Claims
- 1. In the catalytic amination of ethylene glycol or 1,3 propanediol with a secondary amine, the method for selectively favoring the formation of mono-aminated products which comprises:
- effecting said amination at a temperature in the range of 100.degree. to 125.degree. C. in the presence of a catalyst consisting of a compound or complex of ruthenium in chemical combination or in admixture with an organic phosphine modifier selected from the group consisting of PPh.sub.3, P(p-C.sub.6 H.sub.4 F).sub.3, P(Ph)Me.sub.2, P(p-tol).sub.3 and mixtures thereof, in an amount to provide at least one mole of organic phosphine per gram atom of ruthenium.
- 2. The method in accordance with claim 1 wherein said catalyst is at least partially dissolved in a liquid reaction medium.
- 3. The method in accordance with claim 1 wherein said catalyst is selected from the group consisting of:
- (1) RuCl.sub.2 (PPh.sub.3).sub.3, RuHCl(PPh.sub.3).sub.3 ; and
- (2) the following compounds in admixture with PPh.sub.3 : Ru(NH.sub.3).sub.6 Cl.sub.3, K.sub.2 (RuCl.sub.5).sub.2 O, Ru(NO)Cl.sub.3, K.sub.2 RuCl.sub.5, K.sub.2 RuCl.sub.6, Ru((NH.sub.3).sub.6 Cl.sub.2 and K.sub.2 RuO.sub.4.
- 4. The method in accordance with claim 1 wherein said catalyst is a compound selected from the group consisting of:
- Ru(NH.sub.3).sub.6 Cl.sub.3, K.sub.2 (RuCl.sub.5).sub.2 O, Ru(NO)Cl.sub.3, K.sub.2 RuCl.sub.5, K.sub.2 RuCl.sub.6, and Ru(NH.sub.3).sub.6 Cl.sub.2, each admixed with about 3 moles of triphenylphosphine per gram atom of ruthenium.
- 5. The method as defined in claim 1 wherein said amination is effected at a temperature in the range of 120.degree. to 125.degree. C.
- 6. The method as defined in claim 1 wherein said amination is effected in the absence of added hydrogen and at autogeneous pressure.
- 7. The method as defined in claim 1 wherein said secondary amine is selected from the group consisting of: morpholine, dimethylamine, diethylamine, di-isopropylamine, N,N,N'-trimethylethylene diamine and pyrrolidine.
- 8. The method as defined in claim 1 wherein said amination is carried out in the liquid phase.
- 9. The method as defined in claim 1 wherein said amination is carried out with the secondary amine dissolved in the diol at an amine concentration of about 1.8 molar and at a dissolved catalyst concentration of about one-hundredth that of the amine.
- 10. In the catalytic amination of ethylene glycol or 1,3 propanediol with a secondary amine, the method for selectively favoring the formation of di-aminated products which comprises: effecting said amination at a temperature in the range of 100.degree. to 125.degree. C. in the pressure of a catalyst selected from the group consisting of (1) a ruthenium compound or complex in the absence of an organic phosphine modifier, (2)a ruthenium compound or complex in admixture or chemical combination with an organic phosphine modifier selected from the group consisting of PPh(C.sub.6 F.sub.5).sub.2, P(o-C.sub.6 H.sub.4 NMe.sub.2), P(o-tol).sub.3 and mixtures thereof, and (3) an iridium compound or complex free of modifier or in chemical combination or admixture with an organic phosphine modifier; said catalyst modifier being present in an amount sufficient to provide at least one mole or organic phosphine per gram atom of ruthenium.
- 11. The method in accordance with claim 10 wherein said catalyst is at least partially dissolved in a liquid reaction medium.
- 12. The method in accordance with claim 10 wherein said catalyst is selected from the group consisting of phosphine free RuCl.sub.3.xH.sub.2 O and IrCl.sub.3.xH.sub.2 O.
- 13. The method in accordance with claim 10 wherein said catalyst is IrCl.sub.3.xH.sub.2 O in chemical combination or in admixture with triphenyl phosphine.
- 14. The method in accordance with claim 10 wherein said amination is effected at a temperature in the range of 120.degree. to 125.degree. C.
- 15. The method in accordance with claim 10 wherein said amination is effected in the absence of added hydrogen and at autogenous pressure.
- 16. The method as defined in claim 10 wherein said secondary amine is selected from the group consisting of: morpholine, dimethylamine, diethylamine, di-isopropylamine, N,N,N'-trimethylethylene diamine and pyrrolidine.
- 17. The method as defined in claim 10 wherein said amination is carried out in the liquid phase.
- 18. The method as defined in claim 10 wherein said amination is carried out with the secondary amine dissolved in the diol at an amine concentration of about 1.8 molar and at a dissolved catalyst concentration of about one-hundredth that of the amine.
- 19. In the catalytic amination of an alkanediol selected from the group consisting of ethylene glycol and 1,3 propanediol, with a secondary amine, the method of selectively controlling the relative extent of
- (A) mono-amination and (B) di-amination of said diol which comprises: effecting said amination at a temperature in the range of 100.degree. to 125.degree. C. in the presence of a catalyst comprising a ruthenium or iridium complex at least partially dissolved in liquid reaction medium, wherein said catalyst is provided by the introduction of (a) a compound or complex of ruthenium in chemical combination or admixture with an organic phosphine catalyst modifier selected from the group consisting of PPh.sub.3, P(p-C.sub.6 H.sub.4 F).sub.3, P(Ph)Me.sub.2, P(p-tol).sub.3 and mixtures thereof, in an amount to provide at least one mole of organic phosphine per gram atom of ruthenium to selectively favor mono-amination; or as (b) a catalyst selected from the group consisting (1) a ruthenium compound or complex in the absence of an organic phosphine modifier, (2) an iridium compound or complex free of modifier or in admixture or chemical combination with an organic phosphine modifier, and (3) a ruthenium compound in admixture or chemical combination with an organic phosphine catalyst modifier selected from the group consisting of PPh(C.sub.6 F.sub.5).sub.2, P(o-C.sub.6 H.sub.4 MNe.sub.2).sub.3, P(o-tol).sub.3 and mixtures thereof, to selectively favor di-amination.
CROSS REFERENCE TO PARENT APPLICATION
This is a continuation-in-part of U.S. patent application Ser. No. 634,503, filed July 25, 1984, now abandoned, the subject matter which is hereby incorporated by reference.
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3270059 |
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3708539 |
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Number |
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0034480 |
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EPX |
Non-Patent Literature Citations (3)
Entry |
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Continuation in Parts (1)
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Number |
Date |
Country |
Parent |
634503 |
Jul 1984 |
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