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US4042620A Expired / Lapsed US ⏱️ 0.0 years remaining

Continuous process for the production of maeamic acids

Assignee: Rhone Poulenc SA
•
Filing: 1975-04-24
•
Granted: 1977-08-16
•
Expires: 1995-04-24
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Abstract

Abstract A continuous process is provided for the preparation of a maleamic acid of the formula: ##STR1## in which: R represents a linear or branched alkylene, arylene, aralkylene, alkylarylene or cycloalkylene radical or a divalent heterocyclic radical, the free valencies of which are attached to carbon atoms, the radical containing 2 to 20 carbon atoms and X represents either a hydrogen atom or the radical: ##STR2## which comprises passing a solution of a primary monoamine or diamine and a solution of maleic anhydride in amounts such that there is a 5 to 20 mol % excess of anhydride, at a temperature of from 40° to 130° C and at a rate greater than 7 m/second through an injection nozzle into a twin screw reactor, the solvent for the primary amine being the same as, or compatible with, the solvent for the maleic anhydride. This process eliminates clogging problems.

Inventors

  • 👤 Jean Laforest
  • 👤 Louis Silhol
  • 👤 Pierre Renard

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-05 20:51
CPC Classifications
C; C07; C07C; C07C231/00; C07C231/02; C07C51/00; C07C237/00; C07C237/02; C07C237/04; C07C237/12; C07C57/00; C07C57/02; C07C57/13; C07C57/145

Claims Analysis

Total Claims: 8
Claim 1
Independent Claim 102 words
A continuous process for the preparation of a maleamic acid of the formula: ##STR5## in which R represents the radical ##STR6## and X represents the radical: ##STR7## which comprises passing a solution of a primary diamine and a solution of maleic anhydride in amounts such that there is a 5 to 20 mol % excess of anhydride, at a temperature of from 40° to 130° C. and at a rate greater than 7 m/second through an injection nozzle into a twin screw reactor, the solvent for the primary amine being the same as, or miscible with, the solvent for the maleic anhydride.
Claim 2
Dependent Claim 102 words
A continuous process for the preparation of a maleamic acid of the formula: ##STR5## in which R represents the radical ##STR6## and X represents the radical: ##STR7## which comprises passing a solution of a primary diamine and a solution of maleic anhydride in amounts such that there is a 5 to 20 mol % excess of anhydride, at a temperature of from 40° to 130° C. and at a rate greater than 7 m/second through an injection nozzle into a twin screw reactor, the solvent for the primary amine being the same as, or miscible with, the solvent for the maleic anhydride.
Claim 3
Dependent Claim 30 words
A process according to claim 1 in which the solvent or one of the solvents is a hydrocarbon or chlorinated hydrocarbon, a cyclic or acyclic ether or a dialkyl ketone.
Claim 4
Dependent Claim 20 words
A process according to claim 2 in which the solvent for the primary amine and for maleic anhydride is acetone.
Claim 5
Dependent Claim 22 words
A process according to claim 1 in which the concentration of the maleic anhydride solution is from 20 to 70% by weight.
Claim 6
Dependent Claim 19 words
A process according to claim 1 in which the twin screws have a length/diameter ratio from 5/1 to 10/1.
Claim 7
Dependent Claim 17 words
A process according to claim 1 in which the reactor is provided with a water-cooled double jacket.
Claim 8
Dependent Claim 20 words
A process according to claim 1 in which the mixture issuing from the reactor is passed to a static mixer.

References Cited (Backward Citations)

US2459964A Cited
US2723991A Cited
US2793231A Cited
US3947493A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-08-15 1981-02-14 1981-08-16 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-08-15 1985-02-14 1985-08-16 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-08-15 1989-02-14 1989-08-16 $7700.00 Window Closed / Lapsed

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