Amoco Corporation

Bp Corporation North America Inc.

Standard Oil Company (indiana)

Wayne P Schammel

Erik C Scher

Joel M Cizeron

Fabio R Zurcher

Joel Gamoras

Greg Nyce

Juergen K Holzhauer

Michael R Green

Victor A Adamian

Jarod Mccormick

Erik-Jan Ras

Daniel Rosenberg

Walter Partenheimer

David A Young

William H Gong

Philip Nubel

Peter H Kilner

Chengxiang Zhou

Peter D Metelski

Dennis J Michalak

Stephen G Ceisel

Joseph P Egan, Jr

Joel David Vincent

Roger Vogel

Erik Freer

Jeffrey T Miller

George E Kuhlmann

Anja Rumplecker

Neal R Nowicki

Dmitry Karshtedt

Marian Alcid

Steven A Cerefice

Alex Tkachenko

Yenamandra Viswanath

Matthew A Kulzick

Chang-Man Park

Kristi A Fjare

Chang M Park

Kelley R Lane

Rosemary F McMahon

Calvin T Chew

Paul A Sanchez

Stephen P Brugge

Donald E Ruedin

John N Wood

Leo C Fende

Igor V Zakharov

John K Darin, Deceased

Bradley J Huggins

Bryan M Rabatic

Daniel Rosenburg

Catalytic compositions for conversion of substituted aromatic feed materials to oxidized products comprising aromatic carboxylic acid derivatives of the substituted aromatic feed materials comprise solid particles comprising palladium in combination with at least one of antimony, bismuth and gold, and optionally, an additional metal or metalloid component effective to promote activity or selectivity of the palladium and antimony, bismuth or gold for oxidation to aromatic carboxylic acids. A process for oxidizing substituted aromatic feed materials comprises contacting the feed material with oxygen in the presence of such catalytic compositions in a liquid reaction mixture.

Process and catalyst for oxidizing aromatic compounds

Catalytic compositions for conversion of substituted aromatic feed materials to oxidized products comprising aromatic carboxylic acid derivatives of the substituted aromatic feed materials comprise a combination comprising a palladium component, an antimony component and/or a bismuth component, and one or more Group 4, 5, 6 or 14 metal or metalloid components. A process for oxidizing substituted aromatic feed materials comprises contacting the feed material with oxygen in the presence of such a catalytic composition in a liquid reaction mixture.

The present invention relates to the liquid phase oxidation of aromatic hydrocarbons in the presence of at least one heavy metal oxidation catalyst and bromine, which is activated by at least one of anthracene or another polycyclic aromatic compound to produce aromatic carboxylic acids.

Anthracene and other polycyclic aromatics as activators in the oxidation of aromatic hydrocarbons

This invention is related to the production of trimellitic anhydride (TMA). More specifically, the invention is related to the addition of a mineral acid or salt thereof in the production process of trimellitic anhydride to reduce the viscosity of the bottoms fraction when TMA is purified by distillation and thus to prevent fouling/plugging. This permits the use of lower levels of TMA in the bottoms fraction and increases TMA recovery.

Addition of mineral acids or salts thereof to a TMA production process

A process is disclosed for oxidation of pseudocumene to trimellitic acid wherein process residue and bottoms from stripping procedures to recover process solvent are recycled and incorporated in filtrate mother liquor and reinjected into the oxidation reactor at a point in time at least after the first methyl group in the pseudocumene molecule has been oxidized to a carboxy group. Recovery of trimellitic acid is increased, catalyst recovery is increased in a form suitable for immediate recycle to the oxidation reaction, and waste products from the oxidation process are substantially reduced.

Process for pseudocumene oxidation to trimellitic acid with mother

Viscous, liquid polybutenes of at least 50 wt. % vinylidene content are disclosed together with a procedure for preparing the compounds using an aluminum chloride-organic nitro compound catalyst.

Process for preparing polybutenes with increased reactivity

A process is disclosed for liquid phase oxidation of alkyl aromatic hydrocarbons to aromatic carboxylic acids in presence of a multivalent catalyst promoted by a source of bromine. The oxidation is conducted in at least two oxidation reactions. Exothermic heat of reaction is controlled by means of a liquid phase heat exchanger to control temperature and pressure. Oxygen partial pressure in each stage is at least 1.5 psia to minimize oxygen starvation and improve selectivity. Low reactor temperature, high reactor pressure and improved selectivity improve product yield and product quality.

Process for oxidation of alkyl aromatic compounds

A process for the manufacture of trimelitic acid from pseudocumene is disclosed. The pseudocumene is oxidized in the presence of a cerium, cobalt, manganese, and optionally zirconium, bromine catalyst wherein all of the cerium is added in the second stage of the oxidation, and wherein most of the bromine is also added during the second oxidation stage. Trimellitic acid is useful in the manufacture of polyester and polyamide-imides.

Process for the production of trimellitic acid

A method for making 2,6-naphthalene dicarboxylic acid by the oxidation of 2,6-diisopropylnaphthalene or its oxidation derivatives in the presence of a catalyst comprising cobalt, manganese, cerium and bromine components is disclosed.

Method for making 2,6-naphthalene dicarboxylic acid

A process for the oxidation of pseudocumene to TMLA is disclosed which comprises catalytic oxidation of pseudocumene with air in the presence of acetic acid in an oxidation zone in the liquid phase wherein the weight ratio of acetic acid to pseudocumene is in the range of about 0.5-0:1.0 and the catalyst comprises one or more heavy metal oxidation catalysts comprising zirconium, cobalt, and manganese to provide about 0.1 to about 0.4 weight percent total metals based on pseudocumene and a source of bromine. The addition of the bromine component is controlled to provide a total of about 0.10 to about 0.30 weight percent total bromine based on pseudocumene. The total weight ratio of bromine ions to total metals ions is about 0.5 to about 2.0. The zirconium content is about 1 to about 5% and the manganese content is about 14 to about 60% each by weight of the total metals. The reaction temperature is about 300.degree. F. to about 420.degree. F. The crude trimellitic anhydride is hydrolyzed with water or a mixture of a low molecular weight carboxylic acid and water. Alternatively, a trimellitic anhydride/dimethylformamide adduct is prepared and this adduct is hydrolyzed with a mixture of a low molecular weight carboxylic acid and water. Trimellitic acid is useful in the manufacture of polyesters and polyamide-imides.

Process for the production and recovery of trimellitic acid

A process is disclosed for the co-production of aliphatic monocarboxylic acids and polycarboxylic aromatic acids in high selectivity, conversion and yield. The aliphatic monocarboxylic acid can serve as a component of the solvent for the process.

Process for production of polycarboxylic aromatic acids

A process is disclosed for the oxidation of di- or trimethyl benzenes with molecular oxygen under liquid-phase conditions in the presence of a recovered cobalt and manganese catalyst, which has been recovered by heating oxidation incinerator ash in the presence of acetic acid and a reducing agent wherein the weight ratio of acetic acid to said oxidation incinerator ash is from about 1:1 to about 50:1, and the ratio of electrons which the reducing agent can deliver to atoms of the cobalt plus manganese in the oxidation incinerator ash is from about 0.1:1 to about 4:1 at about the boiling point of the acetic acid at atmospheric pressure and recovering the cobalt and manganese in liquid solution as the metal acetic acid salt, wherein the oxidation is carried out at a temperature of from about 100.degree. C. to about 250.degree. C.

Process for the oxidation of di- or trimethylbenzenes in the presence of

A process for the manufacture of polycarboxylic acids is disclosed. In this novel process, antimony is used to improve the selectivity of cobalt-manganese-bromine or zirconium-cobalt-manganese-bromine oxidation system. Polymethylbenzenes such as pseudocumene are converted to their corresponding polycarboxylic acids which are used to manufacture plasticizers and polyamide-imide polymers used as molding compounds for replacement of metals.

Oxidation of polyalkylaromatics

An improved process for the manufacture of trimellitic acid from pseudocumene feedstock is disclosed. In this process, lead (IV) is used as a catalyst component in addition to the cobalt, manganese, and zirconium catalyst. The use of lead (IV) reduces higher boiling impurities and improves the yield. In our novel process, pseudocumene is converted to trimellitic acid which is used to manufacture plasticizers and polyamide-imide polymers used as molding compounds for replacement of metals.

Trimellitic acid process

A process for the purification of trimellitic anhydride is disclosed herein in which molten trimellitic anhydride is mixed with pseudocumene at a temperature of about 200.degree. F. to about 450.degree. F. and wherein the purified trimellitic anhydride is recovered by crystallization from the pseudocumene mother liquor. The recovered trimellitic anhydride is further washed and dried. Trimellitic anhydride is useful in the manufacture of amide imide resins and various polyester.

Trimellitic anhydride purification process

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Naperville, IL, United States of America

Wayne P Schammel