chapter 2 palladium catalysts in suzuki cross- coupling reaction
chapter 2 palladium catalysts in suzuki cross- coupling reaction
chapter 2 palladium catalysts in suzuki cross- coupling reaction
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11). PhB(OH)2 of different sources was tested aga<strong>in</strong> under the improved <strong>reaction</strong><br />
conditions which were applied <strong>in</strong> the case of entry 7. The result from the Aldrich<br />
product was comparable with that obta<strong>in</strong>ed with Merck’s whereas the reagent from<br />
Fluka resulted about 10% lower yield (Table 5.4, entries 12, 13).<br />
To understand the role of the zeolite itself <strong>in</strong> <strong>reaction</strong>s (i.e., whether it plays an<br />
active role), the <strong>reaction</strong> was performed with only ~60 mg of Pd-loaded zeolite <strong>in</strong> the<br />
absence of extra amount of zeolite. Surpris<strong>in</strong>gly, no product formation was observed<br />
(Table 5.5, entry 1). Moreover, when the zeolite additive which was vacuum dried at<br />
140 °C for 2 h prior to the <strong>reaction</strong> (Table 5.5, entry 2) was used, the catalyst displayed<br />
no activity. As a result of these data, we concluded that the <strong>in</strong>tr<strong>in</strong>sic water content of the<br />
zeolite (which was measured to be around 23% based on the weight loss dur<strong>in</strong>g vacuum<br />
dry<strong>in</strong>g at 140 °C for 2 h) was crucial for the activity of the system. When 230 mg of<br />
water (which is equal to the amount of water that would be <strong>in</strong>troduced by the addition<br />
of 1 g of NaY zeolite <strong>in</strong> as-received form) was added <strong>in</strong>to <strong>reaction</strong> medium without the<br />
zeolite additive, a moderate product formation (61%) was observed (Table 5.5, entry 3),<br />
<strong>in</strong>dicat<strong>in</strong>g that the <strong>reaction</strong> can operate only <strong>in</strong> moist medium and, suggest<strong>in</strong>g the<br />
existence of a synergism between water and zeolite comb<strong>in</strong>ation.<br />
Also, the effect of zeolite amount (<strong>in</strong> as-received form) was exam<strong>in</strong>ed at 140 ºC<br />
(Table 5.5, entries 4-7). The yield formation was modest (48%) when the <strong>reaction</strong> was<br />
carried out with an overall zeolite amount of 1 g for 5 m<strong>in</strong> (Table 5.5, entry 4). About 3<br />
to 4 grams of the zeolite seemed to be required for the optimum product recovery<br />
(compare entries 5-7) and the <strong>reaction</strong> proceeded smoothly even at a lower <strong>reaction</strong><br />
temperature of 120 ºC to give 88% coupl<strong>in</strong>g product after 15 m<strong>in</strong> (Table 5.5, entry 8).<br />
Four grams of NaY zeolite would <strong>in</strong>troduce nearly 1 g of water <strong>in</strong>to the <strong>reaction</strong><br />
medium. Therefore, a <strong>reaction</strong> was conducted <strong>in</strong> the presence of 1 g of zeolite along<br />
with 1 g of added water <strong>in</strong> order to clarify if the yield improvement was solely due to<br />
the <strong>in</strong>creased water amount <strong>in</strong> the system. The yield was identical to that obta<strong>in</strong>ed <strong>in</strong> the<br />
experiment performed with 1 g orig<strong>in</strong>al zeolite alone (Table 5.5, compare entries 4, 9).<br />
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