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DE1695982A1 - Process for the preparation of piperidine and its alkyl homologues by catalytic hydrogenation of pyridine and its alkyl homologues - Google Patents

Process for the preparation of piperidine and its alkyl homologues by catalytic hydrogenation of pyridine and its alkyl homologues

Info

Publication number
DE1695982A1
DE1695982A1 DE19671695982 DE1695982A DE1695982A1 DE 1695982 A1 DE1695982 A1 DE 1695982A1 DE 19671695982 DE19671695982 DE 19671695982 DE 1695982 A DE1695982 A DE 1695982A DE 1695982 A1 DE1695982 A1 DE 1695982A1
Authority
DE
Germany
Prior art keywords
pyridine
alkyl homologues
piperidine
catalytic hydrogenation
preparation
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.)
Pending
Application number
DE19671695982
Other languages
German (de)
Inventor
Hans Dr Baltz
Ludwig Dipl-Chem Bruesehaber
Smeykal Karl Dr Dr
Karl-Klaus Dr Moll
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Leuna Werke GmbH
Original Assignee
Leuna Werke GmbH
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Leuna Werke GmbH filed Critical Leuna Werke GmbH
Publication of DE1695982A1 publication Critical patent/DE1695982A1/en
Pending legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D295/00Heterocyclic compounds containing polymethylene-imine rings with at least five ring members, 3-azabicyclo [3.2.2] nonane, piperazine, morpholine or thiomorpholine rings, having only hydrogen atoms directly attached to the ring carbon atoms
    • C07D295/02Heterocyclic compounds containing polymethylene-imine rings with at least five ring members, 3-azabicyclo [3.2.2] nonane, piperazine, morpholine or thiomorpholine rings, having only hydrogen atoms directly attached to the ring carbon atoms containing only hydrogen and carbon atoms in addition to the ring hetero elements
    • C07D295/023Preparation; Separation; Stabilisation; Use of additives
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/74Iron group metals
    • B01J23/75Cobalt
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/74Iron group metals
    • B01J23/755Nickel
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/76Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/84Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/85Chromium, molybdenum or tungsten
    • B01J23/86Chromium
    • B01J23/866Nickel and chromium
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D295/00Heterocyclic compounds containing polymethylene-imine rings with at least five ring members, 3-azabicyclo [3.2.2] nonane, piperazine, morpholine or thiomorpholine rings, having only hydrogen atoms directly attached to the ring carbon atoms
    • C07D295/02Heterocyclic compounds containing polymethylene-imine rings with at least five ring members, 3-azabicyclo [3.2.2] nonane, piperazine, morpholine or thiomorpholine rings, having only hydrogen atoms directly attached to the ring carbon atoms containing only hydrogen and carbon atoms in addition to the ring hetero elements
    • C07D295/027Heterocyclic compounds containing polymethylene-imine rings with at least five ring members, 3-azabicyclo [3.2.2] nonane, piperazine, morpholine or thiomorpholine rings, having only hydrogen atoms directly attached to the ring carbon atoms containing only hydrogen and carbon atoms in addition to the ring hetero elements containing only one hetero ring
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02Impregnation, coating or precipitation
    • B01J37/03Precipitation; Co-precipitation
    • B01J37/031Precipitation

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Catalysts (AREA)
  • Hydrogenated Pyridines (AREA)

Description

Verfahren zur Herstellung von Piperidin und seinen Alkylhomologen durch katalytische Hydrierung von Pyridin und dessen Alkylhomologen Die Erfindung betrifft ein Verfahren zur Herstellung ton Piperidin und seinen Alkylhomologen durch Hydrierung von Pyridin und dessen Alkylhomologen in Gegenwart von Katalysatoren bei Temperaturen von 100 bis 2000 C und Drücken bis zu 250 at. Process for the preparation of piperidine and its alkyl homologues by catalytic hydrogenation of pyridine and its alkyl homologues The invention relates to a process for the preparation of piperidine and its alkyl homologues by Hydrogenation of pyridine and its alkyl homologues in the presence of catalysts at temperatures from 100 to 2000 C and pressures up to 250 at.

Nach dem Hauptpatent .......... (................) ist es bekannt, Piperidin und seine Alkylhomologen durch Katalytische Hydrierung von Pyridin und dessen Alkylhomologen in Gegenwart von Nickelkatalysatoren herzustellen. indem man die Hydrierung bei Temperaturen von 100 bis 2000 0 und Drücken bis zu 250 at, vorzugsweise bei 110 bis 1700 C und 5 bis 50 at, in Gegenwart von Katalysatoren durchfUhrt, die mindestens 30 Gew.-%, vorzugsweise mehr als 50 Gow.-* metallisches Nickel auf Aktivtonerde oder Ohromoxid bzw. Gemischen dieser Trägersubstanzen enthalten. According to the main patent .......... (................) it is known Piperidine and its alkyl homologues by catalytic hydrogenation of pyridine and produce its alkyl homologues in the presence of nickel catalysts. by the hydrogenation at temperatures from 100 to 2000 0 and pressures up to 250 at, preferably at 110 to 1700 C and 5 to 50 at, in the presence of catalysts carried out at least 30% by weight, preferably more than 50% by weight, of metallic nickel on active alumina or ohromoxide or mixtures of these carrier substances.

Es wurde nun gefunden, daB die katalytische Hydrierung von Pyridin und seinen Alkylhomologen zu Piperidin und dessen Alkyl--homologen bei Temperaturen von 100 bis 2000 0 und Drücken bis zu 250 at mit gleiches Erfolg gelingt, wenn man die Umsetzung anstelle von Nickelkatalysatoren in Gegenwart von Kobaltkatalysatoren durchführt, die mindestens 30 Gew.-, vorzugsweise mehr als 50 Gew.-% metallisches Kobalt auf Aktivtonerde enthalten. It has now been found that the catalytic hydrogenation of pyridine and its alkyl homologues to piperidine and its alkyl homologues at temperatures from 100 to 2000 0 and pressures up to 250 at with equal success if you the implementation instead of nickel catalysts in the presence of Carries out cobalt catalysts that are at least 30% by weight, preferably more than 50 Contain% by weight metallic cobalt on active alumina.

In gleicher Weise kann auch in Gegenwart von Katalysatoren gearbeitet werden, die sowohl metallisches Nickel als auch metallisches Kobalt auf Aktivtonerde enthalten. It is also possible to work in the same way in the presence of catalysts that contain both metallic nickel and metallic cobalt on active alumina contain.

Vorteilhafterweise arbeitet man bei Temperaturen von 110 bis 170 cc und Drücken von 15 bis 200 at. It is advantageous to work at temperatures of 110 to 170 cc and pressures from 15 to 200 at.

Beispiel 1 : In einem'Autoklaven von 1,6 Liter Volumen wurden 300 g Pyridin mit einem Schwefelgehalt von 0,03 Gew.-% und 30 g eines Katalysators A bzw. Katalysators B, die in der nachstehend geschilderten Weise hergestellt worden waren, gefüllt. Darauf wurde Wasserstpff bis zu einem Anfangsdruck von 100 at aufgepreßt. Nachdem der Autoklav innerhalb von 2,0 Stunden auf 150 °G erhitzt wurde, wurde er 4 Stunden bei dieser Temperatur unter einem Reaktionsdruck zwischen 150 und 220 at gehalten.Example 1: In an autoclave with a volume of 1.6 liters, 300 g of pyridine with a sulfur content of 0.03% by weight and 30 g of a catalyst A. and Catalyst B, respectively, prepared in the manner described below were filled. Wasserstpff was then injected up to an initial pressure of 100 atm. After the autoclave was heated to 150 ° G within 2.0 hours, it became 4 hours at this temperature under a reaction pressure between 150 and 220 at held.

Katalysator A: Eine wässerige Lösung von Kobaltnitrat und Aluminiumnitrat wurde mit Sodalösung versetzt. Der entstandene Niederschlag wurde abgesaugt, mit Wasser nitratfrei gewaschen, getrocknet, mit Graphit vermahlen und zu Pillen verformt. Die Pillen wurden bei 350 °C mit Wasserstoff reduziert. Der entstandene Katalysator besaß die Zusammensetzung 6 Mol Kobalt und 1 Mol Aluminiumoxid.Catalyst A: An aqueous solution of cobalt nitrate and aluminum nitrate soda solution was added. The resulting precipitate was filtered off with suction Water washed free of nitrates, dried, ground with graphite and shaped into pills. The pills were reduced with hydrogen at 350 ° C. The resulting catalyst the composition had 6 moles of cobalt and 1 mole of alumina.

Katalysator B: Zinke wässerige Lösung von Kobaltnitrat und Aluminiumnitrat wurde mit Sodalösung versetzt. Der entstandene Niederschlag wurde abgesaugt, mit Wasser mitratfrei gewaschen, getrocknet, mit Craphit vermahlen und zu Pillen verformt. Die Pillen wurden mit Wasserstoff bei 310 °C reduziert. Der Katalysator besaß die Zusammensetzung: 25 Mol Kobalt und 1 Mol Aluminiumoxid.Catalyst B: zinc aqueous solution of cobalt nitrate and aluminum nitrate soda solution was added. The resulting precipitate was filtered off with suction Washed water free of entrainment, dried, ground with Craphit and shaped into pills. The pills were reduced with hydrogen at 310 ° C. The catalyst possessed the Composition: 25 moles of cobalt and 1 mole of aluminum oxide.

Die an den erfindungsgemäßen Katalysatoren erhaltenen Reaktionsprodukte zeigten folgende Zusammensetzungen: Reaktionsprodukt Piperidin Pyridin Nebenprodukte Gew.-% Katalysator A 99,0 0,6 0,4 Katalysator B 98, 8 0,6 0, 6 Beispiel 2: 30 cm3 Pyridin mit einem Schwefelgehalt von 0,03 Gew.-% wurden pro Stunde gemeinsam mit 600 Nermalliter Wasserstoff bei 125 °C kontinuierlich in eineX senkrecht stehenden Druckreaktor aus Stahl eingeleitet, der 300 cm3 des Katalysators B nach Beispiel 1 enthielt. Im Verlauf der Reaktion wurde das Nachlassen der Hydrieraktivität des Katalysators durch allmähliche Erhbhung der Reaktionstemperatur auf 170 °C ausgeglichen. The reaction products obtained on the catalysts of the invention showed the following compositions: reaction product piperidine pyridine by-products % By weight of catalyst A 99.0 0.6 0.4 of catalyst B 98.8 0.6 0.6 Example 2: 30 cm3 Pyridine with a sulfur content of 0.03 wt .-% were per hour together with 600 nermal liters of hydrogen at 125 ° C continuously in a vertical position Introduced pressure reactor made of steel, the 300 cm3 of the catalyst B according to example 1 contained. In the course of the reaction, the decrease in the hydrogenation activity of the Catalyst compensated by gradually increasing the reaction temperature to 170 ° C.

Das den Reaktor verlassende Reaktionsgemisch wurde auf Raumtemperatur abgekühlt und auf Normaldruck entspannt. The reaction mixture leaving the reactor was at room temperature cooled and relaxed to normal pressure.

Das Reaktionsprodukt hatte bei Drücken von 5, 15, 50 und 220 at die folgende Zusammensetzung: asac. at 5 15 50 220 Gew.-h Piperidin 97 99, 5 98, 9 98, 5 Gew.-% Pyridin 0,8-1,0 0,1 0,1 0,1 Dauer des Versuches in Tagen 7 31 29 28 Beispiel 3: In einen Autoklaven von 1,6 Liter Volumen wurden 300 g Pyridin mit einem Schwefelgehalt von 0,03 Gew.-% und 25 g eines Katalysators, der in der nachstehend geschilderten Weise hergestellt worden war, gefüllt. Darauf wurde Wasserstoff mit einem Anfangsdruck von 110 at aufgepreßt. Nachdem der Autoklav innerhalb von 1,5 Stunden auf 160 °C erhitzt warde, wurde er 4 Stunden bei dieser Temperatur unter einem Reaktionsdruck zwischen 150 und 220 at gehalten. Die Reaktionsprodukte zeigten folgende Zusammensetzung: 98,7 Gew.-m Piperidin, 0,3 Gew.-% Pyridin, 1,0 Gew.-% Nebenprodukte.The reaction product had at pressures of 5, 15, 50 and 220 at the the following composition: asac. at 5 15 50 220 wt. h piperidine 97 99, 5 98, 9 98, 5% by weight pyridine 0.8-1.0 0.1 0.1 0.1 Duration of the test in days 7 31 29 28 Example 3: In an autoclave of 1.6 liter volume was 300 g of pyridine with a sulfur content of 0.03 wt .-% and 25 g of a catalyst used in the below Way had been made, filled. This was followed by hydrogen at an initial pressure from 110 at. After the autoclave has reached 160 ° C within 1.5 hours was heated, it was kept at that temperature for 4 hours under a reaction pressure held between 150 and 220 at. The reaction products showed following composition: 98.7 wt .-% piperidine, 0.3 wt .-% pyridine, 1.0 wt .-% Byproducts.

Der angewandte Katalysator wurde auf folgende Weise hergestellt: Binde wässerige Lösung von Kobaltnitrat, Nickelnitrat und Aluminiumnitrat wurde mit Sodalösung versetzt. The catalyst used was prepared in the following way: Binding aqueous solution of cobalt nitrate, nickel nitrate and aluminum nitrate was made mixed with soda solution.

Der entstandene Niederschlag wurde abgesaugt, mit Wasser nitratfrei gewaschen, getrocknet, mit Graphit vermahlen und zu Pillen verformt. Die Pillen wurden bei 350 0 mit Wasserstoff reduziert. Der entstandene Katalysator besaß die Zusammensetzung 3 Mol Kobalt, 3 Mol Nickel und 1 Mol Aluminiumoxid.The resulting precipitate was filtered off with suction, nitrate-free with water washed, dried, ground with graphite and shaped into pills. The pills were reduced at 350 0 with hydrogen. The resulting catalyst possessed the Composition 3 moles of cobalt, 3 moles of nickel and 1 mole of aluminum oxide.

Claims (3)

Patentansprüche: 1. Verfahren zur Herstellung von Piperdin and seinen Alkylhomologen durch katalytische Hydrierung von Pyridin und dessen Alkylhomologen bei Temperaturen von 100 bis 200 °C und Drücken bis zu 250 at nach Patent ........... Claims: 1. Process for the preparation of piperdine and its Alkyl homologues by catalytic hydrogenation of pyridine and its alkyl homologues at temperatures from 100 to 200 ° C and pressures up to 250 at according to patent ........... (....................), dadurch gekennzeichnet, daß man die Umsetzung anstelle von Nickelkatalysatoren in Gegenwart von Kobaltkatalysatoren durchführt, die mindestens 30 Gew.-%, vorzugsweise mehr als 50 Gew.-% metallisches Kobalt auf Aktivtonerde enthalten.(....................), characterized in that the implementation instead of nickel catalysts in the presence of cobalt catalysts, which comprises at least 30% by weight, preferably more than 50% by weight, of metallic cobalt Active alumina included. 2. Verfahren nach Anspruch 1, dadurch gekennzeichnet, daß die Umsetzung in Gegenwart eines Katalysators durcngeführt wird, der sowohl metallisches Nickel als auch metallisches Kobalt auf Aktivtonerde enthält. 2. The method according to claim 1, characterized in that the implementation is carried out in the presence of a catalyst which contains both metallic nickel as well as metallic cobalt on active alumina. 3. Verfahren nach Anspruch 1 und 2, dadurch gekennzeichnet, daß die Umsetzung bei Temperaturen von 110 bis 170 cc und Drücken von 15 bis 200 at durchgeführt wird. 3. The method according to claim 1 and 2, characterized in that the Implementation carried out at temperatures of 110 to 170 cc and pressures of 15 to 200 at will.
DE19671695982 1965-09-04 1967-02-09 Process for the preparation of piperidine and its alkyl homologues by catalytic hydrogenation of pyridine and its alkyl homologues Pending DE1695982A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DEV0029272 1965-09-04
DEV0032939 1967-02-09

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DE1695982A1 true DE1695982A1 (en) 1971-05-19

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DE19651620664 Pending DE1620664A1 (en) 1965-09-04 1965-09-04 Process for the preparation of piperidine and its alkyl homologues by catalytic hydrogenation of pyridine and its alkyl homologues
DE19671695982 Pending DE1695982A1 (en) 1965-09-04 1967-02-09 Process for the preparation of piperidine and its alkyl homologues by catalytic hydrogenation of pyridine and its alkyl homologues

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19832810A1 (en) * 1998-07-21 2000-01-27 Basf Ag Hydrogenation of unsaturated heterocyclic compounds, especially pyridine compounds, uses a catalyst containing a Subgroup VIII metal on a macroporous support

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