Air Products and Chemicals, Inc.

Engelhard Corporation

Pierantozzi, Ronald

Listemann, Mark L.

Armor, John N.

John N Armor

Gamini Ananda Vedage

Yuejin Li

Jose G Santiesteban

Hong-Xin Li

Thomas Stephen Farris

Michael E Ford

Alejandro L Cabrera

Thomas Albert Braymer

Lenore Ann Emig

Diwakar Garg

Mark L Listemann

Thomas R Gaffney

Ronald Pierantozzi

John F Kirner

Gene Everad Parris

Timothy Christopher Golden

Charles G Coe

Shankar Nataraj

John Michael Repasky

Kathryn Sue Hayes

Frederick Carl Wilhelm

Dorai Ramprasad

Daniel J Martenak

Lisa Ann Mercando

William Eamon Carroll

Richard S Myers

James G Hansel

Hao Ding

Roy Daniel Bastian

Paula Jean Battavio

Malee Leeaphon

Jack L Stolz

Joan M Schork

Robert A Miller

Yee-Chang Chen

S Venkat Raman

Srivivasan Kannan

Cunchala S Swamy

Paul Titus Kilhefner

A process for prereforming natural gas containing higher hydrocarbons and methane, includes providing a reactor having a nickel catalyst; providing steam, hydrogen, and natural gas containing higher hydrocarbons and methane to the reactor; adding an oxidant to the feedstock, wherein the oxidant provides oxygen in an amount less than the amount required to partially oxidize all higher hydrocarbons to a mixture of carbon monoxide and hydrogen; reacting the oxidant with higher hydrocarbons; and forming a gaseous mixture containing methane, carbon monoxide, carbon dioxide, steam and hydrogen substantially free of higher hydrocarbons and oxygen. The gaseous mixture can be reformed. An apparatus for performing the process includes a reactor; a feedstock source containing steam, hydrogen, and natural gas comprising higher hydrocarbons and methane; an oxidant source; valves and pipes connecting the natural gas source, the oxidant source and the reactor; and a nickel-containing catalyst within the reactor.

Process for improving prereforming and reforming of natural gas containing higher hydrocarbons along with methane

This invention pertains to an improvement in a process for the formation of secondary or tertiary amines by the catalytic reductive amination of a nitrile with a primary amine. The catalyst employed in the improved reductive amination process is one that has been promoted with an acidic promoter preferably a solid phase acidic promoter.

Selective reductive amination of nitriles

An improved process for producing an atmosphere suitable for carburizing steel components by adding a small amount of oxygen to a mixture of natural gas and carbon dioxide, pre-heating the mixture to the desired reaction temperature in the presence of an inert material or a non-nickel-based catalyst that promotes the reaction between oxygen and natural gas without forming coke to avoid catalyst deactivation by coke formation, and reacting natural gas with carbon dioxide at high temperature in the presence of a catalyst.

Process for producing carburizing atmospheres

This invention pertains to an improvement in a process for the formation of secondary or tertiary amines by the catalytic reductive amination of a nitrile with a primary or secondary amine and, particularly to the reductive amination of C,nitrites with a secondary amine. The catalyst employed in the improved reductive amination process is one which has been promoted with a lithium salt or base, e.g., lithium chloride or lithium hydroxide.

This invention relates to an improvement in a process for the catalytic hydrogenation of aromatic amines and to the resultant catalyst. The basic process for hydrogenating both mononuclear and polynuclear aromatic amines comprises contacting an aromatic amine with hydrogen in the presence of a rhodium catalyst under conditions for effecting ring hydrogenation. The improvement in the ring hydrogenation process resides in the use of a rhodium catalyst carried on a lithium aluminate support. Often ruthenium is included.

Lithium aluminate as a catalyst support for hydrogenation of aromatic amines

New compounds, represented by the formulae I and II, ##STR1## wherein R.sub.1, R.sub.2, and R.sub.3, are independently C.sub.3 or C.sub.4, substituted or unsubstituted alkylene groups, are useful for catalyzing the reaction between an organic polyisocyanate and a compound containing a reactive hydrogen to form polyurethanes.

1,4-diazabicyclo[2.2.2]octane compounds and their use for the production

This invention relates to an improved hydrogenation and isomerization process wherein aromatic amines are hydrogenated to their ring hydrogenated counterparts and substantially isomerized to their thermodynamic form. These aromatic amines are presented by the formulas: ##STR1## wherein R is hydrogen or C.sub.1-6 alkyl, R1 and R2 are hydrogen or C.sub.1-6 aliphatic, A is C.sub.1-4 or NH; n is 0-2, x is 1-3 and y is 0 to 2 except the sum of the y groups must be at least 1.

Hydrogenation of aromatic amines to produce their ring hydrogenated

This invention relates to an isomerization process wherein hydrogenated aromatic amines are substantially isomerized to their thermodynamic form. These hydrogenated aromatic amines are presented by the formulas: ##STR1## wherein R is hydrogen or C.sub.1-6 aliphatic, R1 and R2 are hydrogen or C.sub.1-6 aliphatic, A is C.sub.1-4 or NH; n is 0-2, x is 1-3 and y is 1 to 2 except the sum of the y groups in Formula I may be 1. The improvement in the process comprises using a catalytic system comprising cobalt preferably in combination with another Group VIII metal selected from rhodium, ruthenium, platinum, and palladium and the metal, copper. Preferably the catalyst comprises cobalt in combination with rhodium or ruthenium wherein the weight ratio of cobalt to rhodium or ruthenium, calculated on metal content, is from about 0.2 to 100 weight parts cobalt per weight part rhodium or ruthenium and the isomerization is carried out in the presence of hydrogen.

Isomerization of cyclohexylamines to produce their thermodynamic

A process for preparing triethylenediamine and piperazine by passing an ethanolamine, ethyleneamine, piperazine or morpholine over a pentasil-type zeolite at elevated temperature characterized by employing a ZSM-5 zeolite in the hydrogen or ammonium form which has been treated with a passivating agent which is a silicon-containing compound capable of deactivating the acidic sites on the zeolite surface.

Triethylenediamine and piperazine synthesis using zeolite catalysts

A process for the production of aliphatic amines by reacting aliphatic alcohols with an amino compound in the presence of a catalyst containing at least two inter-dispersed metals, in a multi-metallic structure, in which at least one of the metals is nickel or cobalt, and at least one other metal is palladium, platinum, rhodium, ruthenium, or copper.

Multi-metallic actalysts for amination of alcohols to form alkylamines

A process for the production of predominantly primary and secondary amines and little or no tertiary amines by the reductive amination of aliphatic alcohols using a metal exchanged crystalline aluminosilicate catalyst. The catalyst has a silica/alumina ratio ranging from about 10:1 to 40:1, contains about 1 to 10% by weight of cobalt or nickel and about 0.05 to 5% by weight of at least one other metal. High conversion rates are achieved at moderate temperatures and pressures.

Metal exchanged zeolite catalysts for alcohol amination

A process for preparing triethylenediamine by passing an amine compound over a catalyst at elevated temperature to afford a reaction product containing triethylenediamine and piperazine, the amine compound having, in the molecule, a moiety represented by the following general formula ##STR1## where R.sup.1, R.sup.2, R.sup.3 and R.sup.4 are independently a hydrogen atom or an alkyl group having 1 to 4 carbon atoms and X is oxygen or nitrogen characterized by adding an ethylating compound containing at least one nitrogen and/or oxygen atom to the reaction product and contacting the reaction product, under conditions sufficient to produce triethylenediamine from the ethylating compound and piperazine, with a condensation/cyclization shape-selective zeolite catalyst demonstrating a triethylenediamine/piperazine weight ratio uptake value of at least 6:1.

Process for the production of triethylenediamine

A process for preparing triethylenediamine by passing an ethanolamine, ethyleneamine, piperazine or morpholine over a pentasil-type zeolite at elevated temperature characterized by employing a ZSM-5 zeolite in the hydrogen or ammonium form which has been pretreated with an aqueous solution of a chelating agent capable of forming a chelate-aluminum complex.

Production of triethylenediamine using surface acidity deactivated

A process for preparing triethylenediamine by passing an ethanolamine, ethyleneamine, piperaziHe or morpholine over a pentasil-type zeolite at elevated temperature characterized by employing a ZSM-5 zeolite in the hydrogen or ammonium form which has been pretreated with an aqueous caustic solution.

Triethylendiamine synthesis with base-treated zeolites as catalysts

Improved selectivity to tertiary amine production is obtained by the addition of an aliphatic or aromatic halide to the feed during the catalytic hydrogenation of saturated or unsaturated aliphatic or cycloaliphatic nitriles.

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Orefield, PA, United States of America

John N Armor