首页> 外文会议>American Society of Mechanical Engineers(ASME) Summer Heat Transfer Conference(HT2005) vol.3; 20050717-22; San Francisco,CA(UA) >INDEPENDENT HYBRID POWER PLANT 'PEMFC+MEMS' WITH USE OF MOLECULAR CERAMIC MEMBRANES TO SEPARATE CO and H_2
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INDEPENDENT HYBRID POWER PLANT 'PEMFC+MEMS' WITH USE OF MOLECULAR CERAMIC MEMBRANES TO SEPARATE CO and H_2

机译:使用分子陶瓷膜分离CO和H_2的独立混合动力工厂'PEMFC + MEMS'

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As analysis of thermal-technical parameters of the existing polymer exchange membrane fuel cells (PEMFC) indicated, their electrical efficiency is not above 32-37% which is due to relatively high (10-15%) electric power consumption to cover own needs. Its major percentage falls on pump and compressor drive (air, fuel, water supply) using the AC electric engines connected via converter to FC. A real alternative allowing the efficiency increase up to 45% and higher is to apply hybrid plants when an AC turboelectric generator (TEG) is built into the thermodynamic cycle, the latter operating at the expense of utilization of the FC reagent stream power. TEG is a micro turbocompressor with incorporated turbo generator manufactured on the basis of the micro electric-mechanical system (MEMS) technology. The numerical study over the hybrid cycle effectiveness revealed that the optimum efficiency is ensured provided the TEG power does not exceed 12-15% of the total hybrid power plant power. Considering a value of the PEMFC mean power of around 8, a need arises in TEG of 500 to 1500W power to operate as a part of hybrid engine. Among various auxiliaries involved into the PEMFC, there should be devices that ensure getting target values in terms of hydrogen purity, a dominant synthetic gas fraction, at the FC inlet. A need to get and maintain hydrogen purity on the level of 99.99% is related with that if CO content in mixture is higher 0.01%, then a normal operation of FC fails due to "poisoning" effect of the platinum-containing catalysts of the FC electrodes. To forestall this, the palladium molecular membranes are now typically applied which causes the filtered flow temperature limitations within values not exceeding 500-550℃. At the same time, PEMFC in most cases must operate on air and syngas produced by reforming, with their temperature amounting to 800-900℃ . To provide this, we need to have ceramic molecular membranes (CMM) made of a ceramic support in which macropores nano pores are formed (characteristic size of less 0.3nm), the latter achieved through application of a complex of various chemical and physical processes. In the paper presented, findings of numerical studies over a hybrid engine plant are provided, this hybrid plant (PEMFC + MEMS) as compared with alternatives to existing and offered schemes, and, also, test data on the zeolite-based support CMM are demonstrated.
机译:正如对现有聚合物交换膜燃料电池(PEMFC)的热技术参数的分析所表明的,其电效率不高于32-37%,这是由于相对较高的电耗(10-15%)可以满足自己的需求。它的主要百分比落在使用通过转换器连接到FC的交流电动发动机的泵和压缩机驱动(空气,燃料,供水)上。当将AC涡轮发电机(TEG)内置到热力循环中时,允许效率提高到45%或更高的一个真正的替代方案是应用混合动力装置,而后者要以利用FC试剂流功率为代价。 TEG是结合了涡轮发电机的微型涡轮压缩机,该涡轮发电机是基于微机电系统(MEMS)技术制造的。混合动力循环效率的数值研究表明,只要TEG功率不超过混合动力总功率的12-15%,就可以确保最佳效率。考虑到PEMFC的平均功率值约为8,TEG需要500至1500W的功率才能作为混合动力发动机的一部分工作。在PEMFC涉及的各种辅助设备中,应该有一些设备可以确保在FC入口获得氢纯度(占主导地位的合成气馏分)方面的目标值。获得和维持氢纯度在99.99%的需求与混合物中的CO含量高于0.01%时有关,由于FC的含铂催化剂的“中毒”作用,FC的正常运行会失败。电极。为了防止这种情况,现在通常使用钯分子膜,这会导致过滤后的流动温度限制在不超过500-550℃的范围内。同时,PEMFC在大多数情况下必须使用重整产生的空气和合成气,其温度为800-900℃。为此,我们需要一种由陶瓷载体制成的陶瓷分子膜(CMM),在其中形成大孔纳米孔(特征尺寸小于0.3nm),后者是通过应用各种化学和物理过程的复合物来实现的。在本文介绍的论文中,提供了对混合动力工厂进行数值研究的结果,与现有方案和提供方案的替代方案相比,该混合工厂(PEMFC + MEMS)也得到了基于沸石的支撑CMM的测试数据。

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