Thermal-enzymatic Hydrolysis of lignocellulosic Biomass for the
Production of Platform Chemicals
Wienke Hüppop
With growing shortage of global oil resources and increasingly strict environmental regulations, industry and research become more interested in sustainable sources of raw materials. In this context, not only fossil fuel substitutes but in particular alternatives for oil-based polymers and chemicals have to be developed. For some years now, products from starch based biomass have been used, e.g. biodiesel or
bioethanol. However, these products are in strong competition with food and animal feed industry. 2nd generation Biorefineries are an advancement of this concept. Here, lignocellulosic residues from agriculture and forestry are processed. The three major constituents of the lignocelluloses (cellulose, hemicellulose and lignin) are split into sugar monomers and lignin – so-called platform chemicals which are
now available for further processing steps.
Type and composition of the applied biomass strongly varies by season and by cultivation. For commercial
application of the biorefinery concept, the development of a robust and flexible process is essential. At the Institute of Thermal Separation Processes, wheat straw is splitted thermally and enzymatically into its constituents in a single high-pressure fixed-bed reactor. The major benefits of this process are the avoidance of aggressive solvents and chemical additives as well as the low plant complexity.
In current second generation biorefineries, bioethanol from glucose usually is the target product. Most of the existing biorefinery plants only thermally recycle the hemicelluloses and lignin fractions in order to cover their energy demand for ethanol production. However, the processing of lignocellulosic feedstock also allows the production of high-value co-products from hemicellulose and lignin — the key to a costeffective and competitive process. In the context of the BMBF-project „Bioraffinerie 2021“ this research project deals with the characterization of the fixed-bed process, focusing particularly on lignin. Previous works demonstrated the operability of the process at lab scale and small demonstration scale. Further experimental studies as well as process modeling and simulation need to be executed in order characterize the mechanisms inside the reactor in more detail and to investigate scale-up possibilities.