US3366634A - Preparation of tetrahydropyrimidines - Google Patents
Preparation of tetrahydropyrimidines Download PDFInfo
- Publication number
- US3366634A US3366634A US610759A US61075967A US3366634A US 3366634 A US3366634 A US 3366634A US 610759 A US610759 A US 610759A US 61075967 A US61075967 A US 61075967A US 3366634 A US3366634 A US 3366634A
- Authority
- US
- United States
- Prior art keywords
- propanediamine
- acetyl
- tetrahydropyrimidine
- catalyst
- yield
- 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 - Lifetime
Links
- 238000002360 preparation method Methods 0.000 title description 6
- 150000005326 tetrahydropyrimidines Chemical class 0.000 title description 5
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 33
- -1 oxide Chemical compound 0.000 description 31
- 239000003054 catalyst Substances 0.000 description 20
- 239000000047 product Substances 0.000 description 19
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 18
- 238000006243 chemical reaction Methods 0.000 description 15
- 238000000034 method Methods 0.000 description 13
- OTPDWCMLUKMQNO-UHFFFAOYSA-N 1,2,3,4-tetrahydropyrimidine Chemical compound C1NCC=CN1 OTPDWCMLUKMQNO-UHFFFAOYSA-N 0.000 description 12
- 239000002253 acid Substances 0.000 description 11
- 230000008569 process Effects 0.000 description 11
- XFNJVJPLKCPIBV-UHFFFAOYSA-N trimethylenediamine Natural products NCCCN XFNJVJPLKCPIBV-UHFFFAOYSA-N 0.000 description 11
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 10
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 10
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 10
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 9
- WFDIJRYMOXRFFG-UHFFFAOYSA-N Acetic anhydride Chemical compound CC(=O)OC(C)=O WFDIJRYMOXRFFG-UHFFFAOYSA-N 0.000 description 9
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 9
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 9
- 238000004821 distillation Methods 0.000 description 9
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 8
- 229910052739 hydrogen Inorganic materials 0.000 description 8
- 239000000203 mixture Substances 0.000 description 8
- 239000011541 reaction mixture Substances 0.000 description 8
- 230000009467 reduction Effects 0.000 description 8
- 238000006798 ring closing metathesis reaction Methods 0.000 description 8
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 7
- 125000003118 aryl group Chemical group 0.000 description 7
- 239000003795 chemical substances by application Substances 0.000 description 7
- 239000001257 hydrogen Substances 0.000 description 7
- 229910000564 Raney nickel Inorganic materials 0.000 description 6
- 229910052759 nickel Inorganic materials 0.000 description 6
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 5
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 5
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 5
- 150000001412 amines Chemical class 0.000 description 5
- 229910021529 ammonia Inorganic materials 0.000 description 5
- 229910017052 cobalt Inorganic materials 0.000 description 5
- 239000010941 cobalt Substances 0.000 description 5
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 5
- 238000001816 cooling Methods 0.000 description 5
- 229910052802 copper Inorganic materials 0.000 description 5
- 239000010949 copper Substances 0.000 description 5
- 150000004985 diamines Chemical class 0.000 description 5
- 150000004820 halides Chemical class 0.000 description 5
- 238000010438 heat treatment Methods 0.000 description 5
- WPBNNNQJVZRUHP-UHFFFAOYSA-L manganese(2+);methyl n-[[2-(methoxycarbonylcarbamothioylamino)phenyl]carbamothioyl]carbamate;n-[2-(sulfidocarbothioylamino)ethyl]carbamodithioate Chemical compound [Mn+2].[S-]C(=S)NCCNC([S-])=S.COC(=O)NC(=S)NC1=CC=CC=C1NC(=S)NC(=O)OC WPBNNNQJVZRUHP-UHFFFAOYSA-L 0.000 description 5
- 239000000463 material Substances 0.000 description 5
- 229910052751 metal Inorganic materials 0.000 description 5
- 239000002184 metal Substances 0.000 description 5
- 229910052763 palladium Inorganic materials 0.000 description 5
- 229910052697 platinum Inorganic materials 0.000 description 5
- CPELXLSAUQHCOX-UHFFFAOYSA-M Bromide Chemical compound [Br-] CPELXLSAUQHCOX-UHFFFAOYSA-M 0.000 description 4
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 4
- 229910021591 Copper(I) chloride Inorganic materials 0.000 description 4
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 4
- 159000000021 acetate salts Chemical class 0.000 description 4
- 125000001931 aliphatic group Chemical group 0.000 description 4
- 125000004432 carbon atom Chemical group C* 0.000 description 4
- OXBLHERUFWYNTN-UHFFFAOYSA-M copper(I) chloride Chemical compound [Cu]Cl OXBLHERUFWYNTN-UHFFFAOYSA-M 0.000 description 4
- XMBWDFGMSWQBCA-UHFFFAOYSA-N hydrogen iodide Chemical compound I XMBWDFGMSWQBCA-UHFFFAOYSA-N 0.000 description 4
- 238000007363 ring formation reaction Methods 0.000 description 4
- 229910001220 stainless steel Inorganic materials 0.000 description 4
- 239000010935 stainless steel Substances 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 125000001731 2-cyanoethyl group Chemical group [H]C([H])(*)C([H])([H])C#N 0.000 description 3
- DKRQDOPNZFOLQD-UHFFFAOYSA-N 3-(dodecylamino)propanenitrile Chemical compound CCCCCCCCCCCCNCCC#N DKRQDOPNZFOLQD-UHFFFAOYSA-N 0.000 description 3
- 239000007868 Raney catalyst Substances 0.000 description 3
- NPXOKRUENSOPAO-UHFFFAOYSA-N Raney nickel Chemical compound [Al].[Ni] NPXOKRUENSOPAO-UHFFFAOYSA-N 0.000 description 3
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 description 3
- WETWJCDKMRHUPV-UHFFFAOYSA-N acetyl chloride Chemical compound CC(Cl)=O WETWJCDKMRHUPV-UHFFFAOYSA-N 0.000 description 3
- 239000012346 acetyl chloride Substances 0.000 description 3
- 125000000217 alkyl group Chemical group 0.000 description 3
- 150000008064 anhydrides Chemical class 0.000 description 3
- JRBPAEWTRLWTQC-UHFFFAOYSA-N dodecylamine Chemical compound CCCCCCCCCCCCN JRBPAEWTRLWTQC-UHFFFAOYSA-N 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000008188 pellet Substances 0.000 description 3
- 150000003141 primary amines Chemical class 0.000 description 3
- 238000010992 reflux Methods 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 239000007858 starting material Substances 0.000 description 3
- GVTDCVGMVKIFEL-UHFFFAOYSA-N 1-dodecyl-2-methyl-5,6-dihydro-4h-pyrimidine Chemical compound CCCCCCCCCCCCN1CCCN=C1C GVTDCVGMVKIFEL-UHFFFAOYSA-N 0.000 description 2
- VTEDMSWWQJHBBP-UHFFFAOYSA-N 2-dodecylbenzamide Chemical compound CCCCCCCCCCCCC1=CC=CC=C1C(N)=O VTEDMSWWQJHBBP-UHFFFAOYSA-N 0.000 description 2
- GUBPKKGRODRXPY-UHFFFAOYSA-N 3-(octadecylamino)propanenitrile Chemical compound CCCCCCCCCCCCCCCCCCNCCC#N GUBPKKGRODRXPY-UHFFFAOYSA-N 0.000 description 2
- SNRUBQQJIBEYMU-UHFFFAOYSA-N Dodecane Natural products CCCCCCCCCCCC SNRUBQQJIBEYMU-UHFFFAOYSA-N 0.000 description 2
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 2
- 125000002777 acetyl group Chemical group [H]C([H])([H])C(*)=O 0.000 description 2
- PASDCCFISLVPSO-UHFFFAOYSA-N benzoyl chloride Chemical compound ClC(=O)C1=CC=CC=C1 PASDCCFISLVPSO-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 2
- 239000000920 calcium hydroxide Substances 0.000 description 2
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 2
- 239000003518 caustics Substances 0.000 description 2
- 239000007795 chemical reaction product Substances 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 150000001879 copper Chemical class 0.000 description 2
- ORTQZVOHEJQUHG-UHFFFAOYSA-L copper(II) chloride Chemical compound Cl[Cu]Cl ORTQZVOHEJQUHG-UHFFFAOYSA-L 0.000 description 2
- 239000012024 dehydrating agents Substances 0.000 description 2
- 125000003438 dodecyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])* 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 2
- 239000012044 organic layer Substances 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 150000003335 secondary amines Chemical class 0.000 description 2
- VBXZSFNZVNDOPB-UHFFFAOYSA-N 1,4,5,6-tetrahydropyrimidine Chemical class C1CNC=NC1 VBXZSFNZVNDOPB-UHFFFAOYSA-N 0.000 description 1
- SBXYGJBXZOZUNS-UHFFFAOYSA-N 1-dodecyl-2-methyl-1,3-diazinane Chemical compound CCCCCCCCCCCCN1CCCNC1C SBXYGJBXZOZUNS-UHFFFAOYSA-N 0.000 description 1
- YBONBWJSFMTXLE-UHFFFAOYSA-N 2,3-dichlorobenzoyl chloride Chemical class ClC(=O)C1=CC=CC(Cl)=C1Cl YBONBWJSFMTXLE-UHFFFAOYSA-N 0.000 description 1
- IRHHUMKRUINGSZ-UHFFFAOYSA-N 2-(dodecylamino)propanenitrile Chemical compound CCCCCCCCCCCCNC(C)C#N IRHHUMKRUINGSZ-UHFFFAOYSA-N 0.000 description 1
- VTXNOVCTHUBABW-UHFFFAOYSA-N 3,4-dichlorobenzoyl chloride Chemical compound ClC(=O)C1=CC=C(Cl)C(Cl)=C1 VTXNOVCTHUBABW-UHFFFAOYSA-N 0.000 description 1
- AFXXFNVAHYRPIZ-UHFFFAOYSA-N 3-(octylamino)propanenitrile Chemical compound CCCCCCCCNCCC#N AFXXFNVAHYRPIZ-UHFFFAOYSA-N 0.000 description 1
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 description 1
- 102100040996 Cochlin Human genes 0.000 description 1
- 101000748988 Homo sapiens Cochlin Proteins 0.000 description 1
- OAKJQQAXSVQMHS-UHFFFAOYSA-N Hydrazine Chemical compound NN OAKJQQAXSVQMHS-UHFFFAOYSA-N 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 125000003047 N-acetyl group Chemical group 0.000 description 1
- CZPWVGJYEJSRLH-UHFFFAOYSA-N Pyrimidine Chemical compound C1=CN=CN=C1 CZPWVGJYEJSRLH-UHFFFAOYSA-N 0.000 description 1
- 150000008065 acid anhydrides Chemical class 0.000 description 1
- 230000010933 acylation Effects 0.000 description 1
- 238000005917 acylation reaction Methods 0.000 description 1
- 150000001408 amides Chemical class 0.000 description 1
- 125000005605 benzo group Chemical group 0.000 description 1
- 125000002837 carbocyclic group Chemical group 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000009903 catalytic hydrogenation reaction Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000002738 chelating agent Substances 0.000 description 1
- 239000012043 crude product Substances 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 238000007278 cyanoethylation reaction Methods 0.000 description 1
- 238000005984 hydrogenation reaction Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical group [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 1
- 239000000543 intermediate Substances 0.000 description 1
- LSACYLWPPQLVSM-UHFFFAOYSA-N isobutyric acid anhydride Chemical compound CC(C)C(=O)OC(=O)C(C)C LSACYLWPPQLVSM-UHFFFAOYSA-N 0.000 description 1
- 238000006317 isomerization reaction Methods 0.000 description 1
- 125000001449 isopropyl group Chemical group [H]C([H])([H])C([H])(*)C([H])([H])[H] 0.000 description 1
- 239000010410 layer Substances 0.000 description 1
- 239000003863 metallic catalyst Substances 0.000 description 1
- 150000001455 metallic ions Chemical class 0.000 description 1
- 230000005012 migration Effects 0.000 description 1
- 238000013508 migration Methods 0.000 description 1
- 150000002762 monocarboxylic acid derivatives Chemical class 0.000 description 1
- LNIJOCDFSOYTOO-UHFFFAOYSA-N n-(2-methylpropyl)dodecan-1-amine Chemical compound CCCCCCCCCCCCNCC(C)C LNIJOCDFSOYTOO-UHFFFAOYSA-N 0.000 description 1
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 1
- PZYZDSMNHHDRHM-UHFFFAOYSA-N n-dodecylbenzamide Chemical compound CCCCCCCCCCCCNC(=O)C1=CC=CC=C1 PZYZDSMNHHDRHM-UHFFFAOYSA-N 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 150000002825 nitriles Chemical class 0.000 description 1
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 1
- 125000002347 octyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 125000004079 stearyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 125000003107 substituted aryl group Chemical group 0.000 description 1
- 150000003512 tertiary amines Chemical class 0.000 description 1
- 229940073455 tetraethylammonium hydroxide Drugs 0.000 description 1
- LRGJRHZIDJQFCL-UHFFFAOYSA-M tetraethylazanium;hydroxide Chemical compound [OH-].CC[N+](CC)(CC)CC LRGJRHZIDJQFCL-UHFFFAOYSA-M 0.000 description 1
- ZMANZCXQSJIPKH-UHFFFAOYSA-O triethylammonium ion Chemical compound CC[NH+](CC)CC ZMANZCXQSJIPKH-UHFFFAOYSA-O 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D239/00—Heterocyclic compounds containing 1,3-diazine or hydrogenated 1,3-diazine rings
- C07D239/02—Heterocyclic compounds containing 1,3-diazine or hydrogenated 1,3-diazine rings not condensed with other rings
- C07D239/06—Heterocyclic compounds containing 1,3-diazine or hydrogenated 1,3-diazine rings not condensed with other rings having one double bond between ring members or between a ring member and a non-ring member
Definitions
- the ring closure is especially satisfactory when conducted in the presence of nickel, copper, cobalt, manganese, platinum, palladium and the chloride, bromide, iodide, oxide, sulfate, carbonate, and acetate salts thereof, in the presence of a strong base at a temperature of about 170-230 C.
- 3 aliphatic-Z-substituted tetrahydropyrimidines have been formed by heating equal moles of acetic acid and a N aliphatic 1,3-propanediamine at high temperatures to form the amide and then heating at about 250-300 C. and with a dehydrating agent to cyclize the monoamide to form the tetrahydropyrimidine.
- This reaction even with the rigorous reaction conditions, results in low product yield due to the formation of diamide and difiiculty in ring closure of the monoamide which is formed.
- a further object is to provide an improved process for the preparation of 3-aliphatic, 2-aliphatic or aromatic, 3,4,5,6-tetrahydropyrimidines and intermediates thereof through the formation of the acylated diamines and the use of metal catalysts for ring closure.
- a ,9- cyanoethylaliphatic amine having from 8 to 22 carbon atoms which may be a straight or branched chain, saturated or unsaturated with an aliphatic or aromatic acylating agent, such as an acid halide or acid anhydride, and then hydrogenating the resulting N-acyl-N-fl-cyaiioethyl amine over 'a nickel catalyst in the presence of a base.
- the resulting acyl-N-alkyl-1,3-propanediamine is then heated to yield the tetrahydropyrimidine product.
- the acyl-N-alkyl-1,3-propanediamine may be distilled, preferably in vacuo, at a temperature of about -230" C. in the presence of 'a metal catalyst, such a nickel, copper, cobalt, manganese, platinum, palladium, and salts thereof, and preferably in the presence of a strong base selected from the group of potassium hydroxide, sodium hydroxide, calcium hydroxide, etc.
- Particularly useful catalysts may be selected from the group consisting of nickel, copper, cobalt, manganese, platinum, palladium, and the chloride, bromide, iodide, oxide, sulfate, carbonate, and acetate salts thereof. From about 0.5 to 5 weight percent catalyst is preferrred. The use of the catalysts has been found to be extremely effective in bringing about ring closure.
- Step 1 of the above reaction fl-cy'anoethyldodecylamine was allowed to react with acetyl chloride, the resulting N-acetyl, N-B-cyanoethyldodecylamine was hydrogenated over a nickel catalyst in the presence of catstic.
- the product of the second reaction namely, acyl-N- dodecyl-1,3-propanediamine, was distilled in the presence, of copper chloride at 200 C. in vacuo to yield 3-dodecyl- Z-methyl-3,4,5,6-tetrahydropyrimidine.
- the substituted 1,3-propanediamine was distilled at a temperature of from 180- 200" C. at 0.1-0.15 mm. in the presence of Raney nickel to cyclize the substituted 1,3-propanediamine.
- the metal catalyst may also be packed in a heated column and the diamine run through the column to achieve cyclization.
- the use of the nickel or other metal catalyst as described above has been found to be very effective for ring closure reaction.
- the ring closure has been effected only by extremely high temperatures, strong dehydrating agents, and long reaction times.
- the metallic ion may function as a chelating agent which 3 brings the amidoamine into the correct position for ring closure, e.'g.,
- the alkyl acid halide employed in the acylation step may have from 1 to 22 carbon atoms. Any aliphatic or aromatic acylating agent, such 'as acid halides, anhydrides, etc., may be employed.
- an aryl substituent may be inserted into the tetrahydropyrimidine ring at the 2-position in place of the methyl group by using an aromatic acylating agent, such as benzoyl chloride, 3,4- dichlorobenzoyl chloride, mixed dichlorobenzoyl chlorides, alkylated benzoyl chlorides, etc., thus producing aryl and substituted aryl derivatives of tetrahydropyrimidines.
- aromatic acylating agent such as benzoyl chloride, 3,4- dichlorobenzoyl chloride, mixed dichlorobenzoyl chlorides, alkylated benzoyl chlorides, etc.
- the preferred acylating agent is selected from the group consisting of alkyl and mono-carbocyclic aryl acid halides and anhydrides thus forming a diamine selected from the group consisting of alkanoyland mono-carbocyclic aroyl-N-aliphatic-1,3-propanediamine, respectively.
- Reaction 2 above ordinarily yields two isomers shown as I and II.
- the isomers I and H are found to be about equally divided in a mixture when the hydrogenation is carried out at about 300 p.s.i. H pressure. Reductions at higher pressures, for example, at 800 psi, caused almost complete isomerization of isomer I to isomer II, In the case of the octyl and octadecyl derivatives, isomer II was found to exist to the extent of 93-98 percent. This phenomenon involves migration of the acetyl group 0 I] CIIHG" from one nitrogen group to the other during reduction.
- the starting material used in the preparation of the tetrahydro pyrimidine may be prepared by the known proc ess of cyanoethylation of the desired amine.
- dodecylamine may be reacted with a slight excess of acrylonitrile in the presence of about 4 percent water at 70 C. for a period of 2 to 3 hours.
- the product, cyanoethyldodecylamine is obtained in almost quantitative yield.
- a preferred embodiment of this invention is the process for preparing 3 aliphatic-2-substituted-3,4,5,6-tetrahydropyrimidine, the steps of reacting fl-cyanoethyl aliphatic amines having 8 to 22 carbon atoms with an acylating agent selected from the group consisting of alkyl and monocarbocyclic aryl acid halides and anhydrides, hydrogenating the reacted product over a nickel catalyst under pressure and in the presence of a base to produce an acyl-N-aliphatic 1,3-propanediamine, and heating the hydrogenated product in the presence of a catalyst selected from the group consisting of nickel, copper, cobalt, manganese, platinum, palladium, and the chloride, bromide, iodide, oxide, sulfate, carbonate, and acetate salts thereof, in the presence of a strong base at a temperature of about 170230 C.
- an acylating agent selected from the group consisting of al
- the third step may be carried out at subatmospheric pressure, usually in distillation, or the metallic catalyst may be packed in a heated column.
- Acetic anhyride (26.7 g., 0.262 mole) was charged into the flask and the cyanoethyldodecylamine (67.5 g., 0.25 mole) added slowly with stirring. The temperature was maintained between 25 and 35 by external cooling and rate of addition of amine. One and a half hours were necessary for the addition. The reaction mixture was stirred for /2 hour after the addition was completed; after which excess acetic anhydride and acetic acid were removed under vacuum at 6085 C.
- the crude product was obtained with a residual acid value of 21.
- a one-liter, stainless steel autoclave was charged with N-acetyl-N-cyanoethyldodecylamine (480 g., 1.71 moles), Raney nickel (9.6 g, 2% by weight alcohol washed), and tetraethyl ammonium hydroxide (TEAH, 2% by weight).
- the vessel was flushed with hydrogen and heated to C. Hydrogen was then added to a total pressure of 300 p.s.i.g. The temperature and pressure were maintained at 140 C. and 300 p.s.i.g. for 2.5 hours.
- the catalyst was removed by filtration to yield a pale yellow to while solid on cooling, 405 g. (83.5% yield).
- N-acetyl-N-cyanoethyldodecylamine 845 g., 2.97 moles
- N-acetyl-N-dodecyl-l,3-propanediamine 39% N- acetyl-N-dodecyl 1,3 propanediamine
- the material distilling at 164-180/0.l0.35 mm. was collected as a light yellow oil, 705 g. (89% yield).
- a one-liter, stainless steel stirred autoclave was charged with N-acetyl-N-cyanoethyloctylamine (573 g., 2.56 moles) and Raney nickel catalyst (11.5 g. 2% by weight, alcohol washed).
- Ammonia was charged to a pressure of 125 p.s.i.g. at room temperature and the reaction mixture then heated to 130 C.
- Hydrogen was then added to a total pressure of 800 -p.s.i.g. The temperature and pressure were maintained at 130-l50 C. and 800 p.s.i.g. for 3-4 hours.
- the reaction product was filtered to remove the catalyst, then stripped under aspirator vacuum for 2 hours at 55 C.
- the product was obtained as an amber oil in 98% yield, 573 g.
- a one-liter, stainless steel autoclave was charged with N acetyl N cyanoethyloctadecylamine (361.4 g., 0.99 mole) and Raney nickel (7.2 g. 2% by weight alcohol washed).
- Ammonia was charged to a pressure of 125 p.s.i.g. at room temperature and the reaction mixture heated to 130 C.
- Hydrogen was then added to a total pressure of 800 p.s.i.g. Temperature and pressure were maintained at 130 and 800 p.s.i.g. for 3.5-4 hours.
- the catalyst was removed by filtration and excess ammonia stipped under reduced pressure.
- N-acetyl-N-octadecyl-1,3-propanediamine (622 g., 1.69
- N-l-cyanoethyldodecylamine (261.2 g., 1.09 moles), aqueous sodium hydroxide (51.4 g. in 117 ml. water) and 800 ml. of methylene chloride were charged into a fiveliter, three-necked flask.
- Benzo'yl chloride (150.9 g., 1.22 moles) was added slowly over sixty minutes at 5 C.
- the reaction mixture was then stirred for an additional ninety minutes at 5-10 C.
- the organic layer was separated, washed several times with water and dried over anhydrous sodium sulfate.
- Methylene chloride was distilled off under reduced pressure to yield 352 g. (94.4%) of product with a residual acid value of 4.1.
- the primary and secondary amine represents the two isomeric benzoyl N dodecyl 1,3 propanediamine.
- the tertiary amine is probably some tetrahydropyrimidine formed during the reduction.
- the high neutralization equivalent is due to the presence of a neutral material, probably N-dodecylbenzamide, formed by decyanoethylation of the starting material.
- the starting material had the following analysis: NE
- 1 Terttiary amine represents the amount of tetrahydropyrimidine presen 2 Percent Secondary amine.
- a process for preparing tetrahydropyrimidines the step of heating a compound selected from the group consisting of alkanoyland mono carbocyclic aroyl-N- aliphatic-1,3-propanediamine wherein the aliphatic group has from 8 to 22 carbon atoms in the presence of a catalyst selected from the group consisting of nickel, copper, cobalt, manganese, platinum, palladium, and the chloride, bromide, iodide, oxide, sulfate, carbonate, and acetate salts thereof, in the presence of a strong base at a temperature of about -230 C. at subatmospheric pressure.
- diamine is selected from the group consisting of acetyland benzoyl- 5.
- base is selected N-aliphatic-1,3-propanediamine. from the group consisting of potassium hydroxide, sodium 3.
- said catalyst is hydroxide and calcium hydroxide. present in from about 0.5 to 5 weight percent.
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Description
United States Patent ABSTRACT OF THE DISCLCSURE A process for'preparing tetrahydropyrimidines comprising reacting ,B-cyanoethyl aliphatic amines with an acylating agent, hydrogenating the N-acyl- N-B-cyanoethyl aliphatic amine to produce acyl-N-aliphatic-1,3- propanediamine, and bringing about closure of a 6 membered ring by heating the diamine in the presence of a metal catalyst or the salts thereof. The ring closure is especially satisfactory when conducted in the presence of nickel, copper, cobalt, manganese, platinum, palladium and the chloride, bromide, iodide, oxide, sulfate, carbonate, and acetate salts thereof, in the presence of a strong base at a temperature of about 170-230 C.
CROSS-REFERENCE TO RELATED APPLICATION This application is a continuation-in-part of our prior application Ser. No. 328,194, filed Dec. 5, 1963, now abandoned.
BACKGROUND OF THE INVENTION (1) Field of the invention This invention relates to a process for the production of tetrahydropyrimidines by a three step process:
( 1) Acylating a fl-cyanoet-hyl aliphatic amine, then (2) Catalytic hydrogenation to form acyl-N-aliphatic- 1,3-propanediamine, and
(3) Catalytic ring closure to yield 3-aliphatic-2-substituted-3,4,5,6-tetrahydropyrimidine.
(2) Description of the prior art Prior art methods of forming 2-substituted tetrahydropyrimidines have been the reaction of a monocarboxylic acid and a 1,3-propane diamine at temperatures within the range of '0-300 C. to produce cyclization. The lower temperature of about 250 C. has been utilized for ring closure when a chemical dehydrating agent has been employed. Even with the rigorous reaction conditions, these reactions required long periods of time.
3 aliphatic-Z-substituted tetrahydropyrimidines have been formed by heating equal moles of acetic acid and a N aliphatic 1,3-propanediamine at high temperatures to form the amide and then heating at about 250-300 C. and with a dehydrating agent to cyclize the monoamide to form the tetrahydropyrimidine. This reaction, even with the rigorous reaction conditions, results in low product yield due to the formation of diamide and difiiculty in ring closure of the monoamide which is formed.
SUMMARY preparations. A further object is to provide an improved process for the preparation of 3-aliphatic, 2-aliphatic or aromatic, 3,4,5,6-tetrahydropyrimidines and intermediates thereof through the formation of the acylated diamines and the use of metal catalysts for ring closure.
Other specific objects and advantages will appear as the specification proceeds.
In one embodiment of our invention, we react a ,9- cyanoethylaliphatic amine having from 8 to 22 carbon atoms which may be a straight or branched chain, saturated or unsaturated, with an aliphatic or aromatic acylating agent, such as an acid halide or acid anhydride, and then hydrogenating the resulting N-acyl-N-fl-cyaiioethyl amine over 'a nickel catalyst in the presence of a base. The resulting acyl-N-alkyl-1,3-propanediamine is then heated to yield the tetrahydropyrimidine product. In the final step, the acyl-N-alkyl-1,3-propanediamine may be distilled, preferably in vacuo, at a temperature of about -230" C. in the presence of 'a metal catalyst, such a nickel, copper, cobalt, manganese, platinum, palladium, and salts thereof, and preferably in the presence of a strong base selected from the group of potassium hydroxide, sodium hydroxide, calcium hydroxide, etc. Particularly useful catalysts may be selected from the group consisting of nickel, copper, cobalt, manganese, platinum, palladium, and the chloride, bromide, iodide, oxide, sulfate, carbonate, and acetate salts thereof. From about 0.5 to 5 weight percent catalyst is preferrred. The use of the catalysts has been found to be extremely effective in bringing about ring closure.
By way of illustration, the following specific example may be set out in detail, the example dealing with the preparation of 3 dodecyl-2-methyl-3,4,5,6-tetrahydropyrimidine, and the sequence reactions being set out as follows:
(1) B-cyanoethyldodecylamine was 'acylated with acetyl chloride.
RNHCHzCHzCN CHaCOCl RITIOHzCHzCN COCHs R=C12H25 (2) The product of reaction #1 was hydrogenated.
In Step 1 of the above reaction, fl-cy'anoethyldodecylamine was allowed to react with acetyl chloride, the resulting N-acetyl, N-B-cyanoethyldodecylamine was hydrogenated over a nickel catalyst in the presence of catstic. The product of the second reaction, namely, acyl-N- dodecyl-1,3-propanediamine, was distilled in the presence, of copper chloride at 200 C. in vacuo to yield 3-dodecyl- Z-methyl-3,4,5,6-tetrahydropyrimidine. As an alternate to the third step described above, the substituted 1,3-propanediamine was distilled at a temperature of from 180- 200" C. at 0.1-0.15 mm. in the presence of Raney nickel to cyclize the substituted 1,3-propanediamine. The metal catalyst may also be packed in a heated column and the diamine run through the column to achieve cyclization. The use of the nickel or other metal catalyst as described above has been found to be very effective for ring closure reaction. Heretofore the ring closure has been effected only by extremely high temperatures, strong dehydrating agents, and long reaction times. We believe that the metallic ion may function as a chelating agent which 3 brings the amidoamine into the correct position for ring closure, e.'g.,
NHCH: t! M++ OH;
R O NH-CI-Iz GHQ- In the foregoing process, the alkyl acid halide employed in the acylation step may have from 1 to 22 carbon atoms. Any aliphatic or aromatic acylating agent, such 'as acid halides, anhydrides, etc., may be employed.
In Reaction 1, as set out above, an aryl substituent may be inserted into the tetrahydropyrimidine ring at the 2-position in place of the methyl group by using an aromatic acylating agent, such as benzoyl chloride, 3,4- dichlorobenzoyl chloride, mixed dichlorobenzoyl chlorides, alkylated benzoyl chlorides, etc., thus producing aryl and substituted aryl derivatives of tetrahydropyrimidines.
The preferred acylating agent is selected from the group consisting of alkyl and mono-carbocyclic aryl acid halides and anhydrides thus forming a diamine selected from the group consisting of alkanoyland mono-carbocyclic aroyl-N-aliphatic-1,3-propanediamine, respectively.
Reaction 2 above ordinarily yields two isomers shown as I and II. The isomers I and H are found to be about equally divided in a mixture when the hydrogenation is carried out at about 300 p.s.i. H pressure. Reductions at higher pressures, for example, at 800 psi, caused almost complete isomerization of isomer I to isomer II, In the case of the octyl and octadecyl derivatives, isomer II was found to exist to the extent of 93-98 percent. This phenomenon involves migration of the acetyl group 0 I] CIIHG" from one nitrogen group to the other during reduction.
The starting material used in the preparation of the tetrahydro pyrimidine may be prepared by the known proc ess of cyanoethylation of the desired amine. For example, dodecylamine may be reacted with a slight excess of acrylonitrile in the presence of about 4 percent water at 70 C. for a period of 2 to 3 hours. The product, cyanoethyldodecylamine, is obtained in almost quantitative yield.
DESCRIPTION OF THE PREFERRED EMBODI- MENTS A preferred embodiment of this invention is the process for preparing 3 aliphatic-2-substituted-3,4,5,6-tetrahydropyrimidine, the steps of reacting fl-cyanoethyl aliphatic amines having 8 to 22 carbon atoms with an acylating agent selected from the group consisting of alkyl and monocarbocyclic aryl acid halides and anhydrides, hydrogenating the reacted product over a nickel catalyst under pressure and in the presence of a base to produce an acyl-N-aliphatic 1,3-propanediamine, and heating the hydrogenated product in the presence of a catalyst selected from the group consisting of nickel, copper, cobalt, manganese, platinum, palladium, and the chloride, bromide, iodide, oxide, sulfate, carbonate, and acetate salts thereof, in the presence of a strong base at a temperature of about 170230 C. at subatmospheric pressure.
The third step may be carried out at subatmospheric pressure, usually in distillation, or the metallic catalyst may be packed in a heated column.
Specific examples illustrative of our processes and treatment methods may be set out as follows:
EXAMPLE r N-acetyl-N-fl-cyanoethyldodeeylarnine was prepared as follows:
A two-liter, three-nicked flask, equipped with mechanical stirrer, addition funnel, reflux condenser, and thermometer, was charged with cyanoethyldodecylamine (227 g., 0.95 mole), methylene chloride (1070 g.) and aqueous caustic (44 g. NaOH in ml. H O). The mixture was cooled to -5 C. and acetyl chloride (82.5 g., 1.05 mole) in 100 ml. CH Cl Was added slowly, with stirring over 7 045 minutes. The reaction temperature was maintained at 0 to -10 by external cooling. The mixture was stirred for an additional O.51.0 hour after the addition was completed. The aqueous caustic layer was separated, the organic layer dried over anhydrous sodium sulfate, and stripped at 2530 C.
The product was obtained as a pale yellow oil, 259.6 g. (96% yield) with an acid value of 6.9.
EXAMPLE II N-acetyl-N-(,E-cyanoethyl)dodecylamine was prepared as follows:
Acetic anhyride (26.7 g., 0.262 mole) was charged into the flask and the cyanoethyldodecylamine (67.5 g., 0.25 mole) added slowly with stirring. The temperature was maintained between 25 and 35 by external cooling and rate of addition of amine. One and a half hours were necessary for the addition. The reaction mixture was stirred for /2 hour after the addition was completed; after which excess acetic anhydride and acetic acid were removed under vacuum at 6085 C.
The crude product was obtained with a residual acid value of 21.
EXAMPLE III N-acetyl-N-dodecyl-1,3-propanediamine was prepared as follows:
A one-liter, stainless steel autoclave was charged with N-acetyl-N-cyanoethyldodecylamine (480 g., 1.71 moles), Raney nickel (9.6 g, 2% by weight alcohol washed), and tetraethyl ammonium hydroxide (TEAH, 2% by weight). The vessel was flushed with hydrogen and heated to C. Hydrogen was then added to a total pressure of 300 p.s.i.g. The temperature and pressure were maintained at 140 C. and 300 p.s.i.g. for 2.5 hours. The catalyst was removed by filtration to yield a pale yellow to while solid on cooling, 405 g. (83.5% yield).
Analysis.Sec.-amide, 44.4%
H NmonmNEo 0H3] EXAMPLE IV N-dodecyl-2-methyl-3,4,5,6 tetrahydropyrimidine was prepared as follows:
The reduction product of N-acetyl-N-cyanoethyldodecylamine (845 g., 2.97 moles) containing about 45% of N-acetyl-N-dodecyl-l,3-propanediamine and 39% N- acetyl-N-dodecyl 1,3 propanediamine was subjected to distillation over 1% by weight CuCl -2H O and 5 KOH pellets through a 12-inch Vigreux column. The material distilling at 164-180/0.l0.35 mm. was collected as a light yellow oil, 705 g. (89% yield).
Analysis.-NE, 252 (calcd. 266.5); PA, 5.3%; SA. 13.4%; TA, 81.5%.
EXAMPLE V N-acetyl-N-cyanoethyloctylamine was prepared as follows:
A five-liter, three-necked flask, equipped with a mechanical stirrer, addition funnel. reflux condenser, and thermometer, was charged with cyanoethyloctylamine (1,065 g., 5.4 moles). Acetic anhydride (612 g., 6.0
moles) was added slowly, with stirring, over a period of 90 minutes. The temperature of the reaction mixture was maintained at 23-28 C. by external cooling. The mixture was stirred for an additional hour after the addition was completed. The acetic acid liberated in the reaction was removed by stripping at 75 C. at 1 mm; Hg until the acid value dropped to 8.
The product was obtained as a pale yellow oil in almost quantitative yield, 1,261 g.
EXAMPLE VI N-acetyl-N'-octyl-1,3-propanediamine was prepared as follows:
A one-liter, stainless steel stirred autoclave was charged with N-acetyl-N-cyanoethyloctylamine (573 g., 2.56 moles) and Raney nickel catalyst (11.5 g. 2% by weight, alcohol washed). Ammonia was charged to a pressure of 125 p.s.i.g. at room temperature and the reaction mixture then heated to 130 C. Hydrogen was then added to a total pressure of 800 -p.s.i.g. The temperature and pressure were maintained at 130-l50 C. and 800 p.s.i.g. for 3-4 hours. The reaction product was filtered to remove the catalyst, then stripped under aspirator vacuum for 2 hours at 55 C.
The product was obtained as an amber oil in 98% yield, 573 g.
Analysis.-NE, 215 (calcd. 228); PA, 5.7%; SA, 93.5%; TA, 6.8%.
EXAMPLE VII N-octyl-2-methyl-3,4,5,6-tetrahydropyrimidine was prepared as follows:
N acetyl N'-octyl-1,3-propanediamine .(567 g., 2.49 moles) was subjected to distillation over 1% by weight CuCl -2H O (5.67 g.) and 3pellets KOH through a 12- inch Vigreux column. The material distilling at 130- 153 C./3-3.5 mm. was collected as a pale yellow oil (403 g., 77% yield).
Analysis.-NE, 204.8 (calcd. 210.3); TA, 87.4%.
EXAMPLE VIII N-acetyl-N-cyanoethyloctadecylamine was prepared as follows:
A five-liter, creased flask, equipped with mechanical stirrer, addition funnel, and thermometer, was charged with cyanoethyloctadecylamine (976 g., 3.04 moles) and one-liter of ether. Acetic anhydride (346.8 g., 3.4 moles) was added slowly, with stirring, over a period of one hour. The temperature of the reaction mixture was maintained at 25-30" C., by external cooling. A thick white solid was formed during the addition, requiring additional solvent to keep the mixture as a slurry. The mixture was stirred for an additional 40 minutes after the addition was complete. The reaction product was diluted with petroleum ether, cooled, and filtered to yield 845 g. (77.5% yield) of white solid, AV=3.
EXAMPLE IX N acetyl N octadecyl-1,3-propanediamine was prepared as follows:
A one-liter, stainless steel autoclave was charged with N acetyl N cyanoethyloctadecylamine (361.4 g., 0.99 mole) and Raney nickel (7.2 g. 2% by weight alcohol washed). Ammonia Was charged to a pressure of 125 p.s.i.g. at room temperature and the reaction mixture heated to 130 C. Hydrogen Was then added to a total pressure of 800 p.s.i.g. Temperature and pressure were maintained at 130 and 800 p.s.i.g. for 3.5-4 hours. The catalyst was removed by filtration and excess ammonia stipped under reduced pressure.
The product was obtained in almost quantitative yield.
Analysis.-NE, 362 (calcd. 368); PA, 4.4%; SA, 97.1%; TA, nil.
EXAMPLE X N octadecyl 2 methyl-3,4,5,6-tetrahydropyrimidine was prepared as follows:
N-acetyl-N-octadecyl-1,3-propanediamine (622 g., 1.69
EXAMPLE XI N-benzoyl-N-cyanoethyldidecylamine was prepared as follows:
N-l-cyanoethyldodecylamine (261.2 g., 1.09 moles), aqueous sodium hydroxide (51.4 g. in 117 ml. water) and 800 ml. of methylene chloride were charged into a fiveliter, three-necked flask. Benzo'yl chloride (150.9 g., 1.22 moles) was added slowly over sixty minutes at 5 C. The reaction mixture was then stirred for an additional ninety minutes at 5-10 C. The organic layer was separated, washed several times with water and dried over anhydrous sodium sulfate. Methylene chloride was distilled off under reduced pressure to yield 352 g. (94.4%) of product with a residual acid value of 4.1.
EXAMPLE XII Benzoyl-N-dodecyl-1,3-propanediamine Was prepared as follows:
A 300 ml., stainless steel stirred autoclave was charged with N-benzoyl-N-cyanoethyldodecylamine (162 g., 0.47 mole) and Raney nickel catalyst (16.2 g. 10% by weight alcohol washed). Ammonia was added to 150 p.s.i./ 30 C., then hydrogen to a total pressureof 400 p.s.i./ 30 C. The temperature was raised to C. and the total pressure increased to 2000 psi. with hydrogen. The reduction required 10-11 hours, yielding g. (92.5%) of crude benzoyl-N-dodecyl-1,3-propanediamine.
Analysis.Neut. equiv., 510 (calcd. 344 PA, 13.7%; SA, 42.6%; TA, 12.4%.
Infrared analysis shows no nitrile present.
The primary and secondary amine represents the two isomeric benzoyl N dodecyl 1,3 propanediamine. The tertiary amine is probably some tetrahydropyrimidine formed during the reduction. The high neutralization equivalent is due to the presence of a neutral material, probably N-dodecylbenzamide, formed by decyanoethylation of the starting material.
EXAMPLE XIII N dodecyl 2 phenyl 3,4,5,6 tetrahydropyrimidine was prepared as follows:
Crude benzoyl N dodecyl 1,3 propanediamine (141.0 g. containing about 20% dodecylbenzamide) was distilled over 1% CuCl and a trace of potassium hydroxide at -220 C./1 mm. to yield 86.8 g. of crude N- dodecyl 2 phenyl 3,4,5,6 tetrahydropyrimidine.
Analysis.Neut. equiv. 53-8 (calcd. 328), PA-I-SA =1.0%, TA=56.7% (as tetrahydropyrimidine).
The dodecylbenzamide in the above was removed by crystallization from Skellysolve B and the tetrahydropyrimidine thus obtained redistilled as above to give 50 g. (37.5% crude yield) of a yellow oil.
Analysis.Neut. equiv. 405 (calcd. 328), PA-I-SA 1.0%, TA =81.6%.
Infrared analysis indicated the product to be predominantly tetrahydropyrimidine with some monosubstituted amide present.
EXAMPLE XIV The catalyst eifect of the various materials was determined by distillation of the N acetyl N' dodecyl 1,3 propanediamine in the presence of the catalyst and determining the amount of tetrahydropyrimidine in the distillljte. This information is summarized in the following ta e:
Analysis before Analysis after distillation distillation Percent of Compound R= CnHn Catalyst change Pyrimidine distilled N.E Sec. Sec. N.E Sec. See.
amide amine amide amine Wet 1R II RNH(CHz) NHC CH None 100.7 95. 6 278 24.9 98. 6
i RNH CH2 3NHC OH; CuSO 100. 7 95. 6 287 64. 3 97 i RNH(CH)3NHCCH KOH 100.7 95.6 268 43. 5 43. 3 41. 5 48.4 96. 6
ll RNH(CH2) NHC CH CuSO KOH 287. 5 101.3 98 261 68.8 97
i RNH(CH)3NHC CH3 CoClzKOH 100. 7 95. 6 266. 5 24 21.8 59. 5 66. 6 90 RbIKCH CN Ni(R)KOH 308 61. 5 68. 4 266 68. 4 77. 9 ca. 80
O O O 11 Reduction product IR analysis shows primary amine. The reduction product consists of a mixture of 6% tetrahydropyrimidine and 76% EXAMPLE XV N (B cyanoethyl) N Isobutyldodecylamine was prepared as follows:
A one-liter, four-neck creased flask equipped with a mechanical stirrer, thermometer, addition funnel and reflux condenser was charged with 217 g. (0.80 mole) of N-(fl-cyanoethyl) dodecylamine. Isobutyric anhydride of a mixture of its corresponding isomer, to N dodecyl 2 methyl 3,4,5,6 tetrahydropyrimidine. In each case distillation was carried out using a 35-40 gm. charge over 1 wt. percent of the copper salt and 1-2 KOH pellets. Distillation temperatures were in the range of 170230 C./0.31.0
The starting material had the following analysis: NE
(139 g., 0.88 mole) was added at 23-30 C. over a 30 :286 TA minute period, then the reaction mixture stirred overnight at room temperature. The entire reaction mixture was dis- The results are Shown in the following tabla? solved in ether and washed seven times with water and aqueous KOH to remove any free acid. The ether was PREPARATION on N-DODECYL-2-METHYL-3,4,5,6- stripped off under reduced pressure and 249.2 g. (92% r TETRAHYDROPYRIMIDINE mass yield) of product was obtained, leaving an acid value of Catalyst Percent Percent Percent Percent Dlstilled TA 1 SA 2 PA 3 EXAMPLE XVI N (B cyanoethyl) N Isobutyryldodecylamine was ggg 'g-g 1-? gag reduced as follows: 1 1 A one-liter pressure reaction vessel was charged with 8110 245.8 g. of N (cyanoethyl) N isobutyryldodecylamine and 9.8 g. (4% by wt.) of alcohol washed Raney nickel catalyst. Ammonia was then added to 125 p.s.i.g. at room temperature and the temperature raised to 135 C. The total pressure was made up to 800 p.s.i.g. at 135 C., with hydrogen. The reaction temperature and pressure was maintained for two hours, then cooled and filtered to give 239.6 g. (97.2% mass yield) of product having the following analysis:
NE=254 (calcd. 314), PA=76.7%, SA=11.4%, TA =11.9%.
EXAMPLE XVII N dodecyl 2 isopropyl 3,4,5,6 tetrahydropyrirnidine was prepared as follows:
The reduction product obtained in Example XVI (231 g.) was distilled over 1% (by wt.) CuCl and 2-4 KOH pellets through a Claisen head distillation column. A fraction distilling at 170-193 C./1.02.4 mm. was obtained representing 124.6 g. or 51.9% of the charge having the following analysis: NE=237 (calcd. 256), TA=66.3%.
EXAMPLE XVIII Various copper salts were used as catalysts for cyclization of N dodecyl N acetyl 1,3-propanediamine, or
1 Terttiary amine represents the amount of tetrahydropyrimidine presen 2 Percent Secondary amine.
3 Percent Primary amine.
While in the foregoing specification we have set forth procedural steps and treating materials in considerable detail for the purpose of illustrating our invention, it will be understood that such detail or details may be varied widely by those skilled in the art without departing from the spirit of our invention.
We claim:
1. In a process for preparing tetrahydropyrimidines, the step of heating a compound selected from the group consisting of alkanoyland mono carbocyclic aroyl-N- aliphatic-1,3-propanediamine wherein the aliphatic group has from 8 to 22 carbon atoms in the presence of a catalyst selected from the group consisting of nickel, copper, cobalt, manganese, platinum, palladium, and the chloride, bromide, iodide, oxide, sulfate, carbonate, and acetate salts thereof, in the presence of a strong base at a temperature of about -230 C. at subatmospheric pressure.
2. The process of claim 1 wherein said diamine is selected from the group consisting of acetyland benzoyl- 5. The process of claim 1 wherein said base is selected N-aliphatic-1,3-propanediamine. from the group consisting of potassium hydroxide, sodium 3. The process of claim 1 wherein said catalyst is hydroxide and calcium hydroxide. present in from about 0.5 to 5 weight percent.
4. The process of claim 1 wherein said catalyst is 5 No references citedselected from the group consisting of copper chloride and Raney i kel, NICHOLAS S. RIZZO, Primary Examiner.
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
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GB47718/64A GB1075295A (en) | 1963-12-05 | 1964-11-24 | Improvements in or relating to the preparation of tetrahydropyrimidines |
FR997472A FR1415468A (en) | 1963-12-05 | 1964-12-04 | Process for the preparation of tetrahydropyrimidines |
US610759A US3366634A (en) | 1963-12-05 | 1967-01-23 | Preparation of tetrahydropyrimidines |
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Application Number | Priority Date | Filing Date | Title |
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US32819463A | 1963-12-05 | 1963-12-05 | |
US610759A US3366634A (en) | 1963-12-05 | 1967-01-23 | Preparation of tetrahydropyrimidines |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4376201A (en) * | 1981-09-14 | 1983-03-08 | The Dow Chemical Company | Preparation of 2-alkylpyrimidines |
US4999427A (en) * | 1988-05-16 | 1991-03-12 | Dowelanco | Process for the preparation of 2-alkylpyrimidines |
US5180700A (en) * | 1991-05-13 | 1993-01-19 | Dowelanco | Regeneration and extension of lifetime of dehydrogenation catalysts used in the preparation of 2-alkylpyrimidines |
-
1964
- 1964-11-24 GB GB47718/64A patent/GB1075295A/en not_active Expired
-
1967
- 1967-01-23 US US610759A patent/US3366634A/en not_active Expired - Lifetime
Non-Patent Citations (1)
Title |
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None * |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4376201A (en) * | 1981-09-14 | 1983-03-08 | The Dow Chemical Company | Preparation of 2-alkylpyrimidines |
US4999427A (en) * | 1988-05-16 | 1991-03-12 | Dowelanco | Process for the preparation of 2-alkylpyrimidines |
US5180700A (en) * | 1991-05-13 | 1993-01-19 | Dowelanco | Regeneration and extension of lifetime of dehydrogenation catalysts used in the preparation of 2-alkylpyrimidines |
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