Scheme 2. Synthesis of Sch 47687 via the chloropurine
route
complications (dimerization, polymerization, N-oxidations,
oiling of free base, etc.), allowing for good isolated yields
of high-melting crude 14. Crude 14 was then reacted with a
stoichiometric amount of chiral amino alcohol 5 in refluxing
acetonitrile containing an excess of TEA as an HCl scav-
enger. Typically, most of 14 was consumed after 72 h at
which stage the reaction mixture was filtered to remove TEA‚
HCl as well as residual 13. Addition of the reaction mixture
to water allowed for precipitation of 15. Crude 15, after
drying, was dissolved in methylene chloride and treated with
a slight excess of thionyl chloride. A gentle warming (35-
4
0 °C) of the reaction mixture led to essentially complete
cyclization of 15 to 1 as its HCl salt. Neutralization of this
reaction mixture with NH OH allowed for precipitation of
4
free base 1 which was recrystallized from acetonitrile. The
two-step yield, although good, was slightly variable. This
was traced to the degree of neutralization as well as the
uracil to caffeine metabolite A
1
, i.e., 12, via nitrosopyrimidine
7
11 developed and scaled up to kilogram scale in our labora-
4
tories and plant has been reported previously by us. Insolu-
bility of 12 in a variety of solvents posed a serious challenge
to our initial goal of converting it to the xanthine 13. It is
worth noting that the research synthesis1 utilized a benzyl
protecting group at the 5-acetamido nitrogen which mini-
mized the insolubility difficulties. It was also known that
the removal of this benzyl group at the end of the sequence
via catalytic hydrogenation was very difficult, often requiring
amount of water (introduced via aqueous NH
ficient neutralization caused the loss of 1‚HCl in water as
well as CH Cl , whereas an excess of water removed free
4
OH). Insuf-
7,18
2
2
base 1 due to its solubility in water. Since the above
preparation allowed for delivery of Tox and Phase I supplies
of 1, no further optimization work was done to improve the
last-step yield.
Sch 51866, 2, was chosen as the second PDE inhibitor
of interest. Application of the chloropurine route for its
preparation led to many dissimilar and some similar observa-
tions and required changes to the experimental conditions
at every step for a successful ending. Unlike acetic acid or
2
a large amount of 20% Pd(OH) /C. This was undesirable
from both the cost and “residual heavy metal (Pd) in the
API” perspective. Our initial desire was to “activate” 13 to
produce 14 by reacting it with an appropriate activating
reagent (sulfonyl halides, anhydrides, etc. leading to the
corresponding leaving group L in 14) such that the activated
purine 14 with a desirable leaving group L can then
efficiently react with expensive chiral amino alcohol 5. Our
continued work to form xanthine 13 led us to use POCl
When 12 was suspended in POCl and heated (to ensure
enough solubility for reasonable reaction rate), it led to the
formation of xanthine 13 as well as the chloropurine 14. We
further found that 14 is formed under these conditions. As
discussed later in this manuscript under the mechanism of
formation of chloropurines, an addition of excess NH
to the reaction mixture prior to heating 12 in neat POCl
a solvent and a subsequent workup with NH
for an efficient one-pot, two-step conversion of 12 to 14. In
a typical plant procedure, the batch was gradually heated to
reflux over 6-8 h and held at that temperature for 48 h for
complete consumption of 12 and 13. Attempts to minimize
3 2
acetic anhydride, p-CF -Ph-CH COOH is a solid. Thus, the
5
experimental conditions developed for the preparation of 12
via reductive amidation needed changes for the preparation
of 17. To this end it was found that 11 as an aqueous NaOH
solution can be completely hydrogenated to 16. This diamine
is air sensitive, and its isolation was undesirable. Again, it
was discovered that the treatment of a solution of this
diamine in aqueous NaOH with only a slight excess of
3
.
3
6
4
Cl
as
p-CF
3
-Ph-CH
2
COCl (prepared in a quantitative yield by
) led to
3
treatment of the corresponding acid with SOCl
2
4
OH allowed
precipitation of high-quality amide 17 in very good isolated
8
yield. Similar to amide 12, amide 17 could only be isolated
in its hydrated form. Initially this appeared counterproductive
for the next step where POCl was used as a solvent, and
3
hence, some effort was put into drying 17. As discussed later
in this contribution, difficulty in removing this water of
hydration from 17 proved fortuitous.
the use of POCl
lowered yields and/or increased impurities. Fortunately, after
neutralization of HCl and POCl , the isolation of 14 lacking
the protection of imidazole nitrogen(s) did not cause
3
via the use of high-boiling solvents typically
3
Unlike amide 12, initial attempts to convert 17 to xanthine
1
8 and chloropurine 19 led to irreproducible results. The rate
as well as extent (temperature and time) of heating the
suspension of 17 in POCl led to formation of one major to
(
(
(
4) Gala, D.; DiBenedetto, D.; G u¨ nter, F.; Kugelman, M.; Maloney, D.;
Cordero, M.; Mergelsberg, I. Org. Process Res. DeV. 1997, 1, 85.
5) (a) Barr, A.; Frencel, I.; Robinson, J. B. Can. J. Chem. 1977, 55, 4180. (b)
Overman, L. E.; Sugai, S. J. Org. Chem. 1985, 50, 4154.
6) Towards the development/optimization of 2-chloropurine formation/isolation
in high yields with the least number of impurities, several metal halides,
Vilsmeier reagents, phosphorous halides, phase-transfer reagents, amine
HCl salts, cosolvents (toluene, xylenes, chlorobenzene, dichlorobenzenes,
etc.), various workups (quenches with protic solvents, amines, inorganic
bases), and various combination of the above were evaluated. Of these,
3
many other products during its conversion to 19. This had a
significant impact on the yield as well as the quality of 19.
(7) The use of a mild base was desirable in view of the instability of these
PDE inhibitors to strong base such as aqueous NaOH. See Gala, D.; Puar,
M. S.; Czarniecki, M.; Das, P. R.; Kugelman, M.; Kaminiski, J. Tetrahedron
Lett. 2000, 41, 5025.
the use of POCl
3
and NH
4
Cl gave the best results. Since the latter is
(8) Such favorable faster amidation compared to the hydrolysis of this acid
chloride under such basic conditions was unexpected. This procedure was
applicable to several aliphatic as well as aromatic acid chlorides (unpub-
lished results).
inexpensive, appeared to improve solubility/stirability of the reaction
mixtures, and did not interfere with the workup, it was used in excess (3-5
mol).
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