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  • The Electrochemical Society  (5)
  • 2020-2024  (5)
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  • The Electrochemical Society  (5)
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  • 2020-2024  (5)
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  • 1
    Online Resource
    Online Resource
    The Electrochemical Society ; 2023
    In:  ECS Transactions Vol. 111, No. 6 ( 2023-05-19), p. 1575-1583
    In: ECS Transactions, The Electrochemical Society, Vol. 111, No. 6 ( 2023-05-19), p. 1575-1583
    Abstract: Methanol generally needs a steam reforming process before being used in solid oxide fuel cells (SOFCs). This paper calculated and tested the composition of methanol reforming gas under different steam-to-carbon ratio (S/C ratio) and temperature. Results show that when the temperature is between 720°C and 820°C, experiment results are almost consistent with calculation results. When the temperature is around 620°C, a significant deviation exists between the experiment and calculation results, indicating that methanol conversion is incomplete. When the S/C ratio needs to be higher than 1.2 due to the equipment's limit, the appropriate reaction condition is 725°C and S/C ratio of 1.2. Methanol reforming gas under this condition was tested on a commercial SOFC. The peak power is 39.31W under 750°C and 46.97W under 800°C. The highest electrical efficiency reaches 52.4% when fuel utilization is 80%. These results provide a research basis for the future application of methanol in SOFCs.
    Type of Medium: Online Resource
    ISSN: 1938-5862 , 1938-6737
    Language: Unknown
    Publisher: The Electrochemical Society
    Publication Date: 2023
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  • 2
    Online Resource
    Online Resource
    The Electrochemical Society ; 2021
    In:  Journal of The Electrochemical Society Vol. 168, No. 6 ( 2021-06-01), p. 066505-
    In: Journal of The Electrochemical Society, The Electrochemical Society, Vol. 168, No. 6 ( 2021-06-01), p. 066505-
    Abstract: The huge consumption of fossil fuels in industrialization has caused increasingly aggravated greenhouse effect. To address this problem, converting CO 2 into liquid solar fuels by photoelectrochemical technology is highly expected. In order to enhance the photoelectrochemical performance of the photocathodes, the composite thin film photocathodes have been constructed by covering CuFeO 2 nanoparticles (CFO NPs) on CuInS 2 (CIS) thin film surface by the impregnation (I-CFO/CIS) and the template method (T-CFO/CIS). In addition, the p–p heterostructure is formed between CIS and CFO NPs. Furthermore, the adsorption behaviors of intermediates are altered because of the well dispersed and smaller size of CFO NPs on T-CFO/CIS thin films. As a result, enhanced photoelectrocatalytic CO 2 reduction is achieved. The yield of methanol on T-CFO/CIS thin film reaches up to 270 μ M, which is 3.5 and 11.2 times as high as that on I-CFO/CIS and CIS thin films, respectively. At the applied voltage of −0.65 V vs saturated calomel electrode (SCE), the maximal faradic efficiency of methanol on T-CFO/CIS photocathodes is as high as 87%.
    Type of Medium: Online Resource
    ISSN: 0013-4651 , 1945-7111
    RVK:
    Language: Unknown
    Publisher: The Electrochemical Society
    Publication Date: 2021
    Location Call Number Limitation Availability
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  • 3
    Online Resource
    Online Resource
    The Electrochemical Society ; 2021
    In:  ECS Transactions Vol. 103, No. 1 ( 2021-07-09), p. 1033-1045
    In: ECS Transactions, The Electrochemical Society, Vol. 103, No. 1 ( 2021-07-09), p. 1033-1045
    Abstract: Solid Oxide Fuel Cell (SOFC) is an attractive energy conversion device due to its high efficiency and fuel flexibility. Key operation parameters such as current, temperature, and fuel utilization are critical variables in SOFC systems that directly impact efficiency and longevity. The degradation of the SOFC performance not only limits the operating temperature range of the SOFC stack in the system, but also simultaneously generates Joule heat, which further causes the stack to deviate from its initial thermal balance.In this paper, a semi-empirical SOFC dynamic model with degradation is proposed and validated by experiment data. The degradation in the above model is developed based on current density, temperature, and fuel utilization to simulate cell performance decay over time due to ohmic loss growth and the heat generation by cell resistance. The coupling between key parameters, stack performance, and degradation during long-term load following and the impact of stack degradation on the entire system long-term performance is discussed and investigated. An optimized strategy uses both feedback and feed-forward control law is designed to track the desired power demand with the aim of mitigating the degradation and compensating the time differences between dynamics at different time-scale.
    Type of Medium: Online Resource
    ISSN: 1938-5862 , 1938-6737
    Language: Unknown
    Publisher: The Electrochemical Society
    Publication Date: 2021
    Location Call Number Limitation Availability
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  • 4
    Online Resource
    Online Resource
    The Electrochemical Society ; 2023
    In:  ECS Meeting Abstracts Vol. MA2023-01, No. 54 ( 2023-08-28), p. 242-242
    In: ECS Meeting Abstracts, The Electrochemical Society, Vol. MA2023-01, No. 54 ( 2023-08-28), p. 242-242
    Abstract: The availability of hydrocarbon fuel is a unique advantage of solid oxide fuel cells (SOFCs). Methanol is one of the good choices for SOFC fuel because of its wide source, large output and easy storage and transportation. Methanol generally needs the steam reforming process before being used in SOFCs. In this paper, methanol reforming products under different steam-to-carbon ratio and temperature were tested on a commercial reforming equipment. Composition was compared with thermodynamic calculation results. The results show that when the temperature is below 700℃, a large deviation between components and thermodynamic calculation exists, indicating that methanol conversion is incomplete. When the temperature is above 700℃, methanol conversion is generally complete, and the temperature has little effect on the composition under this situation, while the steam-to-carbon ratio becomes the main influence factor. The hydrogen proportion in the products increases with the decrease of the steam-to-carbon ratio. A group of reforming products components were selected and tested on a commercial SOFC, and good performance was obtained, indicating the effectiveness of the optimization, which provides a research basis for the future application of methanol in SOFCs.
    Type of Medium: Online Resource
    ISSN: 2151-2043
    Language: Unknown
    Publisher: The Electrochemical Society
    Publication Date: 2023
    detail.hit.zdb_id: 2438749-6
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  • 5
    Online Resource
    Online Resource
    The Electrochemical Society ; 2021
    In:  ECS Meeting Abstracts Vol. MA2021-03, No. 1 ( 2021-07-23), p. 63-63
    In: ECS Meeting Abstracts, The Electrochemical Society, Vol. MA2021-03, No. 1 ( 2021-07-23), p. 63-63
    Abstract: Solid Oxide Fuel Cell (SOFC) is an attractive energy conversion device due to its high efficiency and fuel flexibility. Key operation parameters such as current, temperature and fuel utilization are critical variables in SOFC systems that directly impact efficiency and longevity. The degradation of the SOFC performance not only limits the operating temperature range of the SOFC stack in the system, but also simultaneously generates Joule heat, which further causes the stack to deviate from its initial thermal balance. In this paper, a semi-empirical SOFC dynamic model with degradation is proposed and validated by experiment data. The degradation in the above model is developed based on current density, temperature and fuel utilization to simulate cell performance decay over time due to ohmic loss growth and the heat generation by cell resistance. The coupling between key parameters, stack performance and degradation during long-term load following and the impact of stack degradation on the entire system long-term performance is discussed and investigated. An optimized strategy uses both feedback and feed-forward control law is designed to track the desired power demand with the aim of mitigating the degradation and compensating the time differences between dynamics at different time-scale. References 1. Shi W, Zhu J, Han M, et al. Operating limitation and degradation modeling of micro solid oxide fuel cell-combined heat and power system[J]. Applied Energy, 2019, 252: 113444. 2. Zaccaria V, Tucker D, Traverso A, et al. Active Control of Fuel Cell Degradation in an SOFC/GT Hybrid System[C], Turbo Expo: Power for Land, Sea, and Air. American Society of Mechanical Engineers, 2017, 50831: V003T06A035. 3. Murshed A K M M, Huang B, Nandakumar K. Control relevant modeling of planer solid oxide fuel cell system[J]. Journal of Power Sources, 2007, 163(2): 830-845. 4. Das T, Weisman R. A feedback based load shaping strategy for fuel utilization control in sofc systems[C], 2009 American Control Conference. IEEE, 2009: 2767-2772. 5. Spivey B J, Hedengren J D, Edgar T F. Constrained control and optimization of tubular solid oxide fuel cells for extending cell lifetime[C], 2012 American Control Conference (ACC). IEEE, 2012: 1356-1361. 6. Sreedhar I, Agarwal B, Goyal P, et al. An overview of degradation in solid oxide fuel cells-potential clean power sources[J]. Journal of Solid State Electrochemistry, 2020, 24: 1239-1270. Figure 1
    Type of Medium: Online Resource
    ISSN: 2151-2043
    Language: Unknown
    Publisher: The Electrochemical Society
    Publication Date: 2021
    detail.hit.zdb_id: 2438749-6
    Location Call Number Limitation Availability
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