US4169853A
Expired / Lapsed
US
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Homogeneous ruthenium catalysts useful in the reduction of ortho-substituted nitroaromatics to amines
Assignee: Huntsman Corp
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Filing: 1978-02-06
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Granted: 1979-10-02
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Expires: 1998-02-06
Abstract
Abstract This invention concerns the use of solubilized ruthenium-containing complexes in combination with quaternary ammonium hydroxides to effect the catalytic hydrogenation of certain classes of ortho-substituted mononitroaromatic substrates to their corresponding aryl amines.
Inventors
- 👤 John F. Knifton
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 19:28
CPC Classifications
C; C07; C07C; C07C209/00; C07C209/30; C07C209/32; C07C209/36; B; B01; B01J; B01J31/00; B01J31/02; B01J31/0234; B01J31/0235; B01J31/0239; B01J31/04; B01J31/16; B01J31/18; B01J31/1895; B01J31/20; B01J31/22; B01J31/2204; B01J31/2208; B01J31/2226; B01J31/223; B01J31/2234; B01J31/24; B01J31/2404; B01J2231/00; B01J2231/60; B01J2231/64; B01J2231/641; B01J2531/00; B01J2531/80; B01J2531/82; B01J2531/821
Claims Analysis
Total Claims: 4
Claim 1
Independent Claim
263 words
A process for selectively hydrogenating the nitro groups of mononitroaromatic substrates wherein said nitroaromatics contain one or more ortho-substituents selected from the group consisting of alkyl, halogenated alkyl, alkoxyl, acetyl, halo, substituted amino and amino substituents, and mixtures thereof, to the corresponding amines, utilizing a homogeneous ruthenium-containing catalyst complex selected from the group consisting of RuCl 2 [P(C 6 H 5 ) 3 ] 3 , [RuCl 2 (CO) 3 ] 2 , RuCl 2 [As(C 6 H 5 ) 3 ] 3 RuHCl[P(C 6 H 5 ) 3 ] 3 , Ru(CH 3 COCHCOCH 3 ) 3 , RuCl 3 .XH 2 O, RuCl 3 NO[P-(C 6 H 5 ) 3 ] 2 , RuCl 2 (CO) 2 [P(C 6 H 5 ) 3 ] 2 and Ru(CH 3 COO) 3 in combination with a quaternary ammonium hydroxide selected from the group consisting of tetramethylammonium hydroxide, tetraethylammonium hydroxide, benzyltrimethylammonium hydroxide, trimethyloctylammonium hydroxide and dimethyldioctylammonium hydroxide, by the process consisting essentially of, a. admixing each mole of said nitroaromatic substrates to be reduced with at least a catalytic amount of one or more of said ruthenium-containing catalyst complexes in an oxidizer-free, non-aqueous solvent media to form a reaction mixture, b. introducing into said reaction mixture an excess of quaternary ammonium hydroxide and at least sufficient hydrogen gas to hydrogenate the nitro groups of said substrates to the corresponding amines, at superatmospheric pressures ranging from about 100 psi to about 2000 psi, and c. heating said pressurized reaction mixture between about 20° to about 160° C. until said nitroaromatic substrates are reduced to amines.
Claim 2
Dependent Claim
263 words
A process for selectively hydrogenating the nitro groups of mononitroaromatic substrates wherein said nitroaromatics contain one or more ortho-substituents selected from the group consisting of alkyl, halogenated alkyl, alkoxyl, acetyl, halo, substituted amino and amino substituents, and mixtures thereof, to the corresponding amines, utilizing a homogeneous ruthenium-containing catalyst complex selected from the group consisting of RuCl 2 [P(C 6 H 5 ) 3 ] 3 , [RuCl 2 (CO) 3 ] 2 , RuCl 2 [As(C 6 H 5 ) 3 ] 3 RuHCl[P(C 6 H 5 ) 3 ] 3 , Ru(CH 3 COCHCOCH 3 ) 3 , RuCl 3 .XH 2 O, RuCl 3 NO[P-(C 6 H 5 ) 3 ] 2 , RuCl 2 (CO) 2 [P(C 6 H 5 ) 3 ] 2 and Ru(CH 3 COO) 3 in combination with a quaternary ammonium hydroxide selected from the group consisting of tetramethylammonium hydroxide, tetraethylammonium hydroxide, benzyltrimethylammonium hydroxide, trimethyloctylammonium hydroxide and dimethyldioctylammonium hydroxide, by the process consisting essentially of, a. admixing each mole of said nitroaromatic substrates to be reduced with at least a catalytic amount of one or more of said ruthenium-containing catalyst complexes in an oxidizer-free, non-aqueous solvent media to form a reaction mixture, b. introducing into said reaction mixture an excess of quaternary ammonium hydroxide and at least sufficient hydrogen gas to hydrogenate the nitro groups of said substrates to the corresponding amines, at superatmospheric pressures ranging from about 100 psi to about 2000 psi, and c. heating said pressurized reaction mixture between about 20° to about 160° C. until said nitroaromatic substrates are reduced to amines.
Claim 3
Dependent Claim
27 words
The process of claim 1 in which said solvent medium is selected from the group consisting of aromatics, alkanols, alkyl ethers, chlorinated aliphatic hydrocarbons and mixtures thereof.
Claim 4
Dependent Claim
27 words
The process of claim 1 wherein the nitroaromatic substrate is selected from the group consisting of o-nitroaniline, N-methyl-o-nitroaniline, N,N-dimethyl-o-nitroaniline, 2-nitro-m-phenylenediamine, 4-nitro-m-phenylenediamine, 2-nitro-p-phenylenediamine, α,α,α-trifluoro-o-nitrotoluene, 1-chloro-2-nitrobenzene, o-nitroanisole and o-nitroacetophenone.
References Cited (Backward Citations)
US3832401A
Cited
US3906045A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1982-10-01 | 1983-04-02 | 1983-10-02 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1986-10-01 | 1987-04-02 | 1987-10-02 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1990-10-01 | 1991-04-02 | 1991-10-02 | $7700.00 | Window Closed / Lapsed |