NO156407B - MIXTURES OF HALOGENATED AROMATIC ISOCYANATES WITH DIPHENYLMETAN STRUCTURE. - Google Patents
MIXTURES OF HALOGENATED AROMATIC ISOCYANATES WITH DIPHENYLMETAN STRUCTURE. Download PDFInfo
- Publication number
- NO156407B NO156407B NO831334A NO831334A NO156407B NO 156407 B NO156407 B NO 156407B NO 831334 A NO831334 A NO 831334A NO 831334 A NO831334 A NO 831334A NO 156407 B NO156407 B NO 156407B
- Authority
- NO
- Norway
- Prior art keywords
- mixture
- isomers
- mixtures
- isocyanate
- isocyanates
- Prior art date
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- 239000012948 isocyanate Substances 0.000 title claims abstract description 27
- 239000000203 mixture Substances 0.000 title claims description 59
- 150000002513 isocyanates Chemical class 0.000 title claims description 21
- -1 Halogenated aromatic isocyanates Chemical class 0.000 claims abstract description 5
- 125000004435 hydrogen atom Chemical group [H]* 0.000 claims abstract description 4
- BSZXAFXFTLXUFV-UHFFFAOYSA-N 1-phenylethylbenzene Chemical compound C=1C=CC=CC=1C(C)C1=CC=CC=C1 BSZXAFXFTLXUFV-UHFFFAOYSA-N 0.000 claims abstract description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N toluene Substances CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 21
- SYSQUGFVNFXIIT-UHFFFAOYSA-N n-[4-(1,3-benzoxazol-2-yl)phenyl]-4-nitrobenzenesulfonamide Chemical class C1=CC([N+](=O)[O-])=CC=C1S(=O)(=O)NC1=CC=C(C=2OC3=CC=CC=C3N=2)C=C1 SYSQUGFVNFXIIT-UHFFFAOYSA-N 0.000 claims description 15
- 150000001875 compounds Chemical class 0.000 claims description 2
- RYHSODLWMJUMBR-UHFFFAOYSA-N [chloro(isocyanato)methyl]benzene Chemical compound O=C=NC(Cl)C1=CC=CC=C1 RYHSODLWMJUMBR-UHFFFAOYSA-N 0.000 claims 3
- CMKXEDRUPCIUQS-UHFFFAOYSA-N 1-[chloro(isocyanato)methyl]-4-methylbenzene Chemical compound ClC(C1=CC=C(C=C1)C)N=C=O CMKXEDRUPCIUQS-UHFFFAOYSA-N 0.000 claims 1
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 42
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 27
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 18
- 239000000047 product Substances 0.000 description 15
- 239000002904 solvent Substances 0.000 description 15
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 13
- 150000001412 amines Chemical class 0.000 description 12
- 238000006243 chemical reaction Methods 0.000 description 12
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 11
- 238000000034 method Methods 0.000 description 11
- 229910017604 nitric acid Inorganic materials 0.000 description 11
- RFFLAFLAYFXFSW-UHFFFAOYSA-N 1,2-dichlorobenzene Chemical compound ClC1=CC=CC=C1Cl RFFLAFLAYFXFSW-UHFFFAOYSA-N 0.000 description 10
- 239000003054 catalyst Substances 0.000 description 10
- YGYAWVDWMABLBF-UHFFFAOYSA-N Phosgene Chemical compound ClC(Cl)=O YGYAWVDWMABLBF-UHFFFAOYSA-N 0.000 description 7
- 125000003118 aryl group Chemical group 0.000 description 7
- 238000006396 nitration reaction Methods 0.000 description 7
- 239000012074 organic phase Substances 0.000 description 7
- 238000009833 condensation Methods 0.000 description 6
- 230000005494 condensation Effects 0.000 description 6
- 238000004821 distillation Methods 0.000 description 6
- 238000004817 gas chromatography Methods 0.000 description 6
- 238000005984 hydrogenation reaction Methods 0.000 description 6
- 230000008018 melting Effects 0.000 description 6
- 238000002844 melting Methods 0.000 description 6
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 6
- 239000007787 solid Substances 0.000 description 6
- 239000000243 solution Substances 0.000 description 6
- 238000005727 Friedel-Crafts reaction Methods 0.000 description 5
- 239000012071 phase Substances 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- CAHQGWAXKLQREW-UHFFFAOYSA-N Benzal chloride Chemical compound ClC(Cl)C1=CC=CC=C1 CAHQGWAXKLQREW-UHFFFAOYSA-N 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 4
- 239000002253 acid Substances 0.000 description 4
- 238000001704 evaporation Methods 0.000 description 4
- 230000008020 evaporation Effects 0.000 description 4
- 238000001914 filtration Methods 0.000 description 4
- 229910052739 hydrogen Inorganic materials 0.000 description 4
- 239000001257 hydrogen Substances 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 238000004949 mass spectrometry Methods 0.000 description 4
- YCWSUKQGVSGXJO-NTUHNPAUSA-N nifuroxazide Chemical group C1=CC(O)=CC=C1C(=O)N\N=C\C1=CC=C([N+]([O-])=O)O1 YCWSUKQGVSGXJO-NTUHNPAUSA-N 0.000 description 4
- 229910052763 palladium Inorganic materials 0.000 description 4
- 239000011541 reaction mixture Substances 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- UVROAJFELBNMRA-UHFFFAOYSA-N (1-chloro-2-phenylethyl)benzene Chemical class C=1C=CC=CC=1C(Cl)CC1=CC=CC=C1 UVROAJFELBNMRA-UHFFFAOYSA-N 0.000 description 3
- 150000007513 acids Chemical class 0.000 description 3
- 238000004458 analytical method Methods 0.000 description 3
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- IQPQWNKOIGAROB-UHFFFAOYSA-N isocyanate group Chemical group [N-]=C=O IQPQWNKOIGAROB-UHFFFAOYSA-N 0.000 description 3
- 239000004814 polyurethane Substances 0.000 description 3
- 229920002635 polyurethane Polymers 0.000 description 3
- 229910000027 potassium carbonate Inorganic materials 0.000 description 3
- 238000003786 synthesis reaction Methods 0.000 description 3
- DLSXTGVHFBZELN-UHFFFAOYSA-N (2-chloro-1,2-dinitro-2-phenylethyl)benzene Chemical class C=1C=CC=CC=1C(Cl)([N+]([O-])=O)C([N+](=O)[O-])C1=CC=CC=C1 DLSXTGVHFBZELN-UHFFFAOYSA-N 0.000 description 2
- UPMLOUAZCHDJJD-UHFFFAOYSA-N 4,4'-Diphenylmethane Diisocyanate Chemical compound C1=CC(N=C=O)=CC=C1CC1=CC=C(N=C=O)C=C1 UPMLOUAZCHDJJD-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 238000005481 NMR spectroscopy Methods 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 2
- ZDVDCDLBOLSVGM-UHFFFAOYSA-N [chloro(phenyl)methyl]benzene Chemical compound C=1C=CC=CC=1C(Cl)C1=CC=CC=C1 ZDVDCDLBOLSVGM-UHFFFAOYSA-N 0.000 description 2
- 230000002378 acidificating effect Effects 0.000 description 2
- 150000001491 aromatic compounds Chemical class 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 239000007859 condensation product Substances 0.000 description 2
- 150000004985 diamines Chemical class 0.000 description 2
- JQVDAXLFBXTEQA-UHFFFAOYSA-N dibutylamine Chemical compound CCCCNCCCC JQVDAXLFBXTEQA-UHFFFAOYSA-N 0.000 description 2
- LYCAIKOWRPUZTN-UHFFFAOYSA-N ethylene glycol Natural products OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 125000005843 halogen group Chemical group 0.000 description 2
- 150000002430 hydrocarbons Chemical group 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
- 150000002828 nitro derivatives Chemical class 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 239000012299 nitrogen atmosphere Substances 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 229920005862 polyol Polymers 0.000 description 2
- 150000003077 polyols Chemical class 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 150000003613 toluenes Chemical class 0.000 description 2
- 239000008096 xylene Substances 0.000 description 2
- OFTPEPKEBMRIQQ-UHFFFAOYSA-N (1,1,2,2-tetrachloro-2-phenylethyl)benzene Chemical class C=1C=CC=CC=1C(Cl)(Cl)C(Cl)(Cl)C1=CC=CC=C1 OFTPEPKEBMRIQQ-UHFFFAOYSA-N 0.000 description 1
- FJEFRYPSCFFXEX-UHFFFAOYSA-N (1,2-dichloro-2-phenylethyl)benzene Chemical class C=1C=CC=CC=1C(Cl)C(Cl)C1=CC=CC=C1 FJEFRYPSCFFXEX-UHFFFAOYSA-N 0.000 description 1
- KLEAZMIFGFLZHP-UHFFFAOYSA-N (1,3-dichloro-1,3-diphenylpropan-2-yl)benzene Chemical class C=1C=CC=CC=1C(Cl)C(C=1C=CC=CC=1)C(Cl)C1=CC=CC=C1 KLEAZMIFGFLZHP-UHFFFAOYSA-N 0.000 description 1
- TWPKIBFRKXFXRJ-UHFFFAOYSA-N (1-bromo-2-phenylethyl)benzene Chemical class C=1C=CC=CC=1C(Br)CC1=CC=CC=C1 TWPKIBFRKXFXRJ-UHFFFAOYSA-N 0.000 description 1
- CFNNQXJXGXEKNA-UHFFFAOYSA-N (1-chloro-2,2-dinitro-2-phenylethyl)benzene Chemical compound C=1C=CC=CC=1C([N+]([O-])=O)([N+](=O)[O-])C(Cl)C1=CC=CC=C1 CFNNQXJXGXEKNA-UHFFFAOYSA-N 0.000 description 1
- AIPJZPPOFWCJRC-UHFFFAOYSA-N 1,2-dichloro-3-(chloromethyl)benzene Chemical compound ClCC1=CC=CC(Cl)=C1Cl AIPJZPPOFWCJRC-UHFFFAOYSA-N 0.000 description 1
- RYHBNJHYFVUHQT-UHFFFAOYSA-N 1,4-Dioxane Chemical compound C1COCCO1 RYHBNJHYFVUHQT-UHFFFAOYSA-N 0.000 description 1
- RGDYIHSZBVIIND-UHFFFAOYSA-N 1-(dichloromethyl)-4-methylbenzene Chemical compound CC1=CC=C(C(Cl)Cl)C=C1 RGDYIHSZBVIIND-UHFFFAOYSA-N 0.000 description 1
- KTMGVNLNWGXJSN-UHFFFAOYSA-N 1-chloro-1,2-diphenylethane-1,2-diamine Chemical class NC(C1=CC=CC=C1)(Cl)C(C1=CC=CC=C1)N KTMGVNLNWGXJSN-UHFFFAOYSA-N 0.000 description 1
- HIXDQWDOVZUNNA-UHFFFAOYSA-N 2-(3,4-dimethoxyphenyl)-5-hydroxy-7-methoxychromen-4-one Chemical compound C=1C(OC)=CC(O)=C(C(C=2)=O)C=1OC=2C1=CC=C(OC)C(OC)=C1 HIXDQWDOVZUNNA-UHFFFAOYSA-N 0.000 description 1
- KZNRNQGTVRTDPN-UHFFFAOYSA-N 2-chloro-1,4-dimethylbenzene Chemical group CC1=CC=C(C)C(Cl)=C1 KZNRNQGTVRTDPN-UHFFFAOYSA-N 0.000 description 1
- PSYVWXCTISIYHQ-UHFFFAOYSA-N 2-chloro-3-[chloro-(4-methylphenyl)methyl]-1,4-dimethylbenzene Chemical class ClC(C1=CC=C(C=C1)C)C=1C(=C(C=CC=1C)C)Cl PSYVWXCTISIYHQ-UHFFFAOYSA-N 0.000 description 1
- ZXVONLUNISGICL-UHFFFAOYSA-N 4,6-dinitro-o-cresol Chemical group CC1=CC([N+]([O-])=O)=CC([N+]([O-])=O)=C1O ZXVONLUNISGICL-UHFFFAOYSA-N 0.000 description 1
- NPDACUSDTOMAMK-UHFFFAOYSA-N 4-Chlorotoluene Chemical compound CC1=CC=C(Cl)C=C1 NPDACUSDTOMAMK-UHFFFAOYSA-N 0.000 description 1
- BWBREJBBPXXUBX-UHFFFAOYSA-N 5-[amino-chloro-(4-methylphenyl)methyl]-2-chloro-3,6-dimethylaniline Chemical class NC(C1=CC=C(C=C1)C)(Cl)C=1C(=C(C(=C(C=1)C)Cl)N)C BWBREJBBPXXUBX-UHFFFAOYSA-N 0.000 description 1
- RZVAJINKPMORJF-UHFFFAOYSA-N Acetaminophen Chemical compound CC(=O)NC1=CC=C(O)C=C1 RZVAJINKPMORJF-UHFFFAOYSA-N 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 description 1
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 1
- FYAUQRPGUUXFLL-UHFFFAOYSA-N [bromo(chloro)methyl]benzene Chemical compound ClC(Br)C1=CC=CC=C1 FYAUQRPGUUXFLL-UHFFFAOYSA-N 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 239000003849 aromatic solvent Substances 0.000 description 1
- KCXMKQUNVWSEMD-UHFFFAOYSA-N benzyl chloride Chemical class ClCC1=CC=CC=C1 KCXMKQUNVWSEMD-UHFFFAOYSA-N 0.000 description 1
- HIFVAOIJYDXIJG-UHFFFAOYSA-N benzylbenzene;isocyanic acid Chemical class N=C=O.N=C=O.C=1C=CC=CC=1CC1=CC=CC=C1 HIFVAOIJYDXIJG-UHFFFAOYSA-N 0.000 description 1
- 150000005524 benzylchlorides Chemical class 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 238000005660 chlorination reaction Methods 0.000 description 1
- MVPPADPHJFYWMZ-UHFFFAOYSA-N chlorobenzene Chemical compound ClC1=CC=CC=C1 MVPPADPHJFYWMZ-UHFFFAOYSA-N 0.000 description 1
- CELCMWUXMBTJRP-UHFFFAOYSA-N chlorobenzene;hydrochloride Chemical compound Cl.ClC1=CC=CC=C1 CELCMWUXMBTJRP-UHFFFAOYSA-N 0.000 description 1
- 150000001913 cyanates Chemical class 0.000 description 1
- 230000006735 deficit Effects 0.000 description 1
- 125000005442 diisocyanate group Chemical group 0.000 description 1
- OPTDDWCXQQYKGU-UHFFFAOYSA-N diphenyldichloromethane Chemical compound C=1C=CC=CC=1C(Cl)(Cl)C1=CC=CC=C1 OPTDDWCXQQYKGU-UHFFFAOYSA-N 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- RTZKZFJDLAIYFH-UHFFFAOYSA-N ether Substances CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 150000008282 halocarbons Chemical group 0.000 description 1
- 229910052736 halogen Inorganic materials 0.000 description 1
- 150000002367 halogens Chemical class 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000004811 liquid chromatography Methods 0.000 description 1
- 239000002075 main ingredient Substances 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical group C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 150000002829 nitrogen Chemical class 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 239000005056 polyisocyanate Substances 0.000 description 1
- 229920001228 polyisocyanate Polymers 0.000 description 1
- 229920001296 polysiloxane Polymers 0.000 description 1
- 239000005297 pyrex Substances 0.000 description 1
- 239000012429 reaction media Substances 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 229910052707 ruthenium Inorganic materials 0.000 description 1
- 229910052938 sodium sulfate Inorganic materials 0.000 description 1
- 235000011152 sodium sulphate Nutrition 0.000 description 1
- 239000008247 solid mixture Substances 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 238000004448 titration Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C265/00—Derivatives of isocyanic acid
- C07C265/12—Derivatives of isocyanic acid having isocyanate groups bound to carbon atoms of six-membered aromatic rings
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/70—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
- C08G18/72—Polyisocyanates or polyisothiocyanates
- C08G18/77—Polyisocyanates or polyisothiocyanates having heteroatoms in addition to the isocyanate or isothiocyanate nitrogen and oxygen or sulfur
- C08G18/773—Polyisocyanates or polyisothiocyanates having heteroatoms in addition to the isocyanate or isothiocyanate nitrogen and oxygen or sulfur halogens
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Polyurethanes Or Polyureas (AREA)
Abstract
Description
Foreliggende oppfinnelse angår blandinger av nye halogen- The present invention relates to mixtures of new halogen
erte aromatiske isocyanater som hydrokarbonskjelett har usymmetriske metyldifenylmetan- eller polymetyldifenyl- pea aromatic isocyanates whose hydrocarbon skeletons have unsymmetrical methyldiphenylmethane or polymethyldiphenyl
metanstruktur, substituert med et eller flere halogenatomer. methane structure, substituted with one or more halogen atoms.
Disse blandinger er brukbare ved fremstilling av polyure- These mixtures are useful in the production of polyurea-
taner og spesielt brannsikre skum. tanners and especially fireproof foams.
Isocyanatene med aromatisk hydrokarbondifenylmetanstruktur The isocyanates with aromatic hydrocarbon diphenylmethane structure
er allerede syntetisert industrielt; det dreier seg om derivater av difenylmetandiisocyanat (MDI), kommersialisert i uren form, dvs. i form av en blanding av diisocyanater og polyisocyanater, eller i ren form etter destillasjon. is already synthesized industrially; it concerns derivatives of diphenylmethane diisocyanate (MDI), commercialized in impure form, i.e. in the form of a mixture of diisocyanates and polyisocyanates, or in pure form after distillation.
I dette tilfelle er blandingen av isomerer som i det vesent- In this case, the mixture of isomers which is essentially
lige inneholder 4,4'-difenylmetandiisocyanat fast ved van- contains 4,4'-diphenylmethane diisocyanate solid at water
lig temperatur og oppviser et smeltepunkt mellom 3 0 og 4 0°C. equal temperature and has a melting point between 30 and 40°C.
Syntesen av polyuretaner gjennomføres ved omsetning av iso- The synthesis of polyurethanes is carried out by reacting iso-
cyanatene med polyoler. Brannsikre kvaliteter kan gis poly- the cyanates with polyols. Fireproof grades can be given poly-
merene ved å anvende halogenerte polyoler og/eller haloge- more by using halogenated polyols and/or halogenated
nerte additiver. Isocyanatene ifølge oppfinnelsen oppviser i seg selv et eller flere halogenatomer i de aromatiske ringer og er således spesielt interessante for fremstilling av polyuretaner med en god motstandsevne mot ild. nerdy additives. The isocyanates according to the invention have in themselves one or more halogen atoms in the aromatic rings and are thus particularly interesting for the production of polyurethanes with a good resistance to fire.
Isocyanatstrukturene i blandingene ifølge oppfinnelsen The isocyanate structures in the mixtures according to the invention
tilsvarer den generelle følgende formel: corresponds to the general following formula:
hvori X = Cl, Br where X = Cl, Br
n = 1, 2 n = 1, 2
x = 0, 1, 2 x = 0, 1, 2
y = 1, 2 y = 1, 2
z = 1, 2, og z = 1, 2, and
en av gruppene R^, , R3, R4 er en NCO-gruppe og one of the groups R^, , R3, R4 is an NCO group and
de andre er hydrogenatomer, idet mengden av NCO i blandingene er fra 4-6,7 ekvivalenter pr. kg. the others are hydrogen atoms, the amount of NCO in the mixtures being from 4-6.7 equivalents per kg.
Syntesene av isocyanatene skjer i tre etter hverandre følgende reaksjonsetapper ut fra en blanding av halogenerte aromatiske hydrokarboner: en nitrering, en hydrogenering og en fosgenering. The isocyanates are synthesized in three successive reaction stages from a mixture of halogenated aromatic hydrocarbons: a nitration, a hydrogenation and a phosgenation.
De halogenerte hydrokarbonstrukturer fremstilles ved Friedel-Crafts kondensasjon i nærvær av katalysatorer som generelt benyttes ved disse reaksjoner for halogenert benzyl-klorid, eventuelt substituert med en metylgruppe, med eventuelt halogenert toluen eller xylen benyttet i overskudd. Således oppnås forskjellige blandinger av halogenerte aromatiske isomerer. Avhengig av driftsbetingelsene og ved å regulere overskuddet av eventuelt halogenert toluen eller xylen, dannes det hovedsakelig kondensasjonsprodukter med to aromatiske kjerner, men produkter med tre kjerner kan også dannes og det hele tilsvarer den generelle formel: The halogenated hydrocarbon structures are produced by Friedel-Crafts condensation in the presence of catalysts which are generally used in these reactions for halogenated benzyl chloride, optionally substituted with a methyl group, with optionally halogenated toluene or xylene used in excess. Various mixtures of halogenated aromatic isomers are thus obtained. Depending on the operating conditions and by regulating the excess of any halogenated toluene or xylene, condensation products with two aromatic nuclei are mainly formed, but trinuclear products can also be formed and all correspond to the general formula:
der X = Cl eller Br, where X = Cl or Br,
x = 0 til 2, x = 0 to 2,
y = 1 eller 2, y = 1 or 2,
z = 1 eller 2, z = 1 or 2,
n = 1 eller 2. n = 1 or 2.
Det er mulig å separere isomerene med to kjerner fra reak-sjonsmediet ved destillasjon, men det kan være økonomisk gunstig å gjennomføre syntesen av isocyanatene i den urene reaksjonsblanding. I praksis inneholder reaksjonsproduktet mellom 70 og 95% diarylkondensater. It is possible to separate the dinuclear isomers from the reaction medium by distillation, but it may be economically advantageous to carry out the synthesis of the isocyanates in the impure reaction mixture. In practice, the reaction product contains between 70 and 95% diaryl condensates.
Blant de aromatiske hydrokarboner som benyttes som basis for oppfinnelsen kan isomerene av (klorbenzo)toluen syntetiseres på forskjellige måter, men det er foretrukket å omsette klorbenzylklorid, oppnådd ved kontrollert fotokje-misk klorering av monoklortoluen, med toluen i nærvær av en katalysator som benyttes ved slike reaksjoner; i dette tilfellet er således toluen det eneste hydrokarbonråstoff. Isomerene av (brombenzyl)toluen syntetiseres på samme måte ut fra brombenzylklorid. Among the aromatic hydrocarbons used as a basis for the invention, the isomers of (chlorobenzo)toluene can be synthesized in different ways, but it is preferred to react chlorobenzyl chloride, obtained by controlled photochemical chlorination of monochlorotoluene, with toluene in the presence of a catalyst used in such reactions; thus, in this case, toluene is the only hydrocarbon feedstock. The isomers of (bromobenzyl)toluene are synthesized in the same way from bromobenzyl chloride.
Syntesen av andre aromatiske hydrokarboner av (polyklor)-metyldifenylmetan eller (polyklor)(polymetyl)-difenylmetan er kjent og er beskrevet i FR-PS 2.432.199 og dettes tillegg 2.449.954. The synthesis of other aromatic hydrocarbons from (polychloro)-methyldiphenylmethane or (polychloro)(polymethyl)-diphenylmethane is known and is described in FR-PS 2,432,199 and its supplement 2,449,954.
De to etapper som utgjør nitreringen og deretter hydrogeneringen gir aminer som tilsvarer isocyanatstrukturene oppnådd ifølge oppfinnelsen: The two stages that make up the nitration and then the hydrogenation give amines that correspond to the isocyanate structures obtained according to the invention:
hvori X = Cl, Br, where X = Cl, Br,
n = 1, 2 n = 1, 2
x = 0, 1, 2, x = 0, 1, 2,
y = 1, 2, y = 1, 2,
z = 1, 2 og z = 1, 2 and
en av gruppene R'^, R^f R<*>3' R<*>4 er en NF^-gruppe, mens de andre er hydrogenatomer. one of the groups R'^, R^f R<*>3' R<*>4 is an NF^ group, while the others are hydrogen atoms.
For nitreringen benyttes det en blanding av salpetersyre For nitration, a mixture of nitric acid is used
og svovelsyre med en konsentrasjon på minst 85 vekt-%, fortrinnsvis minst 95 vekt-%. Salpetersyren kan benyttes i støkiometriske mengder i forhold til den aromatiske forbindelse. Således benyttes 1 mol syre for hver aromatiske kjerne som skal nitreres. Imidlertid er det fordelaktig å arbeide i nærvær av et overskudd av salpetersyre opptil 20% i forhold til støkiometrien. Svovelsyren kan benyttes i en ekvimolar mengde i forhold til salpetersyren, men kan også benyttes i overskudd eller underskudd. Nitrerings-reaksjonen gjennomføres ved temperaturer mellom 0°C og koketemperaturen for blandingen, generelt mellom 0°C og 50°C, idet den aromatiske forbindelse fortrinnsvis er opp-løst i et oppløsningsmiddel slik som metylenklorid. Den øvre, organiske fase separeres deretter fra syrene, nøytra-liseres og fordampes til tørr tilstand. Det er tilrådelig å arbeide under en nitrogenatmosfære i en reaktor utstyrt med midler for effektiv omrøring og temperaturregulering. and sulfuric acid with a concentration of at least 85% by weight, preferably at least 95% by weight. The nitric acid can be used in stoichiometric amounts in relation to the aromatic compound. Thus, 1 mole of acid is used for each aromatic nucleus to be nitrated. However, it is advantageous to work in the presence of an excess of nitric acid up to 20% relative to the stoichiometry. The sulfuric acid can be used in an equimolar amount in relation to the nitric acid, but can also be used in excess or deficit. The nitration reaction is carried out at temperatures between 0°C and the boiling temperature of the mixture, generally between 0°C and 50°C, the aromatic compound preferably being dissolved in a solvent such as methylene chloride. The upper organic phase is then separated from the acids, neutralized and evaporated to dryness. It is advisable to work under a nitrogen atmosphere in a reactor equipped with means for efficient stirring and temperature control.
Råblandingen som oppnås kan hydrogeneres som sådan. Imidlertid er det når diarylforbindelséne skal destilleres, mulig å isolere hovedisomerene fra disse ved oppløsning av blandingen i en minimal mengde metylenklorid og å felle dem ut ved hjelp av eter eller metanol. The crude mixture obtained can be hydrogenated as such. However, when the diaryl compounds are to be distilled, it is possible to isolate the main isomers from these by dissolving the mixture in a minimal amount of methylene chloride and to precipitate them using ether or methanol.
Det andre trinn er hydrogeneringen av nitroderivatene til The second step is the hydrogenation of the nitro derivatives to
de tilsvarende aminer; dert kan være kjemisk, men det er foretrukket å arbeide under hydrogentrykk i en trykkmotstands-dyktig reaktor utstyrt med røreverk og med konvensjonelle styrings- og reguleringsmidler i nærvær av en katalysator basert på nikkel, palladium, platina, ruthenium og lignende. I dette tilfellet benyttes det en hydrogeneringsreaktor som kan arbeide under trykk opptil 100 bar. Reaksjonen kan gjennomføres med et oppløsningsmiddel ved en temperatur the corresponding amines; there may be chemical, but it is preferred to work under hydrogen pressure in a pressure-resistant reactor equipped with agitators and with conventional control and regulation means in the presence of a catalyst based on nickel, palladium, platinum, ruthenium and the like. In this case, a hydrogenation reactor is used which can work under pressure of up to 100 bar. The reaction can be carried out with a solvent at a temperature
ved hvilken nitroderivatet smeltes eller i konvensjonelle hydrogeneringsoppløsninger slik som alkoholer, dioksan, etylenglykoletere og lignende. in which the nitro derivative is melted or in conventional hydrogenation solutions such as alcohols, dioxane, ethylene glycol ethers and the like.
Fortrinnsvis benyttes det en katalysator bestående av palladium avsatt på en bærer i mengder på mellom 1 og 10%, noe som gjør det mulig å arbeide ved temperaturer opptil mellom 30 og 100°C og under trykk fra 20-50 bar. Molforholdet mellom dinitroderivat og palladium er ikke fastlagt, men er fortrinnsvis mellom 200 og 3000. Etter reaksjon og filtrering av katalysatoren blir eventuelt oppløsningsmiddel dampet av og den oppnådde blanding av diaminisomerer kan benyttes som sådan eller destilleres. Preferably, a catalyst consisting of palladium deposited on a support is used in amounts of between 1 and 10%, which makes it possible to work at temperatures up to between 30 and 100°C and under pressure from 20-50 bar. The molar ratio between dinitro derivative and palladium is not determined, but is preferably between 200 and 3000. After reaction and filtration of the catalyst, any solvent is evaporated off and the obtained mixture of diamine isomers can be used as such or distilled.
Det tredje trinn gjør bruk av konvensjonell fosgenerings-teknikk i en reaktor utstyrt med røreverk og omgitt av en kjøler. Aminblandingen anbringes i et aromatisk klorert opplsningsmiddel slik som monoklorbenzen eller ortodiklorbenzen inneholdende den nødvendige mengde fosgen, men temperaturen holdes ved 0°C. Deretter oppvarmes suspensjonen progressivt; reaksjonsblandingen homogenisres ved mellom 45 og 60°C. Temperaturen heves langsomt til kokepunktet for blandingen og deretter destilleres oppløsningsmidlet av slik at de dannede isocyanater kan gjenvinnes. Disse kan destilleres hvis de er tilstrekkelig flyktige eller benyttes som de er. Blandingen av aminer anbringes fortrinnsvis i oppløsningsmidlet i en konsentrasjon fra 5-20% og fosgenet innføres i en støkiometrisk mengde eller i et lett overskudd. En annen metode består i samtidig innføring til reaktoren av en oppløsning, oppvarmet til over 100°C, The third stage makes use of conventional phosgenation techniques in a reactor equipped with agitators and surrounded by a cooler. The amine mixture is placed in an aromatic chlorinated solvent such as monochlorobenzene or orthodichlorobenzene containing the required amount of phosgene, but the temperature is kept at 0°C. The suspension is then progressively heated; the reaction mixture is homogenized at between 45 and 60°C. The temperature is slowly raised to the boiling point of the mixture and then the solvent is distilled off so that the isocyanates formed can be recovered. These can be distilled if they are sufficiently volatile or used as is. The mixture of amines is preferably placed in the solvent in a concentration of 5-20% and the phosgene is introduced in a stoichiometric amount or in a slight excess. Another method consists in the simultaneous introduction into the reactor of a solution, heated to over 100°C,
av aminene i et klorert aromatisk oppløsningsmiddel og en strøm av fosgen oppløst i det samme oppløsningsmiddel som oppvarmes til 120°C eller derover. Reaksjonen er så prak-tisk talt umiddelbar. of the amines in a chlorinated aromatic solvent and a stream of phosgene dissolved in the same solvent heated to 120°C or above. The reaction is practically immediate.
De således oppnådde isocyanater kan i henhold til kjente metoder gi polyuretaner med gode egenskaper, spesielt bedre The isocyanates thus obtained can, according to known methods, give polyurethanes with good properties, especially better ones
flammemotstandsevne. flame resistance.
, : N.itroderivatene og aminene er analysert ved gasskromatografi. Når det gjelder nitreringsproduktene, ble det benyttet en 3,17 mm rustfri stålkolonne med en lengde på 1,5 m, fylt med en "Chromosorb W" 80-100 mesh H.P.-bærer av kommersielt tilgjengelig type, impregnert med 2% XE.60 silikon-fase, også av kommersielt tilgjengelig type; under inji-seringen har kolonnen en temperatur på 100°C og etter 5 minutter oppvarmes den til 220°C. Det er også benyttes en Pyrex-kolonne med indre og ytre diametere på 3 og 6 mm og en lengde på 2 m, fylt med SP 2250-fase impregnert i en mengde av 3% på en "Supelcoport" 100-120 mesh bærer av kommersielt tilgjengelig type på hvilken det ble gjennomført lineær temperaturprogrammering med 4°C pr. minutt fra 180°C til 280°C. , : The nitrogen derivatives and amines have been analyzed by gas chromatography. As for the nitration products, a 3.17 mm stainless steel column of 1.5 m length was used, packed with a commercially available "Chromosorb W" 80-100 mesh H.P. support, impregnated with 2% XE.60 silicone phase, whether or not commercially available; during the injection the column has a temperature of 100°C and after 5 minutes it is heated to 220°C. Also used is a Pyrex column with inner and outer diameters of 3 and 6 mm and a length of 2 m, filled with SP 2250 phase impregnated in an amount of 3% on a "Supelcoport" 100-120 mesh carrier of commercial available type on which linear temperature programming was carried out with 4°C per minute from 180°C to 280°C.
Når det gjelder aminene, ble det benyttet en 2 meters glass-kolonne fylt med "Chromosorb" W.N.A.W. 60-80 mesh av kommersielt tilgjengelig type, impregnert med 5% KOH og 5% "Apiézon N" og arbeidet skjedde isotermt ved 220°C. In the case of the amines, a 2 meter glass column filled with "Chromosorb" W.N.A.W. was used. 60-80 mesh of a commercially available type, impregnated with 5% KOH and 5% "Apiézon N" and the work was carried out isothermally at 220°C.
Nitrerings- eller hydrogeneringsproduktene ble identifisert ved kombinering av gasskromatografi med massespektrometri. The nitration or hydrogenation products were identified by combining gas chromatography with mass spectrometry.
I enkelte tilfeller ble hovedisomeren isolert ved å fange dem ved gass- og/eller væskekromatografi og de ble identifisert ved kjernemagnetisk resonans av 13 C og <1>H. In some cases, the major isomer was isolated by trapping them by gas and/or liquid chromatography and they were identified by nuclear magnetic resonance of 13 C and <1>H.
Innholdet av isocyanatfunksjoner ble bedømt ved kjemisk titrering med dibutylamin. The content of isocyanate functions was assessed by chemical titration with dibutylamine.
EKSEMPEL 1 EXAMPLE 1
22 g eller 0,1 mol .. destillerte isomerer av (klorbenzyl)-toluen, fremstilt ved Friedel-Crafts-kondensasjon av klorbenzylklorid med toluen, oppløses i 40 ml metylenklorid. Mens temperaturen holdes ved ca. 10°C under omrøring, blir en blanding av 15,5 g 98,7%ig salpetersyre og 20 ml 96 %-ig svovelsyre helt inn i løpet av en h time. Så snart all 22 g or 0.1 mol .. distilled isomers of (chlorobenzyl)-toluene, prepared by Friedel-Crafts condensation of chlorobenzyl chloride with toluene, are dissolved in 40 ml of methylene chloride. While the temperature is kept at approx. 10°C with stirring, a mixture of 15.5 g of 98.7% nitric acid and 20 ml of 96% sulfuric acid is poured in over the course of one hour. So soon all
blanding er tilsatt, tilbakeløpskokes den resulterende blanding i 3 timer og 30 minutter under ytterligere omrøring og deretter avkjøles det hele. Det skiller seg ut to faser, en nedre sur fase og en øvre organisk fase. Den organiske fase ekstraheres og syrene vaskes to ganger med metylenklorid. De forskjellige organiske fraksjoner kombineres, nøytraliseres på kaliumkarbonat og oppløsningsmidlet fordampes. Således gjenvinnes 30,5 g av et viskøst lett gult produkt; når dette analyseres ved gasskromatografi koplet med massespektrometri oppdages isomerer av (nitroklorbenzyl) - nitrotoluen. Hovedbestanddelen av blandingen er 3,3'-dinitro-4-metyl-4'-klor-difenylmetan med formelen: 20 g av denne blanding av isomerer anbringes i autoklaven som er beskrevet ovenfor og 200 ml metanol og 0,2 g katalysator bestående av 5% palladium på trekull tilsettes. Etter at reaktoren er spylt med nitrogen, innføres 40 bar hydrogen og reaktoren oppvarmes til 60°C under omrøring. Etter 3 timer og 20 minutters reaksjonstid blir reaktoren satt hen til avkjøling og trykkavlastning og reaksjonsblandingen gjenvinnes og filtreres for å fjerne katalysator. Metanolen fordampes til tørr tilstand og 16 g av et meget tykt mørke-brunt produkt oppnås. Ana-lyse ved gasskromatograf i koplet med massespektrometri viser at det inneholder isomerer av (aminoklorbenzyl)-aminotoluen. 12 g av disse tilsettes til en oppløsning av 29 g fosgen i 100 ml ortodiklorbenzen, mens temperaturen holdes ved 0°C. Deretter tillates det hele å vende tilbake til omgivelsestemperatur, oppvarmes deretter til 45°C i en time, til 60°C i en time og til 100°C i h time. Til slutt blir ved å føre gjennom en nitrogenstrøm temperaturen bragt til 140°C i 2 timer for å fjerne overskytende fosgen og dannet saltsyre. Deretter blir oppløsningsmidlet destillert av i vakuum etter at oppløsningen er filtrert, hvoretter det oppnås 13 g av en blanding av isocyanater med et NCO-innhold tilsvarende 5 ekvivalenter pr. kg, hvis destillasjon gir en gul væske bestående av en blanding av klorbenzyltoluendiisocyanater med NCO-innhold: 2 funksjoner pr. mol, tilsvarende den generelle formel angitt ovenfor, mixture is added, the resulting mixture is refluxed for 3 hours and 30 minutes with further stirring and then the whole is cooled. Two phases stand out, a lower acidic phase and an upper organic phase. The organic phase is extracted and the acids are washed twice with methylene chloride. The various organic fractions are combined, neutralized on potassium carbonate and the solvent is evaporated. Thus, 30.5 g of a viscous light yellow product is recovered; when this is analyzed by gas chromatography coupled with mass spectrometry, isomers of (nitrochlorobenzyl) - nitrotoluene are detected. The main component of the mixture is 3,3'-dinitro-4-methyl-4'-chloro-diphenylmethane of the formula: 20 g of this mixture of isomers is placed in the autoclave described above and 200 ml of methanol and 0.2 g of catalyst consisting of 5% palladium on charcoal is added. After the reactor has been flushed with nitrogen, 40 bar hydrogen is introduced and the reactor is heated to 60°C with stirring. After 3 hours and 20 minutes of reaction time, the reactor is allowed to cool and depressurize and the reaction mixture is recovered and filtered to remove catalyst. The methanol is evaporated to dryness and 16 g of a very thick dark-brown product is obtained. Analysis by gas chromatograph coupled with mass spectrometry shows that it contains isomers of (aminochlorobenzyl)-aminotoluene. 12 g of these are added to a solution of 29 g of phosgene in 100 ml of orthodichlorobenzene, while the temperature is kept at 0°C. The whole is then allowed to return to ambient temperature, then heated to 45°C for one hour, to 60°C for one hour and to 100°C for h hour. Finally, by passing through a stream of nitrogen, the temperature is brought to 140°C for 2 hours to remove excess phosgene and formed hydrochloric acid. The solvent is then distilled off in vacuum after the solution has been filtered, after which 13 g of a mixture of isocyanates with an NCO content corresponding to 5 equivalents per kg, whose distillation gives a yellow liquid consisting of a mixture of chlorobenzyltoluene diisocyanates with NCO content: 2 functions per moles, corresponding to the general formula given above,
der X = Cl, x = 0, y = 1, z = 1, n = 1. where X = Cl, x = 0, y = 1, z = 1, n = 1.
EKSEMPEL 2 EXAMPLE 2
138 g av blandingen av isomerer av (klorbenzyl)-toluener som fremstilt i eksempel 1 oppløses i 240 ml metylenklorid. 138 g of the mixture of isomers of (chlorobenzyl)-toluenes as prepared in example 1 are dissolved in 240 ml of methylene chloride.
Ved å benytte den samme prosedyre som i eksempel 1, tilsettes en blanding av 93 g 98,3 %-ig salpetersyre og 120 ml 96 %-ig svovelsyre. Blandingen kokes under tilbakeløp i Using the same procedure as in example 1, a mixture of 93 g of 98.3% nitric acid and 120 ml of 96% sulfuric acid is added. The mixture is boiled under reflux in
4 timer og 30 minutter, avkjøles så hvoretter den organiske fase ekstraheres. Oppløsningsmidlet fordampes til grensen av oppløseligheten av dinitreringsisomerene, hvoretter metanol tilsettes og på denne måte felles det ut et hvitt fast stoff som filtreres av og vaskes med metanol. Etter tørking oppnås 21,5 g av et hvitt fast stoff med et smeltepunkt på 183°C. Analyse ved gasskromatografi viser klart overveiende nærvær av en isomer av dinitro(klorbenzyl)toluen som identifiseres ved kjernemagnetisk resonans til 3,3'-dinitro-l-metyl-4<1->klor-difenylmetan: 4 hours and 30 minutes, then cooled, after which the organic phase is extracted. The solvent is evaporated to the limit of the solubility of the dinitration isomers, after which methanol is added and in this way a white solid precipitates which is filtered off and washed with methanol. After drying, 21.5 g of a white solid with a melting point of 183°C are obtained. Analysis by gas chromatography clearly shows the predominant presence of an isomer of dinitro(chlorobenzyl)toluene which is identified by nuclear magnetic resonance to 3,3'-dinitro-1-methyl-4<1->chloro-diphenylmethane:
Det metanoliske filtrat inneholder resten av denne overveiende isomer og de andre dinitreringsisomerer. The methanolic filtrate contains the remainder of this predominant isomer and the other dinitration isomers.
20 g av utfellingen hydrogeneres ved bruk av prosedyren som beskrevet i eksempel 2 med 200 ml metanol og 0,4 g 5% Pd på trekull. Etter fordamping av metanolen oppnås 16 g av et pastalignende mørkebrunt produkt, i det vesentlige bestående 20 g of the precipitate is hydrogenated using the procedure described in example 2 with 200 ml of methanol and 0.4 g of 5% Pd on charcoal. After evaporation of the methanol, 16 g of a paste-like dark brown product is obtained, essentially consisting of
av 3,3'-diamino-4-metyl-4<1->klor-difenylmetan. of 3,3'-diamino-4-methyl-4<1->chloro-diphenylmethane.
Deretter gjennomføres fosgeneringen ved bruk av prosedyren som beskrevet i eksempel 1 på 10 g av denne blanding av aminer. således blir 12 g av det pastalignende brune produkt gjenvunnet (NCO-innhold: 6 ekvivalenter pr. kg) som, ved destillasjon under et redusert trykk på 2 mm Hg, gir et pastalignende lett brunt faststoff som helt smelter ved 64°C og som inneholder ca. 66% 4-metyl-4<1->klor-difenylmetan-3,3'-diisocyanat (NCO-innhold: 2 ekvivalenter prl mol). The phosgenation is then carried out using the procedure as described in example 1 on 10 g of this mixture of amines. thus 12 g of the paste-like brown product is recovered (NCO content: 6 equivalents per kg) which, on distillation under a reduced pressure of 2 mm Hg, gives a paste-like light brown solid completely melting at 64°C and containing about. 66% 4-methyl-4<1->chloro-diphenylmethane-3,3'-diisocyanate (NCO content: 2 equivalents per mol).
EKSEMPEL 3 EXAMPLE 3
25,1 g eller 0,1 mol av en blanding av isomerer av (klor-benzyl ) klortoluen , syntetisert fra klortoluener som beskrevet i FR-PS 2.432.199, anbringes i en omrørt 250 ml reaktor under en nitrogenatmosfære. 40 ml metylenklorid tilsettes og i løpet av en ^ time og i mellom 5 og 15°C innføres en blanding av 13,5 g 98,3 %-ig salpetersyre og 20 ml 96 %-ig svovelsyre. Blandingen oppvarmes deretter til 42°C i 3 timer og 30 minutter, avkjøles deretter og dekanteres. Den øvre, organiske fase gjenvinnes og nedre sure fase vaskes med metylenklorid. De organiske ekstrakter som oppnås fra av-trekking og vasking, blandes, nøytraliseres med kaliumkarbonat og tørkes med natriumsulfat. Det oppnås en klar, orangefarget oppløsning som fordampes til tørr tilstand. På denne måte oppnås 32 g meget viskøs orangefarget væske tilsvarende en blanding av isomerer av (nitroklorbenzyl)-nitrotoluen. Hovedbestanddelene i blandingen er 2,3'-dinitro-5-metyl-4,2'-diklor-difenylmetan med formelen: 25.1 g or 0.1 mol of a mixture of isomers of (chloro-benzyl) chlorotoluene, synthesized from chlorotoluenes as described in FR-PS 2,432,199, is placed in a stirred 250 ml reactor under a nitrogen atmosphere. 40 ml of methylene chloride is added and, over the course of an hour and between 5 and 15°C, a mixture of 13.5 g of 98.3% nitric acid and 20 ml of 96% sulfuric acid is introduced. The mixture is then heated to 42°C for 3 hours 30 minutes, then cooled and decanted. The upper organic phase is recovered and the lower acidic phase is washed with methylene chloride. The organic extracts obtained from stripping and washing are mixed, neutralized with potassium carbonate and dried with sodium sulfate. A clear, orange-coloured solution is obtained which is evaporated to dryness. In this way, 32 g of very viscous orange-coloured liquid corresponding to a mixture of isomers of (nitrochlorobenzyl)-nitrotoluene is obtained. The main ingredients in the mixture are 2,3'-dinitro-5-methyl-4,2'-dichloro-diphenylmethane with the formula:
2,3'-dinitro-5-metyl-4,4<1->diklor-difenylmetan med formelen: 3,3'-dinitro-4-metyl-5,4'-diklor-difenylmetan med formelen: 3,3'-dinitro-5-metyl-4,4'-diklor-difenylmetan med formelen: 30 g av denne væske hydrogeneres i en rustfri stålautoklav utstyrt med magnetrører i nærvær av 0,3 g 5% palladium på trekull (ENGELHARD) som katalysator og 300 ml metanol. Reaksjonen tar 1 time og 30 minutter under et trykk på 35 bar og ved 50°C, deretter tømmes reaktoren og etter fordamping av oppløsningsmidlet oppnås 24,5 g av et orange faststoff som smelter ved 45-47°C. Analyse ved gasskromatografi viser at den består av isomerer av det ventede diamin tilsvarende den generelle formel ifølge oppfinnelsen, hvori X = Cl, 2,3'-dinitro-5-methyl-4,4<1->dichloro-diphenylmethane with the formula: 3,3'-dinitro-4-methyl-5,4'-dichloro-diphenylmethane with the formula: 3,3' -dinitro-5-methyl-4,4'-dichloro-diphenylmethane with the formula: 30 g of this liquid is hydrogenated in a stainless steel autoclave equipped with magnetic stirrers in the presence of 0.3 g of 5% palladium on charcoal (ENGELHARD) as catalyst and 300 ml of methanol. The reaction takes 1 hour and 30 minutes under a pressure of 35 bar and at 50°C, then the reactor is emptied and after evaporation of the solvent, 24.5 g of an orange solid is obtained which melts at 45-47°C. Analysis by gas chromatography shows that it consists of isomers of the expected diamine corresponding to the general formula according to the invention, in which X = Cl,
x = 1, y = 1, z = 1, n = 1. x = 1, y = 1, z = 1, n = 1.
Blandingen av aminer fosgeneres ved bruk av de ovenfor beskrevne metoder. Etter reaksjon og fordamping av oppløs-ningsmidlet oppnås 29 g av en uren blanding av isocyanater (NCO-innhold: 5,2 ekvivalenter pr. kg) som, etter destillasjon under et redusert trykk på 2 mm Hg, gir en viskøs gul væske bestående av isomerer av de ventede isocyanater (NCO-innhold: 2 funksjoner pr. mol). The mixture of amines is phosgenerated using the methods described above. After reaction and evaporation of the solvent, 29 g of an impure mixture of isocyanates are obtained (NCO content: 5.2 equivalents per kg) which, after distillation under a reduced pressure of 2 mm Hg, gives a viscous yellow liquid consisting of isomers of the expected isocyanates (NCO content: 2 functions per mol).
EKSEMPEL 4 EXAMPLE 4
27,9 g eller 0,1 mol isomerer av (klor-parametylbenzyl)-klorparaxylen, fremstilt ved Friedel-Crafts kondensering av klorparametylbenzylklorid ved omsetning av dette med klorparaxylen, oppløses i 40 ml metylenklorid. Temperaturen holdes ved ca. 10°C, blandingen omrøres og i løpet av en h time tilføres en blanding av 15,5 g 98,7 %-ig salpetersyre og 20 ml 96 %-ig svovelsyre. Blandingen kokes under tilbakeløp i 3 timer og 30 minutter og avkjøles deretter. Den øvre organiske fase gjenvinnes og syrene vaskes med metylenklorid. De organiske faser kombineres og behandles med kaliumkarbonat, hvoretter oppløsningsmidlet fordampes. Således gjenvinnes 36 g dinitreringsprodukter tilsvarende den følgende formel: 27.9 g or 0.1 mol of isomers of (chloro-paramethylbenzyl)-chloroparaxylene, prepared by the Friedel-Crafts condensation of chloroparamethylbenzyl chloride by reacting this with chloroparaxylene, are dissolved in 40 ml of methylene chloride. The temperature is kept at approx. 10°C, the mixture is stirred and, over the course of one hour, a mixture of 15.5 g of 98.7% nitric acid and 20 ml of 96% sulfuric acid is added. The mixture is refluxed for 3 hours and 30 minutes and then cooled. The upper organic phase is recovered and the acids are washed with methylene chloride. The organic phases are combined and treated with potassium carbonate, after which the solvent is evaporated. Thus, 36 g of dinitration products are recovered corresponding to the following formula:
20 g av denne blanding hydrogeneres ved bruk av den metode som er beskrevet i eksempel 1, med 0,2 1 metanol og 0,4 g 5% Pd/trekull som katalysator. Etter at metanolen er destillert av, gjenvinnes 16,5 g rødaktig krystallinsk produkt med smeltepunkt 73°C, i det vesentlige tilsvarende isomerer av (amino-klor-parametyl-benzyl)-amino-klor-para-xylen. 15 g av denne blanding fosgeneres ved bruk av den metode som er beskrevet i eksempel 1. Etter filtrering og destillering av ortodiklorbenzen, gjenvinnes 15 g av et urent brunt produkt med smeltepunkt 49°C og inneholdende en blanding av de ventede isocyanater (NCO-innhold: 4,4 ekvivalen ter pr. kg), tilsvarende den generelle formel som gis i beskrivelsen, hvori X = Cl, x = 1, y = 1, z = 2, n = 1. 20 g of this mixture is hydrogenated using the method described in example 1, with 0.2 l of methanol and 0.4 g of 5% Pd/charcoal as catalyst. After the methanol has been distilled off, 16.5 g of reddish crystalline product with a melting point of 73°C are recovered, essentially corresponding isomers of (amino-chloro-paramethyl-benzyl)-amino-chloro-para-xylene. 15 g of this mixture is phosgenerated using the method described in example 1. After filtering and distilling orthodichlorobenzene, 15 g of an impure brown product with a melting point of 49°C and containing a mixture of the expected isocyanates (NCO content : 4.4 equiv ter per kg), corresponding to the general formula given in the description, where X = Cl, x = 1, y = 1, z = 2, n = 1.
EKSEMPEL 5 EXAMPLE 5
Friedel-Crafts kondensering av klorbenzylklorid med toluen gir i tillegg til diarylforbindelsene som behandles i eksempel 1, kondensasjonsprodukter med tre aromatiske kjerner. Forbindelser med to kjerner tilsvarende isomerene av (klorbenzyl)toluen, kan separeres ved destillering, The Friedel-Crafts condensation of chlorobenzyl chloride with toluene gives, in addition to the diaryl compounds treated in Example 1, condensation products with three aromatic nuclei. Compounds with two nuclei corresponding to the isomers of (chlorobenzyl)toluene can be separated by distillation,
mens triarylderivatene forblir i kolonnebunnen. while the triaryl derivatives remain at the bottom of the column.
34 g av en blanding bestående i det vesentlige av isomerer av bis-(klorbenzyl)toluen nitreres i henhold til den prosedyre som er beskrevet i eksempel 1 ved bruk av 23,2 g 98,7 %-ig salpetersyre og 20,2 ml 96 %-ig svovelsyre. Ved slutten av reaksjonen gjenvinnes 48 g av et meget viskøst rødaktig produkt, hvorav 2 0 g hydrogeneres ved å anbringe dem i en autoklav med 200 ml metanol og 0,6 g 5 %-ig palladium på trekull (ENGELHARD) som katalysator under et trykk på 40 bar hydrogen og ved 65°C. På denne måte oppnås 14,5 g av en uren blanding av aminer med smeltepunkt 12 7°C som omsettes med 33 g fosgen som beskrevet i eksempel 1. Etter filtrering av reaksjonsblandingen med ortodiklorbenzen fordampes oppløsningsmidlet og man gjenvinner 13 g av et urent produkt som smelter ved 124°C og inneholder isocyanatiso-merer i henhold til den generelle formel ifølge oppfinnelsen, der X = Cl, x = O, y = 1, z=logn=2 (NCO-innhold: 4,4 funksjoner pr. kg). 34 g of a mixture consisting essentially of isomers of bis-(chlorobenzyl)toluene is nitrated according to the procedure described in example 1 using 23.2 g of 98.7% nitric acid and 20.2 ml 96 % sulfuric acid. At the end of the reaction, 48 g of a very viscous reddish product are recovered, of which 20 g are hydrogenated by placing them in an autoclave with 200 ml of methanol and 0.6 g of 5% palladium on charcoal (ENGELHARD) as a catalyst under pressure of 40 bar hydrogen and at 65°C. In this way, 14.5 g of an impure mixture of amines with a melting point of 12 7°C are obtained, which is reacted with 33 g of phosgene as described in example 1. After filtering the reaction mixture with orthodichlorobenzene, the solvent is evaporated and 13 g of an impure product is recovered which melts at 124°C and contains isocyanate isomers according to the general formula according to the invention, where X = Cl, x = O, y = 1, z=logn=2 (NCO content: 4.4 functions per kg) .
EKSEMPEL 6 EXAMPLE 6
Ved å benytte den metode som er beskrevet i eksempel 1 nitreres en uren Friedel-Crafts kondensasjonsblanding av klorbenzenklorid og toluen innholdende 85 vekt-% diaryl-derivater og 15 % i det vesentlige triarylderivater med 18,7 g 98,7 %-ig salpetersyre og 21,5 ml 96 %-ig svovelsyre. Etter reaksjon oppnås det 32 g av et halvfast halv-viskøst nitreringsprodukt, hvorav 20 g hydrogeneres i 200 ml metanol i nærvær av 0,8 g 5 %-ig palladium-på-trekull By using the method described in example 1, an impure Friedel-Crafts condensation mixture of chlorobenzene chloride and toluene containing 85% by weight diaryl derivatives and 15% essentially triaryl derivatives is nitrated with 18.7 g of 98.7% nitric acid and 21.5 ml of 96% sulfuric acid. After reaction, 32 g of a semi-solid, semi-viscous nitration product are obtained, of which 20 g are hydrogenated in 200 ml of methanol in the presence of 0.8 g of 5% palladium-on-charcoal
(ENGELHARD) under et hydrogentrykk på 40 bar og ved 65°C. Etter reaksjon og fordamping av metanolen innsamles 15 g (ENGELHARD) under a hydrogen pressure of 40 bar and at 65°C. After reaction and evaporation of the methanol, 15 g are collected
av en uren blanding av aminer som omsettes med 36,2 g fosgen som beskrevet i eksempel 1. Etter filtrering av reaksjonsoppløsningen med ortodiklorbenzen fordampes oppløs-ningsmidlet og 13,8 g av et pastalignende brunt produkt gjenvinnes og dette settes til hård avkjøling. Undersøkelse av produktet ved massespektrometri viser at det inneholder isomerer av diarylisocyanater og triarylisocyanater tilsvarende den grove formel i beskrivelsen der X = Cl, x = 0, y=l, z=logn=log2. Denne blanding av isocyanater som lett kan helles ved 60°C har et innhold av NCO-funksjoner på 5,4 ekvivalenter pr. kg. of an impure mixture of amines which is reacted with 36.2 g of phosgene as described in example 1. After filtering the reaction solution with orthodichlorobenzene, the solvent is evaporated and 13.8 g of a paste-like brown product is recovered and this is allowed to hard cool. Examination of the product by mass spectrometry shows that it contains isomers of diarylisocyanates and triarylisocyanates corresponding to the rough formula in the description where X = Cl, x = 0, y=l, z=logn=log2. This mixture of isocyanates which can be easily poured at 60°C has a content of NCO functions of 5.4 equivalents per kg.
EKSEMPEL 7 EXAMPLE 7
Ved bruk av 15,5 g 98,7 %-ig salpetersyre og 20 ml 96 %-ig svovelsyre nitreres under de betingelser som er beskrevet i eksempel 1, 32 g av en blanding av isomerer av (diklor-benzyl)diklortoluen fremstilt ved Friedel-Crafts kondensering av diklorbenzylklorid med diklortoluen. 39 g av en meget viskøs orangefarget blanding oppnås. 30 g av denne blanding hydrogeneres i nærvær av 0,3 g 5% palladium-på-trekull (ENGELHARD) i 300 ml metanol ved 60°C under et trykk på 40 bar, noe som gir 25 g av en fast blanding av aminer med mørk brun farge og som fosgeneres under de ovenfor beskrevne betingelser. Til slutt oppnås 28 g råblanding av isocyanater (NCO-innhold: 4,1 ekvivalenter pr. kg) tilsvarende den generelle formel som er gitt i beskrivelsen, hvori X = Cl, x = 2, y = 2, z = 1, n = 1. Using 15.5 g of 98.7% nitric acid and 20 ml of 96% sulfuric acid, 32 g of a mixture of isomers of (dichloro-benzyl)dichlorotoluene produced by Friedel are nitrated under the conditions described in example 1 -Crafts condensation of dichlorobenzyl chloride with dichlorotoluene. 39 g of a very viscous orange colored mixture is obtained. 30 g of this mixture is hydrogenated in the presence of 0.3 g of 5% palladium-on-charcoal (ENGELHARD) in 300 ml of methanol at 60°C under a pressure of 40 bar, giving 25 g of a solid mixture of amines with dark brown color and which phosgenerates under the conditions described above. Finally, 28 g of crude mixture of isocyanates (NCO content: 4.1 equivalents per kg) is obtained corresponding to the general formula given in the description, in which X = Cl, x = 2, y = 2, z = 1, n = 1.
Claims (6)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR8206562A FR2525216B1 (en) | 1982-04-16 | 1982-04-16 | HALOGENATED AROMATIC ISOCYANATES, OR MIXTURES THEREOF, WITH DIPHENYLMETHANE STRUCTURE AND PROCESS FOR PRODUCING THE SAME |
Publications (3)
Publication Number | Publication Date |
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NO831334L NO831334L (en) | 1983-10-17 |
NO156407B true NO156407B (en) | 1987-06-09 |
NO156407C NO156407C (en) | 1987-09-16 |
Family
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Application Number | Title | Priority Date | Filing Date |
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NO831334A NO156407C (en) | 1982-04-16 | 1983-04-15 | MIXTURES OF HALOGENATED AROMATIC ISOCYANATES WITH DIPHENYLMETAN STRUCTURE. |
Country Status (9)
Country | Link |
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EP (1) | EP0092454B1 (en) |
JP (1) | JPS58189150A (en) |
AT (1) | ATE16699T1 (en) |
DE (1) | DE3361328D1 (en) |
DK (1) | DK166283A (en) |
ES (1) | ES521539A0 (en) |
FR (1) | FR2525216B1 (en) |
NO (1) | NO156407C (en) |
PT (1) | PT76541B (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
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FR2545083B1 (en) * | 1983-04-29 | 1987-07-17 | Ugine Kuhlmann | LIQUID COMPOSITION, CONTAINING DIPHENYLMETHANE STRUCTURED DIISOCYANATES, AND PROCESS FOR PRODUCING THE SAME |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
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GB1080739A (en) * | 1963-09-19 | 1967-08-23 | Monsanto Co | Isocyanates containing tertiary-alkyl groups |
US3904666A (en) * | 1973-11-15 | 1975-09-09 | Olin Corp | Tetraisocyanate compositions |
DE2935318A1 (en) * | 1979-08-31 | 1981-03-26 | Bayer Ag, 51373 Leverkusen | NEW DIISOCYANATES OR DIISOCYANATE MIXTURES OF THE DIPHENYLMETHANE SERIES, METHOD FOR THE PRODUCTION THEREOF, AND THEIR USE AS CONSTRUCTION COMPONENT IN THE PRODUCTION OF POLYURETHANE PLASTICS BY THE ISOCYANATE POLYADDITION METHOD |
DE3032358A1 (en) * | 1980-08-28 | 1982-04-08 | Bayer Ag, 5090 Leverkusen | NEW POLYISOCYANATES OR POLYISOCYANATE MIXTURES OF THE DIPHENYLMETHANE SERIES, METHOD FOR THE PRODUCTION THEREOF, AND THEIR USE AS CONSTRUCTION COMPONENT IN THE PRODUCTION OF POLYURETHANE PLASTICS BY THE ISOCYANATE POLYADDITION PROCESS |
-
1982
- 1982-04-16 FR FR8206562A patent/FR2525216B1/en not_active Expired
-
1983
- 1983-03-30 DE DE8383400658T patent/DE3361328D1/en not_active Expired
- 1983-03-30 EP EP83400658A patent/EP0092454B1/en not_active Expired
- 1983-03-30 AT AT83400658T patent/ATE16699T1/en not_active IP Right Cessation
- 1983-04-12 PT PT76541A patent/PT76541B/en unknown
- 1983-04-15 NO NO831334A patent/NO156407C/en unknown
- 1983-04-15 DK DK166283A patent/DK166283A/en not_active IP Right Cessation
- 1983-04-15 ES ES521539A patent/ES521539A0/en active Granted
- 1983-04-16 JP JP58066343A patent/JPS58189150A/en active Pending
Also Published As
Publication number | Publication date |
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FR2525216A1 (en) | 1983-10-21 |
NO831334L (en) | 1983-10-17 |
EP0092454B1 (en) | 1985-11-27 |
ES8404978A1 (en) | 1984-05-16 |
PT76541A (en) | 1983-05-01 |
EP0092454A1 (en) | 1983-10-26 |
ES521539A0 (en) | 1984-05-16 |
PT76541B (en) | 1985-12-09 |
NO156407C (en) | 1987-09-16 |
DK166283D0 (en) | 1983-04-15 |
JPS58189150A (en) | 1983-11-04 |
DK166283A (en) | 1983-10-17 |
ATE16699T1 (en) | 1985-12-15 |
FR2525216B1 (en) | 1985-10-25 |
DE3361328D1 (en) | 1986-01-09 |
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