CA1180348A - Process to prepare fluorocarbon ethers having substituted halogen site(s) - Google Patents

Abstract

ABSTRACT OF THE DISCLOSURE
A method for preparing compounds of the formula which comprises reacting compounds of the formula with compounds of the formula for a time and a temperature sufficient to form said compound;

wherein a = 0 or an integer greater than 0;
b = 0 or an integer greater than 0;
n = zero or an integer greater than zero;
Rf and R? are each independently selected from the group consisting of F, Cl, perfluoroalkyl and fluorochloroalkyl;
X' is independently Cl or Br;
Y is an acid group or an acid derivative easily convertible to an acid group, the products being valuable intermediates in the formation of monomers useful, in polymerized form, in the preparation of chemically stable ion exchange resins or membranes.

Description

3~

The present invention relates to a method for the preparation of a class of fluorine containing ethers.
This application is divided from applicant's copending Canadian application Serial No. 379,~2~ filed June 10~ 1981, the latter relating to a compound represented by the general formula Y(CF2)a-(CFRf)b-CFRf -O- ~F-CF2-~ - (F-CF2~ - CF-C=O
~F2X Jn ~F2X ~m CF2X

where a = O or an integer greater than O;
b = O or an integer greater than O;
m = O or an integer greater than zero;
n = ~ero or an integer greater than 7ero;
Rf and Rf are each indeper.dently selected from the group consisting of F, Cl, perfluoroalkyl and fluorochloroalkyl;
X = F, Cl, Br or mixtures thereof when n > l;
X' = Cl, Br or mixtures thereof;
Y is an acid group or an acid derivative easily convertible to an acid group;
Z = F, Cl, Br, OH, NRR' or OA;
R and R' are independently selected from the group consisting of hydrogen, an alkyl having one or more carbon atom and aryl;

~8~3~

A = alkali metal, quaternary nitrogen, or R.
The present invention concerns the preparation of specific compou]lds within the broad compound definition set forth above.
United States Patent 3,301,893 teaches reacting with F

Rf to form compounds represented by the general formula YS2 ~ CF ~ CF2 ~ - ~F ~ CF2 ~ ~ - CF - C = 0 Rf X n X

3~

where R~ i5 F or perfluoroalkyl radicals hav.ing from 1 to lO carbon atoms;

S X is F or a trifluoromethyl radical, or mi~tures thereof, where there is more than one X;

Y is a radical selected from the group con-sisting of fluorine, amino, hydroxyl and OMe radical where Me is a radical selected from the , group consisting of the ammonium radical, alkali ¦ metals and other monovalent metals; and ! n is a number from O to 12.

U.S. Patent 3,536,733 teaches the preparation ¦ of compounds represented by the general formula ~ /~

where Y is F or CF3.

~ British patent 1,518,387 teaches the following reactions.
CH30CCF2CF2~ + CF3CF-CF2 >

CH30CCF2CF2CF20CFCF2OCFC Na2CO3 .
~ 28,978-F ~3-. ~ .
~., .~

34~3 CH3 0 C-CF2-CF2-CF2-O-CF-CF2-O-CF=CF2 U.S. 3,282,875 teaches pyrolyzing compounds having the general ormulas 10FSO2 - CFCF20 -~CF - CF2 - ~ - CF - C = O
, Rf ~ Jn CF3 and OX
15FSO2 - CFCF20 ~CF - CF2 - O~- CF - C - O
.
Rf ~ ~ n CF3 ` to form compounds represented by the general formula 3, MSO2 CF - CF2 - O -~CF - CF2 - O~- CF = CF2 ! , . , I
~ 20 Rf ~ Jn where Rf is F or a perfluoroalkyl radical having from 1-10 carbon atoms;
25Y is F or a trifluoromethyl radical;
n is an integex of 1-3, inclusive;
. M is F, hydroxyl radical, amino radical or s OMe; and ^' Me is an alkali metal or quaternary nitrogen 30radical.
X is alkali metal .

~. 28,978-F ~ -4-3~

The present invention resides in a method for preparing compounds of the formula F

Y~CF2)a - ~cFR~b-cFRf-o-(cF-cF2-o~-cF=c=o ~ F2X ~n CF2X~

which comprises reacking compounds of the formula /o\
X'CF2 - CF - CF2 with compound of the formula Rf Y(CF2)a - ~CFRf~b - C = O
for a time and a temperature sufficient to form said compound;
wherein a = O or an integer greater than O;
b = O or an integer greater than O;
n - zero or an integer greater than zero;
Rf and Rf are each independently selected from the group consisting of F, Cl, perfluoroalkyl and fluorochloroalkyl;
X' is independently Cl or Br;
Y is an acid group or an acid derivative easily con~ertible to an acid group.

Z' Preferably, Y may be S02-Z', C-0, P=0 or C-N or (Z )2 other appropriate groups (as Z is defined above).
The present invention, together with that disclosedand claimed in aforementioned application Serial No. 379,~24, will now be further discussed.
The compounds of the process of the present invention are intermediates which may be further reacted to form a novel class of monomers, which, in turn, may then b0 polymerized and used in the preparation of chem-ically stable ion exchange resins or membranes.
When the polymers ultimately derived from the intermediates of the invention are formed into sheets for use as membranes such as in chlor-alkali cells, it is desirable to choose Z so thatthe polymers formed are thermoplastic to allow fabrication by conventional means, such as melt extru-sion. After fabrication they can be easily converted to the acid or alkali me~al salt of the acid. As an example, when Y = SO2F ~Z=F), the intermediate is converted to an olefin monomer still having the -SO2F group. The monomer is then copolymerized to form a polymer containing the SO2F group that can be formed into sheets by various plastic fabrication techniques. After fabrication, the Sn2F group is easily converted to the alkali metal salt of the corresponding sulfonic acid, -SO2ONa ~Z = ONa), which can be converted to the sulfonic acid, -S020H ~Z=OH), by reaction with acids, such as mineral acids. -S02F + NaOH --~
-SO2ONa + NaF C -SO2OH + NaCl. When Y is chosen as -C=N, a nitrile, the above conditions are met since it is well known thatnitriles are converted to carboxylic acids by hydrolysis.

When the polymers derived from the olefins from the present intermediates are to be used in particle or powder form, such as for acid catalyst, it is not critical in the choice of Z since fabrication is not as large a factor. In this case, Z can con~eniently be any of the radicals listed. It can be -011 so as to directly have Y
as an acid group or it can be any group rendering Y convertable to an acid group by further reaction.
X is chosen from the halogens Cl, Br or F, while X' is chosen from Cl or Br. While iodine would also be useful for X or X', formations of theethersby the chemistry taught herein is hampered by side reactions causing low or nonexistant yields to the desired compounds .
When X' = Cl or Br and X = F, Cl or Br, new uses and novel and surprising new chemistry results from using the intermediates for additional chemical reactions. The prior art teaches that when Y = S02F, n = 0, M=0, and X' = F ~United States Patent No. 3,560,56~) reaction of the intermediate with a base does not produce the desired vinyl ether monomer,but rather a cyclic sulfone coinpound.
Surprisingly, when n = 0, M = 0, Y = S02F and X' = Cl or Br, reaction of the intermediate with a base produces the desired vinyl ether product in one step. In addition to this benefit, choosing X or X' = Cl or Br in compounds where m or n> 0 resultsin introducing a potential reaction site into polymers ultimately derived from monomers made from these intermediates. When m or n > 0 both an acid site for ion excnange or catalyst ~Y) and a reaction site for further reaction can be obtained by having X or X' = Cl 3~1 or Br. In general, metallation reagents such as alkyl alkali metals can be used for reactions on these reaction sites.
There is an additional benefit for having X' = Cl or Br.
In this case it is helpful to have Cl or Br in this position for the subsequent reactions and uses for these compounds.
l`he variables in the structures have preferred values as follows: n = 0 - 6, m = O - 6, a = O - 3, b = O - 3. Preferred is n = O - 3 and m = O - 3. Most preferably n = O or l and m = O or l.
Preferably X = Cl, X' = Cl and Y = Z'SO2. More preferably Y = Z'SO2 and Z' = F. Rf and R'f are preferably F.
In decarboxylations of the prior art, compounds of the terminal functionality shown below are common.

-O-CF- C=O

These materials generally require high tempera~ure and activators such as ZnO or silica to achieve reasonable yields to the desired vinyl ethers.

~0-CF-C=0 heat ~0-CF=CF
, Activator 2 3~,~

When X' is Cl or Br in the present invention, decarboxylation of these intermediates to vinyl ethers has been found to proceed under mild conditions and in excellent yields.
In the process of the present invention, the reactions are carried out in the presence of a fluoride ion yielding compound metal fluoride-catalyst (MF) at a temperature and a time sufficient to cause a reaction, preferably from -20C to 50C, in the liquid state, desirably in a liquid solvent for the inter-mediate fluoroalkoxide Y(CF~)a - (CFRf)b - CFR~ 0 M formed between the acid fluoride or ketone R~
Y(CF2)a - (CFRf)b - C = O

and the metal or ammonium fluoride, fluorine ion yielding catalyst (MF). The reactions proceed generally according to the equation (n)X'CF2-CF-CF2 ~ Y(CF2)a (CFR~)b-C=0 --~

Y(CF2)a~(CFRf)b -CFRf -0- ~ F-CF2 -~ -CF-C=0 \CF2X ' ~ CF2X

Conversion of acid halides such as the acid fluorides dsscribed herein to carboxylic acids and 39t~
--lU--derivatives by reaction with nucleophiles is well known to those skilled in the art. For example, conversion of the acid fluoride to the corresponding carboxylic acid is easily accomplished by reaction with water.
Conversion to esters or amides is accomplished by reaction with alcohols or amines, respecti~ely. The carboxylic acids ~Z = OH) are easily converted to acid chlorides or bromides (Z - Cl, Br) by reaction with appropriate halogenation agents such as PC15 or PBr5.
Reactions of the carboxylic acid fluoride proceed according to the following eguation:

F Z' ~ C=O -~ PZ' ~ ~ C=o + PF
where Z' = OH, NRR' or OR;
R and R' are independently selected from the group consisting of hydrogen, an alkyl having one or more than one carbon atom and aryl;
P is a cation or capable of forming a cation, such as Na , K , H , etc.
It is of course to be understood that in the reaction of the acid fluorides or ketones with the epoxides the ratio of reactants, the temperature of reaction, the amount of catalyst, as well as the amount and kind of solvent, influence the course, speed and direction of the reaction. Naturally the ratio of reactants bears more directly on the value of m and n in the generic formula than the other factors noted.
For example, employing 1 or more moles of acid halide compound per mole of perhalofluoro epoxide results in a 28,978 F ~10-9341~

product rich in the n=0 product, i.e., greater than 1.5 n=0 to n=l, respectively and if the ratio is 2 to 1, respectively, the n=0 product, respectively, is about 92 to 1, respectively, whereas employing greater than 1 mole epoxide compound per mole of acid fluoride compound, i.e., 2 to 1, respectively, results in a product having a 3:9:1 ratio of n=2: n=l:n=0 products. The ratio of reactants thus can range, for practical purposes, from about 2 ~o 3 moles of ~he acylfluoride or ketone per mole of the halofluoro epoxide to 1 to 20 moles of the epoxide per mole of the acyl fluoride, the high acyl fluoride to epoxide producing predominantly the n=0 and the high epoxide to acyl fluoride producing the n=2=12 ether, respectively, and mixtures thereof.
Solvents employed should be non-reactive (e.g., do not contain hydroxyl groups) and have at 1east a solubility for the reactants and the intermediate fluoroalkoxide formed between the acyl fluoride or ketone compound and the catalyst. Whether or not the products are significantly soluble in the solvent is a matter of choice and can be used as a controlling factor for selectively controlling the n value in the final product. For example, if a high n value is desired, it is advantageous that the product having at least n=0 to 1 be soluble in the solvent to give the intermediates (n=0 and n=l) time to react to produce the final n=l, 2 or higher product. In addition, the amount of solvent can be adjusted to accomplish somewhat similar results. Generally, when the ratio of the weight of solvent to the weight of the acid fluoride is from about 0.3:1 to about 0.8:1, formation of the n=0 product is maximized. As the weight ratio increases, higher n values are obtained. Although there is no theoretical maximum amount of solvent which may be used, one may quickly determine the weight ratio to be used depending upon the value of the n that he desires. Suitable solvents which may be employed to take advantage of the solu-bility plus amount factor are, for example, tetraglyme, di~lyme, glyme, acetonitrile, or nitrobenzene. Exemplary of a preferred solvent is te-traglyme which has a suitable solvency for the intermediate, but in a weight to weight ratio has limited solubility for the product n=0 and therefore can be used advantageously to precipitate the n=0 product (remove it from the reactlon media), effectively controlling (minimizing) the production of higher n values, yet if higher n values are desired, greater quantities of the solvent can be employed to dissolve the product n=0 or an amount sufficient to maintain a quantity thereof in the reaction medium`to permit the epoxide to further react with the n=0 product to produce higher n value products. By controlling the amount, again it is possible to salt-out the inter-mediate n-values as a function of their solubility and quantity in the solvent-reaction media.

In a somewhat similar manner, the catalyst amount functions as a control of the end product n ~alue. While the source of the fluoride ion is not critical, the amount of catalyst will to a significant measure establish the reactivity of the acid fluoride and thus determine the rate of reaction of the acid fluoride with the epoxide. Significant amounts of the catalyst, up to stoichiometric amounts based on the acld fluoride or ketone, will favor epoxide reacting on the feed acid fluoride. Whereas lesser catalytic amounts, with respect to the acid fluoride will favor 28,978-F -12-3~1!3 the reaction of the epoxlde with the n=O acid fluoride product forming higher n products. ~s has been noted, substantially any fluoride ionizable at the reaction conditions may be used as a catalyst, however, CsF and - KF are the most preferred but AgF, tetra alkyl ammonium fluoride as well as others listed ~y Evans, et al., J. Org. Chem. 33 1837 (1968) may be employed with satisfactory results.

The temperature of the reaction also ef~
fectuates a controlling factor on the end product obtained. For example, low temperatures such as -20C
favor n=O products and higher temperatures, 500r and above, favor higher n values.

In summary, the following table illustrates the effect each parameter of the reaction has on the n value of the final product.
n = O -~ n = 12 Ratio of ketone or acyl fluoride to epoxide 3/1 1/20 Solvent amt. small large Temp. low high Catalyst high low EXAMPLES

90 ml of dry tetraglyme and 39.5 gms of anhydrous CsF were added to a 500 ml 3-neck flask 28,978-F -13-~8~3~1~

equipped with a stirrer, thermometer, reflux condenser at a temperature of -78C, and an inlet port. Downstream of the reactor were liquid N2 cold traps maintained at a temperature of 78C. A slight back pressure was maintained on the system with dry N2.

The reactor was cooled to 0C to 5C and 126 grams of fluorosulfonyldifluoroacetylfluoride FSO2 - CF2 - C = O, were added slowly over a 20 minute period and tnen allowed to mix for another 20-30 minutes to ensure formation of the alkoxide.
~O\
64.3 grams of ClCF2 - CF - CF2 were added slowly over an hour and 45 minutes while maintaining the reactor temperature at 0 to 5C. After the epoxide addition, the contents were allowed to mix for an additional hour. The temperature was allowed to rise to room temperature. When stirring ceased, two separate layers formed. The bottom layer was drawn off and weighed 104.7 yrams. VPC (Vapor Phase Chromatography) analysis of this product showed 92% n=O product and - 7.85% lights or product formed by reaction of the epoxide with itself.

- Conversion of the epoxide was essentially ~omplete. Yield of epoxide to the n=O product was 75.3%.

The products were analyzed further by GC-MS
(Gas Chromatography-Mass Spectrophotometry) and the following compounds were identified:

28,978-F --14-3~

F as the light I material Cl(CF2)3 - O - CF - C - O
CF~Cl F as the n=0 product FSO2(CF2)2 - O - CF - C = O
CF2Cl Products were analyzed further by IR. The -COF groups present at 1870-1880 wave no., -FSO2 group at 1460 and 1240 wave nos.; and -SF at 810 wave number for n=O product.
; 15 The products had retention times of 1.35 and

2.74 minutes, respectively, on a VPC uslng six feet columns of 20% Viton~ on Celite~. Column temperature of 60C.

35 ml of dry tetraglyme and 15.6 gms CsF
were added to a 3-neck 100 ml flask equipped with a stirrer, ~hermometer, ~-78C) reflux condenser and an inlet port. Downstream of the reactor were two (-78C) ~ cold traps in series. A slight back pressure was - maintained with dry N2. Tetraglyme and CsF were mixed for 45 min. to 1 hour.

- The reactor was cooled to 0C to 5C and 49.32 grams of fluorosulfonyl difluoro acetyl fluoride FSO2 - CF2 - C = O
F

28,978-F -~15-~L~8q:~3~
. ," --1~

were added slowly over a 20 minute period, allowed to mix at 0 to 5C for 2 hours and then the temperature was raised slowly to xoom temperature to ensure the formation of the alkoxide. After cooling the reactor to 0C, 25 grams of chloropentafluoropropylene oxide, /Q~
ClCF2 - CF - CF2, were added slowly over a 3-4 hour period. After the epoxide addition was complete, the contents were mixed for an additional hour. The temp-lo erature was allowed to rise to room temperature. When stirring wa~ stopped, two liguid phases separated.38.94 gms of the heavy or bottom layer was collected.
Analyses by VPC showed 87.86% of n=0 product, 5~ un-reacted reactants, and 4.2% of a higher molecular wt.
product. This gave an essentially compl~te conversion of the epoxide and a 68.9% yield of epoxide to the n=0 product.

The unreacted reactant (FS02CF2CFO) was distilled off the product.

35 ml of tetraglyme and 8 gm CsF were mixed for 40 minutes. The heavies from the above distillation were added slowly over a 20 minute period and mixed for 1 hour at 0C to 5C. The reactor was warmed to room temperature to ~nsure formation of the alkoxide. After cooling again to 0C to 5C, 19.6 grams of /o\
ClCF2 - CF - CF2 were added slowly over a 2-3 hour period, and then allowed to mix at 0C to 5C for another hour. The reactor was warmed to room temperature. After stirring was stopped, two separate layers formed. 35.67 grams 28,978-F -16-,

3~

of bottom or product layer was collected. Analyses by VPC showed 12.8~ n=0 product, 57.4% n=1, and 6.8% n=2 product. Thus, of the n = o product that reacted, S 45 9% was converted to the n=l product.

The following products were identified by mass spectrometer:

FS02(CF2)2 - 0 - CF - C = 0 n = 0 CF2Cl -F
lS FSO2 - (CF2)2 - 0 - CF - CF2 - 0 - CF - C = 0 n = 1 CF2Cl CF2Cl F
FS02 - (CF2)2 - 0 - ~F - CF2 - 0~- CF - C = 0 n = 2 .
~F2Cl ~ 2 CF2cl Mass spectroscopy fragmentation pattern reported consistent with this structure of n=2.

The infraréd showed the characteristic S02F
and -C F0 bands, VPC retention times using the column described in Example 1 with a temperature program of 4 i min. at 60C, followed by a rise to 220C at 16/min.
were 2.72, 5.74, and 8.18 minutes, respectively.

;

28,978-F -17-~L8~3~1~
, ,.. , --1~--:

75gm of FSO2(CF2)2 - O - CF - C = O
CF2 Cl was added dropwise to a 500 ml vessel containing 200 gm tetraglyme and 15.2 gm CsF. The vessel was fitted with a cold fingex condenser and two traps on the effluent;
one dry ice acetone and the other liquid nitrogen. The acid fluoride was ~tirred for one hour after the addition was completed and then /O~
ClCF2 - CF - F2 was added at a rate such that no reflux was observed on ; the cold finger. A total of 18.3 gm was added, keeping the temperature below 35C. After completing the addition, the mixture was stirred for an hour. The vessel contents were poured into a separatory funnel under dry nitrogen blanket and the lower product layer was allowed to settle out. The product layer was drained off and analyzed chromatographically as: 1 part n=3, 1.1 parts n=2, 12 parts n=1, 4.6 parts residual n=o .

30 ml of dry tetraglyme and 14.15 gms (.0932 mole) CsF were added to a 100 ml 3-neck flask equipped with a stirrer, thermometer, (-78C) reflux condenser, and an inlet port. Downstream of the reactor were two (-78C) cold traps in series. A slight back pressure was 28,978-F -18-.

3~
. .

maintained on the system with dry N2. Tetraglyme and CsF were mixed for at least 45 minutes.

The reactor was cooled to -20C and 16.83 gm (.093 moles) of FS02 - CF2 ~ C - O
F

o added. The temperature was brought up to 20-25 C and 30.2 gm of lS ClCF2 - CF - CF2 were added in increments of 2 to 3 grams over a 4 houx period while maintaining the reactor at 25-28C. After the epoxide addition, the contents were stirred for an 2~ additional 1.5 hours. When stirring ceased, two separate layers formed and were separated with a separatory funnel. 28 gm of product (bottom layer) were collected. Analysis by VPC showed 13.4% n=0 product, 33.8% n=l product, and 4.3% n=2 product. In addition, there were products (dimers and trimers) of the epoxide.

Products were analyzed further by GC-MS and the following compounds were identified:
F
Cl(CF2)3 - O - CF - C = 0 CF~Cl 28,978-F -19-~3L8~8 .. . ,~ ~

FSO2(CF2)z - O - CF - C = o CF2Cl F
Cl(CF2)3 - O - CF - CF2 - 0 CF - C = 0 CF2Cl CF2Cl F
FS02 - ~CF2)2 - 0 - CF - CF2 - 0 - CF - C = 0 CF2Cl CF2Cl lS F
FSO2 - (CF2)2 - 0 ~ F - CF2 - ~- CF - C - 0 ~F2Cl 2 CFz 200 ml of dry tetraglyme and 15.19 gms (O.10 moles) of CsF were added to a 500 ml 3-neck fla~k equipped with a stirrer, thermometer, (-78C) reflux condenser, and an inlet port. Two ~-78C) cold traps in series were located downstream of the reflux condenser. A slight back pressure was maintained on the system with dry N2.
- After stirring for 1 hour, the reactor was cooled to -5C, and 51.22 gms (0.20 moles) of methyl perfluoro-glutaryl fluoride 0 . F
CH30C(CF2)3C=0 28,978-F --~0-3~
., .

wexe added dropwise. The reactants in the reactor were stirred overnight at room temperature. Reactor was cooled to ~5C and 18.25 gms (0.10 moles) of chloropenta-fluoro propylene oxide /o\
ClCF2 - CF - CF2 were added slowly. After the epoxide addition was complete, samples were taken after 30 min. and 1.5 hr.
and analyzed by VPC. The temperature was then raised to room temperature over one hour period and sample analyzed by VPC.

The products were distilled out of the reactor under 30" vacuum while heating to 160C. The overhead temperature was 65C at this point. 49.38 gm of the product was collected in the first cold trap and 2.5 gms was collected in the second trap. The products were analyzed by VPC.

The material caught in the first cold trap was distilled in a microcolumn to remove the unreacted methylperfluoroglutaryl fluoride. All material boiling up to 145C was removed in this manner. Everything - heavier was retained in the pot and weighed 18.44 grams. Heavies were analyzed by VPC, mass spec~roscopy and I.R. ~Infra Red).

Peaks on the VPC were 7.21, 7.62, 8.86, and 10.47 minutes. Mass spectroscopy showed that the 7.21 peak had the structure 28,978-F -21-3~

O F
"
CH30-C-CF2 CF2-CF2-CF2-O-CF-C=O

the 8.86 peak had the structure O F
CH30-C-CF2-CF2-CFz-CF2-O-CF-CF2-O-CF-C=O
CF2Cl CF2Cl IR analysis showed bands at 2960, 1860, and 1770-1780 Cm1. The 1860 Cm 1 band is the -COF group and o the 1770-1780 Cm 1 is the ester -C- group. The 2960 Cm 1 is due to the CH3 group.
Example 6 25 ml of tetraglyme and 6.4 gms of CsF were added to a 50 ml, 3 neck flask equipped with a stirring bar, thermometer, reflux condenser, and an inlet port.
Two (-78C) cold traps in series were located downstream of the reflux condenser. A slight backpressure was maintained on the system with dry N2. The tetraglyme and CsF were allowed to mix for 1 hour at room tempera-ture, lowered to 10C-20C, and 48 grams of FSO2CF2CFO
were added and allowed to mix for 1 hour. The mixture was ~O
- cooled to 0C and 25 grams of CF3CF-CF2 were added over an hour and 20 minute period, while maintaining a temperature of 0C to 10C. After mixing at this temperature for 2 hours, the temperature was increased to room temperature. The product was separated as a clear, dense, bottom layer. 50.5 grams were recovered which was determined to be 80.16%
28,978-F -22-3~

by VPC analysis.

The lower boiling components were removed leaving a mixture containing 88.6% of the desired acid fluoride.

5 ml of tetraglyme and 1.7 gms CsF were added to a 50 ml 3 neck flask equipped as above and the mixture was stirred for 30 minutes. 5 grams of distilled FSO2CF2CF2OCFCFO were added and mixed at 10-20C for 1 hour. 1.4 gms of ClCF2CF-CF2 were added while main-taining a temperature of 0 to 10C, and held at this temperature for 1 hour. The temperature was increased to room temperature, 5 ml of tetraglyme added, and the product separated from the solvent. 3.0 gr~ns of product were obtained and analyzed as 63.98%

CF3 CF2Cl having a 6.47 minutP retention on the VPC and confirmed by I.R. and mass spectroscopy.

28,978-F -23-

Claims (4)

1. A method for preparing compounds of the formula which comprises reacting compounds of the formula with compounds of the formula for a time and a temperature sufficient to form said compound;
wherein a = 0 or an integer greater than 0;
b = 0 or an integer greater than 0;
n = zero or an integer greater than zero;
Rf and R? are each independently selected from the group consisting of F, Cl, perfluoroalkyl and fluorochloroalkyl, X' is independently Cl or Br;
Y is an acid group or an acid derivative easily convertible to an acid group.

2. The method of Claim 1 wherein n = 0 - 6, a = 0 - 3 and b = 0 - 3.

3. The method of Claim 1 wherein Y is selected from the qroup consisting of where Z' is F, Cl, Br, OH, NRR' or OA;
R and R' are independently selected from the group consisting of hydrogen, an alkyl having one or more than one carbon atom and an aryl, A is an alkali metal, quaternary nitrogen or R.

4. The method of Claim 1, 2 or 3 wherein n = 0 or 1 and X' = Cl.