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Annual Report 2006 - Plataforma Solar de Almería

Annual Report 2006 - Plataforma Solar de Almería

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CONCENTRATING SOLAR SYSTEMS UNIT<br />

technological and economic feasibility and their ability to reduce CO 2 emissions<br />

from more conventional hydrogen production systems, such as gasification<br />

and steam reforming.<br />

Purpose: The basic purpose of the project is to study clean hydrogen production<br />

processes in or<strong>de</strong>r to advance in the solution of its current technological<br />

and economic limitations key to being able to carry out a future transition<br />

to the hydrogen economy. The alternatives inclu<strong>de</strong>d in this project are characterized<br />

by avoiding formation of CO 2 as a coproduct of hydrogen and using<br />

renewable resources to provi<strong>de</strong> the energy consumed in the formation and<br />

release of hydrogen.<br />

1. Hydrogen production from water by photo<strong>de</strong>composition<br />

2. Hydrogen production from water by solar thermochemical cycles<br />

3. Hydrogen production from natural gas by catalytic <strong>de</strong>carbonization<br />

4. Comparative analysis of the above possibilities<br />

Results achieved in <strong>2006</strong>: Although CIEMAT participates in several of the subprojects,<br />

its main <strong>de</strong>dication is to Subproject 2, related to thermochemical<br />

hydrogen production. CIEMAT activity in PHISICO2 is largely complemented<br />

by activities and <strong>de</strong>velopments in the Solter-H project. In <strong>2006</strong>, the scientific<br />

effort concentrated on the synthesis, physical-chemical characterization and<br />

thermogravimetric testing of mixed transition-metal oxi<strong>de</strong>s to i<strong>de</strong>ntify their<br />

efficiency in hydrogen production, especially at optimum process temperatures<br />

in or<strong>de</strong>r to select the most suitable for solarization. Work was also done<br />

on assembly of a laboratory test bench. Synthesis, physical-chemical characterization<br />

and thermal reduction of Mn x Ni 1-x Fe 2 O 4-δ in a thermobalance, were<br />

also done by varying Ni/Mn between 0 and 3. Wet synthesis Ni, Fe and Mn<br />

nitrates was performed by the Pechini method from. In all cases, thermogravimetric<br />

tests were ma<strong>de</strong> with different heating ramps using nitrogen, helium<br />

or air as the carrier gas. Air would be best from the point of view of industrial<br />

scale-up, since it would avoid the use of an inert gas with the resulting cost<br />

Figure 3.25 Activation stage weight loss testing done in<br />

the thermogravimetric balance, with<br />

weightloss over temperature for mixed<br />

ferrite Ni x Mn 1-x Fe 2 O 4 samples (with nitrogen<br />

carrier and heat ramp of 20ºC/min)<br />

61

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