Catalyst mixtures are comprised of zinc oxide, calcium carbonate or calcium oxide, and an amount of chromium (III) oxide in an amount sufficient to improve conversion and/or selectivity of cyclohexanol to cyclohexanone under cyclohexanol dehydrogenation conditions.
Andrew J. McNabb - Lake Jackson TX R. Merritt Sink - Lake Jackson TX
Assignee:
BASF Corporation - Mt. Olive NJ
International Classification:
C05C 900 C05C 700 C05B 1500 C05B 700
US Classification:
71 28
Abstract:
Solids having a tendency to cake are treated with distillation heavies that are liquid at about 60. degree. C. or less and are obtained from production of a ketone having the formula: R. dbd. O, wherein R is substituted or unsubstituted, branched, straight chain or cyclic, C. sub. 4 to C. sub. 18. The solids so treated have a reduced tendency to cake.
Andrew J. McNabb - Lake Jackson TX Teresa C. Webb - Leicester NC
Assignee:
BASF Corporation - Mt. Olive NJ
International Classification:
C09K 322
US Classification:
252384
Abstract:
Solid materials are treated with a blend of water or solvents and distillation bottoms obtained from production of an alcohol having the formula: R2--R1--OH, wherein R1 is substituted or unsubstituted, branched, straight chain, or cyclic C. sub. 4 to C. sub. 12 and R2 is OH or H.
Andrew J. McNabb - Lake Jackson TX Rebecca E. Phillips - Lake Jackson TX
Assignee:
BASF Corporation - Mt. Olive NJ
International Classification:
C07C 2726 C07C 3508
US Classification:
568856
Abstract:
A process for increasing the amount of isolatable products in a by-product stream generated in the production of 1,6 hexanediol includes combining the by-product stream with water to form a combination of the water and the by-product stream; and reacting the combination at a temperature between about 250. degree. C. to about 400. degree. C. at a pressure from about 1,000 psig to about 3,000 psig to form one or more reaction products.
Process For The Recovery Of Cyclohexanone And Cyclohexanol From Cyclohexanone Production Distillation Bottoms
Andrew J. McNabb - Lake Jackson TX Deirdre R. Williams - Lake Jackson TX
Assignee:
BASF Corporation - Mt. Olive NJ
International Classification:
C07C 4529
US Classification:
568366
Abstract:
Organic by-products having higher boiling points than cyclohexanone (usually obtained from the bottoms of a distillation operation to separate cyclohexanone from other reaction products during cyclohexanone production) can be converted to recoverable cyclohexanone and cyclohexanol using a catalyst having high aluminum oxide concentrations. The preferred catalyst is one which has an aluminum oxide (Al. sub. 2 O. sub. 3) content of at least about 95 wt. %, and more preferably greater than about 99 wt. %.
Andrew J. McNabb - Lake Jackson TX R. Merritt Sink - Lake Jackson TX
Assignee:
BASF Corporation - Mt. Olive NJ
International Classification:
C05C 900 C05C 700 C05B 1500 C05B 700
US Classification:
71 28
Abstract:
Solids that, untreated, have a tendency to cake are treated with distillation bottoms that are liquid at about 60. degree. C. or less and are obtained from production of an alcohol having the formula: R2-R1-OH, wherein R1 is substituted or unsubstituted, branched, straight chain or cyclic, C. sub. 4 to C. sub. 12 and R2 is OH or H.
Andrew J. McNabb - Lake Jackson TX R. Merritt Sink - Lake Jackson TX
Assignee:
BASF Corporation - Mt. Olive NJ
International Classification:
C05C 900 C05C 700 C05B 1500 C05B 700
US Classification:
71 28
Abstract:
A substantially non-caking solid is treated with distillation bottoms that are liquid at about 60. degree. C. or less and are obtained from production of an alcohol having the formula: R2--R1--OH, wherein R1 is substituted or unsubstituted branched, straight chain or cyclic C. sub. 4 to C. sub. 12 and R2 is OH or H.
Andrew J. McNabb - Lake Jackson TX Teresa C. Webb - Leicester NC
Assignee:
BASF Corporation - Mt. Olive NJ
International Classification:
C09K 300 C09K 322 B01F 1742
US Classification:
252383
Abstract:
A substantially dust-free solid that is treated with a blend of water or other solvent and certain distillation bottoms. The distillation bottoms are at about 60. degree. C. or less and are obtained from production of an alcohol having the formula: R2--R1--OH, wherein R1 is substituted or unsubstituted branched, straight chain or cyclic C. sub. 4 to C. sub. 12 and R2 is OH or H.
Name / Title
Company / Classification
Phones & Addresses
Andrew Mcnabb
270 Lake Street Realty, LLC Nonresidential Building Operator