Abstract:
Para-cresol is separated from a mixture comprising meta-cresol and various other methylated and ethylated phenols by preferentially complexing the para-cresol with one or more anhydrous or dehydrated inorganic salts selected from the group consisting of calcium bromide, lithium bromide, manganese bromide and magnesium chloride. The anhydrous inorganic salt is added to the phenolic mixture in an amount to give a mole ratio of salt to para-cresol in the mixture in the range of about 0.5 mole to one to about 1.5 mole to one. The para-cresol and salt form a complex and the complex is removed from the mixture of methylated and ethylated phenols. Then the complex is decomposed to recover the para-cresol and salt; the recovered salt may be recycled to complex with more para-cresol.
Abstract:
Para-cresol and meta-cresol are separated from a mixture of methylated and ethylated phenols by a two-stage process wherein the para-cresol is preferentially complexed with one or more anhydrous or dehydrated inorganic salts selected from calcium bromide, lithium bromide, manganese bromide and magnesium chloride. Then the meta-cresol is successively preferentially complexed with calcium bromide from the mixture of methylated and ethylated phenols from which the para-cresol complex has been removed. The anhydrous or dehydrated inorganic salt is added to the mixture of methylated and ethylated phenols including para-cresol and meta-cresol in an amount to give a mole ratio of the salt to para-cresol in the mixture in the range of about 0.5 to one to about 1.5 to one. The para-cresol-salt complex is removed from the mixture of methylated and ethylated phenols and then decomposed to recover the para-cresol. The mixture of methylated and ethylated phenols including meta-cresol from which the para-cresol has been removed has added to it calcium bromide in an amount to give a mole ratio of calcium bromide to meta-cresol in the mixture in the range of about 0.5 to one to around 1.0 to one. The addition is performed in the presence of a non-aqueous solvent and at a temperature in the range of -10.degree. C. to about 40.degree. C. The meta-cresol-salt complex is separated from the second mixture of methylated and ethylated phenols and the complex is decomposed to produce a high purity meta-cresol.
Abstract:
A process is disclosed for the stepwise separation of para-cresol and meta-cresol from a mixture of methylated and ethylated phenols. The para-cresol preferentially forms a complex with a dehydrated or anhydrous inorganic salt selected from the group consisting of calcium bromide, lithium bromide, manganese bromide and magnesium chloride. The meta-cresol isomer is separated from the mixture by formation of a complex with urea. Where the anhydrous or dehydrated inorganic salt is added firstly to the mixture of methylated and ethylated phenols including para-cresol and meta-cresol, the salt is provided in an amount to give a mole ratio of the salt to para-cresol in the mixture in the range of about 0.5 to one to about 1.5 to one. The para-cresol complexes with the salt and the complex is then removed from the mixture. The para-cresol-salt complex is thereafter decomposed to recover the para-cresol. The mixture of methylated and ethylated phenols including meta-cresol from which the para cresol has been removed has added to it urea in an amount to give a mole ratio of urea to meta-cresol in the mixture in the range of about 0.7 to one to about 1.3 to one. The meta-cresol-urea complex is then separated from the mixture of methylated and ethylated phenols and thereafter the complex is decomposed by hydrolysis to produce a high purity meta-cresol. It is a feature of the invention that either of the complexing steps may be performed first; that is, either of the anhydrous salt or the urea may be added to the mixture, followed thereafter by addition of the other complexing agent.