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@PHDTHESIS{Albrecht:1023677,
author = {Albrecht, Pascal},
othercontributors = {Klankermayer, Jürgen and Oppel, Iris Marga},
title = {{D}evelopment and upscaling of the catalytic urea synthesis
from formamide and ammonia, and the hydrogenation of
levulinic acid},
school = {RWTH Aachen University},
type = {Dissertation},
address = {Aachen},
publisher = {RWTH Aachen University},
reportid = {RWTH-2025-10661},
pages = {1 Online-Ressource : Illustrationen},
year = {2025},
note = {Veröffentlicht auf dem Publikationsserver der RWTH Aachen
University 2026; Dissertation, RWTH Aachen University, 2025},
abstract = {This thesis deals with the development and design of
technical laboratory plants to perform catalytic urea
synthesis and levulinic acid hydrogenation. The starting
point is a novel catalytic system that enables the effective
production of urea starting from carbon monoxide or carbon
dioxide as the C1 building block via the intermediate
formamide. For the hydrogenation of organic carboxylic
acids, and in particular bio-based levulinic acid, a
tailor-made ruthenium-triphos catalyst was used, which
because of its unique properties, enables this extremely
demanding chemical transformation. Based on previous
fundamental catalysis research on small scale, systematic
optimization studies were carried out with the aim of
maximizing the product yields and catalyst recycling options
in the translation process. Within the scope of this thesis,
the specific requirements for the plants, the selection of
suitable components and precise control of the process
parameters were addressed in detail. Chapter 2.1 discusses
the novel possibility to produce urea and the subsequent
translation to a mini plant. The focus was on the central
reaction pathway for urea synthesis starting from formamide.
The reaction parameters temperature, time, as well as the
amounts of reagents used were investigated on a larger scale
at a laboratory plant tailored for two reaction pathways,
eventually allowing to determine the optimal process
conditions for maximum product yield. Chapter 2.2 deals with
the challenge to establish a complete value chain starting
from biomass via the platform chemical levulinic acid to
various valuable consumer products. The hydrogenation of
levulinic acid, which is in the focus of this thesis, was
transferred to a larger scale at a tailored plant. To
optimize the product yields of this process, the complex
interaction of reaction parameters time, hydrogen pressure,
temperature, as well as substrate and catalyst amounts were
investigated. The levulinic acid produced in the biorefinery
of the Institute of Applied Process Engineering at RWTH
Aachen University with a purity of approximately $75wt\%$
was successfully converted directly into γ-valerolactone,
1,4-pentanediol, and 2-methyltetrahydrofuran. Finally, a
catalyst immobilization concept was developed that can be
used in the future for the continuous hydrogenation of
levulinic acid in flow reactors.},
cin = {154310 / 150000},
ddc = {540},
cid = {$I:(DE-82)154310_20190725$ / $I:(DE-82)150000_20140620$},
typ = {PUB:(DE-HGF)11},
doi = {10.18154/RWTH-2025-10661},
url = {https://publications.rwth-aachen.de/record/1023677},
}