DE1768321C3 - - Google Patents
Info
- Publication number
- DE1768321C3 DE1768321C3 DE1768321A DE1768321A DE1768321C3 DE 1768321 C3 DE1768321 C3 DE 1768321C3 DE 1768321 A DE1768321 A DE 1768321A DE 1768321 A DE1768321 A DE 1768321A DE 1768321 C3 DE1768321 C3 DE 1768321C3
- Authority
- DE
- Germany
- Prior art keywords
- schiff
- nitriles
- hydrogen
- bases
- amines
- 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.)
- Expired
Links
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims description 14
- 239000001257 hydrogen Substances 0.000 claims description 14
- 229910052739 hydrogen Inorganic materials 0.000 claims description 14
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 13
- 150000002825 nitriles Chemical class 0.000 claims description 13
- 239000002262 Schiff base Substances 0.000 claims description 10
- 150000004753 Schiff bases Chemical class 0.000 claims description 9
- 239000007868 Raney catalyst Substances 0.000 claims description 7
- 229910000564 Raney nickel Inorganic materials 0.000 claims description 7
- 229910021529 ammonia Inorganic materials 0.000 claims description 7
- 238000006243 chemical reaction Methods 0.000 claims description 7
- 239000002585 base Substances 0.000 claims description 6
- 238000005984 hydrogenation reaction Methods 0.000 claims description 5
- -1 carbon atoms amines Chemical class 0.000 claims description 4
- 150000001875 compounds Chemical class 0.000 claims description 4
- 150000003141 primary amines Chemical class 0.000 claims description 4
- 238000003756 stirring Methods 0.000 claims description 4
- 150000003335 secondary amines Chemical class 0.000 claims description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims 4
- 238000004519 manufacturing process Methods 0.000 claims 4
- 238000000034 method Methods 0.000 claims 3
- 229920006395 saturated elastomer Polymers 0.000 claims 3
- 230000015572 biosynthetic process Effects 0.000 claims 2
- 230000003197 catalytic effect Effects 0.000 claims 2
- 239000000543 intermediate Substances 0.000 claims 2
- FZNCGRZWXLXZSZ-CIQUZCHMSA-N Voglibose Chemical compound OCC(CO)N[C@H]1C[C@](O)(CO)[C@@H](O)[C@H](O)[C@H]1O FZNCGRZWXLXZSZ-CIQUZCHMSA-N 0.000 claims 1
- 150000001299 aldehydes Chemical class 0.000 claims 1
- 238000005882 aldol condensation reaction Methods 0.000 claims 1
- 150000001412 amines Chemical class 0.000 claims 1
- 125000004432 carbon atom Chemical group C* 0.000 claims 1
- 238000009903 catalytic hydrogenation reaction Methods 0.000 claims 1
- 230000003028 elevating effect Effects 0.000 claims 1
- 230000008030 elimination Effects 0.000 claims 1
- 238000003379 elimination reaction Methods 0.000 claims 1
- 230000036571 hydration Effects 0.000 claims 1
- 238000006703 hydration reaction Methods 0.000 claims 1
- 150000002576 ketones Chemical class 0.000 claims 1
- 229910052759 nickel Inorganic materials 0.000 claims 1
- 238000002360 preparation method Methods 0.000 claims 1
- 238000007086 side reaction Methods 0.000 claims 1
- 239000007787 solid Substances 0.000 claims 1
- 239000002904 solvent Substances 0.000 claims 1
- 238000003786 synthesis reaction Methods 0.000 claims 1
- 238000005829 trimerization reaction Methods 0.000 claims 1
- NPXOKRUENSOPAO-UHFFFAOYSA-N Raney nickel Chemical compound [Al].[Ni] NPXOKRUENSOPAO-UHFFFAOYSA-N 0.000 description 5
- 238000004821 distillation Methods 0.000 description 5
- 239000007789 gas Substances 0.000 description 4
- REYJJPSVUYRZGE-UHFFFAOYSA-N Octadecylamine Chemical compound CCCCCCCCCCCCCCCCCCN REYJJPSVUYRZGE-UHFFFAOYSA-N 0.000 description 3
- FVSKHRXBFJPNKK-UHFFFAOYSA-N propionitrile Chemical compound CCC#N FVSKHRXBFJPNKK-UHFFFAOYSA-N 0.000 description 3
- RHSBIGNQEIPSCT-UHFFFAOYSA-N stearonitrile Chemical compound CCCCCCCCCCCCCCCCCC#N RHSBIGNQEIPSCT-UHFFFAOYSA-N 0.000 description 3
- ZCYVEMRRCGMTRW-UHFFFAOYSA-N 7553-56-2 Chemical compound [I] ZCYVEMRRCGMTRW-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 238000013459 approach Methods 0.000 description 2
- 150000002196 fatty nitriles Chemical class 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 229910052740 iodine Inorganic materials 0.000 description 2
- 239000011630 iodine Substances 0.000 description 2
- HKUFIYBZNQSHQS-UHFFFAOYSA-N n-octadecyloctadecan-1-amine Chemical group CCCCCCCCCCCCCCCCCCNCCCCCCCCCCCCCCCCCC HKUFIYBZNQSHQS-UHFFFAOYSA-N 0.000 description 2
- WGYKZJWCGVVSQN-UHFFFAOYSA-N propylamine Chemical compound CCCN WGYKZJWCGVVSQN-UHFFFAOYSA-N 0.000 description 2
- 239000003760 tallow Substances 0.000 description 2
- HWJPHQNEWARZLH-UHFFFAOYSA-N 1,1,2,2,3,3,4,4,5,5-decafluoro-6,6-bis(trifluoromethyl)cyclohexane Chemical compound FC(F)(F)C1(C(F)(F)F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C1(F)F HWJPHQNEWARZLH-UHFFFAOYSA-N 0.000 description 1
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 1
- MKYBYDHXWVHEJW-UHFFFAOYSA-N N-[1-oxo-1-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)propan-2-yl]-2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carboxamide Chemical compound O=C(C(C)NC(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F)N1CC2=C(CC1)NN=N2 MKYBYDHXWVHEJW-UHFFFAOYSA-N 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- WEHWNAOGRSTTBQ-UHFFFAOYSA-N dipropylamine Chemical compound CCCNCCC WEHWNAOGRSTTBQ-UHFFFAOYSA-N 0.000 description 1
- JRBPAEWTRLWTQC-UHFFFAOYSA-N dodecylamine Chemical compound CCCCCCCCCCCCN JRBPAEWTRLWTQC-UHFFFAOYSA-N 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 238000005194 fractionation Methods 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- MJCJUDJQDGGKOX-UHFFFAOYSA-N n-dodecyldodecan-1-amine Chemical compound CCCCCCCCCCCCNCCCCCCCCCCCC MJCJUDJQDGGKOX-UHFFFAOYSA-N 0.000 description 1
- BEQPUKSNIDHWRY-UHFFFAOYSA-N n-dodecyldodecan-1-imine Chemical compound CCCCCCCCCCCCN=CCCCCCCCCCCC BEQPUKSNIDHWRY-UHFFFAOYSA-N 0.000 description 1
- YMMCFOVWHFLGON-UHFFFAOYSA-N n-propylpropan-1-imine Chemical compound CCCN=CCC YMMCFOVWHFLGON-UHFFFAOYSA-N 0.000 description 1
- 125000002560 nitrile group Chemical group 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 238000001953 recrystallisation Methods 0.000 description 1
- 230000009183 running Effects 0.000 description 1
- 238000004513 sizing Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C249/00—Preparation of compounds containing nitrogen atoms doubly-bound to a carbon skeleton
- C07C249/02—Preparation of compounds containing nitrogen atoms doubly-bound to a carbon skeleton of compounds containing imino groups
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Description
I. R · C s N + H8 -> R · CH =I. R • C s N + H 8 -> R • CH =
NH8 NH 8
2R · C = N + 3H8 ^ R · CH8N = CH · R + NH, gen bilden sich nur in untergeordneter Menge und2R · C = N + 3H 8 ^ R · CH 8 N = CH · R + NH, genes are only formed in minor amounts and
45 verbleiben im Ruckstand der Destillation.45 remain in the residue from the distillation.
abnähme entfernt werden. Bei höhermolekularen sind wertvolle Zwischenverbindungen.would be removed. With higher molecular weight are valuable intermediate compounds.
drierung leichten Überdruck, gegebenenfalls bei 5° In einem Autoklav werden 55Og PropionitrilA slight overpressure drift, if necessary at 5 °. 550 g of propionitrile are placed in an autoclave
erforderliche Reaktionstemperatur zu erreichen. Raney-Nickel vorgelegt. Dann preßt man 15 M9Ito reach the required reaction temperature. Raney nickel submitted. Then you press 15 M9I
fettnitril, bleibt die olefinische Doppelbindung bei der dem Abtrennen des Kontaktes und Abtreiben desfatty nitrile, the olefinic double bond remains when the contact is separated and the
zu erwarten war, daß die Nitrilgruppe sich selektiv und 70% einer Hauptfraktion, die zu 80 Teilen ausIt was to be expected that the nitrile group was selectively and 70% of a main fraction, which was made up of 80 parts
hydrieren läßt, ohne daß die Doppelbindung der sich Di-C3-Schiffscher Base besteht; die restlichen 20 Teilecan be hydrogenated without the double bond of the di-C 3 -Schiff base; the remaining 20 parts
bildenden Schiffschen Base, wie auch die olefinische sind Propionitril und Dipropylamin. 8% höhermole-Schiff's base, as well as the olefinic base, are propionitrile and dipropylamine. 8% higher mol-
mehrere Ansätze verwertet werden kann, abgetrennt N-Propyliden-propylamin, das bei Kp7M 100 bisseveral approaches can be used, separated N-propylidene-propylamine, which at bp 7M 100 to
und das erhaltene Reaktionsgemisch destilliert. Un- 1020C siedet, von dem Nitril-Amin-Azeotrop abgi-and the reaction mixture obtained is distilled. Un- 102 0 C boils, given off by the nitrile-amine azeotrope
umgesetztes Nitril und primäres Amin werden als trennt werden.reacted nitrile and primary amine are considered to be separated.
wieder eingesetzt werde·!. Anschließend destilliert die B e ι s ρ 1 e I 2will be reinstated · !. The B e ι s ρ 1 e I 2 is then distilled
handenes sekundäres Amin kann durch Umkristalli- (=3 Mol) zusammen mit 27 g cyclohexanfeuchtemExisting secondary amine can be moistened by recrystalline (= 3 mol) together with 27 g of cyclohexane
Raney-Nickel vorgelegt und unter Einleiten von etwa 341 Wasserstoff pro Stunde bei 165°C hydriert. In etwa 43/4 Stunden werden 99,0 Normalliter Wasserstoff aufgenommen (Theorie für 4,5 Mol = 100,8 1) und 19,5 g Ammoniak (Theorie 25,5 g) mit dem Abgas ausgetragen. Nach Abtrennen des Kontaktes erhält man bei der Destillation über einen Claisen-Aufsatz 28% Vorlauf, bestehend aus etwa 42 Teilen unumgesetztem Nitril und 58 Teilen Laurylamin und 66% Hauptlauf, der 90% Schiffsche Base (N-Lauryliden-Iaurylamin) und 10% Dilaurylamin enthält. Im Rückstand verbleiben 6% höhermolekulare Verbindungen. Submitted Raney nickel and hydrogenated at 165 ° C while passing in about 341 hydrogen per hour. In about 4 3/4 hour 99.0 normal liters of hydrogen are added (theory for 4.5 mol = 100.8 1) and 19.5 g of ammonia (theory 25.5 g) with the exhaust gas discharged. After the contact has been separated off, the distillation through a Claisen attachment gives 28% first run, consisting of about 42 parts of unreacted nitrile and 58 parts of laurylamine and 66% of the main run, 90% of the Schiff base (N-laurylidene-laurylamine) and 10% of dilaurylamine contains. 6% higher molecular weight compounds remain in the residue.
540 g Stearylnitril (= 2,04 Mol) werden zusammen mit 27 g Raney-Nickel cyrlohexanfeucht in einem Glaskolben vorgelegt und unter kräftigem Rühren mit etwa 301 Wasserstoff bei Normaldruck und 165CC behandelt, in etwa 5 Stunden werden 64,8 Normalliter Wasserstoff aufgenommen (Theorie für 3,06 Mol = 68,41) und 132 g Ammoniak mit dem Abgas ausgetragen (Theorie: 17,3 g). Man filtriert vom Katalysator ab und destilliert das Filtrat im ölpumpenvakuum über einen Claisen-Aufsatz. Nach einem Vorlauf von etwa 25%, bestehend aus 40% unumgesetztem Stearylnitril und 60% Stearylamin, gehen 70% bei 267 bis 33O°C/O,3 bis 0,4 mm über, die zu 90% aus Schiffscher Base (N-Stearyliden-steai-ylamin) bestehen. Der Rest ist Distearylamin, das durch Umkristallisation entfernt werden kann·. Bei einer Kolbentemperatur von 3600C verbleiben 5% höhermolekulare Stoffe als Rückstand.540 g Stearylnitril (= 2.04 mol) are combined with 27 g Raney nickel in a glass flask cyrlohexanfeucht vessel and treated under vigorous stirring with about 301 hydrogen at atmospheric pressure and 165 C C, 64.8 normal liters of hydrogen are added in about 5 hours (Theory for 3.06 mol = 68.41) and 132 g of ammonia discharged with the exhaust gas (theory: 17.3 g). The catalyst is filtered off and the filtrate is distilled in an oil pump vacuum through a Claisen attachment. After a preliminary run of about 25%, consisting of 40% unreacted stearyl nitrile and 60% stearylamine, 70% pass at 267 to 330 ° C./0.3 to 0.4 mm, 90% of which consists of Schiff base (N-stearylidene -steai-ylamin) exist. The remainder is distearylamine, which can be removed by recrystallization ·. At a pot temperature of 360 0 C 5% higher molecular weight substances, remain as residue.
Be i s pi e 1 4 .Example 1 4.
700 g einer reinen Clg-Fraktion aus Talgfettnitril (= 2,65 MoI) (Jodzahl: 74) werden zusammen mit 35 g cyclohexanfeuchteni Raney-Nickel in einem Kolben vorgelegt und bei 165° C mit etwa 401 Wasserstoff pro Stunde unter kräftigem Rühren behandelt. In 43/4 Stunden sind 93,7 Normalliter Wasserstoff aufgenommen (Theorie für 3,98 Mol = 89,11) und 18,1 g700 g of a pure C lg fraction of tallow fatty nitrile (= 2.65 mol) (iodine number: 74) are placed in a flask together with 35 g of Raney nickel cyclohexane and treated at 165 ° C. with about 40 liters of hydrogen per hour with vigorous stirring . In 4 3/4 hour 93.7 normal liters of hydrogen are added (3.98 mol theory = 89.11) and 18.1 g
ίο Ammoniak mit dem Abgas ausgetragen (Theorie: 22,5 g). Nach dem Abtrennen des Kontaktes liefert die Claisen-Destillation 26% Vorlauf, bestehend aus 35% unumgesetztem Nitril und 65% primärem Amin und 66% Hauptlauf, bestehend aus 90% Schiffscher Base der Jodzahl 64 und 8% Rückstand.ίο ammonia discharged with the exhaust gas (theory: 22.5 g). After separating the contact, the Claisen distillation yields 26% foreshot, consisting of 35% unreacted nitrile and 65% primary amine and 66% main run, consisting of 90% Schiffscher Base of iodine number 64 and 8% residue.
704 g einer Mischung aus
a) 322 g frischen Stearylnitril und
b) 269 g Stearylamin und
lOgStearyinitril704 g of a mixture of
a) 322 g of fresh stearyl nitrile and
b) 269 g of stearylamine and
lOg stearyinitrile
(beide aus Vorlauf der vorangegangenen Hydrierung) (both from the forerunner of the previous hydrogenation)
werden zusammen mit 35 g Raney-Nickel cyclohexanes feucht in einem Kolben vorgelegt und unter Einleiten von etwa 16,51 Wasserstoff pro Stunde bei 165°C hydriert. In 4 Stunden wurden 45,0 Normalliter Wasserstoff aufgenommen und 15,9 g Ammoniak mit dem Abgas ausgetragen. Nach dem Abtrennen des Kontaktes gibt die Claisen-Destillation 32% Vorlauf, bestehend aus 28% unumgesetztem Stearylnitril und 72% Stearylamin, sowie 63% Hauptlauf, der aus 90% Schiffscher Base und 10% Distearylamin besteht. Der Destillationsrückstand beträgt 5 %.are presented moist together with 35 g of Raney nickel cyclohexanes in a flask and while introducing hydrogenated by about 16.51 hydrogen per hour at 165 ° C. 45.0 normal liters of hydrogen were achieved in 4 hours added and 15.9 g of ammonia discharged with the exhaust gas. After disconnecting the contact the Claisen distillation gives 32% first runnings, consisting of 28% unreacted stearyl nitrile and 72% stearylamine, as well as 63% main run, which consists of 90% Schiff base and 10% distearylamine. The distillation residue is 5%.
Claims (2)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE1768321A DE1768321B2 (en) | 1968-04-30 | 1968-04-30 | Process for the production of SchifF bases by incomplete catalytic hydrogenation of nitriles |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE1768321A DE1768321B2 (en) | 1968-04-30 | 1968-04-30 | Process for the production of SchifF bases by incomplete catalytic hydrogenation of nitriles |
Publications (3)
| Publication Number | Publication Date |
|---|---|
| DE1768321A1 DE1768321A1 (en) | 1971-09-30 |
| DE1768321B2 DE1768321B2 (en) | 1974-01-24 |
| DE1768321C3 true DE1768321C3 (en) | 1974-09-12 |
Family
ID=5699699
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| DE1768321A Granted DE1768321B2 (en) | 1968-04-30 | 1968-04-30 | Process for the production of SchifF bases by incomplete catalytic hydrogenation of nitriles |
Country Status (1)
| Country | Link |
|---|---|
| DE (1) | DE1768321B2 (en) |
-
1968
- 1968-04-30 DE DE1768321A patent/DE1768321B2/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| DE1768321B2 (en) | 1974-01-24 |
| DE1768321A1 (en) | 1971-09-30 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C3 | Grant after two publication steps (3rd publication) |