Preparation of Mixed Iron Oxides for Solar Hydrogen Production by Means of the Pechini Technique

Author(s):  
Mari´a J. Marcos ◽  
Teresa Herna´ndez ◽  
Miguel Sa´nchez ◽  
Alberto J. Quejido ◽  
Manuel Romero

A process of synthesis of mixed iron oxides for their application to solar hydrogen production is reported. To analyze the suitability of the selected technique, different compositions in the compound MnxNi1−xFe2O4−5 were prepared by varying the Ni/Mn ratio between 0 and 3. The main objective was to identify the optimal amount of dopants for hydrogen production in such a magnetite. The powders were obtained from a solution of Ni, Mn and Fe nitrates by a polymeric method based on the Pechini process and were characterized by XRD and SEM. The characterization results indicated that the magnetite is fully developed at 1200°C by a multi-step solid state reaction between the mixed oxides produced after the resin heating (α- Fe2O3 and nickel-iron spinel). The particles have a polygonal morphology and are softly agglomerate. Their grain size vary with de manganese content and is about 1 micron for 0.25Mn in the mixed ferrite composition and 10 micron in the mixed ferrite without nickel. The activation endothermic step eventually resulting in an oxygen-deficient ferrite was carried out within a thermogravimetric balance. The TGA/DTA mixed magnetite analysis carried out with nitrogen as inert carrier gas showed a weight loss that can be attributed to the partial reduction of the magnetite. The weight losses and the activation temperature increases when the Ni/Mn ratio decreases, being 0.5% at 700°C and 2.57% at 900°C for Ni/Mn ratio 3 and 0 respectively. A series of experimental tests will follow at laboratory test facility with indirect and direct illumination, in order to select the most adequate operation conditions and to quantify the maximum cycle efficiency for a solarized process.

Author(s):  
Martin Roeb ◽  
Christian Sattler ◽  
Ruth Klu¨ser ◽  
Nathalie Monnerie ◽  
Lamark de Oliveira ◽  
...  

A very promising method for the conversion and storage of solar energy into a fuel is the dissociation of water to oxygen and hydrogen, carried out via a two-step process using metal oxide redox systems such as mixed iron oxides, coated upon multi-channeled honeycomb ceramic supports capable of absorbing solar irradiation, in a configuration similar to that encountered in automobile exhaust catalytic converters. With this configuration, the whole process can be carried out in a single solar energy converter, the process temperature can be significantly lowered compared to other thermo-chemical cycles and the re-combination of oxygen and hydrogen is prevented by fixing the oxygen in the metal oxide. For the realization of the integrated concept, research work proceeded in three parallel directions: synthesis of active redox systems, manufacture of ceramic honeycomb supports and manufacture, testing and optimization of operating conditions of a thermochemical solar receiver-reactor. The receiver-reactor has been developed and installed in the solar furnace in Cologne, Germany. It was proven that solar hydrogen production is feasible by this process demonstrating that multi cycling of the process was possible in principle.


2005 ◽  
Vol 128 (2) ◽  
pp. 125-133 ◽  
Author(s):  
Martin Roeb ◽  
Christian Sattler ◽  
Ruth Klüser ◽  
Nathalie Monnerie ◽  
Lamark de Oliveira ◽  
...  

A promising method for the conversion and storage of solar energy into hydrogen is the dissociation of water into oxygen and hydrogen, carried out via a two-step process using metal oxide redox systems such as mixed iron oxides, coated upon multi-channeled honeycomb ceramic supports capable of absorbing solar irradiation, in a configuration similar to that encountered in automobile exhaust catalytic converters. With this configuration, the whole process can be carried out in a single solar energy converter, the process temperature can be significantly lowered compared to other thermo-chemical cycles and the recombination of oxygen and hydrogen is prevented by fixing the oxygen in the metal oxide. For the realization of the integrated concept, research work proceeded in three parallel directions: synthesis of active redox systems, manufacture of ceramic honeycomb supports and manufacture, testing and optimization of operating conditions of a thermochemical solar receiver-reactor. The receiver-reactor has been developed and installed in the solar furnace in Cologne, Germany. It was proven that solar hydrogen production is feasible by this process demonstrating that multicycling of the process was possible in principle.


Author(s):  
Moritz Kölbach ◽  
Kira Rehfeld ◽  
Matthias M. May

We analyse the potential of solar hydrogen production in remote and cold world regions such as Antarctica and quantify the efficiency benefits of thermal coupling.


Energies ◽  
2021 ◽  
Vol 14 (12) ◽  
pp. 3437
Author(s):  
Andreas Rosenstiel ◽  
Nathalie Monnerie ◽  
Jürgen Dersch ◽  
Martin Roeb ◽  
Robert Pitz-Paal ◽  
...  

Global trade of green hydrogen will probably become a vital factor in reaching climate neutrality. The sunbelt of the Earth has a great potential for large-scale hydrogen production. One promising pathway to solar hydrogen is to use economically priced electricity from photovoltaics (PV) for electrochemical water splitting. However, storing electricity with batteries is still expensive and without storage only a small operating capacity of electrolyser systems can be reached. Combining PV with concentrated solar power (CSP) and thermal energy storage (TES) seems a good pathway to reach more electrolyser full load hours and thereby lower levelized costs of hydrogen (LCOH). This work introduces an energy system model for finding cost-optimal designs of such PV/CSP hybrid hydrogen production plants based on a global optimization algorithm. The model includes an operational strategy which improves the interplay between PV and CSP part, allowing also to store PV surplus electricity as heat. An exemplary study for stand-alone hydrogen production with an alkaline electrolyser (AEL) system is carried out. Three different locations with different solar resources are considered, regarding the total installed costs (TIC) to obtain realistic LCOH values. The study shows that a combination of PV and CSP is an auspicious concept for large-scale solar hydrogen production, leading to lower costs than using one of the technologies on its own. For today’s PV and CSP costs, minimum levelized costs of hydrogen of 4.04 USD/kg were determined for a plant located in Ouarzazate (Morocco). Considering the foreseen decrease in PV and CSP costs until 2030, cuts the LCOH to 3.09 USD/kg while still a combination of PV and CSP is the most economic system.


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