Claims
- 1. A process for manufacturing an ester of 1,3-propanediol, comprising, contacting at a temperature of about 0.degree. C. to about 250.degree. C., ethylene, formaldehyde or a form of formaldehyde, a carboxylic acid, and a compound of the formula MZ.sub.n.Q.sub.t, wherein:
- M is a zirconium[IV], cobalt[II], vanadium[IV], bismuth[II], tin[II], a rare earth metal, scandium or yttrium;
- n is the oxidation state of M;
- at least one of Z is an anion of the formula R.sup.1 SO.sub.3.sup.- or R.sup.1 CO.sub.2.sup.-, wherein R.sup.1 is hydrocarbyl or substituted hydrocarbyl containing 1 to 20 carbon atoms or part of a polymer, and the remainder of Z is oxo or one or more monovalent anions;
- Q is a neutral ligand; and
- t is 0 or an integer of 1 to 12.
- 2. The process as recited in claim 1 wherein at least one of Z is R.sup.1 SO.sub.3.sup.-.
- 3. The process as recited in claim 1 wherein all of Z are R.sup.1 SO.sub.3.sup.-.
- 4. The process as recited in claims 1, 2 or 3 wherein R.sup.1 is trifluoromethyl.
- 5. The process as recited in claim 1 wherein R.sup.1 is perfluoroalkyl containing 1 to 12 carbon atoms, and optionally containing one or more ether groups, or part of a fluorinated polymer wherein the carbon atoms alpha and beta to the sulfonate or carboxylate group are together bonded to at least 4 fluorine atoms, or when R.sup.1 SO.sub.3.sup.- is present R.sup.1 is aryl or substituted aryl.
- 6. The process as recited in claim 3 wherein R.sup.1 is perfluoroalkyl containing 1 to 12 carbon atoms, and optionally containing one or more ether groups, part of a fluorinated polymer wherein the carbon atoms alpha and beta to the sulfonate or carboxylate group are together bonded to at least 4 fluorine atoms, or is aryl or substituted aryl.
- 7. The process as recited in claim 1 wherein M is a rare earth metal, scandium or yttrium.
- 8. The process as recited in claim 6 wherein M is a rare earth metal, scandium or yttrium.
- 9. The process as recited in claims 1, 2, 3 or 7 wherein said carboxylic acid is monofunctional.
- 10. The process as recited in claim 9 wherein said carboxylic acid is acetic acid or formic acid.
- 11. The process as recited in claim 9 wherein said carboxylic acid is formic acid.
- 12. The process as recited in claim 1 wherein said carboxylic acid is formic acid.
- 13. The process as recited in claim 1 wherein t is 0.
- 14. The process as recited in claims 1 or 12 wherein said temperature is about 50.degree. C. to about 175.degree. C.
- 15. The process as recited in claim 11 wherein said temperature is about 50.degree. C. to about 175.degree. C.
- 16. The process as recited in claim 1 wherein an ethylene pressure is about 700 kPag to about 10 MPag.
- 17. The process as recited in claims 1 or 3 wherein a molar ratio said carboxylic acid:said formaldehyde is about 2:1 to about 15:1.
- 18. The process as recited in claim 1 wherein said carboxylic acid is difunctional and an oligomer or polymer of said carboxylic acid and 1,3-propanediol is produced.
- 19. An improved process for the production of an ester by the Prins reaction by reacting an olefin, formaldehyde or a form of formaldehyde, and a carboxylic acid and optionally in the presence of a Lewis or Bronsted acid catalyst, wherein the improvement comprises, using formic acid as the carboxylic acid.
- 20. The process as recited in claim 19 wherein a Lewis acid catalyst is used.
- 21. The process as recited in claim 19 wherein a Bronsted acid catalyst is used.
- 22. The process as recited in claim 19 wherein a Lewis or Bronsted acid is not present.
- 23. The process as recited in claims 19, 20, 21 or 22 wherein said olefin is ethylene.
Parent Case Info
This application claims priority benefit of U.S. Provisional Application Serial No. 60/082,552, filed Apr. 21, 1998 and priority benefit of U.S. Provisional Application Serial No. 60/067,934, filed Dec. 8, 1997.
US Referenced Citations (1)
Number |
Name |
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4322355 |
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Mar 1982 |
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Foreign Referenced Citations (1)
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