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Featured researches published by Arash Helmi.


Molecules | 2016

Fluidized Bed Membrane Reactors for Ultra Pure H2 Production—A Step forward towards Commercialization

Arash Helmi; Ekain Fernandez; Jon Melendez; David A. Pacheco Tanaka; F Fausto Gallucci; Martin van Sint Annaland

In this research the performance of a fluidized bed membrane reactor for high temperature water gas shift and its long term stability was investigated to provide a proof-of-concept of the new system at lab scale. A demonstration unit with a capacity of 1 Nm3/h of ultra-pure H2 was designed, built and operated over 900 h of continuous work. Firstly, the performance of the membranes were investigated at different inlet gas compositions and at different temperatures and H2 partial pressure differences. The membranes showed very high H2 fluxes (3.89 × 10−6 mol·m−2·Pa−1·s−1 at 400 °C and 1 atm pressure difference) with a H2/N2 ideal perm-selectivity (up to 21,000 when integrating five membranes in the module) beyond the DOE 2015 targets. Monitoring the performance of the membranes and the reactor confirmed a very stable performance of the unit for continuous high temperature water gas shift under bubbling fluidization conditions. Several experiments were carried out at different temperatures, pressures and various inlet compositions to determine the optimum operating window for the reactor. The obtained results showed high hydrogen recovery factors, and very low CO concentrations at the permeate side (in average <10 ppm), so that the produced hydrogen can be directly fed to a low temperature PEM fuel cell.


Archive | 2017

CHAPTER 2:Chemical Looping for Hydrogen Production and Purification

J.A. Medrano; Arash Helmi; Vincenzo Spallina; Martin van Sint Annaland; F Fausto Gallucci

Chemical Looping is an interesting technology that allows (partial) oxidation of a fuel without direct contact between the fuel and air. Instead, a solid material, referred to as oxygen carrier, is used to transport the oxygen from the air to the fuel by solid circulation between two reactors operated under different conditions. As such, the products of the fuel oxidation are nitrogen free. In the case of combustion (full oxidation), this means that the CO2 is not diluted with nitrogen. In the case of reforming/partial oxidation, the syngas is nitrogen free and thus easier to purify. In the presence of an H2 permselective membrane, the syngas production (through chemical looping) and pure H2 separation are combined in the same unit. This chapter introduces the chemical looping principle and describes a new reactor concept that combines the advantages of chemical looping technology and membrane reactors. This concept is referred to as Membrane-Assisted Chemical Looping Reforming (MA-CLR), which allows high hydrogen purity with integrated CO2 capture and high energy efficiency.


International Journal of Hydrogen Energy | 2015

Development of thin Pd–Ag supported membranes for fluidized bed membrane reactors including WGS related gases

Ekain Fernandez; Arash Helmi; Kai Coenen; Jon Melendez; Jose Luis Viviente; David A. Pacheco Tanaka; Martin van Sint Annaland; F Fausto Gallucci


International Journal of Hydrogen Energy | 2015

Preparation and characterization of thin-film Pd–Ag supported membranes for high-temperature applications

Ekain Fernandez; Kai Coenen; Arash Helmi; Jon Melendez; J. Zuñiga; D.A. Pacheco Tanaka; M. van Sint Annaland; F Fausto Gallucci


International Journal of Hydrogen Energy | 2014

Resource scarcity in palladium membrane applications for carbon capture in integrated gasification combined cycle units

Arash Helmi; F Fausto Gallucci; Martin van Sint Annaland


International Journal of Hydrogen Energy | 2017

Palladium based membranes and membrane reactors for hydrogen production and purification:An overview of research activities at Tecnalia and TU/e

Ekain Fernandez; Arash Helmi; J.A. Medrano; Kai Coenen; Alba Arratibel; Jon Melendez; N.C.A. de Nooijer; Vincenzo Spallina; Jose Luis Viviente; J. Zuñiga; M. van Sint Annaland; D.A. Pacheco Tanaka; F Fausto Gallucci


Catalysis Today | 2016

Effect of Re addition on the WGS activity and stability of Pt/CeO2–TiO2 catalyst for membrane reactor applications

V. del Villar; L. Barrio; Arash Helmi; M. van Sint Annaland; F Fausto Gallucci; J.L.G. Fierro; R.M. Navarro


Applied Mathematical Modelling | 2014

Computational fluid dynamics simulation of fluid particle fragmentation in turbulent flows

Ronnie Andersson; Arash Helmi


Chemical Engineering Journal | 2018

On concentration polarization in fluidized bed membrane reactors

Arash Helmi; R.J.W. Voncken; A.J. Raijmakers; I Ivo Roghair; F Fausto Gallucci; M. van Sint Annaland


Chemical Engineering and Processing | 2017

On the hydrodynamics of membrane assisted fluidized bed reactors using X-ray analysis

Arash Helmi; Evert C. Wagner; F Fausto Gallucci; M. van Sint Annaland; J.R. van Ommen; Robert F. Mudde

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F Fausto Gallucci

Eindhoven University of Technology

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M. van Sint Annaland

Eindhoven University of Technology

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Ekain Fernandez

Eindhoven University of Technology

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Jon Melendez

University of the Basque Country

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Kai Coenen

Eindhoven University of Technology

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D.A. Pacheco Tanaka

Eindhoven University of Technology

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J.A. Medrano

Eindhoven University of Technology

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Jose Luis Viviente

Eindhoven University of Technology

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Ronnie Andersson

Chalmers University of Technology

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