US4051140A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Preparation of pyridines and nicotinonitrile from piperidines
Assignee: Lummus Technology LLC
•
Filing: 1976-07-01
•
Granted: 1977-09-27
•
Expires: 1996-07-01
Abstract
Abstract A piperidine, such as methyl piperidine is converted to the corresponding pyridine by the use of a supported vanadia catalyst. Nicotinonitrile can be produced by conversion of 3-methyl piperidine to 3-methyl pyridine with a supported vanadia catalyst, followed by ammonolysis to nicotinonitrile by the use of a supported vanadia catalyst.
Inventors
- 👤 Abraham P. Gelbein
- 👤 Paul Janssen, deceased
- 👤 Hermann Richtzenhain
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-06 12:39
CPC Classifications
C; C07; C07D; C07D213/00; C07D213/02; C07D213/04; C07D213/06; B; B01; B01J; B01J23/00; B01J23/16; B01J23/20; B01J23/22; C07D213/60; C07D213/78; C07D213/84; Y; Y02; Y02P; Y02P20/00; Y02P20/50; Y02P20/582
Claims Analysis
Total Claims: 13
Claim 1
Independent Claim
216 words
A process for producing nicotinonitrile, comprising: a. converting in a first reaction zone a member selected from the group consisting of 3-alkyl piperidines, 2,3-dialkyl piperidines, and 2,5-dialkyl piperidines to the corresponding pyridine by contacting said member with supported vanadia as a catalyst, at a temperature of from 500° F to 1000° F, said supported vanadia containing from about 25 to about 75 percent, by weight, of the vanadia, said vanadia having been placed in molten form substantially entirely within the pores of the support, the support having a surface area greater than about 50 m 2 /gm and a porosity greater than about 0.4 cc/gm, said support being selected from the group consisting of gamma-alumina and silica-alumina; and b. contacting said corresponding pyridine in a second reaction zone with ammonia at a temperature of from 575° F to 930° F in the presence of oxidized vanadia supported on a porous support to produce nicotinonitrile, said support containing from about 25 to about 75 percent, by weight, of the vanadia having been placed in molten form substantially entirely within the pores of the support, the support having a surface area greater than about 50 m 2 /gm and a porosity greater than about 0.4 cc/gm, said support being selected from the group consisting of gamma-alumina and silica-alumina.
Claim 2
Dependent Claim
216 words
A process for producing nicotinonitrile, comprising: a. converting in a first reaction zone a member selected from the group consisting of 3-alkyl piperidines, 2,3-dialkyl piperidines, and 2,5-dialkyl piperidines to the corresponding pyridine by contacting said member with supported vanadia as a catalyst, at a temperature of from 500° F to 1000° F, said supported vanadia containing from about 25 to about 75 percent, by weight, of the vanadia, said vanadia having been placed in molten form substantially entirely within the pores of the support, the support having a surface area greater than about 50 m 2 /gm and a porosity greater than about 0.4 cc/gm, said support being selected from the group consisting of gamma-alumina and silica-alumina; and b. contacting said corresponding pyridine in a second reaction zone with ammonia at a temperature of from 575° F to 930° F in the presence of oxidized vanadia supported on a porous support to produce nicotinonitrile, said support containing from about 25 to about 75 percent, by weight, of the vanadia having been placed in molten form substantially entirely within the pores of the support, the support having a surface area greater than about 50 m 2 /gm and a porosity greater than about 0.4 cc/gm, said support being selected from the group consisting of gamma-alumina and silica-alumina.
Claim 3
Dependent Claim
108 words
A process for converting an alkyl piperidine to the corresponding alkyl pyridine, comprising: contacting the alkyl piperidine with supported vanadia at a temperature of from 500° F to 1000° F to effect conversion thereof to the corresponding alkyl pyridine, said supported vanadia containing of from about 25 to about 75 percent, by weight, of the vanadia, said vanadia having been placed in molten form substantially entirely within the pores of the support, the support having a surface area greater than about 50 meters square per gm. and a porosity greater than about 0.4 cc per gm., said support being selected from the group consisting of gamma-alumina and silica-alumina.
Claim 4
Dependent Claim
108 words
A process for converting an alkyl piperidine to the corresponding alkyl pyridine, comprising: contacting the alkyl piperidine with supported vanadia at a temperature of from 500° F to 1000° F to effect conversion thereof to the corresponding alkyl pyridine, said supported vanadia containing of from about 25 to about 75 percent, by weight, of the vanadia, said vanadia having been placed in molten form substantially entirely within the pores of the support, the support having a surface area greater than about 50 meters square per gm. and a porosity greater than about 0.4 cc per gm., said support being selected from the group consisting of gamma-alumina and silica-alumina.
Claim 5
Dependent Claim
16 words
The process of claim 2 wherein the conversion is effected in the absence of molecular oxygen.
Claim 6
Dependent Claim
15 words
The process of claim 3 wherein the supported vanadia catalyst is maintained in fluidized form.
Claim 7
Dependent Claim
24 words
The process of claim 4 wherein the alkyl substituted piperidine is selected from the group consisting of 3-alkyl piperidines, 2,3-dialkyl piperidines and 2,5-dialkyl piperidines.
Claim 8
Dependent Claim
18 words
The process of claim 4 wherein the piperidine is 3-methyl piperidine and the corresponding pyridine is 3-methyl pyridine.
Claim 9
Dependent Claim
17 words
The process of claim 4 wherein the catalyst is periodically regenerated by direct contact with molecular oxygen.
Claim 10
Dependent Claim
41 words
The process of claim 2 wherein supported vanadia from step (b) is passed to step (a) and supported vanadia is contacted with molecular oxygen to effect regeneration thereof subsequent to step (a) and regenerated supported vanadia is passed to step (b).
Claim 11
Dependent Claim
14 words
The process of claim 8 wherein said member in step (a) is 3-methyl piperidine.
Claim 12
Dependent Claim
21 words
The process of claim 8 wherein the contacting of steps (a) and (b) are effected in the absence of molecular oxygen.
Claim 13
Dependent Claim
32 words
The process of claim 10 wherein an effluent containing the corresponding alkyl pyridine is withdrawn from the first reaction zone and is introduced into the second reaction zone without separation of components.
References Cited (Backward Citations)
US3555021A
Cited
US3925447A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1980-09-26 | 1981-03-28 | 1981-09-27 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-09-26 | 1985-03-28 | 1985-09-27 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-09-26 | 1989-03-28 | 1989-09-27 | $7700.00 | Window Closed / Lapsed |