomachinery and combustor system development, while Czero is leading the overall system architecture design, mechanical design, controls development, construction, and testing at Czero’s facility. This project was awarded in 2020 and will last through the end of 2024.

Solid Oxide Fuel Cells (SOFCs) electrochemically convert fuel (including hydrocarbons through Steam Methane Reforming (SMR) and Water Gas Shift (WGS) reactions) directly into electricity at efficiencies approaching 60%. A limiting factor in the efficiency of stand-alone SOFCs is the rapid dilution of the fuel stream with electrochemically generated H2O and non-participating constituents from the SMR and WGS reactions. Traditionally this dilution is addressed by burning the anode tailgas to provide heat to support the SOFCs operation, though more dilute fuel is produced than is needed to support the SOFCs thermal losses.

The SOFC/GT architecture (shown below) addresses this deficiency by integrating an SOFC into the hot pressurized path of a Brayton cycle gas turbine. With this configuration the gas turbine’s combustor oxidizes the dilute anode taigas which is expanded through the turbine. The turbine produces enough power to both drive the compressor supplying fresh air (oxidant) to the SOFC and drive a high-speed generator which produces additional electricity (~20% of the system power). While a typical recuperated microturbine has an efficiency on the order of 20-30%, by tightly thermally integrating the SOFC and GT, and operating the SOFC pressurized, the hybrid SOFC/GT system can exceed 70% fuel to electrical conversion efficiency. The overall system efficiency can further be increased by adding a Combined Heat and Power (CHP) cogeneration system.

SOFC/GT System Architecture
SOFC/GT System Architecture

    Quick pilot system facts:

    • 70%+ LHV efficiency
    • 50 kWe electrical power output
    • Natural gas fueled
    • Pressurized operation
    • High-temperature anode recirculation
    • Partial on-anode reforming
    • Low NOx/ dilute combustion
    • Operating temperatures:
      • SOFC: 850°C
      • Turbine: 930°C
    • Turbine speed: 90,000 rpm


    Project team:

    • Nexceris: Prime contractor/PI and SOFC development
    • Czero: System architecture development, dynamic analysis, mechanical design, subsystem design, controls development, fabrication, and testing
    • Brayton: Turbomachinery development

    SOFC/GT Demonstration System at Czero
    SOFC/GT Demonstration System at Czero

    SOFC Reactions
    SOFC Reactions
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    Nexceris logo

    Czero logo

    Brayton Energy logo
    ARPA-E logo
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    Process Design and System Analysis

    SOFC/GT systems are highly complex and interdependent systems. While multiple groups have researched and built various SOFC/GT architectures over the last few decades, there is no consensus on the optimal system configuration. At the project’s onset ARPA-E provided guidance in terms of power level (100 kWe), efficiency target (>70%), fuel (natural gas), and that the SOFC should be integrated with a GT in a pressurized configuration. Beyond this general guidance the project team was responsible for determining how to achieve these objectives.

    To determine the optimal SOFC/GT system design Czero began with our standard approach of developing a high-fidelity physics-based dynamic model of the system. This dynamic plant model was built in MATLAB Simulink using an internally developed block set and featured tracking of nine individual species, real gas properties (NIST REFPROP), mixture modeling, compressible flow dynamics, equilibrium-based chemistry, discretized electrochemical SOFC modeling, and turbomachinery among various other capabilities. This dynamic model was first validated against experimental SOFC and GT data, and then used to explore and optimize the system architecture. Even though the model is highly complex (featuring over 800 states), the model coding is well conditioned enabling average simulation times much faster than real-time. In addition to determining and optimizing the system configuration, the dynamic system model was heavily exercised through a range of startup, shutdown, and failure scenarios (e.g. loss of electrical load on the turbine which could cause rapid over-speeding/destruction of the turbomachinery). This step is very important for complex systems such as the SOFC/GT architecture as it enabled mitigation strategies to be integrated into the system architecture at an early stage, such as a bleed valve on the compressor outlet to address the aforementioned lost electrical load failure scenario.

    In parallel to the dynamic system modeling efforts, Czero developed a detailed Piping and Instrumentation Diagram (P&ID) of the system. The P&ID, along with the system requirement document, serve as key elements detailing the proposed system design ensuring it is well understood and agreed upon between the various internal and external team members.

    A critical step in the system design process which minimizes risk of harm to personnel and equipment are detailed safety reviews. This is especially important for prototypes as potentially dangerous as the SOFC/GT system which operates at high temperatures (850-930°C), pressurized, with high-speed turbomachinery (90,000 rpm), is filled with hazardous gasses (CH4, H2, CO, CO2), and produces high-current DC power (>300 A). One of the more important safety review processes is the Process Hazards Analysis and Hazards and Operability Study (PHA-HazOp). This is a structured approach for evaluating the potential hazards and failure mechanisms of a given system design which Czero frequently leads clients through. In a PHA-HazOp the P&ID is meticulously reviewed, failure mechanisms identified, and mitigating equipment and/or processes determined and incorporated into the system’s design and controls strategy.

    MATLAB Simulink based Dynamic System Model
    MATLAB Simulink based Dynamic System Model

    Example Reforming Equilibrium vs Temperature
    Example Reforming Equilibrium vs Temperature

    PHA-HazOp Matrix
    PHA-HazOp Matrix
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    Mechanical Design

    A major portion of the INTEGRATE Phase II project was the component and system level mechanical design, as well as the overall system integration and Balance of Plant (BOP). One of the core components designed by Czero during this project was the high-temperature (800°C) Alloy 800H pressure vessel which holds the SOFC stacks. This vessel was initially designed by Czero in accordance with ASME BPVC Section VIII, Div 1. A specialized pressure vessel shop was then engaged to review the design, collaborate on design refinements, and then fabricate and certify the vessel. Before being delivered to Czero the vessel underwent post weld heat treatment (PWHT), inspection, and hydro testing.

    As part of the design process, Czero produced manufacturing prints of all manufactured components including full GD&T in accordance with the ASME Y14.5 standard. Czero always strives to right-size the mechanical design and design documentation work for a given project to maximize client value. For this project, it was known that this version of the demonstration system would only be produced once. As such, while the full system was largely designed within CAD, a number of the minor components were fabricated, and field fit by Czero personnel to avoid the expense incurred through full design prints and external fabrication. However, if the intent had been to produce several of these systems, a full Technical Data Package (TDP) including assembly instruction and operation/maintenance manuals would have been created, providing the client with all the design information required to reproduce/operate the system on their own.

    On complex projects such as this, Czero follows an analysis lead design approach to ensure components function safety and as intended the first time. In addition to dynamic system modeling, Czero engineers heavily leverage FEA and CFD to support the mechanical design process. Rapid iteration of the design through FEA on less complex elements is performed by design engineers directly within SolidWorks (Czero’s standard CAD package), while more complex analysis is performed in ANSYS or specialized software like Bentley AutoPIPE. Czero has the full ANSYS suite enabling complex evaluations including coupled transient thermo-structural analysis and CFD (Fluent and CFX). One area ANSYS was used heavily in this project was to evaluate transient thermal stresses within the pressure vessel as the vessel was externally heated by a series of resistive heating elements. CFD was also used extensively in this project to evaluate items such as flow distribution between the stacks, flow characteristics of the internally designed packed bed reformer, and convective/radiative heat transfer within the vessel. For this application Czero utilized STAR-CCM+ for the CFD analysis.

    A unique aspect of working in high-temperature applications is the relative uncertainty of how materials will respond under the design conditions. This was echoed by both the high-temperature materials SME that Czero used on this project who advocated that most materials should be tested/verified in-house, as well as, by various vendors of high-temperature products who were either uncertain of their product’s performance under these conditions, or whose products failed during Czero’s internal testing even though they were rated for the design conditions.

    To this end Czero used an in-house 1200°C test furnace to evaluate materials and processes before implementing them in the system. The most common way a material failed was through corrosion. Even when the corrosion was at an acceptable level for the component, in multiple cases spallation of the oxide layer during thermal cycling would have been highly detrimental to components within the system. Another failure mechanism which occurred multiple times, even with the vendors stating a given material was acceptable for these conditions, was ‘glassing over’ of ceramic materials which left them highly brittle and unsuitable for the intended application. Other evaluations which were performed in the test furnace included testing materials’ electrical conductivity at operating temperature and exploring sealing materials under pressure at the operating conditions. All these material related issues were addressed in the final machinal design, but they highlight the importance of thorough testing during development when addressing these issues is much faster/cheaper/safer than discovering the failures after the system has been built.


      800°C at 2 bar Alloy 800H Pressure Vessel designed by Czero which contains the SOFC Stacks
      800°C at 2 bar Alloy 800H Pressure Vessel designed by Czero which contains the SOFC Stacks

      Interior of the SOFC Pressure Vessel
      Interior of the SOFC Pressure Vessel

      CFD and FEA used to support the design of various subsystems
      CFD and FEA used to support the design of various subsystems

      Nexceris' Planar SOFC Stacks
      Nexceris' Planar SOFC Stacks
      High-Temperature Material Testing at Czero
      High-Temperature Material Testing at Czero

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      Control System Development

      How a system is controlled is a critical aspect of many projects, though too often it is treated as an after-thought. For complex projects such as the INTEGRATE system, it is essential for Czero’s controls group to be closely involved from the project’s onset to ensure a successful project outcome. Not only does this close collaboration ensure the engineers generating the control system develop an intuitive understand of how best to control the system, but there are often multiple changes early in the system’s design made from a controls perspective to improve system robustness and controllability.

      For this project a high-performance Speedgoat platform was selected to serve as the Supervisory Control and Data Acquisition (SCADA) system. Not only is the Speedgoat real-time platform highly capable and modular/expandable, but it also features support for the MATLAB/Simulink environment (comparable to dSPACE, ETAS, MotoHawk, and NI Veristand, all which Czero has used in the past). However in the case of Speedgoat, the MATLAB/Simulink support is native and tightly integrated as Mathwork’s preferred real-time hardware platform. With Speedgoat the entire controls system could be developed in Simulink and then compiled and deployed directly on the real-time target. A key advantage of this workflow for the INTEGRATE program is that full controls code developed in Simulink could be co-simulated with the dynamic plant model (also developed in Simulink) in support of control system development and validation efforts. This process is generally referred to as either Model-in-the-Loop (MIL) or Software-in-the-Loop (SIL), depending on which definitions one follows.

      SIL testing was heavily leveraged during the INTEGRATE program due to the complexities involved with controlling the SOFC/GT system. Control complexities originated not only from the close coupling and interaction of both the SOFC and GT, but also the relatively narrow band of acceptable operating regimes where even small perturbations in temperature, pressure, speed, or flow composition could damage or destroy the very expensive hardware. Furthermore, a hard shutdown (e.g. from an e-stop) could just as easily damage or destroy the system meaning that the control system needed to work well from the onset and controls development work couldn’t realistically be performed directly on the SOFC/GT hardware. As such, SIL testing was used not only to develop and validate controls during normal system operation, but importantly also for startup and shutdown transients as well as fault injection (such a loss of the electrical load on the GT’s generator which would cause a rapid overspeed/destruction of the turbomachinery unless otherwise mitigated).

      One example of a failure mechanism identified during early SIL testing occurred when an inert N2 purge was added to the SOFC fuel stream during shutdown to prevent O2 ingress/degradation of the hot catalyst. While this process may initially seem innocuous, given the large amount of fuel being recirculated in the SOFC, the N2 displaced much of this fuel causing a large increase of fuel to enter the GT’s combustor creating a substantial spike in turbine inlet temperature which would have destroyed the turbomachinery. This failure mechanism would likely have been caught during the detailed PHA-HazOp review, however this is not a certainty and examples such as this help illustrate the value of thorough SIL testing enabling mitigation strategies to be incorporated. Also included in the controls code, and validated using SIL, was a robust fault detection and response system to ensure the system identified and responded appropriately to various faults which would be very difficult for a human to do (especially given the very large number of warnings and faults evaluated by the system).

      As previously mentioned, the Speedgoat platform is a real-time system meaning that the controls code is compiled and deployed to the dedicated target and runs at fixed ‘wall time’ rate. Using a stand-alone system is much more robust than running the controls code off a PC (e.g. a NI-cDAQ), especially for safety critical applications. Operators still need to be able to view and interact with the controller while running and this was accomplished using a UI developed in MATLAB App Designer and then compiled and deployed to a test cell PC. The UI allowed the sensor data gathered by the Speedgoat to be visualized and viewed on the PC and allowed the operator to interact with the system such as specifying setpoints and requesting various system operations. Another benefit of a system such as the Speedgoat platform is that it served as both the supervisory control and data acquisition systems. All the sensors were fed into the Speedgoat where they could either be used for control, or simply logged for subsequent post-processing. This approach is highly preferred for a development system of this complexity compared to having separate control and data acquisition systems where sensors must either be duplicated or read in by one system and passed to the other. With the Speedgoat system, all sensor and controller data were logged and stored in compressed files and configured to periodically create new log files. This was important for system usability given the multi-day nature of SOFC/GT testing. The logged data was remotely accessed and downloaded to a PC via PUTTY without interrupting the data logging processes, and then post-processed and stitched together in MATLAB for more thorough data visualization.

      Control system development involves far more than just the controls software, the controls hardware (including sensors, actuators, wiring, and power) and is another important part of the project. Czero designed and built all the controls panels for the INTEGRATE system in-house along with performing the field wiring. This process is aided by detailed panel and wire harness drawings (generated in AutoCAD and RapidHarness), which while built in-house for this project, are designed with enough detail to be reproduced by external shops if needed.

      Speedgoat SCADA System and Controls Enclosure
      Speedgoat SCADA System and Controls Enclosure

      SIL Testing Methodology
      SIL Testing Methodology

      Speedgoat UI
      Speedgoat UI
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      Fabrication, Assembly and Testing

      Not only was the INTEGRATE system designed at Czero (excluding the SOFC and GT developed by Nexceris and Brayton respectively), but much of the system was also fabricated, assembled, and tested as Czero facility. A large portion of Czero’s 16,000 ft2 facility is dedicated to fabrication and testing in support of projects of this scale. Given the potentially hazardous nature of this project, a dedicated test cell was created out of two 20’ high-top ISO containers which were located outdoors at Czero’s facility. Given the potential for flammable gases to be present in the event of a system failure, all components within the test cell were approved for C1D2 (hazardous location) operation. The test cell included a high-throughput ventilation system, explosion venting panels, and six gas detectors interlocked into the safety system. Czero also worked closely with hydrogen safety experts to ensure testing was performed in as safe a manner as possible.

      Other than the pressure vessel and frame, and high-temperature pipe spools, virtually all the custom components were fabricated in-house at Czero. This improved development speed and reduced costs associated with fully designing/documenting and having external vendors manufacture the parts while also allowing components to be field-fit.

      At present the system is undergoing final SOFC stack testing using bottled gas/dewars (H2, CH4, CO, CO2, N2), a series of mass flow controllers, and internally designed steam superheat generator to emulate the reformate composition supplied to the stack. Additionally an oil-free air compressor, high-temperature (750°C) inline air/fuel heaters to preheat the streams, and backpressure valves to control system pressure are included in the test system. These components, along with a power-electronics based load bank to load the SOFC, enable the SOFC to be tested in a manner identical to how it will function in the full SOFC/GT system. SOFC testing is in the final stages with integration of the GT into the system expected in Q3 2024. Final testing for this project is expected in Q4 2024.

      SOFC Components in the Test Cell
      SOFC Components in the Test Cell

      C1D2 (Hazardous Location) Rated SOFC/GT Test Cell at Czero’s Facility
      C1D2 (Hazardous Location) Rated SOFC/GT Test Cell at Czero’s Facility

      Non-HazLoc Rated BOP Components Inside of Czero’s Facility
      Non-HazLoc Rated BOP Components Inside of Czero’s Facility



      Acknowledgements

      The information, data, or work presented herein was funded in part by the Advanced Research Projects Agency-Energy (ARPA-E), U.S. Department of Energy, under Award Number DE-AR0000956. The views and opinions of authors expressed herein do not necessarily state or reflect those of the United States Government or any agency thereof.

      Links

      ARPA-E Press Release

      INTEGRATE SOFC/ICE Phase I 

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