Participants
| Role | Name | HCID | Charge |
|---|
| Reactant | Phenol | HCID 996 | — |
| Reactant | p-Isopropenylphenol | HCID 584247 | — |
| Solvent | Acetone | HCID 180 | — |
| Product | Bisphenol A | HCID 6623 | — |
Reaction Steps
According to the present invention the following reactions are conducted simultaneously in a reaction system comprising step I of the process: reaction of phenol with acetone, reaction of phenol with p-isopropenylphenol resulting from thermal decomposition of process by-products and recycled to the reaction system, and isomerizational rearrangement of process by-products to obtain bisphenol A in the presence of a micro- and macroporous cation-exchange resin catalyst mixture. Step II of the process comprises cooling the post-reaction mixture together with water and acetone to obtain a precipitate of bisphenol-A/phenol in phenolic solution. Step III of the process comprises separation of the precipitate into crystalline bisphenol-A/phenol adduct and phenolic mother liquor I. The crystalline adduct is washed with the phenolic liquor and step IV follows, wherein the bisphenolA/phenol adduct obtained in step III is dissolved in the phenolic solution and the resulting mixture is cooled to obtain a bisphenol-A/phenol precipitate in phenolic solution. Step V comprises separation of the precipitate obtained in step IV into the crystalline bisphenol-A/phenol adduct and mother liquor II to be turned back to step III of the process. The bisphenol-A/phenol crystalline adduct is then washed with phenolic solution and step VI follows, wherein a high-purity bisphenol A is recovered by removal of phenol from the bisphenol-A/phenol adduct obtained in step V. Step VII of the process consists in distillation of the phenolic mother liquor I obtained in step III, and removal of acetone, water and part of phenol therefrom. Dewatered phenol liquor is turned back to step I of the process to the reaction zone and step VIII follows, consisting of thermal catalytic decomposition of part of the mother liquor I obtained in step(s) III and/or VII, resulting in a distillate comprising phenol, isopropenylphenol and process by-products. Step IX consists of catalytic rearrangement of the reactive components of the distillate obtained in step VIII, while leaving the p-isopropenylphenol contained therein substantially intact and the rearranged distillate is recycled to step I of the process.
Provenance & Evidence
| DOI | 10.6084/m9.figshare.5104873.v1 |
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| Patent number | US05198591 |
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| Source dataset | uspto-grants-1993_03 |
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| ORD ID | ord-fa00785e610448039e860e495aa8551c |
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| Source note | uspto-grants-1993_03 |
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