Novel concept for indirect solar-heated methane reforming

Zahra Mahdi, C. Rendón, C. Schwager, C. Boura, U. Herrmann
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引用次数: 1

Abstract

A model to investigate an indirectly solar-heated bayonet-tube reactor for converting methane to synthetic gas (syngas) through combined steam reforming and dry reforming is presented. Concentrated solar radiation, as generated in solar power towers is capable of efficiently providing heat for this process. Different concepts of reforming reactors have been analyzed and assessed under the following considerations: The risk of carbon deposition at low-temperature regimes in the reactor, the possibility of heat recovery from the syngas, maximized heat extraction for the air stream to improve the receiver efficiency and flexibility. As a result, a novel bayonet-tubes reactor design has been developed. Different simulation software tools have been applied for this purpose. Simulations in EBSILON®Professional show that the heat recovery from the syngas allows a 28 % higher syngas production (8.42 kg/s instead of 6.59 kg/s) based on the same solar resource, since the required heat for the methane reforming is simultaneously transferred from both air and syngas. In the system simulations, the syngas cools down from 900 °C to about 451 °C while the air is cooled down from 930 °C to approx. 220 °C. A one-dimensionally discretized model of a single bayonet-tube reactor was simulated in Dymola to corroborate that the reactor design provides sufficient temperature gradients for the heat transfer from air and syngas to the reactant flow. Further thermal and fluid mechanical analysis were performed in ANSYS® Fluent as preparation for building a first prototype.
太阳能间接加热甲烷重整的新概念
提出了一种研究甲烷蒸汽重整和干重整联合转化为合成气的间接太阳能加热卡口管反应器的模型。太阳能发电塔产生的集中太阳辐射能够有效地为这一过程提供热量。根据以下考虑因素,对重整反应器的不同概念进行了分析和评估:反应器低温状态下碳沉积的风险,合成气热回收的可能性,最大限度地从气流中提取热量以提高接收器的效率和灵活性。因此,开发了一种新的卡口管式反应器设计。为此,应用了不同的仿真软件工具。EBSILON®Professional的模拟表明,基于相同的太阳能资源,合成气的热回收可以使合成气产量提高28% (8.42 kg/s而不是6.59 kg/s),因为甲烷重整所需的热量同时从空气和合成气中转移。在系统模拟中,合成气从900°C冷却到约451°C,空气从930°C冷却到约451°C。220°C。在Dymola中模拟了单卡口管反应器的一维离散模型,以证实反应器设计为空气和合成气向反应物流的传热提供了足够的温度梯度。在ANSYS®Fluent中进行了进一步的热学和流体力学分析,为构建第一个原型做准备。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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