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Improved Methodology for the Preparation of Chiral Amines

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H 2 , toluene, 25 °C, 4 h an ee <strong>of</strong> 96% with full conversion was reported <strong>for</strong> phenyl methyl N-<br />

aryl imine and 92% ee <strong>for</strong> phenyl ethyl N-aryl imnes (structure 1,2 , figure 2.3). Reducing <strong>the</strong><br />

catalyst loading to 0.5 mol % resulted in <strong>the</strong> same enantioselectivity. Lower catalyst loading<br />

(0.1 mol %) <strong>the</strong> hydrogen pressure had to increase to 50 bar to achieve <strong>the</strong> same ee with full<br />

conversion. He tested his system <strong>for</strong> substituted phenyl methyl N-aryl imines. The ee was<br />

96% <strong>for</strong> p-Me phenyl methyl N-aryl imine, <strong>for</strong> m-Me phenyl methyl N-aryl imine <strong>the</strong> ee was<br />

93% and <strong>for</strong> o-Me phenyl methyl N-aryl imine <strong>the</strong> ee was 94%. For o-OMe phenyl methyl N-<br />

aryl imine <strong>the</strong> ee was 90%, <strong>for</strong> p-OMe phenyl methyl N-aryl imine <strong>the</strong> ee was 94% and <strong>for</strong><br />

m-OMe phenyl methyl N-aryl imine <strong>the</strong> ee was 96% with full conversion in all cases<br />

(structure 3, figure 2.3).<br />

Pizzano tested Ir-phosphine–phosphites based catalysts <strong>for</strong> reduction <strong>of</strong> N-aryl imines. [30]<br />

Using 1.0 mol % <strong>of</strong> <strong>the</strong> catalyst (catalyst 11a, figure 2.4), 30 bar (436 psi) <strong>of</strong> H 2 , CH 2 Cl 2 , 25<br />

°C, 24 h an ee <strong>of</strong> 82% with complete conversion <strong>for</strong> phenyl methyl N-aryl imine was<br />

achieved (structure 1, figure 2.3). Later he used ano<strong>the</strong>r derivative <strong>of</strong> <strong>the</strong> catalyst (catalyst<br />

11b, figure 2.3) <strong>for</strong> reduction <strong>of</strong> substituted phenyl methyl N-aryl imine. For p-methyl phenyl<br />

methyl N-aryl imine <strong>the</strong> ee was 72%, <strong>for</strong> p-OMe phenyl methyl N-aryl imine <strong>the</strong> ee was 85%,<br />

<strong>for</strong> p-fluoro phenyl methyl N-aryl imine <strong>the</strong> ee was 79% and <strong>for</strong> p-chloro phenyl methyl N-<br />

aryl imine <strong>the</strong> ee was 82%. [31]<br />

Imamoto reduced N-aryl imines utilizing Ir-phosphine catalyst. [32] Using 0.5 mol % <strong>of</strong> <strong>the</strong><br />

catalyst (catalyst 12, figure 2.4), 1 bar (14.5 psi) <strong>of</strong> H 2 , CH 2 Cl 2 , 25 °C, 1.5 h, <strong>the</strong> ee was 99%<br />

with 95% isolated yield <strong>for</strong> phenyl methyl N-aryl imine (structure 1, figure 2.3). They tested<br />

reduction <strong>of</strong> p-OMe phenyl methyl N-aryl imine imines with 83% ee and 98% yield within 2<br />

h. For p-fluoro phenyl methyl N-aryl imine <strong>the</strong> ee was 84% with 92% yield within 1.5 h<br />

(structure 3, figure 2.3).<br />

Dervisi syn<strong>the</strong>sized a new Ir diphosphine catalyst {[(Ir (ddppm)-(COD)]PF 6 } and tested it <strong>for</strong><br />

<strong>the</strong> N-aryl imine reduction. [32] Using 1.0 mol % <strong>of</strong> <strong>the</strong> catalyst (catalyst 13, figure 2.4), 1 bar<br />

(14.5 psi) <strong>of</strong> H 2 , ClCH 2 CH 2 Cl, 25 °C, 24 h, <strong>the</strong> ee was 84% with 99% yield <strong>for</strong> phenyl<br />

methyl N-aryl imine (structure 1, figure 2.3). Operating at atmospheric pressure allowed <strong>the</strong><br />

hydrogenation to be carried using Schlenk technique instead <strong>of</strong> high pressure autoclaves.<br />

They expanded <strong>the</strong>ir investigation to include p-chloro phenyl methyl N-aryl imines which<br />

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