WORLD INTELLECTUAL_ PROPERTY ORGANIZATION
International Bureau
INTERNATIONAL APPLICATION PUBLISHED UNDER THE PATENT COOPERATION TREATY (PCT)
(51) IIlte1'H3ti0l131 Patent C13-9SifiC3ti0n 6 3 (11) International Publication Number: WO 95/32183
C07C 253/30, 255/23 _ , ,
(43) International Publlcatlon Date: 30 November 1995 (30.11.95)
(21) International Application Number: PCT/IE95/00017 (81) Designated States: AM, AU, BG, BR, BY, CA, CN, CZ, DE,
EE, FI, GB, GE, HU, JP, KG, KP, KR, KZ, LK, LR, LT,
(22) International Filing Date: 8 February 1995 (08.02.95) LV, MD, MN, MX, NO, NZ, PL, RO, RU, SD, SI, SK,
TJ, UA, US, UZ, VN, European patent (AT, BE, CH, DE,
DK, ES, FR, GB, GR, IE, IT, LU, MC, NL, PT, SE), OAPI
(30) Priority Data: patent (BF, BJ, CF, CG, CI, CM, GA, GN, ML, MR, NE,
S940423 24 May 1994 (24.05.94) IE SN, TD, TG), ARIPO patent (KE, MW, SD, SZ).
(71) Applicant (for all designated States except US): SALDANE Published
LIMITED [IHIE]; Molyneux House, Bride Street, Dublin 8 With international search report.
(IE).
(72) Inventors; and
(75) InventorslApplicants (for US only): DYATLOV, Valery
Alexandrovich [RU/RU]; Malyl Levshinskyl per., 12-6,
Moscow, 110934 (RU). MALEEV, Viktor [RU/RU]; Str.
B, Apt. 66, Serpuchovskaya, 70, Moscow, 113093 (RU).
(74) Agent: ANNE RYAN & CO.; 60 Northumberland Road,
Ballsbridge, Dublin 4 (IE).
(54) Title: PROCESS FOR THE PREPARATION OF 2—CYANOACRYLOYL CHLORIDE AND USE OF THE COMPOUND SO
PREPARED FOR THE PREPARATION OF ESTERS OF 2-CYANOACRYLIC ACID
(57) Abstract
A process for the preparation of 2-cyanoacryloyl chloride in pure form comprises reacting 2-cyanoacrylic acid with a chlorinating
agent, said reaction being carried out under side-reaction and polymerisation inhibiting conditions. A preferred chlorinating agent is a
volatile chlorinating agent which forms only volatile by-products during the course of the reaction. Suitable volatile chlorinating agents
include oxalyl chloride, sulfur oxychloride, trifluoroacetyl chloride and phosgene. Various methods can be used to inhibit polymerisation
initiating conditions such as the use of a catalyst which forms an intermediate complex with the chlorinating agent, thereby preventing the
formation of a mixed anhydride. The 2-cyanoacryloyl chloride formed can be used to form esters useful in the manufacture of adhesives
and which esters are free of contaminants which would otherwise affect the setting time of the adhesives.
AT
AU
BB
BE
BF
BG
BJ
BR
BY
CA
CF
CG
CH
CI
CM
CN
CS
CZ
DE
DK
ES
FI
FR
GA
FOR THE PURPOSES OF INFORMATION ONLY
Codes used to identify States party to the PCT on the front pages of pamphlets publishing intemational
applications under the PCT.
Austria
Australia
Barbados
Belgium
Burkina Faso
Bulgaria
Benin
Brazil
Belarus
Canada
Central African Republic
Congo
Switzerland
Cote d’Ivoire
Cameroon
China
Czechoslovakia
Czech Republic
Germany
Denmark
Spain
Finland
France
Gabon
United Kingdom
Georgia
Guinea
Greece
Hungary
Ireland
Italy
Japan
Kenya
Kyrgystan
Democratic People's Republic
of Korea
Republic of Korea
Kazakhstan
Liechtenstein
Sri Lanka
Luxembourg
Latvia
Monaco
Republic of Moldova
Madagascar
Mali
Mongolia
Mauritania
Malawi
Niger
Netherlands
Norway
New Zealand
Poland
Portugal
Romania
Russian Federation
Sudan
Sweden
Slovenia
Slovakia
Senegal
Chad
Togo
Tajikistan
Trinidad and Tobago
Uldaine
United States of America
Uzbekistan
Viet Nam
I
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Description
Process for the preparation of 2-cyanoacryloyl chloride and
use of the compound so prepared for the preparation of esters
of 2-cyanoacrylic acid
Technical Field
This invention relates to a process for the preparation of 2-
cyanoacryloyl chloride and to the use thereof in the preparation of
esters of 2-cyanoacrylic acid. 2-Cyanoacryloyl chloride which has
the formula:
CN
/
H2C=' C
\
0- Cl
ll
0
can potentially be used to prepare a wide range of cyanoacrylate
monomers.
Background Art
The ability of 2-cyanoacrylates to polymerise rapidly under the
influence of moisture or nucleophilic substances has led to their
exploitation as instantaneous adhesives. However, the inherent ability '
of 2-cyanoacrylates to undergo rapid anionic polymerisation gives
rise to complications as regards the synthesis of free 2-cyanoacryloyl
chloride. Accordingly, whereas esters of 2-cyanoacrylic acid are
known and well characterised since the 1940s, 2-cyanoacryloyl
chloride has not been isolated and characterised. 2-Cyanoacryloyl
chloride has been observed in solution only. The first reported
observation of 2-cyanoacryloyl chloride in solution by NMR was
described in 1990 by Kandror, I.I. et al. However, all efforts to
isolate 2-cyanoacryloyl chloride from solution were unsuccessful.
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Kandror, I.l. et al. ((1990) Zh. Obsch. Khemii., Vol. 60, No.
9, p. 2160-8) have described two methods for the preparation of 2-
cyanoacryloyl chloride—containing solutions.
The first method involved the reaction of 2-cyanoacrylic acid
with phosphorus pentachloride at a temperature of 110°C using a
toluene—xylene mixture as a solvent, followed by distillation off of
phosphorus oxychloride and a portion of the solvent. The resulting
solution contained a mixture of 2—cyanoacryloyl chloride,
polyphosphoric acid and polymers formed from 2-cyanoacrylic acid
in the form of a solution in xylene. Conversion of 2-cyanoacrylic
acid to 2—cyanoacryloyl chloride together with polymer was reported
by NMR to be 95-99%, the yield of 2-cyanoacryloyl chloride was not
estimated. 13C and 31P NMR analysis of 2—cyanoacryloyl chloride
prepared by this method shows that deleterious by—products which
are formed include those resulting from chlorination of, and addition
of hydrogen chloride to, the olefinic bond of cyanoacryloyl chloride,
and from the addition of phosphorus oxychloride to its nitrile group
to yield substances containing the -C(Cl)=N-P(O)Cl;;_ function. 2-
Cyanoacryloyl chloride obtained by this method cannot be isolated
from the mixture and polymerises spontaneously once the solvent is
distilled off in vacuo. Vacuum distillation or precipitation of the
product with an inert solvent also leads to instantaneous
polymerisation.
The second method involved the reaction of 2-cyanoacrylic
acid with thionyl chloride in toluene or toluene—xylene solution at a
temperature of 110°C followed by distillation off of hydrochloric
acid, sulfur dioxide and a portion of the solvent to give a mixture of
2—cyanoacryloyl chloride, 2-cyanoacrylic acid and polymers formed
from 2-cyanoacrylic acid in the form of a solution in xylene. No
yield or conversion has been estimated. NMR analysis shows that the
product of the reaction is a solution of a mixture of 2—cyanoacryloyl
chloride and 2-cyanoacrylic acid in a ratio of 65:35, together with
mixed anhydride by-products resulting from the side and
polymerisation reactions. Attempts to complete the reaction and
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convert residual 2-cyanoacrylic acid and mixed anhydrides into 2-
cyanoacryloyl chloride resulted in polymerisation of the mixed
anhydrides, 2-cyanoacryloyl chloride and 2-cyanoacrylic acid. The
2—cyanoacryloyl chloride could not be isolated in pure form from the
reaction mixture using this method and the yield could not be 5
estimated. However, according to NMR data, the yield is less than
65% and it appears that a significant amount of polymeric and side
reaction products were not taken into account.
Thus, pure 2-cyanoacryloyl chloride was not obtained and
chemically characterised in accordance with either of the two
methods described above. In the case of each method, 2-
cyanoacryloyl chloride can only be obtained in the form of a solution
contaminated with non-volatile by—products.
2-Cyanoacryloyl chloride is used as a starting material for
obtaining esters of 2-cyanoacrylic acid. Because of the contamination
of the 2-cyanoacryloyl chloride referred to above this necessitates
that any resulting ester be purified to remove the contaminants
formed during 2-cyanoacryloyl chloride production. If such
contaminants, which are generally of an acidic nature, are not
removed, these can affect the setting times of adhesives formed from
the esters. The highest level of strongly acidic contamination
tolerable in cyanoacrylate adhesive compositions is generally less
than 1 p.p.m. As regards the contaminants, the most undesirable
contaminants are traces of residual phosphorus oxychloride, non-
volatile strong acids such as phosphoric and polyphosphoric acids,
and the deleterious chlorinated by-products mentioned supra. These
by-products can slowly release hydrochloric acid via hydrolysis by
atmospheric moisture during, for example, storage of a
cyanoacrylate adhesive composition, leading to loss of adhesive
properties by acid inhibition of the anionic polymerisation pathway.
Complicated procedures are required to purify the esters from the
non-volatile mixtures of contaminants, in particular in the case of
non—distillable liquid esters which cannot be purified by either
distillation or by recrystallisation.
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