4.7 Article

Process design for green hydrogen production

期刊

INTERNATIONAL JOURNAL OF HYDROGEN ENERGY
卷 45, 期 12, 页码 7266-7277

出版社

PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.ijhydene.2019.08.206

关键词

Ethanol reforming; Membrane reactor; Process scheme; Green hydrogen production; Process intensification

资金

  1. European Union [734561]
  2. Marie Curie Actions (MSCA) [734561] Funding Source: Marie Curie Actions (MSCA)

向作者/读者索取更多资源

A membrane assisted process for green hydrogen production from a bioethanol derived feedstock is here developed and evaluated, starting from the conventional Steam Methane Reforming (SMR) process. Such a process is suitable for centralized hydrogen production, and is here analyzed for a large-scale H-2 production unit with the capacity of 40.000 Nm(3)/h.The basic Steam Ethanol Reforming (SER) process scheme is modified in a membrane assisted process by integrating the Pd-membrane separation steps in the most suitable reaction steps. The membrane assisted process, configured in three alternative architectures (Open architecture, Membrane Reactor and Hybrid architecture) was evaluated in terms of efficiencies and hydrogen yields, obtaining a clear indication of improved process performance. The alternative membrane assisted process architectures are compared to the basic SER process and to the benchmark SMR process fed by natural gas, for an overall comparative assessment of the efficiency and specific CO2 emissions and for an economic analysis based on the operating expenditures. (C) 2019 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.

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