Method of producing dinitrile compounds
View Patent ↗The present invention relates to a process for the manufacture of compounds comprising two nitrile functional groups. It relates more particularly to a process for the manufacture of dinitrile compounds from compounds comprising a nitrile functional group and an ethylenic unsaturation in the presence of a catalytic system comprising an organometallic complex and a cocatalyst of the Lewis acid type. The process of the invention comprises a stage of treatment of the reaction medium resulting from the hydrocyanation which makes it possible to extract and recover the metal element of the Lewis acid.
1. A process for the manufacture of dinitrile compounds by hydrocyanation of mononitrile compounds comprising an ethylenic unsaturation by reaction with hydrogen cyanide in the presence of a catalytic system comprising an organometallic complex and a cocatalyst comprising metal ions, said process comprising the following successive steps:
I) separating the organometallic complex from a liquid reaction medium E 1 obtained after hydrocyanation of unsaturated nitrile compounds and obtaining a second liquid medium E 2 comprising dinitriles and metal ions originating from the cocatalyst,
II) extracting from the second liquid medium E 2 metal ions originating from the cocatalyst with an ion-exchange resin and obtaining a third medium E 3 comprising dinitriles, and
III) separating the dinitriles from the third medium E 3 .
2. The process according to claim 1 , wherein the cocatalyst is a Lewis acid.
3. The process according to claim 1 , wherein the metal ions extracted in step II) are recovered by elution from the resin.
4. The process according to claim 3 , wherein the metal ions recovered are recycled in order to form the cocatalyst of the catalytic system of the hydrocyanation stage.
5. The process according to claim 2 , wherein the Lewis acid is a compound of a metal element belonging to Group Ib, IIb, IIIa, IIIb, IVa, IVb, Va, Vb, VIb, VIIb or VIII of the Periodic Table of the Elements.
6. The process according to claim 2 , wherein the Lewis acid is selected from the group consisting of halides, sulphates, sulphonates, haloalkylsulphonates, perhaloalkylsulphonates, haloacetates, perhaloacetates, carboxylates and phosphates of the metal elements.
7. The process according to claim 6 , wherein the Lewis acid is selected from the group consisting of chlorides, bromides, fluoroalkylsulphonates and perfluoroalkylsulphonates.
8. The process according to claim 2 , wherein the Lewis acid is zinc chloride, zinc bromide, zinc iodide, manganese chloride, manganese bromide, cadmium chloride, cadmium bromide, stannous chloride, stannous bromide, stannous sulphate, stannous tartrate, indium chloride, indium trifluoromethylsulphonate, indium trifluoroacetate, cobalt chloride, ferrous chloride or yttrium chloride.
9. The process according to claim 2 , wherein the Lewis acid is a chloride or a bromide of a rare earth element selected from the group consisting of lanthanum, cerium, praseodymium, neodymium, samarium, europium, gadolinium, terbium, dysprosium, hafnium, erbium, thallium, ytterbium and lutetium.
10. The process according to claim 1 , wherein the resin for extraction of the metal ions used in step II) is a weak cationic resin, a strong cationic resin, an adsorbent resin, a chelating resin or a catalytic resin.
11. The process according to claim 10 , wherein the ion-exchange resin is a sulphonic resin, carboxylic resin or iminodiacetic resin.
12. The process according to claim 1 , wherein the separation of the organometallic complex in step I) is carried out by liquid/liquid extraction with an extraction solvent chosen from the group consisting of alkanes comprising from 5 to 9 carbon atoms, cycloalkanes comprising from 5 to 8 carbon atoms, halogenated hydrocarbons comprising from 1 to 5 carbon atoms, substituted aromatic compounds comprising from 6 to 9 carbon atoms and or unsubstituted aromatic compounds comprising from 6 to 9 carbon atoms.
13. The process according to claim 1 , wherein the separation of the dinitriles in step III) is carried out by distillation of said dinitriles.
14. The process according to claim 1 , wherein said process is for the manufacture of adiponitrile, and wherein the unsaturated mononitrile compounds are pentenenitriles.
15. The process according to claim 14 , wherein the pentenenitriles are obtained by hydrocyanation of butadiene.
16. The process according to claim 1 , wherein said organometallic complex is an organometallic phosphite complex.
17. The process according to claim 1 , wherein said extraction step II) is carried out at ambient temperature.
18. A process for the manufacture of dinitrile compounds by hydrocyanation of mononitrile compounds comprising an ethylenic unsaturation by reaction with hydrogen cyanide in the presence of a catalytic system comprising an organometallic complex and a cocatalyst comprising metal ions, said process comprising the following successive steps:
I) separating the organometallic complex from a liquid reaction medium E 1 obtained after hydrocyanation of unsaturated nitrile compounds and obtaining a second liquid medium E 2 comprising dinitriles and metal ions originating from the cocatalyst,
IIa) separating the dinitriles by distillation from the second liquid medium E 2 , wherein the distillation bottoms comprise said metal ions originating from the cocatalyst, and
III a) extracting from the distillation bottoms of step IIa) metal ions originating from the cocatalyst with an ion-exchange resin.
19. The process according to claim 18 , wherein the metal ions extracted in step IIIa) are recovered by elution from the resin.
20. The process according to claim 18 , wherein said extraction step IIIa) is carried out at ambient temperature, and wherein said organometallic complex is an organometallic phosphite complex.