In one embodiment, we disclose hardened olefin waxes and processes for preparing them. In another embodiment, we disclose oxidized olefin waxes having low viscosity and processes for preparing them. The waxes are suitable for use as polishes, coatings, or inks, among other uses.
Olefin Waxes Having Improved Hardness Or Viscosity
A process to oxidize an olefin wax, comprising: contacting a feedstock olefin wax composition with an oxygen-containing gas at a temperature greater than a melting point of the feedstock olefin wax composition melting point, to prepare an oxidized olefin wax composition wherein the oxidized olefin wax composition has an acid number greater than 1 mg KOH/g oxidized olefin wax composition and a kinematic viscosity at 100 C. less than 70 cSt.
Ronald G. Abbott - Kingwood TX, US Ralph P. Williams - Bartlesville OK, US Marvin M. Johnson - Bartlesville OK, US John W. Vanderveen - Bartlesville OK, US
Assignee:
Phillips Petroleum Company - Bartlesville OK
International Classification:
C07C 2/58
US Classification:
585724, 585723, 585730
Abstract:
A novel alkylation catalyst is described which is used in processes for alkylating olefin hydrocarbons with isoparaffin hydrocarbons to produce high octane alkylate products suitable for use as a blending component of gasoline motor fuel. The novel catalyst comprises a mixture of a hydrogen halide and a sulfone. The novel alkylation catalyst is utilized in a novel process for alkylating olefin hydrocarbons with isoparaffin hydrocarbons.
Olefin Waxes Having Improved Hardness Or Viscosity
Hu Yang - Manvel TX, US Eduardo J Baralt - Kingwood TX, US Willie J Isom - Kingwood TX, US Ronald G Abbott - Kingwood TX, US
International Classification:
C07C 27/12 C08L 91/06 C09D 191/06
US Classification:
208 3, 106270
Abstract:
In one embodiment, we disclose hardened olefin waxes and processes for preparing them. In another embodiment, we disclose oxidized olefin waxes having low viscosity and processes for preparing them. The waxes are suitable for use as polishes, coatings, or inks, among other uses. For example, a hardened olefin wax composition produced from a feedstock olefin wax composition by contacting the feedstock olefin wax composition with an oxygen-containing gas at a temperature greater than a melting point of the feedstock olefin wax composition, the hardened olefin wax composition having: a needle penetration value at 25 C. at least 5 percent less than a needle penetration value at 25 C. of the feedstock olefin wax composition; a a kinematic viscosity at 100 C. of up to about 200% greater than the kinematic viscosity of the feedstock olefin wax composition; and a saponification number less than 5 mg KOH/g hardened olefin wax composition.
Oxygen Scavenging Packaging Having Improved Sensory Properties
Ta Yen Ching - Houston TX, US James Solis - Groves TX, US Ronald Abbott - Kingwood TX, US William Diecks - Houston TX, US Darrell Landry - Nederland TX, US
We disclose a packaging article, defining a package interior and a package exterior, and comprising (i) a first layer, containing an oxygen scavenging polymer the oxygen scavenging polymer comprises (a) an ethylenic backbone or a polyester backbone and (b) at least one cyclic olefinic group; (ii) a second layer, containing a functional barrier polymer; and (iii) a transition metal organic salt in at least one of the first layer or a layer adjacent to the first layer; wherein the second layer is located between the first layer and the package interior. The packaging article can further comprise a functional absorber. Such a packaging article is capable of both scavenging oxygen present in the package interior and inhibiting the migration of off-taste- or off-odor-imparting scavenging byproducts from the first layer to the package interior.
Control Of Synthetic Isopentane Production During Alkylation Of Amylenes
Ronald G. Abbott - Kingwood TX Bruce B. Randolph - Bartlesville OK Richard L. Anderson - Bartlesville OK
Assignee:
Phillips Petroleum Company - Bartlesville OK
International Classification:
C07C 258 C07C 262
US Classification:
585709
Abstract:
A method of minimizing or controlling the production of synthetic isopentane during the catalyzed alkylation reaction of amylenes and isoparaffins by providing a concentration of isopentane in the alkylation reactor feed material.
Ronald G. Abbott - Kingwood TX Ralph P. Williams - Bartlesville OK Marvin M. Johnson - Bartlesville OK John W. Vanderveen - Bartlesville OK
Assignee:
Phillips Petroleum Company - Bartlesville OK
International Classification:
B01J 2702
US Classification:
502216
Abstract:
A novel alkylation catalyst is described which is used in processes for alkylating olefin hydrocarbons with isoparaffin hydrocarbons to produce high octane alkylate products suitable for use as a blending component of gasoline motor fuel. The novel catalyst comprises a mixture of a hydrogen halide and a sulfone. The novel alkylation catalyst is utilized in a novel process for alkylating olefin hydrocarbons with isoparaffin hydrocarbons.
Transition Metal-Magnesium Catalyst Precursors For The Polymerization Of Olefins
Ronald G. Abbott - Kingwood TX Michael J. Krause - East Brunswick NJ David L. Beach - Kingwood TX
Assignee:
Chevron Chemical Company - San Ramon CA
International Classification:
C08F 464 B01J 3100
US Classification:
502104
Abstract:
Disclosed is a catalyst precursor, useful to make catalysts useful in the polymerization of olefins, comprising the product obtained by adding a preformed magnesium source to a solution comprising a solvent having dissolved therein a transition metal compound and an alkyl halide.
Name / Title
Company / Classification
Phones & Addresses
Ronald E Abbott President
TPNB SERVICE CORPORATION Nonclassifiable Establishments
2310 W Interstate 20 STE 101, Arlington, TX 76017 35 S Plz, Paris, TX 75460 PO Box 1750, Paris, TX 75461