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Patent 1152528 Summary

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Claims and Abstract availability

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(12) Patent: (11) CA 1152528
(21) Application Number: 1152528
(54) English Title: PROCESS FOR THE PREPARATION OF ACETOACETIC ACID ALKYL ESTERS
(54) French Title: PREPARATION D'ALKYL-ESTERS D'ACIDE ACETOACETIQUE
Status: Term Expired - Post Grant
Bibliographic Data
(51) International Patent Classification (IPC):
  • C07C 69/72 (2006.01)
(72) Inventors :
  • GUNTHER, KLAUS (Germany)
  • WENDT, HEINZ (Germany)
(73) Owners :
  • HOECHST AKTIENGESELLSCHAFT
(71) Applicants :
  • HOECHST AKTIENGESELLSCHAFT (Germany)
(74) Agent: SMART & BIGGAR LP
(74) Associate agent:
(45) Issued: 1983-08-23
(22) Filed Date: 1981-06-26
Availability of licence: N/A
Dedicated to the Public: N/A
(25) Language of filing: English

Patent Cooperation Treaty (PCT): No

(30) Application Priority Data:
Application No. Country/Territory Date
P 30 24 535.3 (Germany) 1980-06-28

Abstracts

English Abstract


HOE 80/F 139
- 1 -
Abstract:
Process for the preparation of acetoacetic acid alkyl
esters
Acetoacetic acid alkyl esters are prepared
according to the invention by reaction of 2-acetoxy-
crotonic acid alkyl esters or 2-acetoxyvinylacetic acid
alkyl esters or a mixture thereof on the one hand and
an aliphatic alcohol with 1 to 5 carbon atoms on the
other hand. The reaction is carried out in the liquid
phase at 50 to 250°C, the alcohol being employed in at
least equimolar quantity.


Claims

Note: Claims are shown in the official language in which they were submitted.


THE EMBODIMENTS OF THE INVENTION IN WHICH AN EXCLUSIVE PROPERTY
OR PRIVILEGE IS CLAIMED ARE DEFINED AS FOLLOWS:
1. A process for the preparation of an acetoacetic acid
alkyl ester in which a 3-acetoxycrotonic acid alkyl or alkenyl
ester, a 3-acetoxyvinylacetic acid alkyl or alkenyl ester or a
mixture thereof is reacted in the liquid phase at a temperature
of from 50 to 250°C with an aliphatic alcohol which contains 1
to 5 carbon atoms, the alcohol being employed in an at least
equimolar quantity.
2. A process as claimed in claim 1 in which the alkyl or
alkenyl groups of the 3-acetoxycrotonic acid alkyl or alkenyl
ester, or the 3-acetocyvinylacetic acid alkyl or alkenyl
ester are straight-chain or branched and contained 1 to 5 carbon
atoms.
3. A process as claimed in claim 1 in which the alcohol
contains the same alkyl or alkenyl group as the 3-acetoxycrotonic
acid alkyl or alkenyl ester or the 3-acetoxyvinylacetic acid
alkyl or alkenyl ester.
4. A process as claimed in claim 1, claim 2 or claim 3
in which a primary aliphatic alcohol is employed.
5. A process as claimed in claim 1, claim 2 or claim 3
in which methanol or ethanol is employed as the aliphatic
alcohol.
6. A process as claimed in claim 1, claim or claim 3
in which 3-acetoxycrotonic acid alkyl or alkenyl ester and
3-acetoxyvinylacetic acid alkyl or alkenyl ester are employed
in mixtures with an acetoacetic acid alkyl or alkenyl ester,
all three esters having the same alkyl or alkenyl group and
the portion of the acetoacetic acid alkyl or alkenyl ester
12

in the mixture being 40 to 50% by weight.
7. A process as claimed in claim 1, claim 2 or claim 3
in which a reaction is carried out at a temperature of from
100 to 200° C.
13

Description

Note: Descriptions are shown in the official language in which they were submitted.


~5~8
-- 2 --
The industrial preparation of acetoacetic acid
alkyl esters is carried out today, in general, by reaction
of diketene with the corresponding anhydrous aliphatic
alcohol. In this reaction, a crude product is ob-
tained which contains several low-boiling, middle-boiling
and high-boiling compounds, apart from the des1red aceto-
ac_tic acid alkyl ester. Above all, excess alcohol, ace-
~one and alkyl acetate are contained in the crude ester
as low-boiling compounds. In general, dehydroacetic acid
and a thermally little stable residue, which is formed
from diketene, are present as high-boiling compounds.
Mainly 3-acetoxy-crotonic acid alkyl or alkenyl esters, that is, ir.-
the Ci9 form and the trans form, and 3-acetoxyvinylacetic
acid alkyl or alkenyl esters occur as middle-boiling c ~ ounds which
boil in the range of the corresponding acetoacetic acid
alkyl ester. ~he pure acetoacetic acid alkyl ester is
obtained from th s complex mixture by fractional distil-
lation.
Whilst the low-boiling compounds and the high-
boiling compounds may be separa~ed off without difficulty,
this operation in the case of the middle-boiling compounds
3-acetoxycrotonic acid alkyl or alkenyl ester and 3-acetoxyvinyl-
a^etic acid alkyl or alkenyl ester - mostly referred to as AC-ester
or AV-ester in the following text - is not straight-
forward. A separation of these components by fractionaldistillation is troublesome and is successful only with
.
~ J~ i
.. - I
" ~ "
.. .

~5~528
a high re ~u~ ratio,
In ~heory, a simpler possibility would be a
specific chemical conversion o~ these interfering sub-
stances into o~her compounds more easily separable by
distillation. Ho~ever, it had to be taken into con-
sideration, in this case, that the-acetoacetic acid
alkyl ester present as the main component o~ the mixture
contains three reactive groups - a carbonyl group, a
carbalkoxy group and an active methylene grcup - ard is
there~ore very reactive. A chemical conversio~ of the
interfering components AC-esier and AV-ester without
simultaneous undesired reaction of the acetoacetic acid
alkyl ester did not therefore appear possible.
Surprisingly, it has now been found that, by
action of an alcohol on AC- and/or AV-ester, a smooth
conversion o~ these com~ounds to acetoacetic acid alkyl
ester takes place, without this compound itself reac~ing
with the alcohol.
The pLocess according to the invention Ior the
preparation of acetoacetic acid alkyl ester comprises
the reactior. in the liouid phase at a tem~eratu~e of
50 to 250C o 3-aceiox~rcrotonic acid alkyl or alkenyl ester or
3-acetoxyvinylacetic acid alkyl or alkenyl ester or a mixture
thereof ~rith an aliphatic alcohol w~ich cor.tains 1 to 5
carbon atoms, the alcohol being employed in at least
eauimolar auartity.
The alkyl groups n the 3-acetoxycrotonic acid alkyl or
alkenyl ester and in the 3-acetoxyvinylacetic acid aIkyl.or alkenyl
ester preferably have 1 to 5 C atoms ar.d can be saturated
1~ ..

25;~8
-- 4 --
or unsaturated, straight-chain or branched
In the ~eaction of the AC-ester or of the AV-
ester with the alcohol, ~he acetic acid ester of the
alcohol e~ployed, that is the alkyl aceta~e already men-
.. .. . . . . . . . . .. .. . . . . . . . . .
tioned above as the low-boiling compound, is formed in
... . . . .
addition to the acetoacetic acid alkyl ester.
AC-ester or AV-ester can be employed individually
or mixed.
The two esters can be obtained individually or
as a mixture lrom the crude product ~ihich is formed in
the preparation of acetoacetic acid alkyl esters from
diketene and an alcohol by ~irs~ separating off ~e low-
boiling compounds and the high-boiling compounds and then
.. . . . . ....... . .
isolating AC-ester, AV-ester and acetoacetic acid alkyl
ester by fractional disi-llation. In this manner, AC-
ester and AV-ester or a mixture thereof are obtained,
free from acetoacetic acid alkyl ester.
Preferably, however, this relatively troublesome
complete separation of the acetoacetic acid alkyl ester
is not carried out, but the follo~ring procQdure is
folloThTed: firstly, the 1ow-boi1ing compounds and the high-
boiling compo~nds ar~ again separated olf by distillation
f~om the crude product mentioned and the ~ain fraction
containing the acetoacetic acid alkyl ester, the AC-es-ter
~5 an~ the AV-ester is then separated in a second distilla-
tion into pure acetoacetic acid alkyl ester as the top
product and into a mixture Gf acetoacetic acid alkyl
ester/AC-ester/AV-ester as the ~ottom product This
mixture is then reacted according to ihe invention with
~- '
, ;
. . : :. .

- 5 -
an aliphatic alcohol at $0 to 250C, preferably at 140
to 180C, and under a pressure corresponding to the
vapor pressure of the mixture. The resulting reaction
mixture is worked up to acetoacetic acid alkyl ester by
distillation.
It is, however, alsopossible- although this is, as a
- rule, less favora~le - to react the main ~raction me~tioned,
.. . ... . . . . . . ... ..
and obtained after separating off the low-boiling compounds
.... . . . . ... . ..
and high-boiling compounds, directly according to the
invention with an aliphatic alcohol, ænd only then is
.. . .. . . .
:pure acetoacetic acid alkyl ester distilled off as the top
.. . . . . . . . .. ...
- product and a bottom produci which contains the remaining
acetoacetic acid alkyl ester and the unreacted AC- and
AV-ester is obtained.
A corresponding procedure is of co~lrse foll~red
with pure (that is,not containing acetoacetic acid alkyl
ester) AC-ester or AV-ester or a mixture thereo~.
Appropriately, the alcohol which was employed in
the preparation of the acetoacetic acid alkyl ester from
diketene is used in the reaction of an AC-ester/AV-ester/
acetoacetic acid alkyl ester mixture obtained as men-
tioned. In the preparation ol methyl acetoacetate
this alcohol is methanol, for ethyl acetoacetate ethanol etc
The AC-ester ~nd AV-ester components to be reacted have
an alkoxy group which corresponds to the alcohol employed
in the diketene reac~ion. Methyl acetoacetate there-
fore contains acetoxycrotonic acid methyl ester and
acetox-yvinylacetic acid methyl ester as acco~panying
components; the homologous compounds behave correspondingl~.

2 52 8
- 6 -
Basic21ly, ho~rever~ an alcohol which does not
correspond to the carbalkoxy group of these esters may also
be used for the reaction of the AC-ester and the AV-ester.
Thus, for example, acetoxycrotonic acid methyl ester and
-acetoxyvinylacetic acid methyl ~ester may be directly
reacted ~ th butanol.
A reaction time of fro~ 4 to 6 hours has proved
to be the most favorable. In this time, an extensive
conversion takes place. This amounts to 65 to 95%
under the c~nditions i~dicated. After reaction has
taken place, the reaction mixture is worked up, prefer-
ably together wi~h the crude product formed in the reac-
tion of diketene with an alcohol, and a complete conver-
sion of the AC-ester and the AV-ester is therefore not
required in the process according to the invention and
is even inexpedient for reasons o~ cost efficiency.
The ~lorkirg-up of the crude product mantionedg
resulting from the reaction of diketene with an alcohol,
is thus simplified b~j coupling with the process according
to the inven~ion: after the separation o~ the high-
.. . . . . . .. . . .. ..
boiling compounds and low-boiling compounds from th~ crude
_ . . . . . .. . . . . ........................ .. ..
product, onl~ the main portion of ~he acetoace~ic acid
alkyl ester is distilled off (instead of distilling it
off as far a~ possible, as hitherto~ and the remaining
portion, togelher with AC- and A~-esters, is employed
in the process according to the invention
For the process a~ccording to the invention, a
mixture which contains as high a portion as possible of
AC- and AV-esters is preferably employed Such a
.:
~ - ~

:~.5;~5;~8
-- 7 --
mix~ure is obtained from ihe bottom of the column in
which the distillation for the purification of the aceto-
acetic acid alkyl ester, after separation of the high_
..
boiling compounds and low-boilin~ compcunds, is carried
out. The concentration o~ acetoacetic acid alkyl
ester is, in this case, between 20 and 80% by weight,
preferably 40 to 50% by weight. However, even in the
case of substantially higher va~ues, the reaction pro-
ceeds without difficulties
Basically, all aliphatic alcohols ~'nich co-ntain
1 to 5 carbon atoms a~e suitable as t'he alcohol component
in ~he process according io t~e invention. The carbon
chain can be straight-chain or branched and the alconol
can be a primary, secordary or tertiary alcohol; further,
1~ unsaturated alcohols can also be used Thus, for
example, the follo~ing alcohols may be used as reaction
partners: methanol, ethanol, propan-1-ol, propan-2-ol,
butan-1-ol, butan-2-ol, 2-methyl-propan-1-ol, 2-me~hyl~
propan-2-ol, pentan-l-ol, pentan-2-ol, pen-tan-~-ol, 2-
methyl-butan-4-ol, 2-methyl-butan-3-ol, 2-methylbu~an-2-
ol, 2-methylbutan-1-ol, 2,2-dimethyl-propan-1-ol and
prop-l-en-3-ol. Primary alcohols are preferred~ in
particular me~hanol and ethanol.
The two follcwing embodiments ol -the prccess
according to the i~vention are particularly favorable:
.. . ... . . . . . . . . . . .. . ..
- 'a) High-boiling compounds and low-boiling compcunds
_ . . . ~ ...... . . ....... .. . .. . . ... . .
and subseauently the main portion of the methyl aceto-
acetate are separated off from the crude product ~Jhich
has formed in the contin~ous preparation of methyl

~ 2 52 8
- 8 -
acetoacetate fro~ diketene and methanol 3-Acetoxy-
crotonic acid methyl ester, 3-acetox~-vinylacetic acid
methyl ester and the remainder of the methyl acetoacetate
is obtained as the botiom product. This bottom pro-
duct is reacted with methanol according to the inventionto give methyl acetoacetate-. The product obtained in
this reaction is co~bined with the crude product men-
tioned above (from the con~inuous reaction of diketene
and methanol to give methyl acetoacetate) and is w~orked
up ~rith this crude product to give pure methyl aceto-
acetate.
b) Hlgh-bolling compounds and low-bolllng compounds
_ . _ . _ . .. . . ..... . ... .. . . _ . _ ... . .. . .. . . .. _ . .
- ænd subsequently the ~in portion of the ethyl aceto-
acetate are separaied off from the cLude produc~ w~ich
15 has formed in ~he con~inuous preparation of ethyl ;
acetoacetate ~rom diketene and ethanol. 3-Acetoxy-
crotonic acid e~hyl ester, 3-acetoxyvinylacetic acid
ethyl ester and the remairLder of the ethyl acetoacetate
areobiained as the bo~tom product. This bottom pro-
duct is reacted ~i'h ethanol according to the invention
to give ethyl acetoacetate. The product obtained in
this reaction is combined ~.ith the crude ~roduct ~en-
tioned above (from the continuous reac~ion of diketene
and ethanol to give ethyl acetoacetate) and is worked
u~ with this crude product to give pure ethyl aceto-
- - acetate.
The followin~ examples illustrate the process
according to the inNen~ion:
.~'' ' ' ' .
:

52~i2~
_ 9 _ .
- Exam~le 1
50 g of a mLxture of the fol'owing composition
were employed: 53.07' by ~igh~ of methanol, 45 ~ by
weight of 3-acetoxycrotonic acid methyl ester (cis- and
- 5 trans-forms) and 3-acetoxyviny:Lacetic acid methyl ester,
0.60~' by weight of methyl acetoaceiate and 0.5% by ~reight
of other middle- and high-boiling compounds. ~his mix-
_ . . _ . . . . . . . . ........... . . . .. . .. . ture was heated in an autoclave to 170C for 6 hours~
-a pressure of 11.3 oars being established at the end
of the reaction. The reaction mixture ~as again
- analy7ed a er it had cooled do~m, g~ving the following
composition: 67.2 ~ by weight of low-boiling compounds
. _ . _ . . . .. . . .. ... . . . . .. . . _ . . . ...
(for the most par~ methyl acet~te and m~thanol), 31.4%
by weight of methyl acetoacetate, 1 4% by ~eight of
ace~ox-ycrotQnic acid meth-yl ester and acetoxyvinylacetic
acid methyl ester and 0.29S by ~reight of other middle-
... . ... . . _ .. . .. ..
and high-boiling compo~ds.
... . . . . .. . .. . . . ~
Example 2
50 g of a mixture of the follo~g composition
~Jere employed: 53.6~/c by ~eight of methanol, 25.0% by
weight of methyl acetoacetate and 2l.4ob by ~Jeight of 3-
- acetoxycrotonic acid methyl ester ~cis and trans) and
~acetoxyvinylacetic acid methyl ester. This mixture
~las heated in an autoclave to 170C for 6 hours, a pres-
2~ sure of 10.8 bars being established at the end of the
reaction. A sample of ~he reaction mixtl~re ~ad ~he
- followi~ composition aft~er it had cooled down: 57.~b
_ . , . . . ... .. . . , . .. . . . . . . . _ _ ..... . . . . ... _ .
by weight of low-boiling com~ounds (for the most part
.... . .
methyl acetate and methanol), 35.7% by w~ight o~ methyl
.~'' ' ' .
,

;2S28
- -- 10 --
acetoacetate, 6.1% by weight of 3-acetoxycrotonic acid
methyl ester and 3-acetoxyvinylacetic acid methyl ester
and 0.3% by ~reight of other middle-and high-boiling
. .
- compounds.
.. . . . ... _ .~
~ _xGm~le 3
50 g of a mixture of the ~ollowdng composition
- were employed: 51.3% by weight of ethanol, o.goh by ~leight
of ethyl acetoaceta~e, 47 5% by weight of 3-acetoxycroton-
- ic acid ethyl ester (cis and trans) and 3-acetoxyvinyl-
acetic acid ethyl ester, and 0.3% by weight of other
middle- and high-boiling compounds. This mixture was
.. .. . . . ..
heated in an autoclave to 170C for 6 hours, a pressure
of 10.1 bars being esta~lished at the end of the reac- .
tion. The reaction mixture had the follo~ing compo-
sition after it h~d cooled down: 67 0% by ~reight of lo~r-
.. . . .. . . . . .. . . .. ...
boiling compo~mds (for the most part ethyl acetate and
ethanol), 30.5% by ~reight of ethyl acetoacetate, 1~9% by
~;eight of 3-acetoxycrotonic acid ethyl ester and 3-
ace~oxyvinylacetic acid ethyl ester9 and 0.6q~ by ~rei~ht
of other middle- and high-boiling compounds.
_, _ . . .. . . . _
Exæm~le 4
10~ g of a mixture of the follo~ing composition
ere employed: 44.~ by weight of ethanol, 25.7% by
weight o~ ethyl acetoacetate, 30.1% by weight of 3-
acetoxycrotonic acid ethyl ester (cis and trans) and 3-
acetoxyvinylacetic acid ethyl ester, and O.~,S by ~Jeight
. . .
o~ other middle- and high~boiling co pounds. ~his mi~-
- ture ~ias heated in an autocl~ve to 170C lor 6 hours, a
pressure of 9.7 bars being established at the end
~1 . .
~, .
~.
- . . .

S28
of the reaction. A sample of reaction mlxture had
the following compos~tion after it ha~ cooled do~Jn
53.1 % by weight of low-boiling compounds (for the most part
ethyl acetate and ethanol), ~5.4% by weight o~ ethyl
acetoacetate, 10.6~' by weight of 3-acetoxycrotonic acid
ethyl ester and 3-acetox~rvinylacetic acid ethyl ester,
and 0.9% by ~Jeight of other middle- and high~boiling
compounds.
... . . . .
.~ '- '
,
.:
: , ~ .

Representative Drawing

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Administrative Status

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Event History

Description Date
Inactive: Expired (old Act Patent) latest possible expiry date 2000-08-23
Grant by Issuance 1983-08-23

Abandonment History

There is no abandonment history.

Owners on Record

Note: Records showing the ownership history in alphabetical order.

Current Owners on Record
HOECHST AKTIENGESELLSCHAFT
Past Owners on Record
HEINZ WENDT
KLAUS GUNTHER
Past Owners that do not appear in the "Owners on Record" listing will appear in other documentation within the application.
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Document
Description 
Date
(yyyy-mm-dd) 
Number of pages   Size of Image (KB) 
Cover Page 1994-01-13 1 17
Claims 1994-01-13 2 41
Abstract 1994-01-13 1 15
Drawings 1994-01-13 1 8
Descriptions 1994-01-13 10 372