The process being studied
in this project has several advantages over existing technologies
that convert biomass waste into SNG:
-
Process efficiency is possibly higher (eta = 0.6 ÷
0.7)
-
No need for drying first – the moisture is the reaction
media itself
-
Products are clean water and SNG only – all possible
hormones and bioactive proteins (e.g. prions) are destroyed.
There is no solid residue that needs to be dried and burnt as
hazardous waste.
-
Reaction side-product (carbon dioxide) can be easily and economically
separated from the SNG as most of the CO2 is dissolved
in water at system pressure that carries the unburnable gas
out of the system.
The ability of supercritical water to destroy potentially hazardous
substances is also used in the so-called SCWO (supercritical water
oxidation) processes. The difference to our technology is that with
SCWO, the organic material is oxidized ultimately up to CO2
and therefore made chemically inactive, whereas we focus on the
conversion to SNG.
Projects
The aim of this PhD Study is to develop a process capable
of producing synthetic natural gas (SNG) from wet biomass (waste
wood slurries, manure and sewage sludge) by hydrothermal gasification.
For the case of manure, the dissolved salts are collected as mineral
nutriments for further applications. The SNG may be used for heating
purposes or for the use as clean fuel in natural gas vehicles (Vision
Ecogas).

Approach
Several pathways are combined within this PhD project:
-
Development of analytical methods to characterize the biomass
in a complete way with respect to organics, inorganics and elemental
composition
-
Co-Development and testing of several gasification catalysts
-
Development of tools to study the gasification visually at
process conditions (400°C, 30 MPa)
-
Design of a continuously operating plant capable of processing
real biomass up to 10 wt%
-
Modelling of several system components, e.g. salt separation
with FEMLAB.
-
Experiments with real biomass and biomass model substances
in batch wise and continuously operating plants
-
System- and economic analyses to justify the process not only
in an ecologic way (it is CO2- neutral)
Exemplary Results
In the batch reactor, wood and manure slurries were gasified in
presence of a gasification catalyst on nickel basis. See the impressive
conversion in the following picture:
Reactant mixture and liquid product:

The products gained with catalytic gasification
in our batch reactor corresponded to the thermodynamic equilibrium
composition (the chemically reachable composition), as can be
seen in the following graph:
Shown: methane concentration in the product gas
as a function of residence time. Process conditions: 400°C,
30 MPa. After a residence time of more that 20 min. (experiment
HB400R06), the gas composition was nearly at the chemical equilibrium.
If there is no catalyst used at all (experiment HB400NC1), less
than 15 vol% methane were found in the product gas phase.For further
results, please visit our poster
section and list
of publications.
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