Scheme 1a
steps are then repeated until an oligonucleotide of desired
length and sequence is completed.
It is important to note that the amidite coupling process
described creates two high-molecular-weight waste products.
First, the DMT group used for 5′-OH protection amounts to
approximately 35% of the weight of incoming monomeric
phosphoramidite units 3. This mass is released as the DMT
cation in waste dichloromethane. Second, a 0.5 mol excess
of building block 4 is also discarded in waste ACN along
with 1H-tetrazole. Gratifyingly, methods to capture 4 for
a
Reagents and conditions: a, concentration under reduced pressure to an
oil; b, add MeOH and 3 N NaOH solution; c, extraction of DMT-OH in organic
solvent; d, a f AcCl in toluene, reflux 3 h, f a f crystallization from
cyclohexane.
During a standard 60 mmol synthesis of oligonucleotide
1
8
on an OligoProcess reactor, one complete column volume
of deblock solution was collected manually upon completion
of a detritylation step (i in Figure 1). This solution is acidic
9
its recovery by conversion to 3 are already in place.
However, methods to capture the valuable DMT group and
for its reconversion to useful DMT-Cl have never been
published. In synthesizing a high-molecular-weight (∼6000)
drug, such as an oligonucleotide, it becomes very important
to maintain a high level of atom efficiency and atom
economy. In this note, we describe, for the first time, a
convenient process for the capture of currently wasted DMT
group and its conversion to useful DMT-Cl.
(
pH 0.6) and bright red-orange in color. The color is due to
DMT cation present in the solution. The concentration of
this cation is approximately 4.8 mmol/L, measured by its
characteristic UV absorption at 504 nm. The next step in
the recovery (a in Scheme 1) involves concentration of the
red-orange solution under vacuum. During this step, most
of the dichloromethane is removed from the solution and
collected. The dichloromethane recovery is about 90% in
this step, with a purity of >95%. We believe that
dichloromethane recovered by this process is pure enough20
for reuse as a solvent for organic synthesis.
The residual red oil is then dissolved in a minimum
volume of methanol and the solution quenched with 3 N
NaOH solution (step b, Scheme 1). The rationale for use of
NaOH as a quenching base is three-fold. First, it is
inexpensive and environmentally safe; second, it neutralizes
DCA in a very effective manner; and last, it provides
hydroxide ion for generation of DMT-OH. At this point,
the bright red color of the solution fades away, indicating
Results and Discussion
1
9
There are two main reasons why the DMT group has been
widely used for the protection of hydroxyl groups in
1
0
carbohydrate, nucleoside, and oligonucleotide chemistry.
First, a triphenylmethyl group imparts crystallinity to many
compounds that are low-melting solids, and second, the
triphenylmethyl group is easily removed under a variety of
1
1
conditions. Use of the DMT group in oligonucleotide
1
2
synthesis was first described by Nobel laureate Khorana
in 1962. After all these years, DMT is still the preferred
hydroxyl protecting group for oligonucleotide synthesis, both
1
3
14
in solid-supported and in solution-phase syntheses.
21
the formation of DMT-OH, confirmed by MS analysis. The
In a standard automated synthesis15 of a 20-mer phos-
phorothioate oligonucleotide on 100 mmol scale, the 5′-O-
DMT group is removed 19 times using a total of approxi-
mately 380 L of 3% DCA in dichloromethane. Interestingly,
all of that material goes to waste and is typically incinerated
at a premium price.16 Our original manufacturing process
for oligonucleotides not only generated toxic acid waste but
22
pH of the solution is ∼9-10, which does not affect the
DMT-OH.
The basic solution is concentrated under vacuum to
remove most of the methanol, providing a thick orange-
yellow syrup. In the next step (c in Scheme 1), the syrup is
dissolved in toluene and the solution washed with water
several times. Water washing removes DCA as a soluble
sodium salt, an easily disposable waste stream. The toluene
solution is then concentrated to 1/10 of original volume,
which helps remove trace water as an azeotrope, leaving the
solution dry and ready for the chlorination step (d in Scheme
1
7
also threw away an expensive protecting group of high
molecular weight. For this reason, we embarked on a project
to allow (i) salvage of a protecting group which constitutes
35% of the weight of amidite 3, (ii) neutralization of the
acidic halogenated waste stream, and (iii) potential for
recovery and reuse of the toxic solvent dichloromethane. The
process described herein addresses all these issues and is
amenable to scale-up for ton-scale manufacture scenario.
2
3
1
). The literature method for chlorination of DMT-OH
calls for the use of neat acetyl chloride under refluxing
conditions. However, we thought it was unnecessary to use
such a large excess of acetyl chloride. After a few attempts,
we were able to perform the chlorination with only 1/10 of
(9) Scremin, C. L.; Zhou, L.; Srinivasachar, K.; Beaucage, S. L. J. Org. Chem.
1
994, 59, 1963.
(
(
(
(
10) Sonveaux, E. In Protocols for Oligonucleotide Conjugates; Agrawal, S.,
Ed.; Humana: Totowa, NJ, 1994; Chapter 1, pp 1-72.
11) Wang, Y.; McGuigan, C. Synth. Commun. 1997, 27, 3829. Ding, X.; Wang,
W.; Kong, F. Carbohydr. Res. 1997, 303, 445.
12) Smith, M.; Rammler, D. H.; Goldberg, I. H.; Khorana, H. G. J. Am. Chem.
Soc. 1962, 84, 430.
13) White, H. A. In Solid Supports and Catalysts in Organic Synthesis; Smith,
K., Ed.; Ellis Horwood: New York, 1992; Chapter 8, pp 228-249.
14) Reese, C. B.; Song, Q. Bioorg. Med. Chem Lett. 1997, 7, 2787.
15) Using phosphoramidite chemistry, see ref 6 for details.
16) The current cost of disposal by incineration of halogenated waste is $260
per 55-gallon drum.
(18) OligoProcess is the largest automated oligonucleotide synthesizer built to
assemble 10-180 mmol of 20-mer oligonucleotide in less than 12 h. For
more details, contact Amersham Pharmacia Biotech, Piscataway, NJ (phone
1-800-526-3593).
(19) Determined by GC.
(20) Preliminary deblocking and phosphitylation experiments with recovered
dichloromethane indicated no side reactions.
(21) Bleasdale, C.; Ellwood, S. B.; Golding, B. T. J. Chem. Soc., Perkin Trans.
1 1990, 803.
(22) The pKR+ value for DMT-OH is - 1.24, cited from: Deno, N. C.;
Jaruzelski, J. J.; Schriesheim, A. J. Am. Chem. Soc. 1955, 77, 3044.
(23) Rathore, M.; Rani, P.; Mathur, N. K.; Narang, C. K. Indian J. Chem. 1995,
343, 634.
(
(
(
(17) The Aldrich catalog price for DMT-Cl is $81 for 25 g.
416
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Vol. 2, No. 6, 1998 / Organic Process Research & Development