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Lipase-Catalyzed Baeyer-Villiger Oxidation of Cellulose-Derived Levoglucosenone into (S)-γ-Hydroxymethyl-α,β-Butenolide: Optimization by Response Surface Methodology.

Teixeira AR, Flourat AL, Peru AA, Brunissen F, Allais F - Front Chem (2016)

Bottom Line: Response surface methodology (RSM), based on central composite face-centered (CCF) design, was employed to evaluate the factors effecting the enzyme-catalyzed reaction: pka of solid buffer (7.2-9.6), LGO concentration (0.5-1 M) and enzyme loading (55-285 PLU.mmol(-1)).Enzyme loading and pka of solid buffer were found to be important factors to the reaction efficiency (as measured by the conversion of LGO) while only the later had significant effects on the enzyme recyclability (as measured by the enzyme residual activity).A good agreement between experimental and predicted values was obtained and the model validity confirmed (p < 0.05).

View Article: PubMed Central - PubMed

Affiliation: Chaire Agro-Biotechnologies Industrielles, AgroParisTechReims, France; UMR GENIAL, AgroParisTech, Institut National de la Recherche Agronomique, Université Paris-SaclayMassy, France.

ABSTRACT
Cellulose-derived levoglucosenone (LGO) has been efficiently converted into pure (S)-γ-hydroxymethyl-α,β-butenolide (HBO), a chemical platform suited for the synthesis of drugs, flavors and antiviral agents. This process involves two-steps: a lipase-catalyzed Baeyer-Villiger oxidation of LGO followed by an acid hydrolysis of the reaction mixture to provide pure HBO. Response surface methodology (RSM), based on central composite face-centered (CCF) design, was employed to evaluate the factors effecting the enzyme-catalyzed reaction: pka of solid buffer (7.2-9.6), LGO concentration (0.5-1 M) and enzyme loading (55-285 PLU.mmol(-1)). Enzyme loading and pka of solid buffer were found to be important factors to the reaction efficiency (as measured by the conversion of LGO) while only the later had significant effects on the enzyme recyclability (as measured by the enzyme residual activity). LGO concentration influences both responses by its interaction with the enzyme loading and pka of solid buffer. The optimal conditions which allow to convert at least 80% of LGO in 2 h at 40°C and reuse the enzyme for a subsequent cycle were found to be: solid buffer pka = 7.5, [LGO] = 0.50 M and 113 PLU.mmol(-1) for the lipase. A good agreement between experimental and predicted values was obtained and the model validity confirmed (p < 0.05). Alternative optimal conditions were explored using Monte Carlo simulations for risk analysis, being estimated the experimental region where the LGO conversion higher than 80% is fulfilled at a specific risk of failure.

No MeSH data available.


Related in: MedlinePlus

Contour plots of (A) LGO conversion and (B) enzyme residual activity.
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Figure 4: Contour plots of (A) LGO conversion and (B) enzyme residual activity.

Mentions: The relationships between variables and responses can be better understood by examining the contour plots (Figure 4) generated from the models predicting the LGO conversion and enzyme residual activity responses (Equations 3 and 5, respectively). The contour plots can provide the contour lines of the independent variables (xi) that have the same response value Yi.


Lipase-Catalyzed Baeyer-Villiger Oxidation of Cellulose-Derived Levoglucosenone into (S)-γ-Hydroxymethyl-α,β-Butenolide: Optimization by Response Surface Methodology.

Teixeira AR, Flourat AL, Peru AA, Brunissen F, Allais F - Front Chem (2016)

Contour plots of (A) LGO conversion and (B) enzyme residual activity.
© Copyright Policy
Related In: Results  -  Collection

License
Show All Figures
getmorefigures.php?uid=PMC4835721&req=5

Figure 4: Contour plots of (A) LGO conversion and (B) enzyme residual activity.
Mentions: The relationships between variables and responses can be better understood by examining the contour plots (Figure 4) generated from the models predicting the LGO conversion and enzyme residual activity responses (Equations 3 and 5, respectively). The contour plots can provide the contour lines of the independent variables (xi) that have the same response value Yi.

Bottom Line: Response surface methodology (RSM), based on central composite face-centered (CCF) design, was employed to evaluate the factors effecting the enzyme-catalyzed reaction: pka of solid buffer (7.2-9.6), LGO concentration (0.5-1 M) and enzyme loading (55-285 PLU.mmol(-1)).Enzyme loading and pka of solid buffer were found to be important factors to the reaction efficiency (as measured by the conversion of LGO) while only the later had significant effects on the enzyme recyclability (as measured by the enzyme residual activity).A good agreement between experimental and predicted values was obtained and the model validity confirmed (p < 0.05).

View Article: PubMed Central - PubMed

Affiliation: Chaire Agro-Biotechnologies Industrielles, AgroParisTechReims, France; UMR GENIAL, AgroParisTech, Institut National de la Recherche Agronomique, Université Paris-SaclayMassy, France.

ABSTRACT
Cellulose-derived levoglucosenone (LGO) has been efficiently converted into pure (S)-γ-hydroxymethyl-α,β-butenolide (HBO), a chemical platform suited for the synthesis of drugs, flavors and antiviral agents. This process involves two-steps: a lipase-catalyzed Baeyer-Villiger oxidation of LGO followed by an acid hydrolysis of the reaction mixture to provide pure HBO. Response surface methodology (RSM), based on central composite face-centered (CCF) design, was employed to evaluate the factors effecting the enzyme-catalyzed reaction: pka of solid buffer (7.2-9.6), LGO concentration (0.5-1 M) and enzyme loading (55-285 PLU.mmol(-1)). Enzyme loading and pka of solid buffer were found to be important factors to the reaction efficiency (as measured by the conversion of LGO) while only the later had significant effects on the enzyme recyclability (as measured by the enzyme residual activity). LGO concentration influences both responses by its interaction with the enzyme loading and pka of solid buffer. The optimal conditions which allow to convert at least 80% of LGO in 2 h at 40°C and reuse the enzyme for a subsequent cycle were found to be: solid buffer pka = 7.5, [LGO] = 0.50 M and 113 PLU.mmol(-1) for the lipase. A good agreement between experimental and predicted values was obtained and the model validity confirmed (p < 0.05). Alternative optimal conditions were explored using Monte Carlo simulations for risk analysis, being estimated the experimental region where the LGO conversion higher than 80% is fulfilled at a specific risk of failure.

No MeSH data available.


Related in: MedlinePlus