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3
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0036090494
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Baleizao C., Gigante B., Sabater M.J., Garcia H., Corma A. Appl. Catal. A: Gen. 228:2002;279-288.
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(2002)
Appl. Catal. A: Gen.
, vol.228
, pp. 279-288
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Baleizao, C.1
Gigante, B.2
Sabater, M.J.3
Garcia, H.4
Corma, A.5
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10
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85030936714
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Silica gel 60 for preparative column chromatography was bought from Fluka.
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Silica gel 60 for preparative column chromatography was bought from Fluka.
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11
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85030940434
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A catalyst/silica ratio of 1.25 wt%, corresponding to 20 μmol/gram, showed optimal performance. Based on a screening experiment in which a range of catalyst loadings were tested, this sample combined low leaching degrees with good enantioselectivity. Higher catalyst/silica ratios of 2.5, 5.0 and 10 wt% suffered from leaching varying between 5 and 30%.
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A catalyst/silica ratio of 1.25 wt%, corresponding to 20 μmol/gram, showed optimal performance. Based on a screening experiment in which a range of catalyst loadings were tested, this sample combined low leaching degrees with good enantioselectivity. Higher catalyst/silica ratios of 2.5, 5.0 and 10 wt% suffered from leaching varying between 5 and 30%.
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13
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85030939564
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All enantiomeric/diastereomeric excesses were determined by chiral GC on a Chrompack-CHIRASIL-DEX CB column (0.32 mm×0.25 μm×25 m) using FID detection.
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All enantiomeric/diastereomeric excesses were determined by chiral GC on a Chrompack-CHIRASIL-DEX CB column (0.32 mm×0.25 μm×25 m) using FID detection.
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15
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85030935382
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3+ ions have two absorption bands at about 430 and 614 nm due to d-d transitions.
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3+ ions have two absorption bands at about 430 and 614 nm due to d-d transitions.
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16
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85030951475
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In an homogeneous reference experiment with 375 ppm of Cr(salen) carried out in hexane, the conversion and e.e. after 24 h was 25 and 26%, respectively. Consequently, under the conditions described in Table 1, the amount of complex corresponding to a degree of leaching of 1% should not contribute significantly to the conversion.
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In an homogeneous reference experiment with 375 ppm of Cr(salen) carried out in hexane, the conversion and e.e. after 24 h was 25 and 26%, respectively. Consequently, under the conditions described in Table 1, the amount of complex corresponding to a degree of leaching of 1% should not contribute significantly to the conversion.
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17
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85030939326
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During solvent evaporation the catalyst precipitates, while both epoxide and ring opened products can be extracted in hexane, in which the catalyst-precipitate will not dissolve.
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During solvent evaporation the catalyst precipitates, while both epoxide and ring opened products can be extracted in hexane, in which the catalyst-precipitate will not dissolve.
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