The fermentation for succinic acid production outperforms other methods by low energy consumption and environmental benignity
with the resulting products mainly as disodium succinate (DSA). By directly esterifying DSA using CO
2
and CH
3
OH
it is expected to avoid the use of inorganic acids. By high-resolution mass spectrometry analysis and theoretical calculation
this study establishes that the reaction consists of three steps
i.e.
first forming 3-carboxypropanoate
then monomethyl succinate (MMS)
and finally dimethyl succinate (DMS). A detailed kinetic analysis is further performed
the results demonstrate that the transformation of DSA to MMS is regarded to be a second-order reaction for reactant DSA
while the transformation of MMS to DMS is a first-order reaction for reactant MMS. The activation energy for the generation of MMS from DSA is 37.15 kJmol
-1
and that for the generation of DMS from MMS is 85.80 kJmol
-1
indicating the latter one is the rate-determining step.
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Thermal decomposition behavior and kinetics of magnesite under carbon dioxide atmosphere
Heterogeneously catalyzed self-condensation of n-butanal
Investigation of the formation processes of CO2 hydrate films on the interface of liquid carbon dioxide with humic acids solutions
Effect of solvent on the initiation mechanism of living anionic polymerization of styrene: A computational study
Efficient conversion of CO2 into cyclic carbonates under atmospheric by halogen and metal-free poly(ionic liquid)s
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Related Institution
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Nikolaev Institute of Inorganic Chemistry SB RAS, Novosibirsk 630090, Russian Federation
Department of Petroleum Engineering, Kazan Federal University, Kazan 420008, Russian Federation