Peroxygenase-Driven Ethylbenzene Hydroxylation in a Rotating Bed Reactor

Publikation: Beitrag in FachzeitschriftArtikelForschungPeer-Review

Autoren

  • Markus Hobisch
  • Piera De Santis
  • Simona Serban
  • Alessandra Basso
  • Emil Byström
  • Selin Kara

Organisationseinheiten

Externe Organisationen

  • Aarhus University
  • Purolite Ltd.
  • SpinChem AB
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Details

OriginalspracheEnglisch
Seiten (von - bis)2761-2765
Seitenumfang5
FachzeitschriftOrganic Process Research & Development
Jahrgang26
Ausgabenummer9
Frühes Online-Datum11 Aug. 2022
PublikationsstatusVeröffentlicht - 16 Sept. 2022

Abstract

The ability of unspecific peroxygenase (UPO) to hydroxylate a wide range of substrates with just H2O2 as a cosubstrate has attracted a great deal of attention in biocatalytic research. The enzyme's intrinsic limitation to be inactivated by excess amounts of the oxidative cosubstrate has been tackled with in or ex situ hydrogen peroxide (H2O2) provision strategies. In this paper, we present the application of the covalently immobilized UPO mutant PaDa-I in a rotating bed reactor for the hydroxylation of ethylbenzene in a two-liquid-phase system. By monitoring product formation in the organic phase and H2O2 concentration in the aqueous phase, the multiphasic reaction was optimized. Over 58 h, up to 414 mM (R)-1-phenylethanol was accumulated in the organic phase, corresponding to a productivity of 436 mg L-1 h-1 and a selectivity for the alcohol product over the overoxidated ketone product of 62%. It was found that the overoxidation of (R)-1-phenylethanol to acetophenone resulted in part from the H2O2 concentration in the aqueous phase but mainly from the concentration of the target alcohol. Therefore, a repetitive batch was performed over five times for 13 h with similar product concentrations and formation rates as in the conventional approach but a considerably higher selectivity of 79%.

ASJC Scopus Sachgebiete

Zitieren

Peroxygenase-Driven Ethylbenzene Hydroxylation in a Rotating Bed Reactor. / Hobisch, Markus; Santis, Piera De; Serban, Simona et al.
in: Organic Process Research & Development, Jahrgang 26, Nr. 9, 16.09.2022, S. 2761-2765.

Publikation: Beitrag in FachzeitschriftArtikelForschungPeer-Review

Hobisch M, Santis PD, Serban S, Basso A, Byström E, Kara S. Peroxygenase-Driven Ethylbenzene Hydroxylation in a Rotating Bed Reactor. Organic Process Research & Development. 2022 Sep 16;26(9):2761-2765. Epub 2022 Aug 11. doi: 10.1021/acs.oprd.2c00211
Hobisch, Markus ; Santis, Piera De ; Serban, Simona et al. / Peroxygenase-Driven Ethylbenzene Hydroxylation in a Rotating Bed Reactor. in: Organic Process Research & Development. 2022 ; Jahrgang 26, Nr. 9. S. 2761-2765.
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abstract = "The ability of unspecific peroxygenase (UPO) to hydroxylate a wide range of substrates with just H2O2 as a cosubstrate has attracted a great deal of attention in biocatalytic research. The enzyme's intrinsic limitation to be inactivated by excess amounts of the oxidative cosubstrate has been tackled with in or ex situ hydrogen peroxide (H2O2) provision strategies. In this paper, we present the application of the covalently immobilized UPO mutant PaDa-I in a rotating bed reactor for the hydroxylation of ethylbenzene in a two-liquid-phase system. By monitoring product formation in the organic phase and H2O2 concentration in the aqueous phase, the multiphasic reaction was optimized. Over 58 h, up to 414 mM (R)-1-phenylethanol was accumulated in the organic phase, corresponding to a productivity of 436 mg L-1 h-1 and a selectivity for the alcohol product over the overoxidated ketone product of 62%. It was found that the overoxidation of (R)-1-phenylethanol to acetophenone resulted in part from the H2O2 concentration in the aqueous phase but mainly from the concentration of the target alcohol. Therefore, a repetitive batch was performed over five times for 13 h with similar product concentrations and formation rates as in the conventional approach but a considerably higher selectivity of 79%.",
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AU - Hobisch, Markus

AU - Santis, Piera De

AU - Serban, Simona

AU - Basso, Alessandra

AU - Byström, Emil

AU - Kara, Selin

N1 - Funding Information: This project has received funding from the European Union’s Horizon 2020 research and innovation program under the Marie Skłodowska–Curie Grant Agreement No. 764920. Independent Research Fund Denmark (PHOTOX- f project, Grant No. 9063-00031B) was gratefully acknowledged for the grant funding.

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N2 - The ability of unspecific peroxygenase (UPO) to hydroxylate a wide range of substrates with just H2O2 as a cosubstrate has attracted a great deal of attention in biocatalytic research. The enzyme's intrinsic limitation to be inactivated by excess amounts of the oxidative cosubstrate has been tackled with in or ex situ hydrogen peroxide (H2O2) provision strategies. In this paper, we present the application of the covalently immobilized UPO mutant PaDa-I in a rotating bed reactor for the hydroxylation of ethylbenzene in a two-liquid-phase system. By monitoring product formation in the organic phase and H2O2 concentration in the aqueous phase, the multiphasic reaction was optimized. Over 58 h, up to 414 mM (R)-1-phenylethanol was accumulated in the organic phase, corresponding to a productivity of 436 mg L-1 h-1 and a selectivity for the alcohol product over the overoxidated ketone product of 62%. It was found that the overoxidation of (R)-1-phenylethanol to acetophenone resulted in part from the H2O2 concentration in the aqueous phase but mainly from the concentration of the target alcohol. Therefore, a repetitive batch was performed over five times for 13 h with similar product concentrations and formation rates as in the conventional approach but a considerably higher selectivity of 79%.

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