Process for the preparation of fluoropolyoxyalkylenes having...

Organic compounds -- part of the class 532-570 series – Organic compounds – Oxygen containing

Reexamination Certificate

Rate now

  [ 0.00 ] – not rated yet Voters 0   Comments 0

Details

C568S618000, C568S674000, C568S675000, C568S679000, C568S689000

Reexamination Certificate

active

06573411

ABSTRACT:

The present invention relates to a process for the preparation of fluoropolyoxyalkylenes having at least one methylol end group —CH
2
OH and containing at least one chlorine atom in the other end group.
It is known in the prior art, for example GB 1,309,401 or U.S. Pat. No. 3,766,251, that the perfluoropolyethers with methylol end groups can be prepared by reduction of the corresponding perfluoropolyethers having —COOR end groups, wherein R is a C
1
-C
5
alkyl group, in the presence of metal-hydrides reducing agents, such as lithium-aluminum hydride (LiAlH
4
), sodium-boron hydride (NaBH
4
), lithium-boron hydride (LiBH
4
), in the presence of ethyl ether, dioxane, diglyme, tetrahydrofuran, or in the case of NaBH
4
in the presence of water or methanol, followed by the hydrolysis of the obtained reaction product by the aforesaid reduction.
The reduction reaction is carried out by directly adding a solution of perfluoropolyoxyalkylene alkylcarboxy ended in a solvent to a solution or suspension of the metal hydride in a solvent maintained under stirring at temperatures between 0°-100° C.
The reaction process scheme wherein a perfluoropolyether is used with an end group —COOC
2
H
5
and NaBH
4
as reducing agent is as follows:
a) 2R
f
—COOC
2
H
5
+NaBH
4
→(R
f
—CH
2
O)
2
B(OC
2
H
5
)
2
Na
+
b) (R
f
—CH
2
O)
2
B(OC
2
H
5
)
2

Na
+
+HCl+3H
2
O→2R
f
—CH
2
OH+2C
2
H
5
OH+NaCl+H
3
BO
3
R
f
=perfluoropolyoxyalkylene chain.
The Applicant has found that it is not possible to carry out said process, with high yields and selectivity, using as starting compounds fluoropolyethers having in their structure one end group cointaining at least one Cl atom and the other end group being a carboxylic ester, to obtain the corresponding fluoropolyethers with a methylol end group.
Besides, a hardly controllable self-catalytic decomposition of the reducing agent takes place, which implies significant process risks as regards its conduction bringing to very low and non reproducible yields in the desired product.
The need was therefore felt to prepare with high yields and selectivity, by a controllable process, fluoropolyethers having one end group containing one chlorine atom and the other end group being —CH
2
OH.
The Applicant has unexpectedly found that it is possible to solve the above technical problem by starting from fluoropolyethers having one end group containing one Cl atom and the other end group a carboxylic ester to obtain with high yields and selectivity the corresponding fluoropolyethers with —CH
2
OH end groups.
It is therefore an object of the present invention a process to obtain fluoropolyoxyalkylenes having one end group containing one Cl atom and the other end group formed by a methylol group, having structure:
T—O—(CF
2
CF(CF
3
)O)
n−1
—(CF(CF
3
)O)
m
—CF
2
—CH
2
OH  (I)
wherein:
T=C
1
-C
3
perfluoroalkyl containing one Cl atom;
n=an integer from 1 to 15;
m
=0-0.5;
m+n being such to have a number average molecular weight in the range 280-4,000, preferably 280-1,000,
said process comprising the following steps:
a) the gradual addition, in inert gas atmosphere, of a mixture formed by an aprotic or protic solvent and a reducing agent selected from the metal hydrides class, to an ester precursor having the structure
T—O—(CF
2
CF(CF
3
)O)
n−1
—(CF(CF
3
)O)
m
—CF
2
—COOR  (II)
 wherein T, m, n have the above meaning and R represents a C
1
-C
20
alkyl, aromatic, cycloalkyl or heterocyclic residue, said residues being optionally substituted, maintaining the reaction mixture under stirring at a temperature in the range 0°-20° C., preferably 5° C.-15° C.;
b) hydrolysis of the reaction product obtained in step a) with an aqueous acid solution, with formation of an aqueous phase and of an organic phase, and the subsequent separation from the organic phase of the compounds of structure (I) having one end group —CH
2
OH and the other one containing Cl.
The ester precursor (II) can optionally be used in admixture with an aprotic or protic solvent.
The solvents for the reducing agent and for the ester precursor can be aprotic solvents, such as for example tetrahydrofuran, diglyme, dioxane or protic solvents as for example methanol, ethanol, isopropanol, isobutanol, preferably ethanol. It is possible to use mixtures of the aforesaid solvents.
As reducing agents, metal hydrides can be used, such as for example lithium-aluminum hydride (LiAlH
4
), sodium-boron hydride (NaBH
4
), lithium-boron hydride (LiBH
4
) dissolved or in suspension in the above solvents. Preferably a solution or a suspension containing 0.1-15% by weight of sodium-boron hydride (NaBH
4
) is used. The NaBH
4
amount with respect to the ester precursor (II) is comprised between the stoichiometric reaction value and an excess of 30%.
Step b) of hydrolysis and separation of the compound (I) is carried out by known methods. Generally the hydrolysis is carried out by gradually adding the reaction compound obtained in step a) to an aqueous solution of HCl, preferably at a concentration of 5-10% by weight, in an amount at least equiponderal with respect to the precursor (II). The addition of the compounds obtained from step a) to the acid solution is gradually carried out as the optional excess of the unreacted reducing agent hydrolyzes developing gaseous hydrogen. At the end of step b), several aqueous washings can optionally be carried out to completely remove the inorganic salts from the reduced fluorinated compound (I).
The hydrolysis of the reaction mixture of step a) can also be carried out by directly adding to said mixture the aqueous acid solution.
By the process of the present invention it is possible to obtain a complete conversion of the starting ester, a selectivity higher than 99% and an yield on the separated compound higher than or equal to 90%, preferably higher than or equal to 95%.
Furthermore in the present process hydrogen develops only in limited amounts with remarkable advantages as regards the conduction and safety of the process in an industrial plant.
Step a) of the process reduction of the present invention can be carried out in the presence of stabilizers of the reducing agent such the alkaline metal alcoholates, for example sodium ethylate.
The present process, characterized in that the reduction reaction is carried out by gradually adding a solution or suspension of the reducing agent to the fluoroether (II) to be reduced, can be used to reduce fluoroalkanes or fluoroethers free from end groups containing Cl but containing at least one —COOR end group with R as above defined.
In other words by using fluorinated esters as precursors it is possible to obtain the corresponding fluoroethers or fluoroalkanes having at least one methylol —CH
2
OH group with high conversions and selectivity higher than 99% by using a limited excess of the reducing agent, generally lower than 30% of the stoichiometric value.
As precursors to be reduced, monofunctional or bifunctional perfluoropolyethers having the following general formula:
T
1
—CFW
1
—O—R
f1
—CFW
2
—T
2
  (III)
can be used, wherein:
T
1
, T
2
, equal to or different from each other, are selected from end groups of the —COOR type, or —F, —CF
3
, —CF
2
CF
3
with the proviso that at least one between T
1
and T
2
is —COOR;
W
1
and W
2
, equal to or different from each other, are F, CF
3
; R
f1
is a perfluoropolyoxyalkylene chain having a number average molecular weight in the range 300-10,000 comprising one or more repeating units of —CF
2
CF
2
O—, —(CF
2
CF(CF
3
)O)—, —(CF(CF
3
)CF
2
O)— —CF
2
(CF
2
)
z
CF
2
O—, —CR
4
R
5
CF
2
CF
2
O— type;
wherein:
z is an integer equal to 1 or 2;
Y is F or CF
3
;
R
4
and R
5
, equal to or different from each other, are selected from H, linear or branched perfluoroalkyl having a number of C atoms from 1 to 4;
said units being statistically distributed along the perfluoropolyoxyalkylene chain.
In particular the following R
f1
perfluoropolyethers can be mentioned as preferred:
(A) —(CF
2

LandOfFree

Say what you really think

Search LandOfFree.com for the USA inventors and patents. Rate them and share your experience with other people.

Rating

Process for the preparation of fluoropolyoxyalkylenes having... does not yet have a rating. At this time, there are no reviews or comments for this patent.

If you have personal experience with Process for the preparation of fluoropolyoxyalkylenes having..., we encourage you to share that experience with our LandOfFree.com community. Your opinion is very important and Process for the preparation of fluoropolyoxyalkylenes having... will most certainly appreciate the feedback.

Rate now

     

Profile ID: LFUS-PAI-O-3131373

  Search
All data on this website is collected from public sources. Our data reflects the most accurate information available at the time of publication.