首页> 外文会议>International conference on energy sustainability;ES2010 >NUMERICAL OPTIMIZATION OF A VOLUMETRIC SOLAR RECEIVER-REACTOR FOR THERMOCHEMICAL HYDROGEN GENERATION VIA DECOMPOSITION OF SULFUR TRIOXIDE
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NUMERICAL OPTIMIZATION OF A VOLUMETRIC SOLAR RECEIVER-REACTOR FOR THERMOCHEMICAL HYDROGEN GENERATION VIA DECOMPOSITION OF SULFUR TRIOXIDE

机译:通过三氧化硫分解生成热化学氢的体积太阳能接收反应器的数值优化

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A basic concept for a receiver-reactor for solar sulfuric acid decomposition as the key step of thermochemical cycles for hydrogen production has been developed and realized. A prototype reactor has been built and is specialized for the second part of the reaction, the decomposition of sulfur trioxide. For a detailed understanding of the operational behaviour of the developed reactor type a mathematical model was developed. The reactor model was validated using experimental data from the prototype reactor test operation. The present work deals with the optimization of process and design parameters and the evaluation of the achievable performance of the reactor type. Furthermore the reactor model is used for numerical simulations to predict operational points, which are not easy to realize in experiments due to hardware limitations, to save the experimental effort, and to predict the performance of a large-scale reactor on a solar tower.The results of the simulation confirm a central finding of the experiments: Depending on the operation conditions an optimum of reactor efficiency emerges if one parameter is varied. This is in particular true for the absorber temperature. Two oppositional effects compensate each other in a way thatthe reactor efficiency exhibits a maximum at a certain temperature: by increasing process temperature the re-radiation losses increase disproportionately high whereas the chemical conversion decreases when lowering the temperature. Beyond that influences of other operational parameters like feed mass flow, residence time, and initial concentration of the acid were also analyzed.In a scale-up study the reactor was simulated as being part of the aperture area of a large scale tower receiver. The main differences to the prototype system are the diminished gradients of solar flux on the receiver front face and the reduced thermal conduction losses due to the presence of several neighbor modules at comparable temperature level. This leads to higher chemical conversions and better efficiencies. Reactor efficiencies up to 75 % are predicted. Even higher efficiencies are possible if re-radiation losses can be decreased, e.g. by considering a cavity design.
机译:已经开发并实现了用于太阳能硫酸分解的接收反应器的基本概念,该反应器是制氢热化学循环的关键步骤。已经建造了原型反应器,该反应器专门用于反应的第二部分,即三氧化硫的分解。为了详细了解已开发反应堆类型的运行行为,开发了一个数学模型。使用来自原型反应堆测试操作的实验数据验证了反应堆模型。目前的工作涉及工艺和设计参数的优化以及反应器类型可达到的性能评估。此外,反应堆模型用于数值模拟以预测操作点,由于硬件限制,这些点在实验中不容易实现,以节省实验工作,并预测太阳能塔上大型反应堆的性能。 模拟结果证实了实验的主要发现:如果改变一个参数,则根据操作条件,将出现最佳的反应器效率。对于吸收器温度尤其如此。两个对立的效果相互补偿, 在一定温度下,反应器效率达到最大值:通过提高过程温度,再辐射损失会不成比例地增加,而降低温度时化学转化率会降低。除此之外,还分析了其他操作参数(如进料质量流量,停留时间和酸的初始浓度)的影响。 在放大研究中,将反应堆模拟为大型塔式接收器孔径区域的一部分。与原型系统的主要区别在于,接收器正面的太阳通量梯度减小,并且由于在可比较的温度水平下存在多个相邻模块,从而降低了热传导损耗。这导致更高的化学转化率和更高的效率。预计反应堆效率将达到75%。如果可以减少再辐射损失,例如更高的效率,则可能实现更高的效率。通过考虑型腔设计。

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