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BR9911683A - Process for the separation of catalyst in solution from a reaction mixture produced by the oxidation of cyclohexane to adipic acid - Google Patents

Process for the separation of catalyst in solution from a reaction mixture produced by the oxidation of cyclohexane to adipic acid

Info

Publication number
BR9911683A
BR9911683A BR9911683-9A BR9911683A BR9911683A BR 9911683 A BR9911683 A BR 9911683A BR 9911683 A BR9911683 A BR 9911683A BR 9911683 A BR9911683 A BR 9911683A
Authority
BR
Brazil
Prior art keywords
solvent
reaction mixture
catalyst
adipic acid
oxidation
Prior art date
Application number
BR9911683-9A
Other languages
Portuguese (pt)
Inventor
David C Decoster
Eustathios Vassiliou
Mark W Dassel
Ader M Rostami
Douglas J Dudgeon
Original Assignee
Rpc Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Rpc Inc filed Critical Rpc Inc
Priority claimed from PCT/US1999/015133 external-priority patent/WO2000001655A1/en
Publication of BR9911683A publication Critical patent/BR9911683A/en

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  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

"PROCESSO PARA A SEPARAçãO DE CATALISADOR EM SOLUçãO DE UMA MISTURA DE REAçãO PRODUZIDA PELA OXIDAçãO DE CICLOHEXANO EM áCIDO ADìPICO" Esta invenção se refere a processos de controle da oxidação de ciclohexano em ácido adípico, na presença de um solvente ácido monobásico, por separação do catalisador da mistura de reação, fora da zona de reação. Substancialmente todo o ciclohexano não reagido, a maior parte do ácido adípico e substancialmente todo o solvente ácido monobásico são, de preferência, removidos. Um solvente prótido pode ser adicionado intermitente ou continuamente na mistura de reação, durante a remoção do solvente ácido monobásico, de preferência por destilação, para evitar a precipitação de sólidos. Um solvente aprótico dipolar é, então, adicionado, na presença de uma quantidade adequada do solvente prótico, para manter uma fase líquida única, seguido por uma etapa de formação de duas fases líquidas, uma fase líquida prótica livre de sólidos, contendo substancialmente todo o catalisador, e uma fase líquida aprótica livre de sólidos, contendo pelo menos a maior parte dos ingredientes da mistura de reação. A formação das duas fases é efetuada por um processo selecionado no grupo que consiste em redução da primeira temperatura a uma segunda temperatura, adição de mais solvente prótico, adição de um solvente aprótico apolar e uma combinação dessas."PROCESS FOR THE SEPARATION OF CATALYST IN SOLUTION OF A REACTION MIXTURE PRODUCED BY THE OXIDATION OF CYCLEHEXAN IN ADIPIC ACID" This invention relates to processes for controlling the oxidation of cyclohexane in adipic acid, in the presence of a monobasic acid solvent, by separating it from the monobasic acid. catalyst of the reaction mixture, outside the reaction zone. Substantially all unreacted cyclohexane, most adipic acid and substantially all monobasic acid solvent are preferably removed. A protid solvent can be added intermittently or continuously to the reaction mixture, during the removal of the monobasic acid solvent, preferably by distillation, to prevent precipitation of solids. A dipolar aprotic solvent is then added, in the presence of an adequate amount of the protic solvent, to maintain a single liquid phase, followed by a two-liquid phase formation phase, a solid-free protic liquid phase, containing substantially all of the catalyst, and an aprotic liquid phase free of solids, containing at least most of the ingredients of the reaction mixture. The formation of the two phases is carried out by a process selected from the group that consists of reducing the first temperature to a second temperature, adding more protic solvent, adding an apolar aprotic solvent and a combination of these.

BR9911683-9A 1998-07-02 1999-07-02 Process for the separation of catalyst in solution from a reaction mixture produced by the oxidation of cyclohexane to adipic acid BR9911683A (en)

Applications Claiming Priority (5)

Application Number Priority Date Filing Date Title
US9148398P 1998-07-02 1998-07-02
US9325698P 1998-07-17 1998-07-17
US10504898P 1998-10-20 1998-10-20
US11020698P 1998-11-30 1998-11-30
PCT/US1999/015133 WO2000001655A1 (en) 1998-07-02 1999-07-02 Methods of separating catalyst in solution from a reaction mixture produced by oxidation of cyclohexane to adipic acid

Publications (1)

Publication Number Publication Date
BR9911683A true BR9911683A (en) 2001-03-20

Family

ID=27492484

Family Applications (2)

Application Number Title Priority Date Filing Date
BR9911676-6A BR9911676A (en) 1998-07-02 1999-07-02 Catalyst extraction processes from a reaction mixture in the oxidation of hexane cycle to adipic acid
BR9911683-9A BR9911683A (en) 1998-07-02 1999-07-02 Process for the separation of catalyst in solution from a reaction mixture produced by the oxidation of cyclohexane to adipic acid

Family Applications Before (1)

Application Number Title Priority Date Filing Date
BR9911676-6A BR9911676A (en) 1998-07-02 1999-07-02 Catalyst extraction processes from a reaction mixture in the oxidation of hexane cycle to adipic acid

Country Status (1)

Country Link
BR (2) BR9911676A (en)

Also Published As

Publication number Publication date
BR9911676A (en) 2001-03-20

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Legal Events

Date Code Title Description
FA10 Dismissal: dismissal - article 33 of industrial property law
B11Y Definitive dismissal - extension of time limit for request of examination expired [chapter 11.1.1 patent gazette]