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@INPROCEEDINGS{Sarner:1016763,
author = {Sarner, Stephan and Menzler, Norbert H. and Guillon,
Olivier},
title = {({S}emi-){C}losed {L}oop {R}ecycling of {S}olid {O}xide
{C}ells},
school = {RWTH Aachen University},
reportid = {FZJ-2023-03749},
year = {2023},
abstract = {Fuel cell and hydrogen applications will be key to enable
the transition towards decarbonization and achieving the
EU's targets of zero net greenhouse gas emissions by 2050.
In the next years, priority will be set on the expansion of
suitable hydrogen electrolyzers, such as solid oxide
electrolysis cells (SOECs). Compared to other types of
electrolyzers, the SOEC has a moderate technology readiness
level (TRL 5-7). In order to facilitate the market entry and
at the same time recover valuable raw materials, recycling
concepts have to be developed and implemented at an early
stage.The task of reusing or recovering high-temperature
electrolyzer components is being addressed and focusses on
the reprocessing of ceramic components of End-of-Life SOECs.
Recycling in a closed-loop is particularly desirable, while
the process is designed to be as scalable as possible. The
biggest challenge for SOC recycling arises from the fact
that no standardized manufacturing process for hydrogen
electrolysis stacks/cells is currently existing. As a
result, several cell types are available, sometimes
differing significantly in their structures, materials and
materials shares used. The cell designs can be divided into
metal-supported cells (MSCs), electrolyte-supported cells
(ESCs), and fuel electrode-supported cells (FESCs). Even
within one cell type, differences can occur depending on the
manufacturer. Therefore, it is likely that a classification
and separation according to comparable cell types will be
needed in the future.We focus mainly on the recycling of
FESC-type cells. After separation from the stack, the cell
will undergo different stages within the recycling process,
illustrated in Figure 1. After re-oxidizing the whole cell,
the air electrode and contact layer (~15 $wt\%)$ are removed
by acid treatment, however most parts of the cell remain
stable (~85 $wt\%).$ This solid fraction is further milled
down and reprocessed to substrate slurry. Defined portions
of the recycled slurry are admixed with standard slurry. The
resulting green tapes and sintered bodies are investigated
in terms of microstructure and mechanical stability.Parts of
the liquid fraction of the cell, according to ~15 $wt\%$ of
the cell, are recovered by oxalate precipitation of
lanthanum. It was possible to recover $~95\%$ of the
lanthanum contained, which corresponds to about 60 $wt\%$ of
the total dissolved load.},
month = {Sep},
date = {2023-09-25},
organization = {9th International Conference on
Fundamentals $\&$ Development of Fuel
Cells, Ulm (Germany), 25 Sep 2023 - 27
Sep 2023},
subtyp = {After Call},
cin = {IEK-1},
cid = {I:(DE-Juel1)IEK-1-20101013},
pnm = {1231 - Electrochemistry for Hydrogen (POF4-123) / SOFC -
Solid Oxide Fuel Cell (SOFC-20140602)},
pid = {G:(DE-HGF)POF4-1231 / G:(DE-Juel1)SOFC-20140602},
typ = {PUB:(DE-HGF)6},
doi = {10.34734/FZJ-2023-03749},
url = {https://juser.fz-juelich.de/record/1016763},
}