Edgar Donald Allan - Katy TX Roberto Carlos Longoria - Houston TX David Werner Daum - Seabrook TX Robert Lawrence Blackbourn - Houston TX
Assignee:
Shell Oil Company - Houston TX
International Classification:
C07C 3768
US Classification:
568754
Abstract:
There is provided a process for the manufacture of phenolic compounds by separating a neutralized aralkyl hydroperoxide cleavage mass stream containing salts of neutralization into a crude ketone stream and a crude phenolic stream containing the salts of neutralization; separating the crude phenolic stream into a concentrated phenolic-rich stream, enriched in phenolic compounds, and a crude phenolic bottoms stream enriched in tars and alpha methyl styrene dimers, each compared to the crude phenolic stream, said crude phenolic bottoms stream containing salts of neutralization; to the crude phenolic bottoms stream, adding water and a diluent composition, thereby forming a phase separable crude phenolic bottoms stream, said diluent composition comprised of hydrocarbons phase compatible with the crude phenolic bottoms stream and having a combined density lower than the density of the crude phenolic bottoms stream; separating the separable crude phenolic bottoms stream into a hydrocarbon phase and an aqueous phase containing salts of neutralization; whereby the amount of salts of neutralization in the hydrocarbon phase is reduced compared to the amount of salts of neutralization present prior to separation.
Removal Of Salts In The Manufacture Of Phenolic Compound
Edgar Donald Allan - Katy TX, US Roberto Carlos Longoria - Houston TX, US David Werner Daum - Seabrook TX, US Robert Lawrence Blackbourn - Houston TX, US
Assignee:
Shell Oil Company - Houston TX
International Classification:
C07C037/68
US Classification:
568754, 568768
Abstract:
There is provided a process for the manufacture of phenolic compounds by separating a neutralized aralkyl hydroperoxide cleavage mass stream containing salts of neutralization into a crude ketone stream and a crude phenolic stream containing the salts of neutralization; separating the crude phenolic stream into a concentrated phenolic-rich stream, enriched in phenolic compounds, and a crude phenolic bottoms stream enriched in tars and alpha methyl styrene dimers, each compared to the crude phenolic stream, said crude phenolic bottoms stream containing salts of neutralization; to the crude phenolic bottoms stream, adding water and a diluent composition, thereby forming a phase separable crude phenolic bottoms stream, said diluent composition comprised of hydrocarbons phase compatible with the crude phenolic bottoms stream and having a combined density lower than the density of the crude phenolic bottoms stream; separating the separable crude phenolic bottoms stream into a hydrocarbon phase and an aqueous phase containing salts of neutralization; whereby the amount of salts of neutralization in the hydrocarbon phase is reduced compared to the amount of salts of neutralization present prior to separation.
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David Daum (1985-1989), Matt Bess (1992-1999), Margaret Botts (1963-1966), Patricia Eiseman (1944-1953), Raymond Thompson (1948-1952), David Rotthoff (1948-1949)