Claims
- 1. In a process comprising providing at least one organic reactant in the presence of an acid catalyst and subjecting the combination to conditions to cause a reaction of the organic reactant, the improvement wherein the acid catalyst comprises cation-exchange fluoropolymer, prepared by a process comprising: (a) providing a cation-exchange fluoropolymer having an equivalent weight in the range of from 250 to 1000 and having counter-ions which are organic quaternary ammonium cations, and (b) exchanging at least 50 percent of such counter-ions with hydrogen ions or metal ions.
- 2. The acid-catalyzed organic reaction of claim 1 wherein the cation-exchange fluoropolymer contains pendant groups of the formula:
- --O--CF.sub.2 --CF.sub.2 --A.sup.- NR.sub.1 R.sub.2 R.sub.3 R.sub.4.sup.+
- wherein A is --COO or --SO.sub.3 ; R.sub.1, R.sub.2, R.sub.3 and R.sub.4 are independently C.sub.1-30 alkyl, aryl, aralkyl or cycloalkyl; and the cation has a molecular weight of at least 300.
- 3. The acid-catalyzed organic reaction of claim 2 wherein A is --SO.sub.3.
- 4. The acid-catalyzed organic reaction of claim 2 wherein at least one R group is dodecylbenzyl.
- 5. The acid-catalyzed organic reaction of claim 2 wherein the polymer used in step (a) has cationic groups derived from dodecylbenzyltrimethylammonium hydroxide or dimethyldidecylammonium chloride.
- 6. The acid-catalyzed organic reaction of claim 2 wherein substantially all of the organic quaternary ammonium cations are replaced with hydrogen ions in step (b).
- 7. The process of claim 1 wherein the reaction is selected from the group consisting of alkylation of aromatic compounds, esterification of carboxylic acids, nitration of aromatic compounds, acylation of aromatic compounds, hydrolysis of ethers and polymerization of olefins.
- 8. In an electrolytic cell comprising an anode, a cathode and a membrane between the anode and the cathode, the improvement wherein the membrane comprises a cation-exchange fluoropolymer, prepared by a process comprising: (a) providing a cation-exchange fluoropolymer having an equivalent weight in the range of from 250 to 1000 and having counter-ions which are organic quaternary ammonium cations, and (b) exchanging at least 50 percent of such counter-ions with hydrogen ions or metal ions.
- 9. The electrolytic cell of claim 8 wherein the cation-exchange fluoropolymer contains pendant groups of the formula:
- --O--CF.sub.2 --CF.sub.2 --A.sup.- NR.sub.1 R.sub.2 R.sub.3 R.sub.4.sup.+
- wherein A is --COO or --SO.sub.3 ; R.sub.1, R.sub.2, R.sub.3 and R.sub.4 are independently C.sub.1-30 alkyl, aryl, aralkyl or cycloalkyl; and the cation has a molecular weight of at least 300.
- 10. The electrolytic cell of claim 9 wherein A is --SO.sub.3.
- 11. The electrolytic cell of claim 9 wherein at least one R group is dodecylbenzyl.
- 12. The electrolytic cell of claim 9 wherein the polymer used in step (a) has cationic groups derived from dodecylbenzyltrimethylammonium hydroxide or dimethyldidecylammonium chloride.
- 13. The electrolytic cell of claim 9 wherein substantially all of the organic quaternary ammonium cations are replaced with hydrogen ions in step (b).
- 14. In a process comprising providing a charge selected from the group consisting of miscible liquids and mixtures of gases, bringing the charge into contact with a membrane such that one component of the charge preferentially permeates through the membrane, and removing the permeated component, the improvement wherein the membrane comprises a solid cation-exchange medium comprising cation-exchange fluoropolymer, prepared by a process comprising: (a) providing a cation-exchange fluoropolymer having an equivalent weight in the range of from 250 to 1000 and having counter-ions which are organic quaternary ammonium cations, and (b) exchanging at least 50 percent of such counter-ions with hydrogen ions or metal ions.
- 15. The process of claim 14 wherein the cation-exchange fluoropolymer contains pendant groups of the formula:
- --O--CF.sub.2 --CF.sub.2 --A.sup.- NR.sub.1 R.sub.2 R.sub.3 R.sub.4.sup.+
- wherein A is --COO or --SO.sub.3 ; R.sub.1, R.sub.2, R.sub.3 and R.sub.4 are independently C.sub.1-30 alkyl, aryl, aralkyl or cycloalkyl; and the cation has a molecular weight of at least 300.
- 16. The process of claim 15 wherein A is --SO.sub.3.
- 17. The process of claim 15 wherein at least one R group is dodecylbenzyl.
- 18. The process of claim 15 wherein the polymer used in step (a) has cationic groups derived from dodecylbenzyltrimethylammonium hydroxide or dimethyldidecylammonium chloride.
- 19. The process of claim 15 wherein substantially all of the organic quaternary ammonium cations are replaced with hydrogen ions in step (b).
Parent Case Info
This application is a Divisional of prior application Ser. No. 08/775,659 filed Dec. 3, 1996 now U.S. Pat. No. 5,747,546.
US Referenced Citations (10)
Foreign Referenced Citations (1)
Number |
Date |
Country |
9519222 |
Jul 1995 |
WOX |
Non-Patent Literature Citations (1)
Entry |
Cahan, B.D. et al., "AC Impedance Investigations of Proton Conduction in Nafion.TM.", J. Electrochem. Soc., vol. 140, No. 12, pp. 185-186 (1993) no month. |
Divisions (1)
|
Number |
Date |
Country |
Parent |
775659 |
Dec 1996 |
|