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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