Process design for green hydrogen production

Lorena Mosca; Jose Antonio Medrano Jimenez; Solomon Assefa Wassie; Fausto Gallucci; Emma Palo; Michele Colozzi; Stefania Taraschi; Giulio Galdieri

doi:10.1016/j.ijhydene.2019.08.206

Process design for green hydrogen production

Lorena Mosca (Corresponding author)
, Jose Antonio Medrano Jimenez
, Solomon Assefa Wassie
, Fausto Gallucci
, Emma Palo
, Michele Colozzi
, Stefania Taraschi
, Giulio Galdieri

Research output: Contribution to journal › Article › Academic › peer-review

104 Citations (Scopus)

3736 Downloads (Pure)

Abstract

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 H₂ production unit with the capacity of 40.000 Nm³/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.

Original language	English
Pages (from-to)	7266-7277
Number of pages	12
Journal	International Journal of Hydrogen Energy
Volume	45
Issue number	12
Early online date	24 Sept 2019
DOIs	https://doi.org/10.1016/j.ijhydene.2019.08.206
Publication status	Published - 4 Mar 2020

Funding

This project has received funding from the European Union's Horizon 2020 research and innovation program under the Marie Skłodowska-Curie grant agreement No 734561 . The paper reflects only the author's view and that the Agency is not responsible for any use that may be made of the information it contains.

Funders	Funder number
European Union's Horizon 2020 - Research and Innovation Framework Programme
Marie Skłodowska‐Curie
European Union's Horizon 2020 - Research and Innovation Framework Programme	734561
European Union's Horizon 2020 - Research and Innovation Framework Programme

UN SDGs

This output contributes to the following UN Sustainable Development Goals (SDGs)

SDG 7 Affordable and Clean Energy

Keywords

Ethanol reforming
Green hydrogen production
Membrane reactor
Process intensification
Process scheme

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10.1016/j.ijhydene.2019.08.206

publishers versionFinal published version, 1.65 MBLicence: TAVERNE

Cite this

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title = "Process design for green hydrogen production",

abstract = "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 H2 production unit with the capacity of 40.000 Nm3/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.",

keywords = "Ethanol reforming, Green hydrogen production, Membrane reactor, Process intensification, Process scheme",

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AU - Mosca, Lorena

AU - Medrano Jimenez, Jose Antonio

AU - Wassie, Solomon Assefa

AU - Gallucci, Fausto

AU - Palo, Emma

AU - Colozzi, Michele

AU - Taraschi, Stefania

AU - Galdieri, Giulio

PY - 2020/3/4

Y1 - 2020/3/4

N2 - 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 H2 production unit with the capacity of 40.000 Nm3/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.

AB - 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 H2 production unit with the capacity of 40.000 Nm3/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.

KW - Ethanol reforming

KW - Green hydrogen production

KW - Membrane reactor

KW - Process intensification

KW - Process scheme

UR - https://www.scopus.com/pages/publications/85072580413

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DO - 10.1016/j.ijhydene.2019.08.206

M3 - Article

AN - SCOPUS:85072580413

SN - 0360-3199

VL - 45

SP - 7266

EP - 7277

JO - International Journal of Hydrogen Energy

JF - International Journal of Hydrogen Energy

IS - 12

ER -

Process design for green hydrogen production

Abstract

Funding

UN SDGs

Keywords

Access to Document

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