nonsatisfied long-term stability, catalyst leaching, abrasion
of the immobilizate, and a wide particle distribution (instead
of a well-defined macroscopic size) in the case of powdered
first the cross-linking process was carried out only with
glutaraldehyde, but the resulting cross-linked enzymes
showed a drastically decreased activity (probably due to
deactivation of the enzyme). However, a combination of
glutaraldehyde and chitosan led to an improved cross-linked
enzyme which showed 89% of its original activity.
In a subsequent step, this cross-linked enzyme was
entrapped in a hydrogel matrix which is (mainly) based on
poly(vinyl alcohol). In this step a lens-shaped catalyst with
a well-defined particle diameter of 3 or 5 mm and a thickness
of 0.3-0.4 mm is produced. These lens-shaped hydrogels
are highly elastic and flexible toward mechanical treatment.10
The concept of this two-step immobilization method is shown
in Scheme 1, and a corresponding synthetic protocol is given
in the Supporting Information.
5
,6
immobilizates.
On the other hand, Vorlop et al. has recently developed a
highly efficient immobilization method for cells by entrap-
ping them in a hydrogel matrix mainly based on poly(vinyl
7
alcohol). This method represents a cheap, efficient, and
industrially feasible immobilization technique, which not only
shows negligible catalyst leaching but also gives macroscopi-
cally well-defined and highly flexible lens-shaped particles
with a high activity (type, LentiKats; diameter, 3-5 mm;
thickness, 300-400 µm).7 Several successful applications
of this concept have been previously reported by Vorlop and
co-workers, e.g., for the synthesis of itaconic acid and 1,3-
propanediol.7 It is noteworthy from an industrial point of
view that these lens-shaped hydrogels can easily be separated
a
c,d
(
due to a diameter of 3-5 mm), are suitable for stirred tank
Scheme 1. Two-Step Procedure for Entrapping
reactors, and show no abrasion as well as minimized
(R)-Oxynitrilases
diffusion limitations (due to low thickness of <0.5 mm). This
8
technology has been already commercialized by geniaLab.
We envisioned that this concept could be extended to a
suitable immobilization method for oxynitrilases (and more-
over for enzymes in general).
In the following we report the first application of LentiKat-
entrapped enzymes (here: oxynitrilases) in organic catalysis,
namely in the synthesis of (R)-mandelonitrile. For our studies
we used a nonpurified (R)-oxynitrilase for economical
9
reasons. To prepare an efficient entrapped oxynitrilase, a
two-step procedure has been chosen. In a first step, a cross-
linking process was carried out which led to an increased
molecular weight of the (cross-linked) enzymes. This cross-
linking procedure is necessary since enzymes with a mo-
lecular weight of 50000 maximum (as in the case of
oxynitrilases) would not be restrained in the hydrogels. At
(5) One of the rare exceptions of a very practical immobilization method
represents the production of (R)-mandelonitrile with the continuous
membrane reactor technique which is mainly applied for continuous
processes, see: (a) Vasic-Racki, D.; Jonas, M.; Wandrey, C.; Hummel, W.;
Kula, M.-R. Appl. Microbiol. Biotechnol. 1989, 31, 215-222. (b) Bom-
marius, A. S.; Drauz, K.; Groeger, U.; Wandrey, C. In Chirality in Industry;
Collins, A. N., Sheldrake, G. N., Crosby, J., Eds.; John Wiley & Sons Ltd:
New York, 1992; Chapter 20, pp 371-397.
(6) (a) Despite the high potential of immobilized biocatalysts, in a United
Nations publication from 1989, only eight industrial processes have been
reported which are based on immobilized enzymes or microbial cells, see:
Klyosov Report, A. A. UNIDO/IPTC. 93, V-89-61316. Order No. PB90-
Regarding the synthetic potential of the “catalytic cap-
sules”, investigations have been carried out using “free” and
entrapped oxynitrilases. In the presence of the free, non-
purified oxynitrilase with an activity of 15 U/mmol a
satisfactory result (95% ee, 85% yield) was obtained at pH
4.5 under biphasic conditions (Table 1, entry 1).4e
2
10360, 111 pp. (b) The manufacture of 7-aminocephalosporanic acid
represents (probably) the most important industrial process which is based
on the use of an immobilized enzyme.
(
7) (a) Jekel, M.; Buhr, A.; Willke, T.; Vorlop, K.-D. Chem. Eng.
Technol. 1998, 21, 275-278. (b) Wittlich, P.; Schlieker, M.; Jahnz, U.;
Willke, T.; Vorlop, K.-D. Proc. 9th Eur. Congr. Biotechnol. 1999, No.
P2762, ISBN 805215-1-5. (c) Welter, K.; Willke, T.; Vorlop, K.-D. SchrR
Nachwachsende Rohstoffe 1999, 14, 520-521. (d) Wittlich, P.; Schlieker,
M.; Lutz, J.; Reimann, C.; Willke, T.; Vorlop, K.-D. SchrR Nachwachsende
Rohstoffe 1999, 14, 524-532. (e) Durieux, A.; Nicolay, X.; Simon, J.-P.
Biotechnol. Lett. 2000, 22, 1679-1684.
11
When applying the entrapped catalyst (8.16 U/g) in the
model reaction, we were pleased to find thatsdespite
modifying the enzyme by cross-linking and entrappingsa
comparable result was obtained regarding enantioselectivity
as well as yield. The desired (R)-mandelonitrile was obtained
with 94% ee and 93% yield (Table 1, entry 2) which
(8) For information about commercial applications of this type of
immobilization technology as well as commercial products from geniaLab,
see: http://www.geniaLab.de.
(9) The experiments described herein have been carried out using a
nonpurified oxynitrilase purchased from ASA Spezialenzyme GmbH,
Braunschweig (specific activity, 13.6 U/mg proteine; amount of proteine,
(10) The physical properties of such type of lens-shaped hydrogels in
general have been described earlier; for details, see ref 7.
7
.6 mg/mL). Although purity and activity are somewhat lower compared
with those of other commercially available, highly purified oxynitrilases,
this enzyme was chosen on basis of cost.
(11) The reaction conditions for the preparation of the lens-shaped
hydrogels can be varied widely, e.g., resulting in a different catalyst loading.
1970
Org. Lett., Vol. 3, No. 13, 2001