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Dive into the research topics where Harold E. Swift is active.

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Featured researches published by Harold E. Swift.


Journal of Catalysis | 1971

Dehydrodimerization of propylene using bismuth oxide as the oxidant

Harold E. Swift; John E. Bozik; J.A. Ondrey

Abstract Bismuth oxide, Bi2O3, serves as an oxidant for the conversion of propylene to mainly 1,5-hexadiene. The main secondary product is benzene with small amounts of normal and cyclohexadiene also formed. The formation of 1,5-hexadiene most likely involves the combination of two allylic radicals. As the reaction temperature is increased from 475 to 500 °C, the yield of 1,5-hexadiene decreases while the benzene yield increases. To selectively produce 1,5-hexadiene from propylene, the reaction has to be carried out cyclically, where the propylene reacts with bismuth oxide for a given period of time, and then the oxygen that is consumed is rapidly replenished with air. If a sufficient amount of gas-phase oxygen is used with propylene, the bismuth oxide serves as a catalyst to give a continuous reaction.


Journal of Catalysis | 1968

Metallic phases and activities of nickel-tin-silica catalysts: Dehydrogenation of cyclohexanone, cyclohexanol, and cyclohexane

Harold E. Swift; John E. Bozik

Abstract Addition of tin to a nickel-silica catalyst greatly promotes the activity and gives a longer catalyst life for the dehydrogenation of cyclohexanone and/or cyclohexanol to phenol. Outstanding results are obtained with a catalyst having a nickel-to-tin molar ratio of 2.5:1. Reduction of the nickel-to-tin molar ratio to 0.9:1 gives very little dehydrogenation of cyclohexanone; however, a new reaction takes place, which is the aldolization of cyclohexanone to 2-(1-cyclohexenyl)cyclohexanone. An explanation of the promoting effect of tin and the change in reaction selectivity with nickel-to-tin ratio is given. An investigation of the reduced nickel-tin-silica catalysts by X-ray diffraction has revealed the presence of a supported nickel-tin alloy phase.


Journal of Catalysis | 1970

Specific catalysis with iron coordination complexes

Harold E. Swift; John E. Bozik; Ching-Yong Wu

A novel three-component catalyst system has been found which is very active for the polymerization of isoprene. The catalyst consists of iron(III)acetyl-acetonate-triethylaluminum and specific bidentate ligands. The three bidentate ligands found which greatly promote the polymerization are in order of decreasing promoting ability: phenyl-2-pyridylacetonitrile, 2-cyanopyridine, and 2-pyridine-aldoxime. The ligand must contain certain functionalities to result in an active catalyst. The polymerization of isoprene proceeds best at low temperatures, such as −23 °C, and the rate and polymer yield decreases with increasing temperature. This unusual temperature effect is probably due to a greater catalyst stability at lower temperatures. This catalyst produces a polyisoprene which consists of approximately equal amounts of cis-1,4 and 3,4 linkages.


Chemical Engineering Science | 1954

Preparation of cumene hydroperoxide

Ching-Yong Wu; Harold E. Swift; John E. Bozik

Cumene hydroperoxide is prepared by the oxidation of cumene with molecular oxygen in the presence of a minute amount of solid barium oxide.


Archive | 1977

PREPARATION OF ETHYLBENZENE HYDROPEROXIDE

Ching-Yong Wu; Harold E. Swift; John E. Bozik


Archive | 1970

POLYMERIZATION PROCESS AND CATALYST SYSTEM THEREFOR

John E. Bozik; Harold E. Swift; Ching-Yong Wu


Archive | 1971

Process for coupling propylene and isobutylene

John E. Bozik; John A Ondrey; Harold E. Swift


Archive | 1970

POLYMERIZING UNSATURATED MONOMERS WITH A CATALYST OF AN IRON COMPLEX, A DIALKYL ALUMINUM COMPOUND AND A BIDENTATE LIGAND

John E. Bozik; Harold E. Swift; Ching Yong Wu


Archive | 1973

PROCESS FOR COUPLING LOWER OLEFINS

John E. Bozik; John A Ondrey; Harold E. Swift


Archive | 1968

DIOLEFIN ALKYLATION PROCESS

John E. Bozik; Harold E. Swift; Ching Yong Wu

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