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AssigneeThe Dow Chemical Company
InventorsRalph A. Davis, Ronald G. Tigner, Joseph J. Pedjac, Laurence I. Peterson
Estimating the term…
Brominated pentaerythritols are prepared at reaction temperatures of from about 85.degree. to 135.degree.C. by reacting pentaerythritol with HBr in the liquid phase employing a solvent medium containing from about 0.8 to about 25 mole percent of an aliphatic carboxylic acid of 2 to 8 carbon atoms and their anhydrides, based on the pentaerythritol. The HBr is fed continuously to the reactor throughout the reaction. The water formed as a result of the reaction remains in the reaction mixture until substantial completion of the reaction. The product can be predominantly dibromoneopentyl glycol or tribromoneopentyl alcohol and is characterized by the absence of tar formation.
In the process for preparing brominated pentaerythritols by contacting pentaerythritol with HBr, the improvement comprising reacting the pentaerythritol with HBr in the liquid phase at a temperature of from about 85.degree. to about 135.degree.C. in a solvent selected from the groups consisting of benzene, toluene, xylene, a saturated hydrocarbon solvent, a substantially nonreactive brominated or chlorinated hydrocarbon solvent, and water, containing as a catalyst an alkanoic acid of from 2 to 8 carbon atoms or its anhydride having a concentration of from about 0.8 to about 25 mole percent per mole of pentaerythritol, by feeding the HBr to the reactor containing the pentaerythritol and solvent continuously throughout the reaction to saturate the reaction mixture with HBr while retaining in the reaction mixture until completion of the reaction water formed during the reaction and any water used as solvent.
In the process for preparing brominated pentaerythritols by contacting pentaerythritol with HBr, the improvement comprising reacting the pentaerythritol with HBr in the liquid phase at a temperature of from about 85.degree. to about 135.degree.C. in a solvent selected from the group consisting of water and perchloroethylene, containing as a catalyst acetic acid or its anhydride having a concentration of from about 0.8 to about 25 mole percent per mole of pentaerythritol, by feeding the HBr to the reactor containing the pentaerythritol and the solvent continuously throughout the reaction to saturate the reaction mixture with HBr while retaining in the reaction mixture until completion of the reaction water formed during the reaction and any water used as solvent.
Dependencies are inferred from the claim text.