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.
Removal Of Hydrogenation Catalyst From Polymer Solutions By Contact With Silicates
Ajay M. Madgavkar - Edwardsville IL Carma J. Gibler - Houston TX David W. Daum - Seabrook TX
Assignee:
Shell Oil Company - Houston TX
International Classification:
C08F 608
US Classification:
528488
Abstract:
A process is provided comprising the steps of contacting a Group VIII metal hydrogenation catalyst residue containing polymer solution with a silicate, and recovering a polymer solution comprising less than 5 ppm by weight, based on the solution, of the Group VIII metal. In a preferred embodiment, the silicate is calcium silicate, magnesium silicate or diatomaceous earth.
Removal Of Hydrogenation Catalyst From Polymer Solutions By Contact With Activated Carbon
Ajay M. Madgavkar - Edwardsville IL David W. Daum - Seabrook TX Carma J. Gibler - Houston TX
Assignee:
Shell Oil Company - Houston TX
International Classification:
C08G 6391
US Classification:
523310
Abstract:
A process is provided comprising the steps of contacting a polymer solution which contains Group VIII metal hydrogenation catalyst residue with molecular oxygen, contacting the polymer solution with activated carbon, and recovering a polymer cement comprising less than 5 ppm by weight, based on the solution of Group VIII metals.
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David Daum
David Daum
David Daum
Lived:
Boulder, Colorado USA, Indonesia, Thailand, India, Marshall Islands, Nepal, Austrailia,
Work:
Future World Productions - Work on Funding The Third World Woman Project
David Daum (1985-1989), Matt Bess (1992-1999), Margaret Botts (1963-1966), Patricia Eiseman (1944-1953), Raymond Thompson (1948-1952), David Rotthoff (1948-1949)