The Dow Chemical Company

Other

Steve A Sims

Thomas M Knobel

John L Burba, Iii

Donald M Maschmeyer

Allan E Fowler

G Eldon White

Christopher P Christenson

Ha Q Pham

Douglas L Hunter

Avis L McCrary

Wilfred C Meyer

Jose V Saavedra

Peter A Doty

Arthur E Read, Jr

Edgar F Hoy

Billy Duane Head

William E Shewbart

Gordon E White

Andrea H Hazlitt

Susan K Falcone

Stanley F Simpson

Betty J Smith

An accessory for modifying the decay pattern of vibrations set up in an implement to which the accessory is attached, and the combination of a decay pattern modifying accessory and an implement. Methods of manufacturing decay pattern modifying accessories are also disclosed.

Vibration decay modifying accessories and methods of making the same

Coating formulations which behave as elastic solids having reversible stress-induced fluidity are prepared by creating a fluid having distributed therein effective amounts of ionic charge sites and countercharge sites. For instance, elastic solids having reversible stress-induced fluidity are prepared by combining liquid formulations with a dispersion of a small, but effective, amount of at least one crystalline mixed metal hydroxide conforming substantially to the formula

Coating composition comprising solids having reversible stress-induced

Crystalline layered mixed metal hydroxides (LMMHs) which are substantially free of unbound water and which conform substantially to the general formula

Layered mixed metal hydroxides made in non-aqueous media

This invention is an antistatic polyurethane shoe sole which is prepared by reacting in a closed mold a reaction mixture comprising

Antistatic polyurethane shoe sole compositions

Butene-1 and ethylene mixtures are made by reacting ethylene with a trialkyl aluminum in a boiling bed reactor. The process is more efficient in that it is selective for making butene-1 and more butene-1 is produced per unit weight of the trialkyl aluminum.

Process for making a mixture of ethylene and butene-1

A method for preparing C.sub.4 to C.sub.10 .alpha.-olefins employing trialkyl aluminum compounds, in a growth zone having a recirculation rate through an external heat transfer zone such that the contents of the zone are recirculated in a period of time sufficient to remove the heat of the reaction using added lower .alpha.-olefins at 100.degree.-150.degree. C., 200-2000 psig, and 5-90 minute contact time followed by displacement with lower .alpha.-olefins in a static mixer zone to free the growth .alpha.-olefins and regenerate the trialkyl aluminum compounds. The growth .alpha.-olefins are separated with all of the lower .alpha.-olefins recycled to the growth and displacement steps.

Linear alpha olefin production using a tank growth reactor

A method for preparing C.sub.4 to C.sub.10 .alpha.-olefins having a major portion C.sub.6 .alpha.-olefins employing tri alkyl aluminum compounds, e.g., Al(C.sub.2 H.sub.5).sub.3 or Al(C.sub.4 H.sub.9).sub.3 or mixtures of Al(C.sub.2 H.sub.5).sub.3 and Al(C.sub.4 H.sub.9).sub.3 as well as the unmixed C.sub.2, C.sub.4 alkyl aluminum isomers or homologs in the growth step using added ethylene at about 120.degree. C., 500-700 psig, 5-90 minute contact time followed by displacement with C.sub.2 H.sub.4, C.sub.4 H.sub.8, or C.sub.2 H.sub.4 and C.sub.4 H.sub.8 to free the growth alkyl and regenerate the tri alkyl aluminum compounds. The growth .alpha.-olefins are separated with all of the C.sub.2 H.sub.4 recycled to the growth and displacement steps, and part or all of the C.sub.4 H.sub.8 recycled to the displacement step.

Linear alpha olefin production

Growing community of inventors

Angleton, TX, United States of America

Steve A Sims