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1.
Org Biomol Chem ; 13(6): 1634-8, 2015 Feb 14.
Article in English | MEDLINE | ID: mdl-25519974

ABSTRACT

A chemoenzymatic two-step cascade process, with both steps having incompatible reaction conditions, was successfully performed in continuous flow. The chemoenzymatic aqueous formation of cyanohydrins was integrated with a subsequent organic phase protection step in a single flow process utilising a membrane-based phase separation module. The wider applicability of our setup was demonstrated with the synthesis of nine protected cyanohydrin derivatives, all obtained in good yields and high to excellent enantioselectivity.


Subject(s)
Acetonitriles/chemical synthesis , Acetonitriles/chemistry , Molecular Structure , Stereoisomerism
2.
Beilstein J Org Chem ; 9: 1813-8, 2013.
Article in English | MEDLINE | ID: mdl-24062847

ABSTRACT

Ethyl diazoacetate is a versatile compound in organic chemistry and frequently used on lab scale. Its highly explosive nature, however, severely limits its use in industrial processes. The in-line coupling of microreactor synthesis and separation technology enables the synthesis of this compound in an inherently safe manner, thereby making it available on demand in sufficient quantities. Ethyl diazoacetate was prepared in a biphasic mixture comprising an aqueous solution of glycine ethyl ester, sodium nitrite and dichloromethane. Optimization of the reaction was focused on decreasing the residence time with the smallest amount of sodium nitrite possible. With these boundary conditions, a production yield of 20 g EDA day(-1) was achieved using a microreactor with an internal volume of 100 µL. Straightforward scale-up or scale-out of microreactor technology renders this method viable for industrial application.

3.
ChemSusChem ; 5(2): 289-92, 2012 Feb 13.
Article in English | MEDLINE | ID: mdl-22134987

ABSTRACT

Epoxidation of both terminal and non-terminal olefins with peroxy acids is a well-established and powerful tool in a wide variety of chemical processes. In an additional step, the epoxide can be readily converted into the corresponding trans-diol. Batch-wise scale-up, however, is often troublesome because of the thermal instability and explosive character of the peroxy acids involved. This article describes the design and semi-automated optimization of a continuous flow process and subsequent scale-up to preparative production volumes in an intrinsically safe manner.


Subject(s)
Alkenes/chemistry , Microtechnology/methods , Epoxy Compounds/chemistry , Hydroxylation , Safety , Solvents/chemistry , Temperature , Time Factors
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