首页> 外文会议>ASME international conference on fuel cell science, engineering, and technology >5 KW_E + 5 KW_T PEM-FC GENERATOR FROM BIOETHANOL: FUEL PROCESSOR AND DEVELOPMENT OF NEW REFORMING CATALYSTS
【24h】

5 KW_E + 5 KW_T PEM-FC GENERATOR FROM BIOETHANOL: FUEL PROCESSOR AND DEVELOPMENT OF NEW REFORMING CATALYSTS

机译:5 kW_e + 5 kW_t PEM-FC发电机来自生物乙醇:燃油处理器和新型重整催化剂的开发

获取原文

摘要

A power unit constituted by a reformer, a H_2 purification section and a fuel cell is being tested c/o the Dept. of Physical Chemistry and Electrochemistry of Universita degli Studi di Milano, on the basis of a collaboration with Helbio S.A. Hydrogen and Energy Production Systems (supplier of the unit) and some sponsors (Linea Energia S.p.A., Parco Tecnologico Padano and Provincia di Lodi). The system size allows to cogenerate 5 kW_e (a.c.) + 5 kW_t (hot water at 65°C) as peak output. Bioethanol, obtainable by different non-food competitive biomass is transformed into syngas by a pre-reforming and a reforming stage and the reformate is purified from CO to a concentration below 20 ppmv, suitable to feed the proton exchange membrane fuel cells (PEMFC) stack integrated in the fuel processor. This result is achieved by feeding the reformate to two water gas shift reactors, connected in series and operating at high and low temperature, respectively. CO concentration in the outcoming gas is ca. 0.7 vol% and the final CO removal to meet the specifications is accomplished by two methanation stages in series. The second methanation step acts as a guard since ca. 15 ppmv of CO are obtained even after the first reactor. The purified H_2 is suitable for feeding a 5 kW_e PEMFC stack, which should have an expected overall efficiency higher than 80% (including thermal output). The main goal of the present project is to check system performance under different operating conditions, to verify the effectiveness of the proposed technology and to suggest adequate improvements. In particular, the system will be tested under different load, to check for the readyness of response. Another point will be the effect of bioethanol origin, purity and concentration, so to open the way to separation processes different from distillation. Due to the demonstrative character of the project the main part of the experimentation focuses on the accumulation of a suitable amount of hours-on-stream to validate the system feasibility. A parallel investigation is active on the development of alternative nanostructured catalysts for the present application. In particular, Ni, Co and Cu-based catalysts, supported over La_2O_3, TiO_2 and SiO_2 were tested at 500, 625 and 750°C. At the moment no perfect candidate has been found to operate the steam reforming at the lowest temperature, due to unsatisfactory material balances and by-products formation at 500°C with most catalysts. Good H_2 productivity, with 100% C balance has been achieved at higher temperature (≥ 625°C).
机译:由重整器,H_2净化部分和燃料电池构成的电力单元是在与Helbio SA氢气和能量产生的合作的基础上进行的C / O.的物理化学和Universita degli Studi Di Milano的电影学。系统(单位供应商)和一些赞助商(Linea Energia Spa,Parco Tecnologico Padano和Provincia di Lodi)。系统尺寸允许将5 kW_e(a.c.)+ 5kw_t(65°C的热水)作为峰值输出。通过不同的非食物竞争生物量可获得的生物乙醇通过预重整而转化为合成气,重整阶段和重整阶段从CO至40ppmV的浓度纯化,适用于喂养质子交换膜燃料电池(PEMFC)堆叠集成在燃料处理器中。通过将重整液进入两个水煤气换档反应器,分别在高温和低温下运行来实现该结果。外贸气体中的CO浓度是CA。 0.7 Vol%和最终的CO去除以满足规格,通过两个串联的甲烷化阶段完成。自加州以来,第二个甲烷化步骤用作防护。即使在第一反应器之后也可以获得15ppmV的CO。纯化的H_2适用于进给5kW_E PEMFC堆叠,其应具有高于80%(包括热输出)的预期整体效率。目前项目的主要目标是在不同的操作条件下检查系统性能,以验证所提出的技术的有效性,并提出了充分的改进。特别是,系统将在不同的负载下测试,以检查响应的人工。另一个点将是生物乙醇来源,纯度和浓度的影响,从而打开与蒸馏不同的分离过程的方式。由于该项目的示范性特征,实验的主要部分侧重于累积适量的单流程,以验证系统可行性。平行研究对于本申请的替代纳米结构催化剂的开发是活性的。特别地,在500,625和750℃下测试支持过La_2O_3,TiO_2和SiO_2的Ni,Co和Cu基催化剂。目前,没有发现在最低温度下的蒸汽重整器没有完美的候选者,由于在大多数催化剂的500℃下形成令人满意的材料余额和副产物。良好的H_2生产力,在较高温度下实现100%C平衡(≥625°C)。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号