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Rose Marie Mendoza Joy Marie Mora Rinlee Butch Cervera Po-Ya Abel Chuang 《化学工程与技术》2020,43(12):2350-2358
A 1-D electrochemical model for a solid oxide electrolysis cell (SOEC) is developed and validated using published experimental data. The model combines thermodynamics, kinetic, ohmic, and concentration overpotentials to predict cell performance. For the anode-supported SOEC, good agreement is obtained between the model and experimental data, with ohmic loss being the major contributor to the cell's total overpotential. Both kinetic and concentration losses are less significant due to high-temperature operation. Due to the dominating performance loss, reducing the anode thickness is effective in diminishing the cell potential. Overall, this simple 1-D model can be employed as a design tool to evaluate component design and estimate system performance for industrial applications. 相似文献
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Properties and Performance of Cation-Doped Ceria Electrolyte Materials in Solid Oxide Fuel Cell Applications 总被引:1,自引:0,他引:1
Christopher Milliken Sivaraman Guruswamy Ashok Khandkar 《Journal of the American Ceramic Society》2002,85(10):2479-2486
Cation-doped CeO2 electrolyte has been evaluated in single-cell and short-stack tests in solid oxide fuel cell environments and applications. These results, along with conductivity measurements, indicate that an ionic transference number of ∼0.75 can be expected at 800°C. Single cells have shown a power density >350 mW/cm2 . Multicell stacks have demonstrated a peak performance of >100 mW/cm2 at 700°C using metallic separators. 相似文献
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以大面积电池和千瓦级电堆为对象,研究了温度、燃料成分、流量等对阳极支撑型电堆性能的影响。结果表明:温度的影响最大,复数阻抗谱中高频弧对应的活化能最高;欧姆阻抗的活化能较低,表明其不全是离子电导的电阻,还包括双极板的表面电阻和可能的接触电阻。利用干氢气燃料测试时,在开路电压附近表现出较大的活化极化,且其活化能很小,表明该活化极化的速率控制步骤并非是电荷转移过程,而是对应某种表面扩散过程。模拟重整气燃料测试过程中活化极化不明显,但开路电压较低,性能比氢气燃料差。随着电堆工作电流的增加,燃料尾气的温度增加,表现出明显的热效应。 相似文献
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In this study it is theoretically analyzed how flue gas recirculation at the hydrogen electrode of solid oxide cells (SOC) systems effects fuel utilization and carbon formation. Interdepence between cell fuel utilization, system fuel utilization and gas recirculation is investigated numerically. Tendency towards carbon deposits is evaluated via thermodynamic equilibrium calculations. It is quantified which gas recirculation rates are necessary to achieve high values of system fuel utilization even if the cell fuel utilization is kept at a moderate level. Furthermore, tendency towards carbon deposition strongly depends on temperature, pressure and feed gas composition and can be reduced by adequate recirculation rates. The presented results can be used for the configuration of gas recirculation in SOC systems. 相似文献
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A microscale model of a solid oxide fuel cell (SOFC) involving the mass transfer together with the electrochemical reaction, the transportation of electrons and ions through the respective spherical shaped electron conducting and ion conducting particles inside the electrodes was mathematically developed. Couples of useful parameters were introduced in order to represent the characteristics of the cell. The predicted cell performance was showed according to various operating and design conditions. The effects of microscale electrode geometry on the cell performance were also taken into account. Parametric study according to the volumetric fraction of ionic and electronic conducting particles was conducted in order to examine the effects of operating conditions on the cell overpotentials. The study results substantiate the fact that SOFC overpotential could be effectively decreased by increasing the operating temperature as well as operating pressure. This present study reveals the working mechanisms of SOFC at the microscale level, while demonstrating the use of microscale relations to enhance the SOFC performance. The accuracy of the presented model was validated by comparing with already existing experimental results from the available literatures. 相似文献
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The microstructure, thermal expansion, mechanical property, and ionic conductivity of samaria-doped ceria (SDC) prepared by coprecipitation were investigated in this paper. The results revealed that the average particle size ranged from 10.9±0.4 to 13.5±0.5 nm, crystallite dimension varied from 8.6±0.3 to 10.7±0.4 nm, and the specific surface area distribution ranged from 62.6±1.8 to 76.7±2.2 m2 /g for SDC powders prepared by coprecipitation. The dependence of lattice parameter, a, versus dopant concentration, x , of Sm3+ ion shows that these solid solutions obey Vegard's rule as a ( x )=5.4089+0.10743 x for Ce1− x Sm x O2−1/2 x . For SDC ceramics sintered at 1500°C for 5 h, the bulk density was over 95% of the theoretical density; the maximum ionic conductivity, σ800°C =(22.3±1.14) × 10−3 S/cm with minimum activation energy, E a =0.89±0.02 eV, was found in the Ce0.80 Sm0.20 O1.90 ceramic. A dense Ce0.8 Sm0.2 O1.9 ceramic with a grain size distribution of 0.5–4 μm can be obtained by controlling the soaking time at 1500°C. When the soaking time was increased, the microhardness of Ce0.8 Sm0.2 O1.9 ceramic increased, the toughness slightly decreased, which was related to grain growth with the soaking time. 相似文献
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A flat tubular segmented‐in‐series (SIS) solid oxide fuel cell (SOFC) was fabricated using decalcomania paper. The performance of a two‐cell stack with 4.5‐mm‐wide electrodes was investigated in a temperature range of 650–800 °C. The decalcomania paper allowed fabrication of the SIS‐SOFC on all sides of the flat tubular support and achieve an effective electrode area larger than that obtained using typical SOFC fabrication techniques such as screen printing or slurry coating. SEM observations revealed that each component layer was flat, uniformly thick, and well adherent to adjacent layers. Measured values of open circuit voltages were very close to the theoretical values; confirming that the processing technique utilizing decalcomania paper is suitable for SIS‐SOFC fabrication. The power densities of the two‐cell‐stack were 437.4, 375.6, 324.6, and 257.1 mW cm−2 at 800, 750, 700 and 650 °C, respectively. 相似文献
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We develop a phenomenological theory of oxygen‐ion‐conducting porous cermet anode for solid oxide fuel cells utilizing hydrogen, based on a simple picture of macro‐ and microkinetics of charge and gas transport in the cermet. Its basic equations account for the transport of hydrogen molecules and oxygen anions to the reaction spots, the hydrogen oxidation reaction (whose various mechanisms, including different adsorption stages, are considered) and the water‐product removal. Simple analytical results are obtained for a linear current‐voltage regime, which demonstrate the interplay of these three processes. The nonlinear behavior is analyzed and classified. Various mechanisms of reaction kinetics are considered, subject to three possible mechanisms of water adsorption, in order to specify the law of conversion of ionic current into electronic one. Revealed is the nature of the intermediate quasi‐Tafel regime, in which the anode is usually employed, and of two possible large current regimes: the saturation regime and the blocking regime (due to oxidation of the anode). The study rationalizes principles of anode functioning and builds a basis for a systematic analysis of the effects due to composite structure, that enter through the basic parameters of the theory. 相似文献
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Kaori Jono Seiichi Suda Masatoshi Hattori 《Journal of the American Ceramic Society》2009,92(S1):S112-S116
A novel ionic-conductive skeletal structure was developed for an electrode-supported solid oxide fuel cell (SOFC). The skeletal structure was formed as an ionic-conductive frame that accumulated two thick porous layers and one dense thin layer. Two types of green sheets were used to form the frame. Thin green sheets (thickness: 15–30 μm) for the dense layers were fabricated with a well-dispersed Gd0.2 Ce0.8 O x (GDC) slurry and thick sheets (thickness: 150–300 μm) were fabricated with a GDC/pore-former slurry by the tape casting method. Sintering laminated sheets at 1450°C for 8 h in air resulted in an ionic-conductive frame that was suitable for electrode-supported SOFC. The relative density of the inner thin layer, which works as an electrolyte, was higher than 98%, and the outer thick layers remained porous after the sintering. The porous structure of the outer layers was controlled using agglomerated slurries instead of well-dispersed slurries. Electrochemical measurements of the ionic-conductive frame attached with platinum electrodes exhibited potential as high-performance cells. 相似文献
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固体氧化物燃料电池是一种典型的电化学装置,可以把燃料气和空气(或氧气)的化学能直接转化为电能。电池的整个反应过程可以根据还原剂和氧化剂反应自由焓来进行热力学计算。对于最简单的氢气和氧气的反应来说,可以根据可逆反应平衡方程式计算电池的可逆功,而且SOFC系统和外部环境的热交换也是可逆的。SOFC作为一种伴生热能的发电装置,对热力学的理解必不可少。所以本文将首先介绍一下SOFC的热力学基础,而作为一种电化学发电装置,需要系统了解SOFC的电化学基础,其中重点介绍SOFC的电化学分析曲线——i-V曲线。 相似文献
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The effects of methane concentration and current load cycle on the performance and durability of integrated planar solid oxide fuel cell (IP‐SOFC) obtained from Rolls Royce Fuel Cell Systems Ltd (RRFCS) has been investigated. The IP‐SOFC was operated with hydrogen–methane fuel mixture with up to 20% methane concentration at 900 °C for short term operation of the cells with high methane concentration increased the voltage of the IP‐SOFC due to increase in Gibbs free energy. However, it degraded the performance of the IP‐SOFC in long term operation due to carbon deposition on the anode surface. The current load cycle tests were carried out with 95% H2–5% CH4 and 80% H2–20% CH4 fuel mixtures at 900 °C with a constant current of 1 A. At low methane concentration, the decrease in the IP‐SOFC voltage was observed after operating nine current load cycles (384 h). At higher methane concentration, the voltage of IP‐SOFC decreased by almost 30% just after one current load cycle (48 h) due to faster carbon deposition. So future work is therefore required to identify viable alternative materials and optimum operating conditions. 相似文献
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The paper reports a new concept of planar‐tubular solid oxide fuel cell (PT‐SOFC). Emphasis is on the fabrication of the required complex configuration of Ni‐yttria‐stabilised zirconia (YSZ) porous anode support by tert‐butyl alcohol (TBA) based gelcasting, particularly the effects of solid loading, amounts of monomers and dispersant on the rheological behaviour of suspension, the shrinkage of a wet gelcast green body upon drying, and the properties of final sample after sintering at 1350 °C and reduction from NiO‐YSZ to Ni‐YSZ. The results show that the gelcasting is a powerful method for preparation of the required complex configuration anode support. The anode support resulted from an optimised suspension with the solid loading of 25 vol% has uniform microstructure with 37% porosity, bending strength of 44 MPa and conductivity of 300 S cm—1 at 700 °C, meeting the requirements for an anode support of SOFC. Based on the as‐prepared anode support, PT‐SOFC single cell of Ni‐YSZ/YSZ/LSCF has been fabricated by slurry coating and co‐sintering technique. The cell peak power density reaches 63, 106 and 141 mW cm—2 at 700, 750 and 800 °C, respectively, using hydrogen as fuel and ambient air as oxidant. 相似文献
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U.‐J. Yun J.‐W. Lee S.‐B. Lee T.‐H. Lim S.‐J. Park R.‐H. Song D.‐R. Shin 《Fuel Cells》2012,12(6):1099-1103
A tubular segmented‐in‐series (SIS) solid oxide fuel cell (SOFC) sub module for intermediate temperature (700–800 °C) operation was fabricated and operated in this study. For this purpose, we fabricated porous ceramic supports of 3 YSZ through an extrusion process and analyzed the basic properties of the ceramic support, such as visible microstructure, porosity, and mechanical strength, respectively. After that, we fabricated a tubular SIS SOFC single cell by using dip coating and vacuum slurry coating method in the case of electrode and electrolyte, and obtained at 800 °C a performance of about 400 mW cm–2. To make a sub module for tubular SIS SOFC, ten tubular SIS SOFC single cells with an effective electrode area of 1.1 cm2 were coated onto the surface of the prepared ceramic support and were connected in series by using Ag + glass interconnect between each single cell. The ten‐cell sub module of tubular SIS SOFC showed in 3% humidified H2 and air at 800 °C a maximum power of ca. 390 mW cm–2. 相似文献
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In this research a 100 W solid oxide fuel cells (SOFCs) stack was tested. After 3,700 hours of continuous operation a subsequent post‐test analysis of the anodes' microstructure was conducted using a combination of focused ion beam and scanning electron microscopy. The obtained data was reconstructed into three‐dimensional images, based on which the microstructure parameters were obtained. The microstructure parameters were quantified at nine different locations in the stack. The discussion focuses on tripe phase boundaries as the most important microstructure parameter strongly affecting the anode performance and degradation. The obtained results indicate strong non‐homogeneous microstructure morphology changes after long‐term operation. 相似文献
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Subsolidus phase relations in the La2 O3 –BaO–CuO system were studied at 950°C. Three previously reported binary compounds exist (La2 CuO4 , BaLa2 O4 , and BaCuO2 ) and five previously reported ternary phases occur (La2-x Bax CuO4-(x/2)+δ , La4-2x Ba2+2x Cu2-x O10-2x , La2-x Ba1+x Cu2 O6-(x-2) , La3-x Ba3+x Cu6 O14±δ , and La4 BaCu5 O13+δ ). Of the seven phases in the diagram, all but BaLa2 O4 , BaCuO2 , and La4 BaCu5 O13+δ were shown to exhibit significant ranges of solubility. The diagram is important in that both >30 K (La2-x Bax CuO4-(x/2)+δ ) and >90 K (La3-x Ba3+x Cu6 O14+δ , x=1) superconductors occur. 相似文献