DE2123969A1 - Production of mixed polyesters based on caprolactone - Google Patents
Production of mixed polyesters based on caprolactoneInfo
- Publication number
- DE2123969A1 DE2123969A1 DE19712123969 DE2123969A DE2123969A1 DE 2123969 A1 DE2123969 A1 DE 2123969A1 DE 19712123969 DE19712123969 DE 19712123969 DE 2123969 A DE2123969 A DE 2123969A DE 2123969 A1 DE2123969 A1 DE 2123969A1
- Authority
- DE
- Germany
- Prior art keywords
- catalyst
- antimony
- caprolactone
- production
- acid
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 229920000728 polyester Polymers 0.000 title claims description 15
- 238000004519 manufacturing process Methods 0.000 title claims description 6
- PAPBSGBWRJIAAV-UHFFFAOYSA-N ε-Caprolactone Chemical compound O=C1CCCCCO1 PAPBSGBWRJIAAV-UHFFFAOYSA-N 0.000 title description 10
- 239000003054 catalyst Substances 0.000 claims description 19
- -1 alkyl radical Chemical class 0.000 claims description 16
- 238000000034 method Methods 0.000 claims description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 11
- 229920005862 polyol Polymers 0.000 claims description 9
- 150000003839 salts Chemical class 0.000 claims description 9
- 239000003795 chemical substances by application Substances 0.000 claims description 8
- 150000003077 polyols Chemical class 0.000 claims description 8
- OFOBLEOULBTSOW-UHFFFAOYSA-N Malonic acid Chemical compound OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 claims description 6
- 125000004432 carbon atom Chemical group C* 0.000 claims description 6
- 150000001991 dicarboxylic acids Chemical class 0.000 claims description 6
- 125000000217 alkyl group Chemical group 0.000 claims description 4
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 claims description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 claims description 3
- 229910021630 Antimony pentafluoride Inorganic materials 0.000 claims description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 claims description 2
- VBVBHWZYQGJZLR-UHFFFAOYSA-I antimony pentafluoride Chemical compound F[Sb](F)(F)(F)F VBVBHWZYQGJZLR-UHFFFAOYSA-I 0.000 claims description 2
- QUPDWYMUPZLYJZ-UHFFFAOYSA-N ethyl Chemical compound C[CH2] QUPDWYMUPZLYJZ-UHFFFAOYSA-N 0.000 claims description 2
- 125000004435 hydrogen atom Chemical group [H]* 0.000 claims description 2
- 239000012442 inert solvent Substances 0.000 claims description 2
- 238000002955 isolation Methods 0.000 claims description 2
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 claims description 2
- QZRSVBDWRWTHMT-UHFFFAOYSA-M silver;3-carboxy-3,5-dihydroxy-5-oxopentanoate Chemical compound [Ag+].OC(=O)CC(O)(C([O-])=O)CC(O)=O QZRSVBDWRWTHMT-UHFFFAOYSA-M 0.000 claims description 2
- 125000001931 aliphatic group Chemical group 0.000 claims 1
- ZDINGUUTWDGGFF-UHFFFAOYSA-N antimony(5+) Chemical compound [Sb+5] ZDINGUUTWDGGFF-UHFFFAOYSA-N 0.000 claims 1
- 239000003921 oil Substances 0.000 claims 1
- 230000032050 esterification Effects 0.000 description 9
- 238000005886 esterification reaction Methods 0.000 description 9
- WNLRTRBMVRJNCN-UHFFFAOYSA-N adipic acid Chemical compound OC(=O)CCCCC(O)=O WNLRTRBMVRJNCN-UHFFFAOYSA-N 0.000 description 8
- 238000006243 chemical reaction Methods 0.000 description 5
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 5
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 4
- 239000001361 adipic acid Substances 0.000 description 4
- 235000011037 adipic acid Nutrition 0.000 description 4
- 150000002596 lactones Chemical class 0.000 description 4
- XNGIFLGASWRNHJ-UHFFFAOYSA-N phthalic acid Chemical compound OC(=O)C1=CC=CC=C1C(O)=O XNGIFLGASWRNHJ-UHFFFAOYSA-N 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- 150000005846 sugar alcohols Polymers 0.000 description 4
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 description 3
- IWHLYPDWHHPVAA-UHFFFAOYSA-N 6-hydroxyhexanoic acid Chemical compound OCCCCCC(O)=O IWHLYPDWHHPVAA-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 238000012694 Lactone Polymerization Methods 0.000 description 2
- KKEYFWRCBNTPAC-UHFFFAOYSA-N Terephthalic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-N 0.000 description 2
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 2
- 238000004061 bleaching Methods 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 150000002009 diols Chemical class 0.000 description 2
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000011541 reaction mixture Substances 0.000 description 2
- ZWVMLYRJXORSEP-UHFFFAOYSA-N 1,2,6-Hexanetriol Chemical compound OCCCCC(O)CO ZWVMLYRJXORSEP-UHFFFAOYSA-N 0.000 description 1
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 description 1
- GBURUDXSBYGPBL-UHFFFAOYSA-N 2,2,3-trimethylhexanedioic acid Chemical compound OC(=O)C(C)(C)C(C)CCC(O)=O GBURUDXSBYGPBL-UHFFFAOYSA-N 0.000 description 1
- ITFDYXKCBZEBDG-UHFFFAOYSA-N 2-(1-methylpyrrol-2-yl)ethanamine Chemical compound CN1C=CC=C1CCN ITFDYXKCBZEBDG-UHFFFAOYSA-N 0.000 description 1
- LFQSIOGYPMEIGZ-UHFFFAOYSA-N 2-heptyldodecanedioic acid Chemical compound CCCCCCCC(C(O)=O)CCCCCCCCCC(O)=O LFQSIOGYPMEIGZ-UHFFFAOYSA-N 0.000 description 1
- DBBJDJNEABXOIX-UHFFFAOYSA-N 3-ethyloxepan-2-one Chemical compound CCC1CCCCOC1=O DBBJDJNEABXOIX-UHFFFAOYSA-N 0.000 description 1
- KDYFGRWQOYBRFD-UHFFFAOYSA-N Succinic acid Natural products OC(=O)CCC(O)=O KDYFGRWQOYBRFD-UHFFFAOYSA-N 0.000 description 1
- ZJCCRDAZUWHFQH-UHFFFAOYSA-N Trimethylolpropane Chemical compound CCC(CO)(CO)CO ZJCCRDAZUWHFQH-UHFFFAOYSA-N 0.000 description 1
- YIMQCDZDWXUDCA-UHFFFAOYSA-N [4-(hydroxymethyl)cyclohexyl]methanol Chemical compound OCC1CCC(CO)CC1 YIMQCDZDWXUDCA-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000008064 anhydrides Chemical class 0.000 description 1
- 150000001450 anions Chemical class 0.000 description 1
- 229910052787 antimony Inorganic materials 0.000 description 1
- WATWJIUSRGPENY-UHFFFAOYSA-N antimony atom Chemical compound [Sb] WATWJIUSRGPENY-UHFFFAOYSA-N 0.000 description 1
- LJCFOYOSGPHIOO-UHFFFAOYSA-N antimony pentoxide Inorganic materials O=[Sb](=O)O[Sb](=O)=O LJCFOYOSGPHIOO-UHFFFAOYSA-N 0.000 description 1
- 238000010533 azeotropic distillation Methods 0.000 description 1
- KDYFGRWQOYBRFD-NUQCWPJISA-N butanedioic acid Chemical compound O[14C](=O)CC[14C](O)=O KDYFGRWQOYBRFD-NUQCWPJISA-N 0.000 description 1
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 238000003776 cleavage reaction Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- QYQADNCHXSEGJT-UHFFFAOYSA-N cyclohexane-1,1-dicarboxylate;hydron Chemical compound OC(=O)C1(C(O)=O)CCCCC1 QYQADNCHXSEGJT-UHFFFAOYSA-N 0.000 description 1
- PDXRQENMIVHKPI-UHFFFAOYSA-N cyclohexane-1,1-diol Chemical compound OC1(O)CCCCC1 PDXRQENMIVHKPI-UHFFFAOYSA-N 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 125000004177 diethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 1
- 125000000118 dimethyl group Chemical group [H]C([H])([H])* 0.000 description 1
- 150000002148 esters Chemical group 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- XXMIOPMDWAUFGU-UHFFFAOYSA-N hexane-1,6-diol Chemical compound OCCCCCCO XXMIOPMDWAUFGU-UHFFFAOYSA-N 0.000 description 1
- 230000003301 hydrolyzing effect Effects 0.000 description 1
- 239000003456 ion exchange resin Substances 0.000 description 1
- 229920003303 ion-exchange polymer Polymers 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000012948 isocyanate Substances 0.000 description 1
- 150000002513 isocyanates Chemical class 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 238000005580 one pot reaction Methods 0.000 description 1
- 235000006408 oxalic acid Nutrition 0.000 description 1
- 239000002685 polymerization catalyst Substances 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 230000000379 polymerizing effect Effects 0.000 description 1
- 229920002635 polyurethane Polymers 0.000 description 1
- 239000004814 polyurethane Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 150000003254 radicals Chemical class 0.000 description 1
- 238000007142 ring opening reaction Methods 0.000 description 1
- 230000007017 scission Effects 0.000 description 1
- CXMXRPHRNRROMY-UHFFFAOYSA-N sebacic acid Chemical compound OC(=O)CCCCCCCCC(O)=O CXMXRPHRNRROMY-UHFFFAOYSA-N 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 125000000542 sulfonic acid group Chemical group 0.000 description 1
- ITMCEJHCFYSIIV-UHFFFAOYSA-M triflate Chemical compound [O-]S(=O)(=O)C(F)(F)F ITMCEJHCFYSIIV-UHFFFAOYSA-M 0.000 description 1
- 229940113165 trimethylolpropane Drugs 0.000 description 1
Classifications
-
- 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
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/40—High-molecular-weight compounds
- C08G18/42—Polycondensates having carboxylic or carbonic ester groups in the main chain
- C08G18/4266—Polycondensates having carboxylic or carbonic ester groups in the main chain prepared from hydroxycarboxylic acids and/or lactones
- C08G18/4286—Polycondensates having carboxylic or carbonic ester groups in the main chain prepared from hydroxycarboxylic acids and/or lactones prepared from a combination of hydroxycarboxylic acids and/or lactones with polycarboxylic acids or ester forming derivatives thereof and polyhydroxy compounds
-
- 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
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/40—High-molecular-weight compounds
- C08G18/42—Polycondensates having carboxylic or carbonic ester groups in the main chain
- C08G18/4266—Polycondensates having carboxylic or carbonic ester groups in the main chain prepared from hydroxycarboxylic acids and/or lactones
-
- 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
- C08G63/00—Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
- C08G63/02—Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds
- C08G63/60—Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds derived from the reaction of a mixture of hydroxy carboxylic acids, polycarboxylic acids and polyhydroxy compounds
-
- 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
- C08G63/00—Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
- C08G63/78—Preparation processes
- C08G63/82—Preparation processes characterised by the catalyst used
- C08G63/823—Preparation processes characterised by the catalyst used for the preparation of polylactones or polylactides
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Polyesters Or Polycarbonates (AREA)
Description
SCHERING AGSCHERING AG
PatentabteilungPatent department
Λχβη/BuΛχβη / Bu
Herstellung von Mischpolyestern auf Giiprolacton-BasisProduction of mixed polyesters Giipro I act on- Basi s
Gegenstand der Erfindung ist eine weitere Ausbildung des Verfahrens des Hauptpatentes (Patentanmeldung P 21 15 072.1) zur Herstellung von Mischpolyestern aus Caprolactonen der allgemeinen PormelThe subject of the invention is a further development of the process of the main patent (patent application P 21 15 072.1) for the production of mixed polyesters from caprolactones of the general formula
R-CH- (GR2J4- -C = O-R-CH- (GR 2 J 4- -C = O-
0 0
worin R ein Wasserstoffatom, ein Methyl- oder ein Äthylrest sein kann und worin .R höchstens dreimal ein Alkylrer, π sein soll, und aus Dicarbonsäuren und Polyolen mit oder ohne Verwendung inerter Lösungsmittel, wobei in erster Stufe die Caprolactone mit einem aliphatischen Polyol in Gegenwart eines anorganischen Katalysators, nämlich Antimon^)-Chlorid oder Antimon(V)-fluorid, umgesetzt, danach gegebenenfalls mit einer geringen Menge Wasser versetzt und die gebildeten hydroxidgruppenhaltigen ICster-Verb indungen ohne Isolierung in zweiter Stufe mit der Dicarbonsäure umgesetzt werden, wobei das Äquivalentverhältnis Polyol : Dicarbonsäure >1 sein soll, die dadurch gekennzeichnet ist, daß anstelle der Antimon(V)-halogenide ein Trialkyloxonium-SaIz, dessen Alkylgruppen 1 bis 4 Kohlenstoffatome enthalten und bevorzugt Äthylgruppen sind, als Katalysator verwendet wird·wherein R is a hydrogen atom, a methyl or an ethyl radical can be and where .R is at most three times an alkylrer, π should be, and from dicarboxylic acids and polyols with or without the use of inert solvents, in the first stage the caprolactones with an aliphatic polyol in the presence an inorganic catalyst, namely antimony ^) chloride or antimony (V) fluoride, reacted, then optionally mixed with a small amount of water and the hydroxide-containing ICster compounds formed be reacted with the dicarboxylic acid in the second stage without isolation, the equivalent ratio of polyol: Dicarboxylic acid should be> 1, which is characterized in that instead of the antimony (V) halides, a trialkyloxonium salt, whose alkyl groups contain 1 to 4 carbon atoms and are preferably ethyl groups, is used as a catalyst
Eine besondere Ausführungoform des erfindungsgemäßen Verfahrens ist dadurch gekennzeichnet, daß als Trialkyloxonium-SaI/, fJ1r.iäthyloxoniiUii-hexachloroantimonat(V) verwendet wird.A particular Ausführungoform of the inventive method is characterized in that the trialkyloxonium SaI /, J 1 r.iäthyloxoniiUii hexachloroantimonate (V) is used f.
Eu sind bereits Mischpolyester aus Caprolacton, Polyolen ■und Dicarbonsäuren und deren Herstellung beschriebenEu are already mixed polyesters made from caprolactone and polyols ■ and dicarboxylic acids and their preparation described
209847/1163209847/1163
SCHERING· AGSCHERING AG
PatentabteilungPatent department
Axen/Bu -2-Ax / Bu -2-
(deutsche Offenlegungsschriften 1 940 942 und 1 946 430).(German Offenlegungsschriften 1 940 942 and 1 946 430).
In der deutschen Offenlegungsschrift 1 940 942 wird die Herstellung von flüssigen Polyestern auf Basis von ε-Caprolacton oder 6-Hydroxy~capronsäure, einer Dicar "bonsäure oder deren Anhydrid, einem Glykol in einem Überschuß von 5 bis 20 Gew.-$ und einem Polyol mit mindestens 3 Hydroxidgruppen im Molekül beschrieben.In the German Offenlegungsschrift 1 940 942, the Production of liquid polyesters based on ε-caprolactone or 6-hydroxycaproic acid, a dicarboxylic acid or their anhydride, a glycol in an excess of 5 to 20 wt .- $ and a polyol with at least 3 hydroxide groups described in the molecule.
|l Die Polymerisation dieser 4 Komponenten wird bei einer| l The polymerization of these 4 components is carried out in a
Temperatur von 220 bis 24O0C in Gegenwart von Tetraalkyltitanat als Katalysator und einem Lösungsmittel und/oder einem Schleppmittel durchgeführt, wobei die Katalysatorrückstände bei einer Weiterverwendung des Produktes unerwünscht sind und weshalb auf eine Katalyse verzichtet werden muß.Temperature carried out from 220 to 24O 0 C in the presence of tetraalkyl titanate as a catalyst and a solvent and / or entrainer, in which the catalyst residues are undesirable in a re-use of the product and must therefore not required catalysis.
In der deutschen Offenlegungsschrift 1 946 430 werden flüs-'sige hydroxylgruppenhaltige Polyester beschrieben. Zu deren Herstellung wird ε-Caprolacton in Gegenwart eines Sulfonsäure-rGruppen tragenden Ionenaustauscher-Harzes mit einem k großen Überschuß an Wasser zur 6-Hydroxy-capronsäure hydrolysiert. \In the German Offenlegungsschrift 1 946 430 liquid hydroxyl-containing polyesters described. To produce them, ε-caprolactone is used in the presence of a sulfonic acid group bearing ion exchange resin is hydrolyzed with a large excess of water to give 6-hydroxycaproic acid. \
Danach wird eine Dicarbonsäure und ein Gemisch zweier verschiedener Dialkohole im Überschuß von 5 bis 20 Gew.-$ zugegeben, unter erheblichem Aufwand (bei 230 ) das zugesetzte Wasser abgetrieben und danach unter Zusatz eines weiteren Katalysators (Tetraalkyl-titanat) bei 250 C die polymerisierende Veresterung vorgenommen.Then a dicarboxylic acid and a mixture of two different Dialcohols are added in excess of 5 to 20% by weight, with considerable effort (at 230) the added Driven off water and then with the addition of a further catalyst (tetraalkyl titanate) at 250 C die polymerizing esterification made.
Zur weiteren Verarbeitung muß.in einer anderen Apparatur die Reaktionsmischung unter Heizung im Vakuum entwässert und entgast werden.For further processing, it must be done in a different apparatus the reaction mixture can be dehydrated and degassed under heating in vacuo.
2 09 847/11632 09 847/1163
BAD ORfGfNAL^BAD ORfGfNAL ^
SCHi)RIHG AGSCHi) RIHG AG
PatentabteilungPatent department
Axen/Bu . -3-Ax / Bu. -3-
Um ein Produkt mit den gewünschten Eigenschaften zu erhalten, muß bei der Herstellung zusätzlich ein Polyalkohol mit mindestens 3 OH-Gruppen pro Molekül eingesetzt werden.To get a product with the properties you want, a polyalcohol with at least 3 OH groups per molecule must also be used during production.
Den beiden genannten Offenlegungsschriften gegenüber hat das erfindungsgemäße Verfahren jeweils mehrere der folgenden Vorteile:Has opposed both of the above-mentioned disclosure documents the method according to the invention each has several of the following advantages:
1. Das eingesetzte Lacton wird nicht hydrolysiert.1. The lactone used is not hydrolyzed.
2. Es genügt der Einsatz eines einzigen Katalysators (Trialkyloxonium-Salz).2. The use of a single catalyst (trialkyloxonium salt) is sufficient.
3„ Das e:"findungs£omäßp Verfahren benötigt niedrigere 1 Temperaturen als die bekannten Verfahren.3 "The e:" finding method requires lower levels 1 temperatures than the known method.
4. Bei der Filtration des Endproduktes werden der Katalysator und dessen Zersetzungsprodukte entfernt.4. When the final product is filtered, the catalyst and its decomposition products removed.
5. Es ist nicht notwendig, ein Dialkoholgeiaiseh einzusetzen. 5. It is not necessary to use a dialcohol geiaiseh.
6ο Es wird kein zusätzlicher Polyalkohol benötigt.6ο No additional polyalcohol is required.
7. Es wird kein Überschuß an Dialkohol benötigt, der anschließend entfernt werden muß und/oder während der Reaktion wegen zu hoher Temperatur verloren geht.7. No excess of dialcohol is required, which must then be removed and / or during the reaction is lost because the temperature is too high.
8. Das erfindungsgemäße Verfahren benötigt für seine aufeinanderfolgenden Reaktionsstufen nur einen Reaktor und bedarf zwischendurch keiner Reinigungs- oder Trennverfahren.8. The process according to the invention requires only one reactor for its successive reaction stages and does not require any cleaning or separation processes in between.
Nach einem nicht zum bekannten Stand der Technik gehörenden Vorschlag wird ε-Caprolacton in Gegenwart eines Antimon(V)-halogenide oder eines Trialkyloxonium-Salzes als Katalysator durch einen Dialkohol als RingöffnungsagensAccording to one that does not belong to the known state of the art Proposal is ε-caprolactone in the presence of an antimony (V) halide or a trialkyloxonium salt as a catalyst by a dialcohol as a ring opening agent
-4-209847/1163 -4- 209847/1163
SCHBRIlTG AGSCHBRIlTG AG
PatentabteilungPatent department
Axen/Bu -4-Ax / Bu -4-
zu einem an den Kettenenden OH-Gruppen tragenden ester polymerisiert. Nach dem gleichen Vorschlag wird der Katalysator darfach gegebenenfalls durch eine geringe Menge Wasser zum Aiitimon(V)-oxid--hydrat zersetzt, das bei einer nachfolgenden Wärmezufuhr, gegebenenfalls unter Zufuhr einer geringen Menge eines Mono-, Di- oder Polyalkohole, die Veresterung der noch freien Carboxyl-Gruppen katalysiert. Nach dem gleichen Vorschlag werden der Katalysator und dessen Rückstände beim üblichen Filtrieren des Reaktions-P produktes restlos entfernt.polymerized to form an ester bearing OH groups at the chain ends. Following the same suggestion, the Catalyst darfach optionally by a small amount of water to Alitimon (V) oxide - decomposed hydrate, which in a subsequent heat supply, optionally with the supply of a small amount of a mono-, di- or polyalcohol that catalyzes the esterification of the still free carboxyl groups. According to the same proposal, the catalyst and its residues in the usual filtering of the reaction P product completely removed.
In gleicher Weise lassen sich die erfindungsgemäßen Katalysatoren, Trialkyloxonium-Salze, einsetzen. Deren Alkylgruppen sollen 1 bis 4 Kohlenstoffatome enthalten und bevorzugt Äthylgruppeh sein. Als Anionen dieser Katalysator-Salze kommen solche in Frage, die Trialkyloxoniuin-Salze stabilisieren können, beispielsweise Tetrafluoroborat-, Trifluormethan-sulfonat-, Hexafluoroantimonat(V)- und bevorzugt Hexachloroantimonat(V)-Ion.In the same way, the catalysts of the invention, Trialkyloxonium salts, use. Their alkyl groups should contain 1 to 4 carbon atoms and preferably be ethyl groups. As anions of these catalyst salts those are possible, the trialkyloxoniuin salts can stabilize, for example tetrafluoroborate, trifluoromethane sulfonate, hexafluoroantimonate (V) - and preferred Hexachloroantimonate (V) ion.
Bei der erfindungsgemäßen Umsetzung von Di- bzw. Polyoleii mit dem Lacton werden die Polyalkohole durch die Kettenverlängerung weniger flüchtig gemacht, was für die nachfolgende Veresterung mit Dicarbonsäuren von besonderem Wert ist. Das nach der Lactonpolymerisation zugesetzte oder das durch Veresterung rasch gebildete V/asser zerstört anschließend den Polymerisationskatalysator und liefert Antimon(V)-oxid-hydx-at, das als Veresterungskatalj^sator die weitere Veresterung deutlich katalysiert.In the implementation of diols or polyols according to the invention with the lactone the polyalcohols become through the chain extension made less volatile, which is of particular value for the subsequent esterification with dicarboxylic acids is. The water added after the lactone polymerization or the water quickly formed by esterification is then destroyed the polymerization catalyst and supplies antimony (V) oxide hydroxate, which acts as an esterification catalyst the further esterification is clearly catalyzed.
Die bei der Lactonpolymerisation vorzugsweise benutzten Katalysatormengen von 0,03 - 0,06 Gew.-^ Trialkyloxonium-SaIz (bezogen auf das Reaktionsprodukt fertiger Polyester)The amounts of catalyst preferably used in the lactone polymerization of 0.03-0.06% by weight trialkyloxonium salt (based on the reaction product of finished polyester)
-5-209 847/1 163-5-209 847/1 163
BAD ORIGINALBATH ORIGINAL
SCH^RIITG AGSCH ^ RIITG AG
•Patentabteilung• Patent Department
Axen/Bu -5-Ax / Bu -5-
sind gegebenenfalls nach ihrer hydrolytischen Spaltung ein wirksamer Veresterungskatalysator, der aucli in ε-oxycaproylfreien Polyestern mit Erfolg einzusetzen ist. Durch die Anwendung von Trialkyloxonium-Salzen in diesem stufenweisen "Eintopfveresterungsverfahren" lassen sich die Veresterungszeiten deutlich verkürzen, die Keaktionstemperaturen verringern (nicht über 200 C), die azeotrope Entfernung des Wassers mit Schleppmitteli wird überflüssig, und die üblicherweise eingesetzten 5-20 ?&igen Glykolüberschüsse (über die berechnete Menge) können deutlich gesenkt werden (vorzugsweise auf 1 °/o der berechneten Menge) oder sogar ganz entfallen. Das hier beschriebene Verfahren ist allgemein anwendbar und liefert auch beim Einsatz von aromatischen Dicarbonsäuren (z.B. Phthalsäure) neben aliphatischen Dicarbonsäuren (z.B. Adipinsäure) gute Ergebnisse. Die nach, dem erfindungsgemäßen Verfahren hergestellten hydroxidgruppenhaltigen Polyester können wegen ihres geringen bzw. fehlenden Gehaltes an Katalysatorresten in Lösung zu Polyurethanen umgesetzt werden. Für die Reaktion der hydroxidgruppenhaltigen Polyester mit Isocyanaten in der Schmelze kann eine Reinigung mit Bleicherden notwendig sein, d.h., der Polyester wird mit aktiven Bleicherden (ca. 1 - 2 $) in der Wärme wenige Stunden behandelt und dann abfiltriert.may be an effective esterification catalyst after hydrolytic cleavage, which can also be used successfully in ε-oxycaproyl-free polyesters. By using trialkyloxonium salts in this step-by-step "one-pot esterification process", the esterification times can be significantly shortened, the reaction temperatures can be reduced (not above 200 C), the azeotropic removal of the water with an entrainer becomes superfluous, and the 5-20% glycol excesses usually used (above the calculated amount) can be reduced significantly (preferably to 1 % of the calculated amount) or even omitted entirely. The process described here is generally applicable and also gives good results when using aromatic dicarboxylic acids (eg phthalic acid) in addition to aliphatic dicarboxylic acids (eg adipic acid). The polyesters containing hydroxide groups produced by the process according to the invention can be converted into polyurethanes in solution because of their low or no content of catalyst residues. For the reaction of the hydroxide-containing polyesters with isocyanates in the melt, cleaning with bleaching earth may be necessary, ie the polyester is treated with active bleaching earth (approx. 1 - 2 $) in the heat for a few hours and then filtered off.
Erfindungsgeinäß zu verwendende lactone sind unsubstituerte oder substituierte ε-Caprolactone der allgemeinen FormelLactones to be used according to the invention are unsubstituted or substituted ε-caprolactones of the general formula
R-CH- (CIt2) 4 -C =R-CH- (CIt 2 ) 4 -C =
0-0-
mit R - H, CIIV, C2H1-, wobei höchstens 3 der Reste R ein Alkylreiit sein dürfen. .with R - H, CII V , C 2 H 1 -, where a maximum of 3 of the radicals R may be an alkyl group. .
-6-209847/1163-6-209847 / 1163
SCHu)RIiJG AGSCHu) RIiJG AG
PatentabteilungPatent department
Axen/Bu -6-Ax / Bu -6-
Beispiele für solche Lactone sind:Examples of such lactones are:
ε-Caprolacton,ε-caprolactone,
α-, ß-, γ-, δ- oder s-Methyl-B-eaprolacton,α-, ß-, γ-, δ- or s-methyl-B-eaprolactone,
Äthyl-ε-caprolacton,Ethyl-ε-caprolactone,
Dimethyl- oder Diäthyl-B'-caprolacton oderDimethyl or diethyl B'-caprolactone or
β,β,δ- oder ß^jö-Trimethyl-E-caprolacton.β, β, δ- or ß ^ jö-trimethyl-E-caprolactone.
Beispiele für erfindungsgemäß einzusetzende Pcüyole sindExamples of Pcüyole to be used according to the invention are
* a) lineare oder verzweigte Diole mit "bis zu 12 Kohlenstoffatomen, wie lthandiol-(l,2), B-^.!.aiidiol-(l,4), Hexandiol-(1,6) oder Trimethyl-hexandiol-(l,6) odc-r* a) linear or branched diols with "up to 12 carbon atoms, like lthandiol- (l, 2), B - ^.!. aiidiol- (l, 4), hexanediol- (1,6) or trimethyl-hexanediol- (1,6) odc-r
b) lineare oder verzweigte Polyole mit mindestens 3 OH-Gruppen pro Molekül,b) linear or branched polyols with at least 3 OH groups per molecule,
wie Butantriol-(l,2,4), Trimethylol-propan oder Hexantriol-(l,2,6) odersuch as butanetriol- (1,2,4), trimethylol-propane or Hexanetriol- (1,2,6) or
c) unsubstituierte oder substituierte cycloaliphatische Polyole, wie Cyclohexandiol oder 1,4-Bis(hydroxymethyl)-cyclohexan. c) unsubstituted or substituted cycloaliphatic Polyols such as cyclohexanediol or 1,4-bis (hydroxymethyl) cyclohexane.
Beispiele für erfindungsgemäß zu verv/endende Dicarbonsäuren sindExamples of dicarboxylic acids to be used according to the invention are
a) lineare oder verzv/eigte aliphatische Dicarbonsäuren mit 2 bis 12 Kohlenstoffatomen, wie Oxalsäure, Bernsteinsäure, Adipinsäure, Trimethyl-adipinsäure, Decan-dicarbonsäure odera) linear or branched aliphatic dicarboxylic acids with 2 to 12 carbon atoms, such as oxalic acid, succinic acid, adipic acid, trimethyladipic acid, decanedicarboxylic acid or
b) 1,9- oder 1,10-Heptadecan-dicarbonsäure oderb) 1,9- or 1,10-heptadecanedicarboxylic acid or
c) unsiibstituierte oder substituierte cycloaliphatischec) unsubstituted or substituted cycloaliphatic
209847/116 BAD ORIGINAL209847/116 ORIGINAL BATHROOM
SCILiRIHG AGSCILiRIHG AG
P at ent ab t e ilungP at ent division
Axen/Bu _7_Axen / Bu _7_
Dicarbonsäuren mit insgesamt "bis 12 Kohlenstoffatomen, wie Cyclohexan-dicarbonsäure, oderDicarboxylic acids with a total of "up to 12 carbon atoms, such as cyclohexane-dicarboxylic acid, or
d) aromatische Dicarbonsäuren, wie Phthalsäure oder Terephthalsäure.d) aromatic dicarboxylic acids such as phthalic acid or Terephthalic acid.
-8-209 8 47/1163, -8- 209 8 47/1163,
■ « ■ 1 * tv ■ « ■ 1 * tv
- ■-! ■■". Ϊ >- tr-S - ■ -! ■■ ". Ϊ > - tr-S
SCHÜRIUG AGSCHÜRIUG AG
PatentabteilungPatent department
Axen/Bu -8-Ax / Bu -8-
Be i' spielExample
Mischpolyester aus e-Caprolacton/lIexandiol-CljöJ/Adipinsäure im Molverhältnis 6:9:8, Caprolacton-Anteil ca. 26 fo: Mixed polyester of e-caprolactone / lexanediol-CljöJ / adipic acid in a molar ratio of 6: 9: 8, caprolactone content approx. 26 fo:
551 g Hexandiöl-(1,6) und 342 g ε-Caprolacton werden bei 40 - 500C vorgelegt. Dann setzt man 0,43 S (entsprechend 0,03 i° auf Gesamt-Polyester) Triäthyloxonium-hexachloroantimonat dazu und läßt 4 Stunden "bei 40 - 500C unter Rühren reagieren. Anschließend gibt man zur Zerstörung des Katalysators ca. 0,5 ml Wasser hinzu und erhitzt das Reaktionsgemisch auf 1000C. Dann setzt man 584 g Adipinsäure und 5,31 g He-xandiol-(l, 6) (1 # der eingesetzten Hexandiolmenge) dazu und verestert unter Stickstoff nach folgendem Schema:551 g Hexandiöl- (1.6) and 342 g of ε-caprolactone at 40 - 50 0 C presented. Then added 0.43 S (corresponding to 0.03 i ° to total polyester) triethyloxonium hexachloroantimonate thereto and stirred for 4 hours, "at 40 - 50 0 C under stirring to react are then added to the destruction of the catalyst approximately 0.5. ml of water are added and the reaction mixture heated to 100 0 C. Then Substituting 584 g of adipic acid and 5.31 g He-xandiol- (l, 6) (1 # Hexandiolmenge used) was added and esterified under nitrogen according to the following scheme:
1 Stunde von 150-1750C
1 Stunde von 1'75-2000C 3 Stunden bei 2000C
9 Stunden bei 200°C/l5 Torr1 hour from 150-175 0 C for 1 hour of 1'75-200 0 C for 3 hours at 200 0 C.
9 hours at 200 ° C / 15 torr
Man erhält einen kristallinen Polyester mit folgendenA crystalline polyester is obtained with the following
Kennzahlen: /Key figures: /
ber. gef.ber.
Hydroxylzahl ■ 42,7 39,7Hydroxyl number ■ 42.7 39.7
Säurezahl 0 0,6Acid number 0 0.6
-9-209 8 4 7/ 1 163-9-209 8 4 7/1 163
Claims (2)
Priority Applications (8)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE19712115072 DE2115072A1 (en) | 1971-03-29 | 1971-03-29 | Production of mixed polyesters based on caprolactone |
| DE19712123969 DE2123969A1 (en) | 1971-03-29 | 1971-05-14 | Production of mixed polyesters based on caprolactone |
| DE19712135307 DE2135307A1 (en) | 1971-03-29 | 1971-07-15 | PRODUCTION OF MIXED POLYESTERS BASED ON CAPROLACTONE |
| IT2234172A IT950727B (en) | 1971-03-29 | 1972-03-24 | PREPARATION OF MIXED POLYESTERS BASED ON CAPROLACTONE |
| FR7210856A FR2132139B1 (en) | 1971-03-29 | 1972-03-28 | |
| BE781391A BE781391A (en) | 1971-03-29 | 1972-03-29 | MIXED POLYESTERS BASED ON CAPROLACTONS |
| NL7204281A NL7204281A (en) | 1971-03-29 | 1972-03-29 | |
| GB1480772A GB1376353A (en) | 1971-03-29 | 1972-03-29 | Manufacture of copolyesters base on caprolactones |
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE19712115072 DE2115072A1 (en) | 1971-03-29 | 1971-03-29 | Production of mixed polyesters based on caprolactone |
| DE19712123969 DE2123969A1 (en) | 1971-03-29 | 1971-05-14 | Production of mixed polyesters based on caprolactone |
| DE19712135307 DE2135307A1 (en) | 1971-03-29 | 1971-07-15 | PRODUCTION OF MIXED POLYESTERS BASED ON CAPROLACTONE |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| DE2123969A1 true DE2123969A1 (en) | 1972-11-16 |
Family
ID=27183310
Family Applications (3)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| DE19712115072 Pending DE2115072A1 (en) | 1971-03-29 | 1971-03-29 | Production of mixed polyesters based on caprolactone |
| DE19712123969 Pending DE2123969A1 (en) | 1971-03-29 | 1971-05-14 | Production of mixed polyesters based on caprolactone |
| DE19712135307 Pending DE2135307A1 (en) | 1971-03-29 | 1971-07-15 | PRODUCTION OF MIXED POLYESTERS BASED ON CAPROLACTONE |
Family Applications Before (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| DE19712115072 Pending DE2115072A1 (en) | 1971-03-29 | 1971-03-29 | Production of mixed polyesters based on caprolactone |
Family Applications After (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| DE19712135307 Pending DE2135307A1 (en) | 1971-03-29 | 1971-07-15 | PRODUCTION OF MIXED POLYESTERS BASED ON CAPROLACTONE |
Country Status (6)
| Country | Link |
|---|---|
| BE (1) | BE781391A (en) |
| DE (3) | DE2115072A1 (en) |
| FR (1) | FR2132139B1 (en) |
| GB (1) | GB1376353A (en) |
| IT (1) | IT950727B (en) |
| NL (1) | NL7204281A (en) |
Families Citing this family (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4096125A (en) * | 1976-05-26 | 1978-06-20 | Union Carbide Corporation | Polycaprolactone derivatives and coating compositions thereof |
| ES2123466B1 (en) * | 1997-06-11 | 1999-11-16 | Merquinsa Mercados Quimicos S | THERMOPLASTIC OF POLYURETHANE AND PROCEDURE FOR ITS OBTAINING. |
| DE102006048288A1 (en) | 2006-10-12 | 2008-04-17 | Bayer Materialscience Ag | Polyester polyols, process for their preparation and their use |
| KR101793746B1 (en) * | 2009-08-21 | 2017-11-03 | 켐트라 코포레이션 | Copolyester polyols, prepolymers, and polyurethane elastomers formed therefrom and processes for making same |
| KR20160048163A (en) | 2013-08-28 | 2016-05-03 | 바스프 코팅스 게엠베하 | Dimer fatty acid/polyester diol reaction product and the use thereof in coating agents |
| GB201317113D0 (en) | 2013-09-26 | 2013-11-06 | Croda Int Plc | A co-polymer polyol |
| GB201402580D0 (en) | 2014-02-14 | 2014-04-02 | Croda Int Plc | Polyurethane elastomers |
| GB201402585D0 (en) | 2014-02-14 | 2014-04-02 | Croda Int Plc | Polyurethane dispersions |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1076877A (en) * | 1964-06-03 | 1967-07-26 | Asahi Chemical Ind | Method for producing linear copolyesters |
-
1971
- 1971-03-29 DE DE19712115072 patent/DE2115072A1/en active Pending
- 1971-05-14 DE DE19712123969 patent/DE2123969A1/en active Pending
- 1971-07-15 DE DE19712135307 patent/DE2135307A1/en active Pending
-
1972
- 1972-03-24 IT IT2234172A patent/IT950727B/en active
- 1972-03-28 FR FR7210856A patent/FR2132139B1/fr not_active Expired
- 1972-03-29 BE BE781391A patent/BE781391A/en unknown
- 1972-03-29 NL NL7204281A patent/NL7204281A/xx unknown
- 1972-03-29 GB GB1480772A patent/GB1376353A/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| BE781391A (en) | 1972-09-29 |
| DE2115072A1 (en) | 1972-10-05 |
| DE2135307A1 (en) | 1973-01-25 |
| NL7204281A (en) | 1972-10-03 |
| FR2132139A1 (en) | 1972-11-17 |
| IT950727B (en) | 1973-06-20 |
| GB1376353A (en) | 1974-12-04 |
| FR2132139B1 (en) | 1977-08-19 |
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