Claims
- 1. Method of making hydroxypivaldehyde and 3-hydroxy-2,2-dimethyl propyl hydroxypivalate comprising reacting paraformaldehyde with isobutyraldehyde in the presence of a catalyst comprising a tertiary amine and an oxide selected from the group consisting of cadmium oxide and yttrium oxide.
- 2. Method of making neopentyl glycol comprising reacting paraformaldehyde with isobutyraldehyde in the presence of a catalyst comprising a tertiary amine and an oxide selected from the group consisting of cadmium oxide and yttrium oxide to obtain a reaction product containing hydroxypivaldehyde and at least about 20% 3-hydroxy-2,2-dimethylpropylhydroxypivalate and hydrogenating the reaction product.
- 3. Method of claim 1 wherein the tertiary amine is triethylamine.
- 4. Method of claim 2 wherein the tertiary amine is triethylamine.
- 5. Method of claim 1 wherein the ratio of paraformaldehyde to isobutyraldehyde is about 0.5:1 to about 2:1.
- 6. Method of claim 2 including the step of recovering the oxide catalyst prior to hydrogenation of the 3-hydroxy-2,2-dimethylpropylhydroxypivalate/hydroxypivaldehyde mixture.
- 7. Method of claim 1 wherein the amine has the formula R.sup.1 R.sup.2 R.sup.3 N where R.sup.1, R.sup.2, and R.sup.3 are alkyl groups of the general formula C.sub.1 -C.sub.15 and R.sup.1 and R.sup.2 may form a subsituted or unsubstituted cyclic group having from 5 to about 15 carbon atoms.
- 8. Method of claim 2 wherein the amine has the formula R.sup.1 R.sup.2 R.sup.3 N where R.sup.1, R.sup.2, and R.sup.3 are alkyl groups of the general formula C.sub.1 -C.sub.15 and R.sup.1 and R.sup.2 may form a subsituted or unsubstituted cyclic group having from 5 to about 15 carbon atoms.
- 9. Method of claim 2 wherein the hydrogenation step is performed by (a) mixing the reaction product containing hydroxypivaldehyde and at least 20% HNHP with at least about 20% of an alcohol of the formula RR'CHOH where R and R' are independently selected from the group consisting of hydrogen and alkyl groups having one to five carbon atoms and (b) contacting the mixture with hydrogen in the presence of a hydrogenation catalyst.
- 10. Method of claim 9 wherein the alcohol is methanol.
- 11. Method of claim 9 wherein the hydrogenation is conducted at a pressure of about 500 to 3000 psig and a temperature of about 100.degree. to 200.degree. C.
- 12. Method of claim 9 wherein the hydrogenation catalyst comprises copper chromite.
RELATED APPLICATION
This application is a continuation-in-part of Ser. No. 716,177, filed Jun. 17, 1991, now abandoned entitled "Manufacture of Neopentyl Glycol (II)".
US Referenced Citations (16)
Foreign Referenced Citations (1)
Number |
Date |
Country |
1017618 |
Jan 1966 |
GBX |
Continuation in Parts (1)
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Number |
Date |
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Parent |
716177 |
Jul 1991 |
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