Atlantic Richfield Company

Arco Chemical Technology, L.p.

John J Leonard

John A Sofranko

C Andrew Jones

Jar-lin Kao

Howard P Withers, Jr

Harold Shalit

Anne Mae Gaffney

John A Jaecker

Marvin F Johnson

John J McCoy

Hsiang-ning Sun

Howard P Withers

E William Breder, Jr

Mary T Arnold

William J Piel

Gordon A Sullivan

Herry E Eilerts-de Haan

The present invention provides a novel integration of an existing MTBE process unit with new propylene oxide producing facilities whereby through this integration new propylene oxide production is achieved without significant increase in MTBE production.

Integrated production of propylene oxide and methyl T-butyl ether

A method for dehydrogenating dehydrogenatable hydrocarbons which comprises contacting said hydrocarbons with a solid comprising at least one reducible oxide of at least one metal which oxides when contacted with hydrocarbons at the temperature are reduced and produce dehydrogenated hydrocarbon products and water, the solid being associated with a silica support. The oxide is reduced by the contact which is carried at about 500.degree. to 100.degree. C. The reducible metal oxides are regenerated by oxidizing the reduced composition with oxygen.

Hydrocarbon dehydrogenation

An improved method for converting methane to higher hydrocarbon products by contacting a hydrocarbon gas comprising methane, an oxygen-containing gas and a reducible metal oxide under conditions effective to produce higher hydrocarbon products and water, the improvement which comprises conducting the contacting in the presence of at least one stabilizer selected from the group consisting of chalcogens and compounds thereof.

Methane conversion process

A continuous method for synthesizing hydrocarbons from a methane source which comprises contacting methane with moving beds of particles comprising an oxidative synthesizing agent under synthesis conditions wherein particles recirculate between two physically separate zones: a methane contact zone and an oxygen contact zone.

Methane conversion

An improved method for converting methane to higher hydrocarbon products by contacting a hydrocarbon gas comprising methane, an oxygen-containing gas and a reducible metal oxide under conditions effective to produce higher hydrocarbon products and water, the improvement which comprises conducting the contacting in the presence of at least one promoter selected from the group consisting of halogens and compounds thereof.

A class of mixed oxide catalysts comprising Mn-containing oxides, alkali metals or compounds thereof, and at least one member of the group consisting of oxides of Si, oxides of alkaline earth metals, and mixed oxides of Si and at least one alkaline earth metal. In the more preferred embodiments, the third component serves as a carrier for the Mn and alkali metal components. The composition preferably comprises a major amount of the carrier material and minor amounts of the other components. The compositions are useful for hydrocarbon coversion, methane conversion, and oxidative dehydrogenation processes characterized by formation of coproduct water.

Alkali promoted manganese oxide compositions containing silica and/or

A method of synthesizing hydrocarbons from a methane source which includes the steps of contacting a methane with an oxide of a metal which oxide when contacted with methane at between about 500.degree. and 1000.degree. C. is reduced and produces higher hydrocarbon products and water, recovering ethylene from the effluent of the contacting and oligomerizing the ethylene to produce higher hydrocarbon products.

Two-step methane conversion process

A continuous method for synthesizing hydrocarbons from a methane source which comprises contacting methane with particles comprising an oxidative synthesizing agent under synthesis conditions wherein particles recirculate between two physically separate zones: a methane contact zone and an oxygen contact zone. Preferably, particles are maintained in each of the two zones as fluidized beds of solids. Particularly effective oxidative synthesizing agents are reducible oxides of metals selected from the group consisting of Mn, Sn, In, Ge, Pb, Sb, and Bi.

A method for synthesizing hydrocarbons from a methane source which comprises contacting methane with an oxidative synthesizing agent under elevated pressures, preferably at pressures within the range of about 5 to 30 atmospheres. Particularly effective oxidative synthesizing agents are reducible oxides of metals selected from the group consisting of Mn,Sn,In,Ge,Pb,Sb, and Bi.

A method is disclosed for converting methane to higher hydrocarbon product by contacting the methane with a solid which comprises a reducible metal oxide which when contacted with methane at a temperature within the range of about 500.degree. to 1000.degree. C. is reduced and produces higher hydrocarbon products and water, the improvement comprising recycling C.sub.2 + alkanes recovered during subsequent processing of the effluent produced by the contacting to the contacting step.

An improved method for converting methane to higher hydrocarbon products by contacting a hydrocarbon gas comprising methane, an oxygen-containing gas and a reducible metal oxide under synthesis conditions, the improvement which comprises contacting methane and oxygen with a contact solid which also contains a promoting amount of alkali metal, alkaline earth metal, and/or compounds thereof. Sodium is a particularly effective promoter. Stability of the promoted contact agent is enhanced by the presence of minor amounts of phosphorus.

Synthesis of dialkyl oxalates by the oxidative carbonylation of liquid monohydric saturated alcohols of from 1 to 20 carbon atoms with carbon monoxide and oxygen or an oxygen-containing gas in the presence of a catalytic amount of a catalyst comprising palladium or a salt thereof in combination with vanadium in the oxide (V.sub.2 O.sub.5, V.sub.2 O.sub.4, V.sub.2 O.sub.3) form and titanium or a non-hydrolyzable salt thereof, said catalyst being present in a heterogeneous phase.

Synthesis of dialkyl oxalates by the heterogeneously catalyzed oxidative

A process for the preparation of .alpha.-hydroxyisobutyric acid by the catalytic oxidation of isobutyric acid with oxygen in an aqueous solution in the presence of a TlCl.sub.3 or TlBr.sub.3 catalyst and a Cu, Sn, or Fe halide compound as a redox agent. Optionally alkali metal halides may be employed to promote catalysis and control the halide concentration.

Preparation of .alpha.-hydroxyisobutyric acid using a thallic halide

A process for the preparation of alpha-hydroxyisobutyric acid by the stoichiometric oxidation of isobutyric acid in aqueous solution at temperatures of from about 50.degree. C. to 200.degree. C. in the presence of a thallic (Tl.sup.+3) salt.

Oxidation of isobutyric acid to alpha-hydroxyisobutyric acid

A method for synthesizing hydrocarbons from a methane source which comprises contacting methane with an oxide of tin at a temperature of about 500.degree. to 1000.degree. C. The oxide is reduced by the contact and coproduct water is formed. A reducible oxide of tin is regenerated by oxidizing the reduced composition with molecular oxygen. The oxide SnO.sub.2 is a particularly effective synthesizing agent.

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Springfield, PA, United States of America

John J Leonard