9864
J. Am. Chem. Soc. 2000, 122, 9864-9865
Platinum-Catalyzed Enantioselective Hydrogenation
of r-Ketoesters: An Unprecedented Surface Reaction
of Methyl Pyruvate
†
,†
Jonathan M. Bonello, Richard M. Lambert,*
‡
‡
Niklaus K u¨ nzle, and Alfons Baiker
Department of Chemistry, UniVersity of Cambridge
Cambridge CB2 1EW, United Kingdom
Laboratory of Technical Chemistry
Swiss Federal Institute of Technology
ETH-Zentrum, CH-8092 Z u¨ rich, Switzerland.
ReceiVed May 17, 2000
Figure 1. Fixed-bed reactor transient kinetic experiment of platinum-
catalyzed hydrogenation of methyl pyruvate (MP). Feed conditions during
Enantioselective heterogeneous catalysts are rarities although
their inherent technical importance is huge. Under appropriate
conditions they afford a high degree of stereochemical control
and large rate enhancement effects. Indeed, chiral heterogeneous
catalysis is a subject of indisputable importance in current chemi-
cal research. Such reactions constitute a relatively unexplored field
whose theoretical and practical implications are potentially far
reaching. Although the number of known systems is growing,
the subject as a whole remains, nevertheless, at a relatively early
different periods of time on stream are indicated. Conditions: Pt/Al
2 3
O
catalyst 500 mg; hydrogen pressure 50 bar; flow rates, hydrogen 5.2
-
1
-1
mL‚min , methyl pyruvate 0.5 mL‚min ; room temperature.
1,2
stage of development as is evident from recent reviews. This
is especially true in regard to fundamental studies of the surface
phenomena involved, even in the case of the most studied reac-
tions,includingtheonewhichisthesubjectofthiscommunications
the asymmetric hydrogenation of R-ketoesters on chirally modified
Pt surfaces.3 Although considerable effort has been expended
in the past decade to gain a detailed insight into the functioning
of this system, there are still a number of key issues requiring
clarification. Among these is the question of why the behavior
of this catalytic system depends on the sequence of introduction
of the reactants (methyl pyruvate, hydrogen) and modifier, as
-5
6
demonstrated earlier by transient kinetic measurements.
We have employed a combination of complementary methods
involving solution phase kinetic measurements on a practical
dispersed catalyst and studies on a Pt{111} single-crystal surface
by means of STM and NEXAFS. We show that in the absence
of the cinchona modifier and under conditions of hydrogen
starvation the catalyst deactivates due to blocking of the platinum
surface by self-condensation of the methyl pyruvate reactant.
Catalytic studies were performed using a 4 mm inner diameter
stainless steel tubular fixed-bed reactor system. Details of the
Figure 2. STM image (raw data) of methyl pyruvate on Pt{111} at
-5
2
98 K in the presence of a background pressure of 2 × 10 mbar
hydrogen [constant current mode, 1000 Å × 1000 Å, Ugap ) -1 V, I
T
)
10 nA].
reactor, analysis system, and experimental technique are given
7
elsewhere. The catalyst (5 wt % Pt/Al
2 3
O , Engelhard 4759) was
and a H pressure of 50 bar. STM experiments were carried out
2
pretreated before use in a separate reactor by flushing with 12
using an Omicron UHV STM-1 instrument operating under
-
1
-11
mL‚min
reductive treatment in H
temperature. After being cooled to room temperature in H
N
2
(99.995%) at 673 K for 30 min, followed by a
(99.999%) for 90 min at the same
, the
ultrahigh vacuum conditions (base pressure 5 × 10 mbar). This
2
apparatus incorporated LEED and Auger spectroscopy facilities
8
2
used for surface characterization prior to adsorption experiments.
catalyst was immediately transferred to the reactor and held under
nitrogen. Catalyst (500 mg) was applied, resulting in a bed length
of 30 mm. Methyl pyruvate (MP, Fluka, 97%) was used without
further purification. The reactor was operated at room temperature
Images were acquired in constant current mode and control
experiments indicated that there were no tip-induced artifacts:
neither molecular displacements, nor adsorbate decomposition.
The reaction was started by pre-flushing the reactor with hydro-
-
1
gen (5.2 mL‚min ) for 5 min and then adding methyl pyruvate
*
Address correspondence to this author.
University of Cambridge.
-
1
†
(0.5 mL‚min ). After 30 min the hydrogen flow was stopped
and the reactor was flushed with pure methyl pyruvate for 30
min. After this sequence the reaction was started again by adding
‡
Swiss Federal Institute of Technology.
(
1) Baiker, A.; Blaser, H. U. Handbook of Heterogeneous Catalysis; VCH-
Publishers: Weinheim, 1997; Vol. 5, pp 2422-2436.
-
1
H
2
(5.2 mL‚min ) for 30 min. Figure 1 illustrates the effect of
(
(
2) Baiker, A. Curr. Opin. Solid State Mater. Sci. 1998, 3(1), 86-93.
3) Blaser, H. U.; Jallet, H. P.; M u¨ ller, M.; Studer, M. Catal. Today 1997,
exposing the catalyst to methyl pyruvate in the absence of H . It
2
3
7, 441-463.
is apparent that catalytic activity was strongly suppressed as a
result of the hydrogen starvation step. Conversion of pyruvate to
methyl lactate fell from 80% to ∼ 40%. The cause of this
(8) Baddeley, C. J.; Stephenson, A. W.; Hardacre, C.; Tikhov, M.; Lambert,
R. M. Phys. ReV. B 1997, 56, 12589-12598.
(
(
(
4) Wells, P. B.; Wilkinson, A. G. Top. Catal. 1998, 5, 39-50.
5) Baiker, A. J. Mol. Catal. 1997, 115, 473-493.
6) Margitfalvi, J. L.; Minder, B.; Talas, E.; Botz, L.; Baiker, A. Stud. Surf.
Sci. Catal. 1993, 75, 2471-2474.
(
7) K u¨ nzle, N.; Hess, R.; Mallat, T.; Baiker, A. J. Catal. 1999, 186, 239-
2
41.
1
0.1021/ja0017211 CCC: $19.00 © 2000 American Chemical Society
Published on Web 09/22/2000