21
Hugh E Romine: Lubricant additive. Continental Oil Company, Bayless E Rutherford Jr, March 29, 1977: US04014803 (9 worldwide citation)

Novel compounds, which are useful as additives in lubricating oils, are disclosed. The novel compounds are represented by the formula ##STR1## wherein R is an alkenyl group containing 10 to 100 carbon atoms; R' is an alkylene group containing 1 to 5 carbon atoms; n is an integer of 1 to 4; X is sele ...


22
Charles M Starks: Preparation of alcohols and ethers. Continental Oil Company, Bayless E Rutherford Jr, January 6, 1976: US03931238 (9 worldwide citation)

Alcohols and ethers are prepared by reacting a substituted hydrocarbon compound containing halogen or alkyl sulfate groups with an alkali metal hydroxide, in aqueous solution, in the presence of a catalytic amount of certain betaines and recovering from the reaction mixture the desired alcohol and/o ...


23
Derry D Sparlin, Charles M Starks: High strength silicate form and method for producing same. Continental Oil Company, Bayless E Rutherford Jr, June 8, 1976: US03961972 (8 worldwide citation)

A silicate foam composition having improved strength is produced using a particular combination of ingredients comprising an alkali metal silicate, a filler material, a cementing agent, a vinyl chloride telomer having an average molecular weight from about 600-1,000, a gelling agent, and other addit ...


24
Marvin L Peterson, Orwin G Maxson: Sacrificial anode apparatus. Conoco, Bayless E Rutherford Jr, February 17, 1981: US04251343 (7 worldwide citation)

A sacrificial anode apparatus for providing cathodic protection of metal structures, a portion of which is in water is disclosed. The anode apparatus comprises:


25
Ronald J Convers, David P Higley, James A DeBernardi: Method for removal of water from activated carbon. Conoco, Bayless E Rutherford Jr, September 1, 1981: US04287089 (7 worldwide citation)

A method of removing water from activated carbon is disclosed. Briefly, the method comprises (a) passing liquid 1,2-dichloroethane through a bed of activated carbon until a bulk water phase ceases to exit the bed or until from about 60 to about 80 weight percent of the water present in a water-satur ...


26
Bruce E Leach: Preparation of prehnitenol. Continental Oil Company, Bayless E Rutherford Jr, December 21, 1976: US03998892 (7 worldwide citation)

Prehnitenol (2,3,4,5-tetramethylphenol) is prepared by reacting pentamethylphenol with phenol in the liquid phase using a catalyst selected from the group consisting of activated carbon, magnesium oxide and calcium oxide.


27
Bruce E Leach: Catalyst composition useful for preparing 2,6-xylenol. Conoco, Bayless E Rutherford Jr, September 22, 1981: US04290924 (7 worldwide citation)

A process for preparing 2,6-xylenol in high selectivity and a catalyst composition useful therein are disclosed. The process comprises reacting phenol, o-cresol or mixtures thereof with methanol in presence of water, hydrogen and a catalyst consisting essentially of Fe.sub.2 O.sub.3, SnO.sub.2, Cr.s ...


28
Charles M Starks: Preparation of o-benzylphenol. Continental Oil Company, Bayless E Rutherford Jr, August 8, 1978: US04105699 (7 worldwide citation)

A process for preparing o-benzylphenol in high selectivity is disclosed. The process comprises heating a mixture of benzyl alcohol and phenol in the presence of an effective amount of activated alumina as a catalyst.


29
John R Dodd: Oxidative coupling of alkylphenols. Conoco, Bayless E Rutherford Jr, December 25, 1979: US04180686 (6 worldwide citation)

A method of preparing carbon-carbon coupled condensation products of alkylphenols is disclosed. Briefly, the method comprises oxidation of certain specific alkylphenols using palladium acetate as the catalyst in acetic acid or other suitable solvent.


30
Thomas E Goodwin, Charles M Starks: Preparation of methyl-substituted phenols. Continental Oil Company, Bayless E Rutherford Jr, July 11, 1978: US04100207 (6 worldwide citation)

A method of preparing methyl-substituted phenols is disclosed. The method comprises heating a mixture of mono- or di-hydrocarbyl-substituted cresols and methanol at an elevated temperature in the presence of a catalytic amount of magnesium oxide.