U.S. patent application number 14/661500 was filed with the patent office on 2015-07-09 for process for the preparation of fluoroalkyl (alkyl carbonates and carbamates.
The applicant listed for this patent is SOLVAY FLUOR GMBH. Invention is credited to Martin BOMKAMP, Jens OLSCHIMKE.
Application Number | 20150191414 14/661500 |
Document ID | / |
Family ID | 41360274 |
Filed Date | 2015-07-09 |
United States Patent
Application |
20150191414 |
Kind Code |
A1 |
BOMKAMP; Martin ; et
al. |
July 9, 2015 |
PROCESS FOR THE PREPARATION OF FLUOROALKYL (ALKYL CARBONATES AND
CARBAMATES
Abstract
Fluoroalkyl alkyl carbonates and fluorosubstituted carbamates
which are suitable as additives or solvents in lithium ion
batteries are prepared from fluoroalkyl fluoroformates and the
respective alcohol or amine. Methanol is the preferred alcohol,
dimethylamine and diethylamine are preferred amines. Fluoromethyl
methyl carbonate is the preferred compound to be produced.
Fluoroalkyl fluoroformates can be prepared from aldehydes and
carbonyl fluoride.
Inventors: |
BOMKAMP; Martin; (Hannover,
DE) ; OLSCHIMKE; Jens; (Hannover, DE) |
|
Applicant: |
Name |
City |
State |
Country |
Type |
SOLVAY FLUOR GMBH |
Hannover |
|
DE |
|
|
Family ID: |
41360274 |
Appl. No.: |
14/661500 |
Filed: |
March 18, 2015 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
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13383543 |
Jan 30, 2012 |
9000204 |
|
|
PCT/EP2010/059795 |
Jul 8, 2010 |
|
|
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14661500 |
|
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Current U.S.
Class: |
558/260 |
Current CPC
Class: |
C07C 68/02 20130101;
C07C 269/04 20130101; C07C 68/02 20130101; C07C 69/96 20130101;
C07C 269/04 20130101; C07C 271/14 20130101; C07C 69/96
20130101 |
International
Class: |
C07C 69/96 20060101
C07C069/96 |
Foreign Application Data
Date |
Code |
Application Number |
Jul 16, 2009 |
EP |
09165665.2 |
Claims
1. A fluoroalkyl (fluoro)alkyl carbonate of the general formula
(I), FCHR--OC(O)--OR', wherein R is a linear or branched alkyl with
1 to 5 carbon atoms; and R' is 2,2,2-trifluoroethyl.
2. The fluoroalkyl (fluoro)alkyl carbonate according to claim 1,
wherein the fluoroalkyl (fluoro)alkyl carbonate is
(1-fluoroethyl)-(2,2,2-trifluoroethyl)carbonate or
(fluoromethyl)-(2,2,2-trifluoroethyl)carbonate.
3. The fluoroalkyl (fluoro)alkyl carbonate according to claim 2,
wherein the fluoroalkyl (fluoro)alkyl carbonate is
(1-fluoroethyl)-(2,2,2-trifluoroethyl)carbonate.
4. The fluoroalkyl (fluoro)alkyl carbonate according to claim 2,
wherein the fluoroalkyl (fluoro)alkyl carbonate is
(fluoromethyl)-(2,2,2-trifluoroethyl)carbonate.
Description
[0001] This application is a continuation of U.S. application Ser.
No. 13/383,543, filed Jan. 30, 2012, which is a U.S. national stage
entry under 35 U.S.C. .sctn.371 of International Application No.
PCT/EP2010/059795, filed Jul. 7, 2008, which claims priority
benefit to European Application No. 09165665.2, filed Jul. 16,
2009. The entire contents of these applications are explicitly
incorporated herein by this reference.
[0002] The present invention concerns a process for the preparation
of fluoroalkyl (fluoro)alkyl carbonates (i.e. fluoroalkyl alkyl
carbonates and fluoroalkyl fluoroalkyl carbonates--the term in
brackets denotes an optional fluorine substitution), especially of
fluoromethyl methyl carbonate, and fluoroalkyl carbamates.
[0003] Fluoromethyl methyl carbonate is a known solvent additive
for lithium ion batteries. It can be prepared by the reaction of
dimethyl carbonate and elemental fluorine, as described in JP
patent application 2004010491, or by electrochemical fluorination,
see JP2006001843. Difluorinated products--difluoromethyl methyl
carbonate and bis-fluoromethyl carbonate--and higher fluorinated
products reduce yield and make separation processes necessary.
[0004] Partially fluorinated carbamates, as is described in U.S.
Pat. No. 6,159,640 have a high thermal stability, a high flash
point, a low vapor pressure, a high boiling point and other
advantageous properties which make them suitable as solvents for
lithium ion batteries, or as solvent additives for lithium ion
batteries.
[0005] Object of the present invention is to provide a process
which allows the selective manufacture of monofluorinated
fluoroalkyl alkyl carbonates and monofluoroalkyl fluoroalkyl
carbonates, namely fluoroalkyl alkyl carbonates and especially
fluoromethyl methyl carbonate, and of partially fluorinated
carbamates.
[0006] The process according to the present invention provides for
the manufacture of fluoroalkyl (fluoro)alkyl carbonates of the
general formula (I), FCHR--OC(O)--OR', and for the manufacture of
carbamates of general formula (VI), R.sup.1R.sup.2N--C(O)OCHRF,
wherein the process for the manufacture of fluoroalkyl
(fluoro)alkyl carbonates of the general formula (I),
FCHR--OC(O)--OR' wherein R denotes linear or branched alkyl with 1
to 5 C atoms, CH(CH.sub.3).dbd.CH, C(CH.sub.3).sub.2.dbd.CH,
CH.sub.2.dbd.CHX wherein X is CH.sub.2, C.sub.2H.sub.4, or H and R'
denotes linear or branched alkyl with 1 to 7 carbon atoms; linear
or branched alkyl with 2 to 7 carbon atoms, substituted by at least
one fluorine atom; phenyl; phenyl, substituted by 1 or more C1 to
C3 alkyl groups atoms or phenyl substituted by 1 or more chlorine
or fluorine atoms; or benzyl comprises a step of reacting a
fluoroalkyl fluoroformate of formula (II), FCHROC(O)F, or a
fluoroalkyl chloroformate of formula (II'), FCHROC(O)Cl, with an
alcohol of formula (III), R'OH, wherein R and R' have the meanings
given above, or comprises a step of reacting a chloroalkyl
fluoroformate of formula (IV), ClCHROC(O)F, or a chloroalkyl
chloroformate of formula (IV'), ClCHROC(O)Cl, wherein R has the
meaning given above, with an alcohol of formula (III), R'OH wherein
R' has the meaning given above, and a subsequent chlorine-fluorine
exchange, or wherein the process for the manufacture of carbamates
of general formula (VI), R.sup.1R.sup.2N--C(O)OCHRF, wherein
R.sup.1 and R.sup.2 independently of one another are identical or
different, linear C1 to C3 alkyl, branched C3 alkyl, wherein,
optionally, one or more hydrogen atoms in the R.sup.1 and R.sup.2
groups are substituted by fluorine atoms, and wherein R denotes
linear or branched alkyl with 1 to 5 C atoms, CH(CH.sub.3).dbd.CH,
C(CH.sub.3).sub.2.dbd.CH, or CH.sub.2.dbd.CHX wherein X is a
CH.sub.2 or C.sub.2H.sub.4 group, comprises a step of reacting a
fluoroalkyl fluoroformate of formula (II), FCHROC(O)F, or a
fluoroalkyl chloroformate of formula (II'), FCHROC(O)Cl, with an
amine of formula (VII), R.sup.1R.sup.2NH, wherein R.sup.1 and
R.sup.2 have the meanings given above, or comprises a step of
reacting a chloroalkyl fluoroformate of formula (IV), ClCHROC(O)F,
or a chloroalkyl chloroformate of formula (IV'), ClCHROC(O)Cl,
wherein R has the meaning given above, with an amine of formula
(VII), R.sup.1R.sup.2NH, wherein R.sup.1 and R.sup.2 have the
meanings given above, and a subsequent chlorine-fluorine
exchange,
[0007] Instead of the amine of formula (VII), a silylsubstituted
amine can be applied, especially an amine of formula (IX),
R.sup.1R.sup.2NSiAlk.sub.3 wherein the Alk groups are the same or
different and denote alkyl selected from the group consisting of
methyl, ethyl and propyl. The reaction of the fluoroformiate and
the amine can be performed in the presence of acid scavengers, e.g.
in the presence of tertiary amines like trimethylamine or
triethylamine.
[0008] Preferably, the process according to the present invention
provides for the manufacture of fluoroalkyl (fluoro)alkyl
carbonates of the general formula (I), FCHR--OC(O)--OR' wherein R
denotes linear or branched alkyl with 1 to 5 C atoms or H and R'
denotes linear or branched alkyl with 1 to 7 carbon atoms; linear
or branched alkyl with 2 to 7 carbon atoms, substituted by at least
one fluorine atom; phenyl; phenyl, substituted by 1 or more C1 to
C3 alkyl groups atoms or phenyl substituted by 1 or more chlorine
or fluorine atoms; or benzyl
comprising a step of reacting a fluoroalkyl fluoroformate of
formula (II), FCHROC(O)F, or a fluoroalkyl chloroformate of formula
(II'), FCHROC(O)Cl, with an alcohol of formula (III), R'OH, wherein
R and R' have the meanings given above, or comprising a step of
reacting a chloroalkyl fluoroformate of formula (IV), ClCHROC(O)F,
or a chloroalkyl chloroformate of formula (IV'), ClCHROC(O)Cl,
wherein R has the meaning given above, with an alcohol of formula
(III), R'OH wherein R' has the meaning given above, and a
subsequent chlorine-fluorine exchange.
[0009] An especially preferred embodiment of the present invention
provides for the manufacture of fluoroalkyl (fluoro)alkyl
carbonates of the general formula (I), FCHR--OC(O)--OR', and for
the manufacture of carbamates of general formula (VI),
R.sup.1R.sup.2N--C(O)OCHRF,
wherein the process for the manufacture of fluoroalkyl
(fluoro)alkyl carbonates of the general formula (I),
FCHR--OC(O)--OR' wherein R denotes linear or branched alkyl with 1
to 5 C atoms, CH(CH.sub.3).dbd.CH, C(CH.sub.3).sub.2.dbd.CH,
CH.sub.2.dbd.CHX wherein X is CH.sub.2, C.sub.2H.sub.4, or H and R'
denotes linear or branched alkyl with 1 to 7 carbon atoms; linear
or branched alkyl with 2 to 7 carbon atoms, substituted by at least
one fluorine atom; phenyl; phenyl, substituted by 1 or more C1 to
C3 alkyl groups atoms or phenyl substituted by 1 or more chlorine
or fluorine atoms; or benzyl comprises a step of reacting a
fluoroalkyl fluoroformate of formula (II), FCHROC(O)F, or a
fluoroalkyl chloroformate of formula (II'), FCHROC(O)Cl, with an
alcohol of formula (III), R'OH, wherein R and R' have the meanings
given above.
[0010] The term "(fluoro)alkyl" indicates alkyl groups, including
groups of the structure CH(CH.sub.3).dbd.CH,
C(CH.sub.3).sub.2.dbd.CH, CH.sub.2.dbd.CHX wherein X is a single
bond, CH.sub.2, or C.sub.2H.sub.4, and alkyl groups substituted by
at least one fluorine atom. Consequently, the present invention
provides for the manufacture of monofluorosubstituted fluoroalkyl
alkyl carbonates and fluoroalkyl fluoroalkyl carbonates wherein one
fluoroalkyl group is monosubstituted and the other fluoroalkyl
group may be substituted by one or more fluorine atoms. In
fluoroalkyl fluoroalkyl carbonates, the fluoroalkyl groups may be
the same or different; at least one of the fluoroalkyl groups is
monofluorinated.
[0011] Instead of the alcohol or additionally to the alcohol, a
respective alkali metal alcoholate can be applied, for example, the
respective lithium, sodium, potassium or cesium alcoholate. It is
preferred to manufacture carbonates wherein R denotes C1 to C3
alkyl, CH.sup.2.dbd.CH--CH.sup.2, CH(CH.sub.3).dbd.CH,
C(CH.sub.3).sub.2.dbd.CH, or H, and more preferably, C1 to C3 alkyl
or H. It is most preferred to manufacture carbonates wherein R is
H. According to this preferred embodiment, a process is provided
for the manufacture of fluoromethyl (fluoro)alkyl carbonates said
process comprising a step of reacting fluoromethyl fluoroformate or
fluoromethyl chloroformate and an alcohol, or, in an alternative,
to react chloromethoxy chloroformate with an alcohol and to perform
a subsequent chlorine fluorine exchange. It is especially preferred
to use fluoromethyl fluoroformate which has the formula
FCH.sub.2--O--C(O)F.
[0012] The invention will now be explained in detail in view of the
preferred alternative, namely the preparation of fluoroalkyl
(fluoro)alkylcarbonates from fluoromethyl fluoroformate and an
alcohol; also in this embodiment, the alcohol can be partially or
completely be substituted by the respective alkali metal
alcoholate, for example, by lithium, sodium, potassium or cesium
alcoholate. The alcohol preferably denotes a C1 to C5 alcohol; a C2
to C5 alcohol substituted by at least one fluorine atom; allyl
alcohol; crotyl alcohol; prenyl alcohol; phenol or phenol,
substituted by 1 or more C1 to C3 alkyl groups; or benzyl.
Preferably, R' is a linear or branched C1 to C5 alkyl group, and
thus, the alcohol is a C1 to C5 alkanol, more preferably, it is
methanol, ethanol, n-propanol, i-propanol, allyl alcohol,
n-butanol, i-butanol, 2-methylpropanol, n-pentanol, i-pentanol, or
2,2,2-trifluoroethanol. If trifluoroethanol is applied, it is
possible to produce carbonates which comprise fluorine substituents
on both alkyl groups, for example,
fluoromethyl-(2,2,2-trifluoroethyl)carbonate or
(1-fluoroethyl)-(2,2,2-trifluoroethyl)carbonate. Especially
preferably, the alcohol is methanol, ethanol, allyl alcohol,
n-propanol and i-propanol. The most preferred alcohol is
methanol.
[0013] If desired, a mixture of alcohols can be applied in a
desired molar ratio. For example, a mixture of methanol and ethanol
can be applied in a molar ratio of 1:1. In this case, a mixture of
the respective methyl carbonate and ethyl carbonate in a molar
ratio of approximately 1:1 is obtained.
[0014] The alcoholysis reaction can be performed in the presence of
an HF scavenger e.g. LiF, NaF, KF or CsF, or in the presence of
base, e.g. in the presence of ammonia or a primary, secondary or
tertiary amine, e.g. triethylamine or pyridine. Preferably, it is
performed in the absence of a base.
[0015] The molar ratio between alcohol and formate preferably is
equal to or greater than 0.9:1. Preferably, it is equal to or lower
than 5:1. Very good results are achieved when the ratio of alcohol
and formate is in the range of 0.95:1 to 1.2:1.
[0016] The reaction temperature during the alcoholysis reaction is
not critical. Often, the reaction is exothermic, thus, it may be
advisable even to cool the reaction mixture, especially if an
alkali metal alcoholate is applied. The temperature during
alcoholysis is preferably equal to or higher than -80.degree. C.,
more preferably, equal to or higher than -78.degree. C. The upper
temperature can be dependent from pressure and boiling point of the
starting materials, e.g. from the boiling point of the alcohol.
Often, the temperature is equal to or lower than 85.degree. C.
[0017] The reaction can be performed in any suitable reactor, e.g.
in an autoclave.
[0018] The reaction can be performed batch wise or
continuously.
[0019] The resulting reaction mixture can be separated by known
methods, e.g. by distillation, precipitation and/or
crystallization. If desired, the reaction mixture can be contacted
with water to remove water-soluble constituents. Due to the
specific type of reaction, organic carbonates with a higher degree
of fluorination are formed, if at all, in only very minor
proportions.
[0020] According to another alternative, fluoroalkyl (fluor)alkyl
carbonates of the general formula (I), FCHR--OC(O)--OR' wherein R
and R' have the meaning given above are prepared in a process
[0021] comprising a step of reacting a chloroalkyl fluoroformate of
formula (IV), ClCHROC(O)F, or a chloroalkyl chloroformate of
formula (IV'), ClCHROC(O)Cl, wherein R has the meaning given above,
with an alcohol of formula (III), R'OH wherein R' has the meaning
given above, and a subsequent chlorine-fluorine exchange.
[0022] Thus, in a first step, an intermediate carbonate of formula
(V), ClCHR--OC(O)--OR', is produced. In this formula (V), R and R'
have the meanings given above. This intermediate carbonate is then
reacted with a reactant capable of substituting a fluorine atom for
the chlorine atom. This reaction is known as "Halex" reaction.
Reactants suitable to perform a chlorine-fluorine exchange are
generally known. Especially suitable as such a reactant are
alkaline or alkaline earth metal fluorides, ammonium fluoride,
amine hydrofluorides of formula (IX), N(R.sup.1).sub.4F wherein the
substituents R.sup.1 are the same or different and denote H or C1
to C5 groups with the proviso that at least 1 substituent R.sup.1
is a C1 to C5 alkyl group. Also amine hydrofluorides are suitable
in which the nitrogen atom is part of a heterocyclic ring system,
for example, pyridinium hydrofluoride,
1,8-diazabicyclo[5.4.0]undec-7-ene, and
1,5-diaza-bicyclo[4.3.0]non-5-ene. Instead of the fluorides, or
additionally to them, hydrofluoride adducts can be used for the
Halex reaction, e.g. CsF.HF. Other fluorides are likewise suitable
as reactant, e.g. AgF. The Halex reaction can be performed in the
absence or in the presence of a solvent, for example, in the
presence of a nitrile. Often, the reaction is performed at elevated
temperature, e.g. at a temperature equal to or higher than
50.degree. C.
[0023] The workup of the reaction mixture which comprises the
chloride salt and possibly excess fluoride salt of the fluorinating
reactant, and the fluorinated carbonate and possibly unreacted
starting material, is performed in a known manner. For example,
solids are removed by filtration, and the liquid phase is subjected
to a fractionated distillation or precipitation after removal of
any solvents.
[0024] The fluorinated organic carbonates produced by the process
of the present invention are useful as additives or solvents for
lithium ion batteries. They provide advantages like modifying the
viscosity, reduce flammability and appear to modify the electrodes
under formation of beneficial films.
[0025] Preferred amines R.sup.1R.sup.2NH for the manufacture of
carbamates are those wherein R1 and R2 are the same or different
and correspond to methyl, ethyl, n-propyl and i-propyl. As to the
manufacture of the carbamates, the molar ratio between amine and
formate is preferably equal to or greater than 0.9:1. If the amine
functions also as acid scavenger, the ratio is preferably equal to
or greater than 1.8:1. Preferably, the ratio between amine and
formate is equal to or lower than 5:1. Preferably, the ratio
between amine and formate are between 0.95:1 to 1.2:1, or, if the
amine functions as a base, in the range of 1.9:1 to 2.4:1. The
reaction temperature is preferably in the range of 0 to 50.degree.
C. The workup of the reaction mixtures is performed in a known
manner. Solids are filtered off, and the carbamates can be isolated
from the resulting liquid raw product by distillation.
[0026] Compounds of formula (II), FCHROC(O)F, can be prepared from
the respective chloroalkyl chloroformates in a "Halex" type
reaction, i.e. substitution of fluorine atoms for the chlorine
atoms by fluorinating agents, as already described above, e.g.
using a fluorinating reactant like alkali or alkaline earth metal
fluorides, e.g. LiF, KF, CsF, NaF, NH.sub.4F or amine
hydrofluorides, or the respective HF adducts. The chloroalkyl
chloroformates themselves are available through the reaction
between phosgene and an aldehyde as described in U.S. Pat. No.
5,712,407. It is preferred to produce the intermediate compounds of
formula (II), FCHROC(O)F, from carbonyl fluoride and an aldehyde.
Thus, another aspect of the present invention concerns a process
for the manufacture of intermediate compounds of formula (II),
FCHROC(O)F, from carbonyl fluoride and an aldehyde of formula
RC(O)H wherein R denotes linear or branched alkyl with 1 to 5 C
atoms or H. Preferably, it denotes H; here, the aldehyde is
formaldehyde. The formaldehyde can be can be applied in the form of
paraformaldehyde or trioxane which must be cracked, e.g. thermally,
to form the monomeric formaldehyde.
[0027] The molar ratio between carbonyl fluoride and the aldehyde
is preferably equal to or greater than 0.9:1. It is preferably
equal to or lower than 5:1.
[0028] Preferably, the molar ratio between carbonyl fluoride and
aldehyde is in the range of 0.9:1 to 5:1. More preferably, the
molar ratio between carbonyl fluoride and aldehyde is in the range
of 0.9:1 to 3:1.
[0029] Preferably, the reaction between carbonyl fluoride and the
aldehyde is catalyzed.
[0030] The reaction can be catalyzed, for example, by F.sup.-. For
example, the reaction can be catalyzed by HF, which may be added as
such or prepared in situ by the addition of low amounts of
water.
[0031] Preferred catalysts are those which contain fluoride anions,
e.g. alkaline earth metal fluorides or alkali metal fluorides such
as CsF, or catalysts which contain fluoride ions formed from
carbonyl fluoride and a pre-catalyst. Preferred pre-catalysts are
dialkyl formamides, especially dimethyl formamide. It is assumed
that the formamide and carbonyl fluoride form a "naked" fluoride
ion which starts a nucleophilic reaction on the aldehyde. The
negatively charged oxygen of the formed adduct of the fluoride ion
and the aldehyde molecule then reacts with a carbonyl fluoride
molecule forming fluoromethyl fluoroformate or generally, the
fluoroalkyl fluoroformate.
[0032] Pyridine, advantageously 4-dialkylaminopyridines, especially
4-dimethylaminopyridine, are also considered as suitable
pre-catalysts.
[0033] The reaction preferably is performed batch wise, e.g. in an
autoclave. Alternatively, it can be performed continuously.
[0034] The reaction temperature can vary. For example, when a very
effective catalyst is applied, the reaction may even be performed
at ambient temperature. It has to be kept in mind, however, that in
the case of formaldehyde as starting material, the monomeric form
must be provided by cracking of paraformaldehyde or 1,3,5-trioxane.
Thus, while the reaction as such often could be performed at low
temperature, nevertheless heat must be applied for cracking
[0035] In the case of formaldehyde as starting material, the
reaction preferably is performed at a temperature equal to or
higher than 100.degree. C. It is preferably performed at a
temperature equal to or lower than 300.degree. C. When aldehydes
are used as starting material which must not be thermally cracked,
the reaction can be performed at a temperature equal to or higher
than 0.degree. C. and equal to or lower than 200.degree. C. It is
preferred to perform the reaction at such an elevated temperature
and/or for a sufficient time until the desired conversion has taken
place.
[0036] It is performed in the liquid phase or under supercritical
conditions. The pressure is selected such that at least a part of
the carbonyl fluoride is present in the liquid phase. The pressure
depends from the reaction temperature; the higher the reaction
temperature, the higher is the pressure in the reactor. The
reaction can be performed at ambient pressure (about 1 Bar
absolute). For example, COF.sub.2 can be introduced into the liquid
reaction mixture or starting material though an immersed pipe.
Preferably, the reaction is performed at a pressure equal to or
higher than 5 bar (abs.). Preferably, the reaction is performed at
a pressure equal to or lower than 50 bar (abs.). If, as done in one
example, the reaction temperature is sufficiently high, the content
of the reactor is in a supercritical state. The reaction vessel can
be pressurized, if desired, with an inert gas, especially with
nitrogen.
[0037] If desired, the fluoroalkyl fluoroformates, and especially
the fluoromethyl fluoroformate, can be isolated from the reaction
mixture according to methods known in the art, e.g. by
distillation. The fluorosubstituted formates formed can be applied
for any purposes for which compounds with a C(O)F function or a
FCH.sub.2O function are used. For example, they can be used as
fluorinating agent or to introduce a protecting group in aminoacids
or peptides. In a preferred embodiment, the formates are reacted,
as described above, with an alcohol to produce fluoromethyl alkyl
esters of carbonic acid.
[0038] A preferred aspect of the present invention concerns a
process comprising 2 or 3 steps for the manufacture of compounds of
formula (I), FCHROC(O)--OR', wherein R denotes linear or branched
alkyl with 1 to 5 C atoms or H and R' denotes linear or branched
alkyl with 1 to 7 carbon atoms; linear or branched alkyl with 2 to
7 carbon atoms substituted by at least one fluorine atom; phenyl;
benzyl; phenyl, substituted by 1 or more C1 to C3 alkyl groups
atoms or phenyl substituted by 1 or more chlorine or fluorine
atoms. This process is performed according to two alternatives.
[0039] The first alternative comprises:
[0040] A step of preparing a fluoroalkyl fluoroformate of formula
(II), FCHROC(O)F, from carbonyl fluoride and an aldehyde RC(O)H
wherein R denotes linear or branched alkyl with 1 to 5 C atoms or
H; and a step of reacting the fluoroalkyl fluoroformate of formula
(II) with an alcohol of formula (III), R'OH, wherein R and R' have
the meanings given above.
[0041] Instead of the alcohol or additionally to the alcohol, the
respective alkali metal alcoholate can be applied, for example, the
respective potassium or sodium alcoholate.
[0042] Also here, the group R preferably denotes H, and the
aldehyde concerned is formaldehyde. The formaldehyde can be applied
in the form of paraformaldehyde or 1,3,5-trioxane which must be
cracked, e.g. thermally, to form the monomeric formaldehyde.
[0043] A preferred embodiment of this 2-step process according to
the present invention provides for the manufacture of fluoromethyl
alkyl carbonates comprising:
A step of preparing fluoromethyl fluoroformate from carbonyl
fluoride and formaldehyde, 1,3,5-trioxane or paraformaldehyde, and,
with or without isolation, and subsequently, A step of reacting the
fluoromethyl fluoroformate with an alcohol of formula (III), R' OH,
wherein R' preferably denotes linear or branched alkyl with 1 to 7
C atoms; CH.sub.2.dbd.CHX wherein X is CH.sub.2 or C.sub.2H.sub.4;
CH(CH.sub.3).dbd.CH, C(CH.sub.3).sub.2.dbd.CH; phenyl; phenyl,
substituted by 1 or more C1 to C3 alkyl groups atoms or phenyl
substituted by 1 or more chlorine or fluorine. Preferably, the
alcohol is selected from the group consisting of methanol, ethanol,
n-propanol, i-propanol, allyl alcohol, n-butanol and n-pentanol.
Especially preferably, the alcohol is allyl alcohol, methanol or
ethanol, and most preferably, methanol.
[0044] Preferred embodiments of the steps are those already
described above, especially what concerns the preferred use of a
catalyst, using a formamide, especially dimethyl formamide, as
preferred pre-catalyst in the first step, the pressure and
temperature in the first and second step, the optional use of a
base in the second step, the respective pressures, reaction
temperatures etc; the preferred embodiments described above for the
respective reaction steps apply also for the 2-step process of the
invention.
[0045] The other alternative comprises a process which includes a
Halex reaction.
[0046] In this alternative, in a first step, carbonyl chloride
(phosgene) is reacted with RC(O)H wherein R denotes linear or
branched alkyl with 1 to 5 C atoms or H. The formed intermediate
chloroalkyl chloroformate of formula (IV'), ClCHRC(O)Cl wherein R
has the meaning given above is then either subjected to a Halex
reaction to form the fluoroalkyl formate of formula (I) which is
then reacted with an alcohol or an alcoholate as described above to
produce the fluoroalkyl (fluoro)alkyl carbonates of formula (I); or
the formed intermediate chloroalkyl chloroformate of formula (VII),
ClCHROC(O)Cl wherein R has the meaning given above, is then reacted
with an alcohol or an alcoholate as described above to produce the
chloroalkyl (fluoro)alkyl carbonate of formula (V) which then is
subjected to a Halex reaction as described above to produce the
fluoroalkyl (fluoro)alkyl carbonates of formula (I).
[0047] Another preferred aspect of the present invention concerns a
process for the manufacture of compounds of formula (VI),
R.sup.1R.sup.2N--C(O)--OCHFR, wherein R denotes linear or branched
alkyl with 1 to 5 C atoms and R.sup.1 and R.sup.2 have the meaning
given above. This process is performed according to two
alternatives.
[0048] The first alternative comprises:
A step of preparing a fluoroalkyl fluoroformate of formula (II),
FCHROC(O)F, from carbonyl fluoride and an aldehyde RC(O)H wherein R
denotes linear or branched alkyl with 1 to 5 C atoms or H; and a
step of reacting the fluoroalkyl fluoroformate of formula (II) with
an amine of formula (VIII), R.sup.1R.sup.2NH, wherein R.sup.1 and
R.sup.2 have the meanings given above.
[0049] Another embodiment of the present invention are chloroalkyl
fluoroalkyl carbonate intermediates of formula (V'), ClCHRC(O)OR''
wherein R denotes linear or branched alkyl with 1 to 5 C atoms or H
and wherein R'' denotes linear or branched alkyl with 1 to 7 carbon
atoms, substituted by at least one fluorine atom. Preferably, in
compounds of formula (V'), R denotes CH.sub.3 or H, and R'' denotes
2,2,2-trifluoroethyl, with the exception of 1-chloroethyl
2,2,2-trifluoroethyl carbonate.
[0050] These intermediates can be prepared from 1-chloroalkyl
chloroformates and a fluorinated alcohol or the alcoholate of a
fluorinated alcohol, e.g. the lithium, sodium, potassium or cesium
alcoholate of a fluorinated alcohol; trifluoroethanolates are
possibly instable. These intermediates can be used, as described,
as starting material to produce the fluoroalkyl fluoroalkyl
carbonates of the present invention. They can also be used as
intermediates in chemical synthesis.
[0051] The process of the present invention concerning the
preparation of fluoromethyl alkyl carbonates allows for the
selective production of monofluorinated products; higher
fluorinated products are formed, if at all, in only minor amounts.
The compounds can be used neat as a solvent in the Li ion
batteries, or, as an additive, e.g. for reducing the viscosity of
the solvent. The amount as an additive is, for example, in a range
from 0.5 to 60% by weight.
[0052] Since a main application field for the compounds of formula
(I) is the use as solvents or additives in lithium ion batteries,
it is preferred not start from chlorinated compounds because
chlorine is undesired as impurity in the technical field. Thus, the
reaction path without the necessity of Halex reactions is
preferred.
[0053] Compounds wherein R has the meaning of CH(CH.sub.3).dbd.CH,
C(CH.sub.3).sub.2.dbd.CH, CH.sub.2.dbd.CHX wherein X is CH.sub.2,
C.sub.2H.sub.4, preferably CH.sub.2, are suitable as monomers for
copolymerization reactions.
[0054] Should the disclosure of any patents, patent applications,
and publications which are incorporated herein by reference
conflict with the description of the present application to the
extent that it may render a term unclear, the present description
shall take precedence.
[0055] The invention will now be further described in examples
without intending to limit it.
EXAMPLE 1
Preparation of fluoromethyl fluoroformate
[0056] Paraformaldehyde (10.2 g; 340 mmol) and dimethylformamide
(1.5 g; 71 mmol) were given into an autoclave with an internal
volume of about 500 ml. The autoclave was closed, evacuated and
pressurized to about 5 bar (abs.) with dry nitrogen and evacuated
again. Then, carbonyl fluoride (32 g; 485 mmol) was given into the
autoclave. The autoclave was heated overnight to about 230.degree.
C.; the pressure rose to about 35 bar (abs.). Then, the autoclave
was cooled to ambient temperature, the pressure fell now to about
10 bar (abs.). Gaseous components of the autoclave were purged
through a washer. The autoclave was then pressurized two times with
nitrogen, each time up to a pressure of about 5 bar (abs.).
[0057] If desired, fluoromethyl fluoroformate formed can be
isolated by distillation.
EXAMPLE 2
Preparation of fluoromethyl methyl carbonate ("F1DMC")
[0058] Into the autoclave cooled to -10.degree. C. containing the
reaction residue of example 1, methanol (10 ml; 247 mmol) is added.
The autoclave was closed, and the reaction mixture was stirred
overnight at ambient temperature. A sample was taken from the
reaction mixture and analyzed by gas chromatography (GC) and gas
chromatography/mass spectrum (GC-MS). The reaction mixture
contained F1DMC in about 25% (area in GC). Further, methanol and
dimethoxymethane were identified (the latter obtained probably as
reaction product of excess methanol and formaldehyde).
[0059] If desired, the reaction mixture can be washed with water to
remove water-soluble constituents. After drying, e.g. using
MgSO.sub.4, fluoromethyl methyl carbonate can be isolated in pure
form by distillation.
EXAMPLE 3
Preparation of fluoroethyl fluoroformate
[0060] Acetaldehyde (12 g; 272 mmol) and dimethylformamide (200 mg;
71 mmol) were given into an autoclave with an internal volume of
about 40 ml. The autoclave was closed, evacuated and pressurized to
about 5 bar (abs.) with dry nitrogen and evacuated again. Then,
carbonyl fluoride (18 g; 272 mmol) was given into the autoclave
over a period of 30 min. The mixture was stirred at room
temperature for 30 min after which the pressure fell from 20 bar to
0 bar. The autoclave was then pressurized two times with nitrogen,
each time up to a pressure of about 5 bar (abs.).
[0061] If desired, fluoroethyl fluoroformate formed can be isolated
by distillation.
EXAMPLE 4
Preparation of fluoroethyl methyl carbonate ("F1EMC")
[0062] In a 100 mL PFA-flask fluoroethyl fluoroformate (24.7 g, 225
mmol) was cooled to -78.degree. C. Methanol (12 mL, 310 mmol) was
added over a period of 15 min. The mixture was stirred at
-78.degree. C. for 30 min. After warming up to room temperature the
reaction was stirred for further 16 h. The resulting mixture was
washed with water (3.times.10 ml), molecular sieve (0.4 nm) was
added, and after stirring for 4 h at room temperature, all solids
were removed by filtration and the resulting crude product was
purified by distillation under reduced pressure (100 mbar).
[0063] The boiling point was 50.degree. C. at a pressure of 200
mbar.
Yield: 19.1 g (70% of theory).
EXAMPLE 5
Preparation of fluoroethyl ethyl carbonate ("F1DEC")
[0064] In a 100 mL PFA-flask fluoroethyl fluoroformate (27.0 g, 245
mmol) was added to dry NaF (15 g; 357 mmol). After cooling the
mixture to -78.degree. C. ethanol (12 mL, 310 mmol) was added over
a period of 15 min. The mixture was stirred at -78.degree. C. for
30 min. After warming up to room temperature the reaction was
stirred for further 16 h. After addition of 5 g molecular sieve
(0.4 nm) and stirring for 4 h at room temperature, all solids were
removed by filtration and the resulting crude product was purified
by distillation under reduced pressure (100 mbar).
EXAMPLE 6
Preparation of fluoromethyl methyl carbonate Including a Halex
Reaction
[0065] In a 100 mL one necked flask equipped with a dropping
funnel, a solution of chloromethyl chloroformate (10.0 g; 78 mmol)
in 30 mL diethyl ether was cooled to 0.degree. C. Over a period of
15 minutes a mixture of methanol (4 mL, 100 mmol) and pyridine (7
mL, 86 mmol) was added slowly to the stirred solution and kept at
0.degree. C. for 2 h. The obtained white precipitate was removed by
filtration and the resulting solution was added to a mixture of
potassium fluoride (9 g, 145 mmol) and 18-crown-6 (1.2 g, 5 mmol).
After stirring the mixture for 18 h, formation of fluoromethyl
methyl carbonate could be proven by GC and MS.
EXAMPLE 7
Preparation of Et.sub.2N--C(O)OCH.sub.2F
[0066] In a 100 mL PFA-flask, fluoromethyl formate (27.0 g, 245
mmol) is given. Diethylamine (50.5 mL; 0.490 mmol) is added
dropwise at about 0.degree. C. The mixture is stirred for 1 hour.
Solids are filtered off, and the resulting liquid is subjected to a
distillation to isolate pure fluoromethyl N,N-diethylcarbamate.
* * * * *