Oxymethylene dimethyl
ethers (OME
n
)
have high potential as diesel fuels or blending components due to
their promising combustion properties and can be produced from hydrogen
(H2) and carbon dioxide (CO2) by combining existing
process concepts. However, such a process chain has not been analyzed
in detail yet, so its performance and bottlenecks are unknown. In
this second part of our two-part article, we analyze a process chain
for production of the longer chain variant OME3–5 from renewable H2 and green CO2 via trioxane
and OME1. We simulate in Aspen Plus using detailed thermodynamic
models with coupled oligomerization reactions and rigorous unit operation
models. The overall exergy efficiency of OME3–5 production
from H2 and CO2 using established process concepts
is 53%. Therein, the trioxane process step has the highest losses
due to its high heat demand. Considering a pinch-based heat integration
throughout the entire process chain its total heat demand can be reduced
by 16%. Thus, the exergy efficiency increases to 54%. This is still
significantly lower compared to the production of other alternative
fuels like OME1, methane, and dimethyl ether. Thus, more
efficient processes, e.g., by avoiding trioxane production, are required.