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(Table-1, No- 6). Next reaction temperature (Table-1, No-8-9) was investigated.<br />

Decrease of the reaction temperature resulted in lover yield (Table-1, No-9). Then the<br />

examination the catalyst effect on a reaction (Table-1, No-7-13) was done. However<br />

replacement of Cu(Oac)2 with CuSO4 resulted in lower yield (Table-1, No-11). While<br />

in case of Cu Powder (200 mesh) used only traces amount of desire product observed<br />

(Table-1, No-13). Moreover it was observed that the catalyst was mandatory for<br />

successfully performing the reaction, as no product was formed in the absence of the<br />

catalyst (Table-1, No-12). Finally optimum reaction conditions were achieved when a<br />

mixture of hydroxy salt, 1.2 equiv of phenyl acetylene, 5 mol % of Cu(Oac)2 in 1 ml<br />

of Ethenol : water (4: 1) was irradiated for 2 min at a ceiling temperature of 100 o C<br />

applying a maximum power of 36 W, affording the desired compound in 90 % yield<br />

(Table 1 No-8). The protocol was checked with conventional condition providing<br />

lower yield of 24 % of after 24 hrs.<br />

N<br />

N N<br />

Ph OH<br />

N3 One-Pot microwave-assisted<br />

Cu salt (mol %)<br />

Br<br />

3<br />

N2H4 (equiv.)<br />

Ph (1.2 equiv.)<br />

EtOH : Water (4:1, 1ml)<br />

Ph<br />

No.<br />

time<br />

(min)<br />

N<br />

N<br />

H<br />

NH<br />

5<br />

N N<br />

N<br />

temp ( o C) Cu salt (mol %) yield (%) b<br />

1 c 20 100 °C Cu(Oac)2, 10 51<br />

2 d 20 100 °C Cu(Oac)2, 10 84<br />

3 20 100 °C Cu(Oac)2, 10 86<br />

4 10 100 °C Cu(Oac)2, 10 80<br />

5 5 100 °C Cu(Oac)2, 10 90<br />

6 2 100 °C Cu(Oac)2, 10 90<br />

7 1 100 °C Cu(Oac)2, 10 53<br />

8 2 100 °C Cu(Oac)2, 5 90<br />

9 2 90 °C Cu(Oac)2, 5 73<br />

10 2 100 °C Cu(Oac)2, 2 57<br />

11 2 100 °C CuSO4.5H2O, 5 67<br />

Ph

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