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Or gP al en ai sc e& d Bo i on mo to al ed cj uu ls at r mC ha re gmi ni ss try
DOI: 10.1039/C8OB01438H
Journal Name
ARTICLE
To evaluate the reusable efficiency of HS-cellulose sulphate as a 1.
desilylating agent we recovered the catalyst from the reaction mass
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2
3
.
.
after the synthesis of compound 6a. The synthesis of compound 6a
from 5a was repeated thrice by recovering HS-cellulose sulphate
each time, and we observed that the catalyst could be
quantitatively recovered and reused in these three successive
TBDMS deprotection reactions without considerable loss of
catalytic activity, and with minimal change in the yield of product
1
, 2001, DOI: 10.1039/B103282H, 2109-2135.
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6
.
(99.0%, 97.5% and 96.5%). We also determined that the chemical
structure of the catalyst was retained after recovery from the 7.
reaction mass by running H and C-NMR spectra on the recovered 8.
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13
HS-cellulose sulphate and comparing the spectra with that of the
9
1
1
.
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fresh catalyst.
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0.
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1
Conclusions
1
In conclusion, HS-cellulose sulphate prepared from commercially
available α-cellulose, is an efficient, thermally stable and
recoverable acid catalyst that can be used for the deprotection of
alcoholic TBDMS ethers in methanol at 25°C. Selective desilylation
of TBDMS ethers of alcohols in the presence of TBDMS phenolic
1
1
2.
3.
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4.
1
ethers can also be achieved. This protocol is the first report of the 15.
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considerable loss of catalytic activity and without any significant
1
7.
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change in the yields of the products. Considering the utility of the
above features, we believe that this catalyst could be an excellent
choice for selective alcohol group deprotection in both lab-scale
and manufacturing scale chemistries.
3
04-309.
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1
2
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8.
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General procedure for the deprotection of alcoholic TBDMS ethers
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To a solution of TBDMS ether (1 mmol) in methanol (5 mL) was
added HS-cellulose sulphate (2; 5% w/w). The heterogenous
reaction mixture was stirred at 25°C for 0.5 to 1.5 hrs. Progress of
the deprotection reaction was monitored by TLC. After completion
of the reaction the catalyst was separated by filtration and the
filtrate was concentrated under reduced pressure to remove
4
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2
2
3.
4.
methanol to afford the corresponding deprotected crude alcohol. 25.
The crude product was purified by silica gel column
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Conflicts of interest
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There are no conflicts to declare.
8
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Acknowledgements
This research work was supported by EPSCoR grant no. 216 EPSCoR
G1-51050-03-03.
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Notes and references
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