CA2552158A1 - Catalyst for synthesis of 2- and 4-picolines, process for preparing 2- and 4-picoline and process for preparing the catalyst - Google Patents
Catalyst for synthesis of 2- and 4-picolines, process for preparing 2- and 4-picoline and process for preparing the catalyst Download PDFInfo
- Publication number
- CA2552158A1 CA2552158A1 CA002552158A CA2552158A CA2552158A1 CA 2552158 A1 CA2552158 A1 CA 2552158A1 CA 002552158 A CA002552158 A CA 002552158A CA 2552158 A CA2552158 A CA 2552158A CA 2552158 A1 CA2552158 A1 CA 2552158A1
- Authority
- CA
- Canada
- Prior art keywords
- acid
- catalyst
- range
- alumina
- group
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/02—Boron or aluminium; Oxides or hydroxides thereof
- B01J21/04—Alumina
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/06—Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof
- B01J21/08—Silica
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/12—Silica and alumina
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/16—Clays or other mineral silicates
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/002—Mixed oxides other than spinels, e.g. perovskite
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- B01J27/14—Phosphorus; Compounds thereof
- B01J27/186—Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J27/188—Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium with chromium, molybdenum, tungsten or polonium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- B01J27/14—Phosphorus; Compounds thereof
- B01J27/186—Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J27/195—Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium with vanadium, niobium or tantalum
- B01J27/198—Vanadium
- B01J27/199—Vanadium with chromium, molybdenum, tungsten or polonium
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D213/00—Heterocyclic compounds containing six-membered rings, not condensed with other rings, with one nitrogen atom as the only ring hetero atom and three or more double bonds between ring members or between ring members and non-ring members
- C07D213/02—Heterocyclic compounds containing six-membered rings, not condensed with other rings, with one nitrogen atom as the only ring hetero atom and three or more double bonds between ring members or between ring members and non-ring members having three double bonds between ring members or between ring members and non-ring members
- C07D213/04—Heterocyclic compounds containing six-membered rings, not condensed with other rings, with one nitrogen atom as the only ring hetero atom and three or more double bonds between ring members or between ring members and non-ring members having three double bonds between ring members or between ring members and non-ring members having no bond between the ring nitrogen atom and a non-ring member or having only hydrogen or carbon atoms directly attached to the ring nitrogen atom
- C07D213/06—Heterocyclic compounds containing six-membered rings, not condensed with other rings, with one nitrogen atom as the only ring hetero atom and three or more double bonds between ring members or between ring members and non-ring members having three double bonds between ring members or between ring members and non-ring members having no bond between the ring nitrogen atom and a non-ring member or having only hydrogen or carbon atoms directly attached to the ring nitrogen atom containing only hydrogen and carbon atoms in addition to the ring nitrogen atom
- C07D213/08—Preparation by ring-closure
- C07D213/09—Preparation by ring-closure involving the use of ammonia, amines, amine salts, or nitriles
- C07D213/10—Preparation by ring-closure involving the use of ammonia, amines, amine salts, or nitriles from acetaldehyde or cyclic polymers thereof
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2523/00—Constitutive chemical elements of heterogeneous catalysts
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Dispersion Chemistry (AREA)
- Pyridine Compounds (AREA)
- Catalysts (AREA)
Abstract
The present invention provides a catalyst comprising a composite of a heteropolyacid impregnated on a support for the synthesis of 2- and 4-picolines and a process for the preparation thereof and use thereof for the synthesis of 2- and 4-picolines.
Claims (17)
1. A catalyst useful for synthesis of 2- and 4- Picolines which comprises a heteropoly acid selected from the group consisting of silicotungstic acid, phosphotungstic acid, phosphomolybdic acid and vanadotungstic acid provided on a support.
2. A catalyst as claimed in claim 1 wherein the support is selected from the group consisting of silica gel, alumina, silica-alumina, clays and montmorillonite.
3. A process for the preparation of a catalyst useful for the synthesis of 2-and 4-picolines, the process comprising dissolving a heteropoly acid in distilled water; mixing the resulting mixture with desired amount of a binder to obtain a slurry; stirring the slurry till uniform impregnation is achieved; drying the slurry in air at 200-250°C
for a time period in the range of 0.5 to 1.5 hours; further heating the slurry at a temperature in the range of 300 to 400°C for time period in the range of 0.5 to 1.5 hours and cooling the resultant product to room temperature in a desiccator to get the desired catalyst.
for a time period in the range of 0.5 to 1.5 hours; further heating the slurry at a temperature in the range of 300 to 400°C for time period in the range of 0.5 to 1.5 hours and cooling the resultant product to room temperature in a desiccator to get the desired catalyst.
4. A process as claimed in claim 3 wherein the heteropolyacid is selected from the group consisting of silicotungstic acid, phosphotungstic acid, phosphomolybdic acid and vanadotungstic acid.
5. A process as claimed in claim 3 wherein the binder is selected from the group consisting of silica, alumina, silica-alumina, clays and montmorillonite.
6. A process as claimed in claim 3 wherein the heteropoly acid is dissolved in distilled water in a ratio of 0.5:4.5 (w/w).
7. A process as claimed in claim 3 wherein the binder comprises silica gel of mesh size 6-14.
8. A process as claimed in claim 3 wherein the slurry is stirred for a time period in the range of 30-40 minutes.
9. A process for the preparation of 2- and 4- picolines which comprises reacting acetaldehyde and ammonia under heat in the presence of a catalyst comprising a composite of a heteropolyacid impregnated on a support, the catalyst being present in an amount in the range of 5 to 15 wt %, and separating the 2- and 4- picoline formed.
10. A process as claimed in claim 9 wherein the acetaldehyde and ammonia are taken in a ratio of 0.8 to 1.2 (w/w) and are reacted at a temperature in the range of 300 to 500°C.
11. A process as claimed in claim 9 wherein the reaction is carried out in a glass reactor.
12. A process as claimed in claim 9 wherein weight hourly space velocity of the acetaldehyde and ammonia is maintained in the range of 0.1 to 10 g/g of catalyst.
13. A process as claimed in claim 12 wherein the weight hourly space velocity of the acetaldehyde and ammonia is maintained in the range of 1 to 3 g/g of the catalyst.
14. A process as claimed in claim 9 wherein the the 2- and 4-picolines are separated by fractional distillation.
15. A process as claimed in claim 9 wherein the heteropolyacid is selected from the group consisting of silicotungstic acid, phosphotungstic acid, phosphomolybdic acid and vanadotungstic acid.
16. A process as claimed in claim 9 wherein the binder is selected from the group consisting of silica, alumina, silica-alumina, clays and montmorillonite.
17. A process as claimed in claim 9 wherein the binder comprises silica gel of mesh size 6-14.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/IN2003/000467 WO2005063389A1 (en) | 2003-12-31 | 2003-12-31 | Catalyst for synthesis of 2-and 4-picolines, process for preparing 2- and 4-picoline and process for preparing the catalyst |
Publications (2)
Publication Number | Publication Date |
---|---|
CA2552158A1 true CA2552158A1 (en) | 2005-07-14 |
CA2552158C CA2552158C (en) | 2010-06-22 |
Family
ID=34717583
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA2552158A Expired - Fee Related CA2552158C (en) | 2003-12-31 | 2003-12-31 | Catalyst for synthesis of 2- and 4-picolines, process for preparing 2- and 4-picoline and process for preparing the catalyst |
Country Status (5)
Country | Link |
---|---|
EP (1) | EP1708811A1 (en) |
CN (1) | CN100448534C (en) |
AU (1) | AU2003300723B2 (en) |
CA (1) | CA2552158C (en) |
WO (1) | WO2005063389A1 (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100446857C (en) * | 2006-11-02 | 2008-12-31 | 武汉理工大学 | Method for preparing heteropoly acid/ordered mesic porous silicon oxide catalyst, and its application |
CN107983398B (en) * | 2017-10-27 | 2020-07-17 | 苏州盖德精细材料有限公司 | Production method of nano-attapulgite composite catalyst for preparing 3-methylpyridine |
CN110586187B (en) * | 2019-10-11 | 2022-05-13 | 沧州那瑞化学科技有限公司 | Supported phosphotungstic acid catalyst, and preparation method and application thereof |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2463466A (en) * | 1948-09-29 | 1949-03-01 | Socony Vacuum Oil Co Inc | Production of nitriles |
CA1333793C (en) * | 1988-09-30 | 1995-01-03 | Gerald L. Goe | Pyridine base synthesis process and catalyst for same |
GB9419387D0 (en) * | 1994-09-26 | 1994-11-09 | Bp Chem Int Ltd | Olefin hydration process |
CN1093000C (en) * | 1996-12-27 | 2002-10-23 | 吉林化学工业公司研究院 | Catalyst for ether pyrolysis isobutylene and applications |
US5856575A (en) * | 1997-01-22 | 1999-01-05 | Council Of Scientific Industrial Research | Process for the preparation of N-acetyl aminophenols |
US5994550A (en) * | 1998-12-30 | 1999-11-30 | Mobil Oil Corporation | Pyridine/picoline production process |
-
2003
- 2003-12-31 CN CNB2003801109444A patent/CN100448534C/en not_active Expired - Fee Related
- 2003-12-31 EP EP03819218A patent/EP1708811A1/en not_active Withdrawn
- 2003-12-31 WO PCT/IN2003/000467 patent/WO2005063389A1/en active Application Filing
- 2003-12-31 CA CA2552158A patent/CA2552158C/en not_active Expired - Fee Related
- 2003-12-31 AU AU2003300723A patent/AU2003300723B2/en not_active Ceased
Also Published As
Publication number | Publication date |
---|---|
EP1708811A1 (en) | 2006-10-11 |
AU2003300723A1 (en) | 2005-07-21 |
CN100448534C (en) | 2009-01-07 |
WO2005063389A1 (en) | 2005-07-14 |
AU2003300723B2 (en) | 2010-01-14 |
CA2552158C (en) | 2010-06-22 |
CN1886195A (en) | 2006-12-27 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
EEER | Examination request | ||
MKLA | Lapsed |
Effective date: 20181231 |