Claims
- 1. In a process for the production of substantially sulfur-free thiobisphenols of the formula: ##STR5## wherein x is 1, 2, 3 or 4 and R.sub.1 and R.sub.2 are straight or branch-chained alkyl groups of 1-10 carbon atoms, which comprises reacting a 2,6-dialkylphenol with sulfur in a solvent comprising a mixture of water and an alcohol of the formula ROH, wherein R is alkyl of 1 to 5 carbon atoms, the improvement wherein said solvent contains from 10 wt. % to 50 wt. % of water, the reaction is carried out by heating said phenol and said sulfur at a temperature from about 50.degree. C. to the boiling point of the solvent in the presence of a basic reactant, cooling, removing unreacted sulfur, then extracting with a n-alkane and recovering the substantially sulfur-free thiobisphenol product.
- 2. A process according to claim 1, wherein the phenol reactant is 2,6-di-tertiary-butylphenol.
- 3. A process according to claim 1, wherein the basis reactant is an alkali metal hydroxide or alkaline earth metal hydroxide.
- 4. A process according to claim 1, wherein the solvent is a mixture of water and ethanol containing from 10 to 50 wt. % of water.
- 5. A process according to claim 4, wherein the alkane is n-pentane, n-hexane, n-heptane or n-octane.
- 6. A process for the production of substantially sulfur-free thiobisphenols of the formula: ##STR6## wherein x is 1, 2, 3, or 4, and R.sub.1 and R.sub.2 are straight or branch chained alkyl groups containing one to 10 carbon atoms, the process comprising reacting a 2,6-dialkylphenol with sulfur in a solvent which comprises a mixture of water and an alcohol of the formula ROH, wherein R is alkyl of 1-5 carbon atoms, and wherein said solvent contains from 10 wt. % to 50 wt. % of water, the reaction being conducted by heating said phenol and said sulfur at a temperature of from 50.degree. C. to the boiling point of the solvent in the presence of an alkali metal hydroxide basic reactant, cooling the reaction mixture, recovering and purifying to remove sulfur contamination by extracting with hot methanol, filtering, then extracting with a liquid alkane containing up to 10 carbon atoms, the sulfur contamination remaining in the alkane extractant, and recovering the substantially sulfur-free thiobisphenol.
- 7. A process according to claim 6, wherein the solvent is a mixture of ethanol and 10-50 wt. % of water.
- 8. A process according to claim 6, wherein the alkane extractant is selected from the group consisting of n-pentane, n-hexane, n-heptane and n-octane.
Parent Case Info
This application is a continuation of application Ser. No. 07/831,584 filed Feb. 5, 1992 now abandoned.
US Referenced Citations (1)
Number |
Name |
Date |
Kind |
3835196 |
Fujisawa et al. |
Sep 1974 |
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Continuations (1)
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Number |
Date |
Country |
Parent |
831584 |
Feb 1992 |
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