[go: up one dir, main page]

EP0683763A1 - Process for producing light-coloured polyolesters - Google Patents

Process for producing light-coloured polyolesters

Info

Publication number
EP0683763A1
EP0683763A1 EP94907513A EP94907513A EP0683763A1 EP 0683763 A1 EP0683763 A1 EP 0683763A1 EP 94907513 A EP94907513 A EP 94907513A EP 94907513 A EP94907513 A EP 94907513A EP 0683763 A1 EP0683763 A1 EP 0683763A1
Authority
EP
European Patent Office
Prior art keywords
acid
fatty acids
esters
fatty
transesterification
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.)
Withdrawn
Application number
EP94907513A
Other languages
German (de)
French (fr)
Inventor
Jörg-Dieter KLAMANN
Johann Klein
Peter Daute
Erwin Fleischer
Peter Wedl
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Henkel AG and Co KGaA
Original Assignee
Henkel AG and Co KGaA
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Henkel AG and Co KGaA filed Critical Henkel AG and Co KGaA
Publication of EP0683763A1 publication Critical patent/EP0683763A1/en
Withdrawn legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C67/00—Preparation of carboxylic acid esters
    • C07C67/03—Preparation of carboxylic acid esters by reacting an ester group with a hydroxy group
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C67/00—Preparation of carboxylic acid esters
    • C07C67/08—Preparation of carboxylic acid esters by reacting carboxylic acids or symmetrical anhydrides with the hydroxy or O-metal group of organic compounds
    • C—CHEMISTRY; METALLURGY
    • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11C—FATTY ACIDS FROM FATS, OILS OR WAXES; CANDLES; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS, OILS, OR FATTY ACIDS OBTAINED THEREFROM
    • C11C3/00—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom
    • C11C3/003—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom by esterification of fatty acids with alcohols

Definitions

  • the invention relates to a process for producing light-colored polyol esters, in which fatty acids or fatty acid glycerol esters are esterified or transesterified with polyols in the presence of lithium salts and the reaction products are then treated with bleaching agents, the process products and their use as plastic auxiliaries.
  • plastic auxiliaries are used in the manufacture and processing of plastics. Their tasks include, for example, reducing friction during extrusion, providing the polymers with antistatic properties or protecting them from yellowing by UV radiation.
  • plastic auxiliaries are polyesters, which are usually obtained by esterifying fatty acids or transesterifying fatty oils with polyols - generally Gly- cerin - are produced in the presence of catalytic amounts of tin salts.
  • tin salts are suitable esterification or transesterification catalysts.
  • new oleic acid-rich rapeseed oil with glycerin can be obtained in 8 hours in a satisfactory yield from a mixture of the mono- and transesterify diglycerides.
  • the disadvantage here is the high tin content in the products, which is undesirable for reasons of application technology. Instead of complex removal of the tin from the partial glycerides, the catalysts are therefore usually used in small amounts of typically 0.02 to 0.04% by weight. Although partial esters with a tolerably low tin content can be produced in this way, the advantage of the low catalyst concentration is offset by the disadvantage of significantly longer reaction times.
  • Another very decisive disadvantage is that the use of tin catalysts - especially when unsaturated feedstocks are used - leads to products of inadequate color quality which cannot or only to a very limited extent be lightened with hydrogen.
  • the object of the invention was therefore to provide a process for producing light-colored polyolesters which is free from the disadvantages described. Description of the invention
  • the invention relates to a process for the preparation of light-colored polyol esters, in which fatty acids or fatty acid glycerol esters in the presence of 0.001 to 0.1% by weight, based on the fatty substances, of lithium salts with polyols are subjected to an esterification or transesterification and the resulting Tating polyol ester then treated in a manner known per se with bleaching agents.
  • lithium salts are not only able to catalyze the esterification or transesterification at comparatively very low concentrations and to shorten the reaction time considerably, but also that polyol esters are obtained which, compared to the products of the prior art Technology is much more easily accessible to bleaching, for example with hydrogen peroxide.
  • a further advantage of the process according to the invention is that neutralization and / or separation of the lithium salts in the polyolesters can be dispensed with, since the small amounts used neither the properties of the products nor their behavior in further processing ⁇ influence negatively.
  • the fatty acids are aliphatic carboxylic acids of the formula (I)
  • R ⁇ CO stands for a linear or branched aliphatic, optionally hydroxy-substituted acyl radical having 6 to 22 carbon atoms and 0 or 1 to 5 double bonds.
  • Typical examples are caproic acid, caprylic acid, isononanoic acid, capric acid, undecanoic acid, lauric acid, myristic acid, palmitic acid, palmoleic acid, stearic acid, isostearic acid, oleic acid, elaidic acid, petroselinic acid, linoleic acid, linolenic acid, elaeostearic acid, hydroxynacetic acid, ricinystearic acid, 12 , Gadoleic acid, behenic acid and erucic acid as well as their technical mixtures as they occur, for example, in the pressure splitting of fats and oils or in the oxidation of aldehydes from Roelen's oxosynthesis.
  • Fatty acids with 16 to 18 carbon atoms and 0 or 1 double bond, for example technical grade fatty acid are preferably used.
  • the fatty acid glycerol esters are triglycerides which follow the formula (II)
  • R ⁇ CO, R 3 CO and R ⁇ CO independently of one another for linear or branched aliphatic, optionally hydroxy-substituted tuiert Acylreste with 6 to 22 carbon atoms and 0 or 1 to 5 double bonds.
  • Typical examples are synthetic, but preferably natural, fatty acid glycerol esters of plant or animal origin, for example based on palm oil, palm kernel oil, coconut oil, rape oil from old and new varieties, sunflower oil old and new varieties, castor oil, soybean oil, peanut oil, olive oil, linseed oil, beef tallow or fish oil as well as chemically modified triglycerides of the so-called "soy polyol type", which are obtained by epoxidation of soybean oil and subsequent opening of the oxirane rings with suitable nucleophiles, for example alcohols. Vegetable triglycerides with a high proportion of unsaturated fatty acids, in particular rape oil and sunflower oil from new breeds, are preferably used.
  • Suitable polyols are compounds which have at least 2, preferably 3 to 5, hydroxyl groups. Typical examples are glycerol, oligoglycerols with an average degree of oligomerization of 1.5 to 10, trimethylolpropane and pentaerythritol. Glycerin is preferably used. Accordingly, the preferred products obtainable by the process according to the invention thus represent fatty acid glycerides, in particular industrial mixtures of mono- and diglycerides. Lithium salts
  • lithium salts are also suitable as lithium salts, that is to say salts of lithium with optionally hydroxy-functionalized fatty acids having 6 to 22 carbon atoms and 0, 1, 2 or 3 double bonds.
  • Typical examples are the lithium salts of caproic acid, caprylic acid, capric acid, lauric acid, myristic acid, palmitic acid, palmitoleic acid, stearic acid, oleic acid, elaidic acid, petroseline acid, linoleic acid, linolenic acid, 12-hydroxystearic acid, ricinoleic acid, arachic acid, eradic acid, gadolic acid .
  • the lithium salts can be used in the form of an aqueous or alcoholic solution. Because of their ease of metering, the lithium salts of unsaturated fatty acids, which are in any case liquid, are preferably used.
  • the lithium soaps can be added directly to the reaction mixture; however, they can also form in situ, for example from lithium hydroxide and a fatty acid ester.
  • the amount of lithium salts used can be 0.001 to 0.1, preferably 0.002 to 0.05 and in particular 0.004 to 0.01% by weight, based on the starting materials. Since lithium ions can exchange with the alkali ions contained in glasses, which can lead to a reduction in the concentration of lithium ions, it is advisable to carry out the process in devices made of steel or similarly inert materials.
  • the use of lithium carbonate together with aluminum oxide for the self-condensation of glycerol is known from JP Patent Abstract .13, 372 (C-627) (3270) 17. Esterification or transesterification and bleaching
  • the molar ratio between fatty acids or fatty acid glycerol esters and polyols can be 10: 1 to 1:10, preferably 3: 1 to 1: 3.
  • the esterification or transesterification can be carried out in a manner known per se in the temperature range from 100 to 250 ° C.
  • the esterification or transesterification can be complete, i. H. with saturation of all available hydroxyl groups. In a preferred embodiment of the invention, however, only partial esterification or transesterification is desired. Partial here means a degree of esterification of 10 to 95, preferably 25 to 75% of the available hydroxyl groups. It should be pointed out that the person skilled in the art is able to control the degree of esterification via the use ratio of the starting materials without having to be inventive.
  • the bleaching can also be carried out in a manner known per se by adding 0.3 to 1, preferably 0.2 to 1% by weight, based on the polyol esters, of hypochlorite or preferably hydrogen peroxide to the polyol esters and Stirring for 0.5 to 2 hours.
  • Another object of the invention relates to light-colored polyol esters, which are obtained by subjecting fatty acids or fatty acid glycerol esters in the presence of 0.001 to 0.1% by weight, based on the fatty substances, of lithium salts with polyols to an esterification or transesterification and the resul ⁇ tating polyol ester then treated in a manner known per se with bleaching agents.
  • the light-colored polyol esters obtainable by the process according to the invention improve the sliding behavior in the production of polymers, are suitable for the antistatic finishing of plastics and have a color-stabilizing effect against UV radiation.
  • Another object of the invention therefore relates to the use of the light-colored polyol esters obtainable by the process according to the invention as plastic auxiliaries, in which they contain 0.1 to 5, preferably 0.5 to 1.5% by weight, based on 100 parts of plastic - May be included.
  • auxiliaries of the type mentioned are lubricants, antistatic agents and UV stabilizers.
  • the light-colored polyol esters can be used together with other customary starting materials, for example: metal soaps, optionally oxo or hydroxy-substituted fatty acids, optionally chemically modified hydrotalcites, alkyl phosphates, alkyl phosphites, dipetones, epoxidized fatty acid lower alkyl esters or glycates - rinester and the like.
  • Suitable plastics are in particular PVC and polycarbonate.
  • the resulting bright, light yellow oil showed a Lovibond color number (1 inch cuvette) of yellow 5.8 and red 1.8.
  • b) bleach A portion of this oil was mixed with 0.5% by weight, based on the oil, of aqueous hydrogen peroxide (35% by weight) and stirred at 90 ° C. for 30 minutes. A slight vacuum was then applied, the mixture was heated to 105 ° C. over a period of 90 min and the water was removed. The resulting bare, clearly lightened oil showed a Lovibond color number (1 inch cuvette) of yellow 3.3 and red 0.3.
  • Example 1 was repeated using 475.3 g of new beet oil, 31.3 g of glycerin and 12 g of oleic acid. However, 0.1 g of tin oxalate - corresponding to 0.02% by weight, based on the triglyceride - was used as the catalyst instead of the lithium salt. However, the limit value of the residual glycerol content of approx. 1% by weight was only reached after a reaction time of 13 h.
  • Example 2 bleach. As in Example 1, part of the oil was bleached with hydrogen peroxide. The resulting bare, but little brightened oil showed a Lovibond color number (1 inch cuvette) of yellow 3.4 and red 1.0.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Wood Science & Technology (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

Light-coloured polyolesters can be produced by esterification or transesterification of fatty acids or fatty acid glycerin esters in the presence of between 0.001 to 0.1 % by weight, based on the fatty acid, of lithium salts with polyols, after which the polyolesters are treated with bleaching agents in a known manner. The materials are suitable as plastics adjuvants.

Description

Verfahren zur Herstellung hellfarbiger Polyolester Process for the production of light colored polyol esters
Gebiet der Erfi-ndunσArea of Erfi-ndunσ
Die Erfindung betrifft ein Verfahren zur Herstellung hellfar¬ biger Polyolester, bei dem man Fettsäuren bzw. Fettsäuregly- cerinester in Gegenwart von Lithiumsalzen mit Polyolen ver- estert bzw. umestert und die Reaktionsprodukte anschließend mit Bleichmitteln behandelt, die Verfahrensprodukte sowie deren Verwendung als Kunststoffhilfsmittel.The invention relates to a process for producing light-colored polyol esters, in which fatty acids or fatty acid glycerol esters are esterified or transesterified with polyols in the presence of lithium salts and the reaction products are then treated with bleaching agents, the process products and their use as plastic auxiliaries.
Stand der TechnikState of the art
Bei der Herstellung und Verarbeitung von Kunststoffen finden eine Vielzahl von Hilfsmitteln Verwendung. Zu ihren Aufgaben gehört beispielsweise die Herabsetzung der Reibung während der Extrusion, die antistatische Ausrüstung der Polymeren oder deren Schutz vor Vergilbung durch UV-Strahlung. Zu den wichtigsten Inhaltsstoffen derartiger Kunststoffhilfsmittel zählen neben Metallseifen und Phosphorverbindungen Polyol¬ ester, die üblicherweise durch Veresterung von Fettsäuren bzw. Umesterung fetter Öle mit Polyolen - in der Regel Gly- cerin - in Gegenwart katalytischer Mengen von Zinnsalzen hergestellt werden.A variety of aids are used in the manufacture and processing of plastics. Their tasks include, for example, reducing friction during extrusion, providing the polymers with antistatic properties or protecting them from yellowing by UV radiation. In addition to metal soaps and phosphorus compounds, the most important ingredients of such plastic auxiliaries are polyesters, which are usually obtained by esterifying fatty acids or transesterifying fatty oils with polyols - generally Gly- cerin - are produced in the presence of catalytic amounts of tin salts.
Grundsätzlich stellen Zinnsalze geeignete Veresterungs- bzw. Umesterungskatalysatoren dar. So läßt sich beispielsweise ölsäurereiches neues Rüböl mit Glycerin in Gegenwart von 1 bis 2 Gew.-% Zinnoxalat - bezogen auf das öl - innerhalb von 8 h mit befriedigenden Ausbeuten zu einem Gemisch der Mono- und Diglyceride umestern. Von Nachteil hierbei ist jedoch der hohe Zinngehalt in den Produkten, der aus anwendungstechni¬ schen Gründen unerwünscht ist. Anstelle einer aufwendigen Abtrennung des Zinns aus den Partialglyceriden setzt man die Katalysatoren daher üblicherweise in geringen Mengen von typischerweise 0,02 bis 0,04 Gew.-% ein. Auf diese Weise lassen sich zwar Partialester mit einem tolerierbar niedrigen Zinngehalt herstellen, dem Vorteil der niedrigen Katalysator¬ konzentration steht jedoch der Nachteil deutlich längerer Reaktionszeiten gegenüber. Ein weiterer sehr entscheidender Nachteil besteht ferner darin, daß die Verwendung von Zinn¬ katalysatoren - insbesondere bei Einsatz ungesättigter Ein¬ satzstoffe - zu Produkten einer unzureichenden Farbqualität führt, die sich nicht oder nur sehr bedingt mit Wasserstoff aufhellen lassen.Basically, tin salts are suitable esterification or transesterification catalysts. For example, new oleic acid-rich rapeseed oil with glycerin can be obtained in 8 hours in a satisfactory yield from a mixture of the mono- and transesterify diglycerides. The disadvantage here is the high tin content in the products, which is undesirable for reasons of application technology. Instead of complex removal of the tin from the partial glycerides, the catalysts are therefore usually used in small amounts of typically 0.02 to 0.04% by weight. Although partial esters with a tolerably low tin content can be produced in this way, the advantage of the low catalyst concentration is offset by the disadvantage of significantly longer reaction times. Another very decisive disadvantage is that the use of tin catalysts - especially when unsaturated feedstocks are used - leads to products of inadequate color quality which cannot or only to a very limited extent be lightened with hydrogen.
Die Aufgabe der Erfindung hat somit darin bestanden, ein Verfahren zur Herstellung von hellfarbigen Polyolestem zur Verfügung zu stellen, das frei von den geschilderten Nach¬ teilen ist. Beschreibung der ErfindungThe object of the invention was therefore to provide a process for producing light-colored polyolesters which is free from the disadvantages described. Description of the invention
Gegenstand der Erfindung ist ein Verfahren zur Herstellung von hellfarbigen Polyolestem, bei dem man Fettsäuren bzw. Fettsäureglycerinester in Gegenwart von 0,001 bis 0,1 Gew.-% - bezogen auf die Fettstoffe - Lithiumsalzen mit Polyolen einer Veresterung bzw. Umesterung unterwirft und die resul¬ tierenden Polyolester anschließend in an sich bekannter Weise mit Bleichmitteln behandelt.The invention relates to a process for the preparation of light-colored polyol esters, in which fatty acids or fatty acid glycerol esters in the presence of 0.001 to 0.1% by weight, based on the fatty substances, of lithium salts with polyols are subjected to an esterification or transesterification and the resulting Tating polyol ester then treated in a manner known per se with bleaching agents.
Überraschenderweise wurde gefunden, daß Lithiumsalze nicht nur in der Lage sind, die Veresterung bzw. Umesterung bei vergleichsweise sehr niedrigen Konzentrationen zu katalysie¬ ren und die Reaktionszeit erheblich zu verkürzen, sondern daß auch Polyolester erhalten werden, die im Vergleich zu den Produkten des Stands der Technik sehr viel leichter einer Bleiche beispielsweise mit Wasserstoffperoxid zugänglich sind. Ein weiterer Vorteil des erfindungsgemäßen Verfahrens ist darin zu sehen, daß auf eine Neutralisation und/oder Ab¬ trennung der Lithiumsalze in den Polyolestem verzichtet wer¬ den kann, da die geringen Einsatzmengen weder die Eigenschaf¬ ten der Produkte, noch deren Verhalten in der Weiterverarbei¬ tung negativ beeinflussen.Surprisingly, it was found that lithium salts are not only able to catalyze the esterification or transesterification at comparatively very low concentrations and to shorten the reaction time considerably, but also that polyol esters are obtained which, compared to the products of the prior art Technology is much more easily accessible to bleaching, for example with hydrogen peroxide. A further advantage of the process according to the invention is that neutralization and / or separation of the lithium salts in the polyolesters can be dispensed with, since the small amounts used neither the properties of the products nor their behavior in further processing ¬ influence negatively.
Rohstofferaw materials
Bei den Fettsäuren handelt es sich um aliphatische Carbon¬ säuren der Formel (I),The fatty acids are aliphatic carboxylic acids of the formula (I)
Rl-CO-OH (I) in der R^CO für einen linearen oder verzweigten aliphati- schen, gegebenenfalls hydroxysubstituierten Acylrest mit 6 bis 22 Kohlenstoffatomen und 0 oder 1 bis 5 Doppelbindungen steh .Rl-CO-OH (I) in which R ^ CO stands for a linear or branched aliphatic, optionally hydroxy-substituted acyl radical having 6 to 22 carbon atoms and 0 or 1 to 5 double bonds.
Typische Beispiele sind Capronsäure, Caprylsäure, Isononan- säure, Caprinsäure, Undecansäure, Laurinsäure, Myristinsäure, Palmitinsäure, Palmoleinsäure, Stearinsäure, Isostearinsäure, ölsäure, Elaidinsäure, Petroselinsäure, Linolsäure, Linolen- säure, Elaeostearinsäure, Ricinolsäure, 12-Hydroxystearin- säure, Arachinsäure, Gadoleinsäure , Behensäure und Erucasäure sowie deren technische Gemische, wie sie beispielsweise bei der Druckspaltung von Fetten und ölen oder bei der Oxidation von Aldehyden aus der Roelen'sehen Oxosynthese anfallen. Vorzugsweise werden Fettsäuren mit 16 bis 18 Kohlenstoff- atomen und 0 oder 1 Doppelbindung, beispielsweise technische Taigfettsäure, eingesetzt.Typical examples are caproic acid, caprylic acid, isononanoic acid, capric acid, undecanoic acid, lauric acid, myristic acid, palmitic acid, palmoleic acid, stearic acid, isostearic acid, oleic acid, elaidic acid, petroselinic acid, linoleic acid, linolenic acid, elaeostearic acid, hydroxynacetic acid, ricinystearic acid, 12 , Gadoleic acid, behenic acid and erucic acid as well as their technical mixtures as they occur, for example, in the pressure splitting of fats and oils or in the oxidation of aldehydes from Roelen's oxosynthesis. Fatty acids with 16 to 18 carbon atoms and 0 or 1 double bond, for example technical grade fatty acid, are preferably used.
Bei den Fettsäureglycerinestern handelt es sich um Triglyce- ride, die der Formel (II) folgen,The fatty acid glycerol esters are triglycerides which follow the formula (II)
CH20-CO-R2 CH 2 0-CO-R 2
II.
CH-O-CO-R3 (I)CH-O-CO-R 3 (I)
I CH20-CO-R4 I CH 2 0-CO-R 4
in der R^CO, R3CO und R^CO unabhängig voneinander für lineare oder verzweigte aliphatische, gegebenenfalls hydroxysubsti- tuierte Acylreste mit 6 bis 22 Kohlenstoffatomen und 0 oder 1 bis 5 Doppelbindungen stehen.in which R ^ CO, R 3 CO and R ^ CO independently of one another for linear or branched aliphatic, optionally hydroxy-substituted tuiert Acylreste with 6 to 22 carbon atoms and 0 or 1 to 5 double bonds.
Typische Beispiele sind synthetische, vorzugsweise jedoch na¬ türliche Fettsäureglycerinester pflanzlicher oder tierischer Herkunft beispielsweise auf Basis von Palmöl, Palmkernöl, Kokosöl, Rüböl alter und neuer Züchtung, Sonnenblumenöl alter und neuer Züchtung, Ricinusöl, Sojaöl, Erdnußöl, Olivenöl, Leinöl, Rindertalg oder Fischöl sowie chemisch modifizierte Triglyceride vom Typ der sogenannten "Sojapolyole", die man durch Epoxidation von Sojaöl und nachfolgende Öffnung der Oxiranringe mit geeigneten Nucleophilen, beispielsweise Al¬ koholen, erhält. Vorzugsweise werden pflanzliche Triglyceride mit hohem Anteil an ungesättigten Fettsäuren, insbesondere Rüböl und Sonnenblumenöl neuer Züchtung eingesetzt.Typical examples are synthetic, but preferably natural, fatty acid glycerol esters of plant or animal origin, for example based on palm oil, palm kernel oil, coconut oil, rape oil from old and new varieties, sunflower oil old and new varieties, castor oil, soybean oil, peanut oil, olive oil, linseed oil, beef tallow or fish oil as well as chemically modified triglycerides of the so-called "soy polyol type", which are obtained by epoxidation of soybean oil and subsequent opening of the oxirane rings with suitable nucleophiles, for example alcohols. Vegetable triglycerides with a high proportion of unsaturated fatty acids, in particular rape oil and sunflower oil from new breeds, are preferably used.
Als Polyole kommen Verbindungen in Betracht, die mindestens 2, vorzugsweise 3 bis 5 Hydroxylgruppen aufweisen. Typische Beispiele sind Glycerin, Oligoglycerine mit einem durch¬ schnittlichen Oligomerisierungsgrad von 1,5 bis 10, Trime- thylolpropan und Pentaerythrit. Vorzugsweise wird Glycerin eingesetzt. Demzufolge stellen die bevorzugten nach dem er¬ findungsgemäßen Verfahren erhältlichen Produkte somit Fett- säureglyceride, insbesondere technische Mischungen von Mono- und Diglyceriden dar. LithiumsalzeSuitable polyols are compounds which have at least 2, preferably 3 to 5, hydroxyl groups. Typical examples are glycerol, oligoglycerols with an average degree of oligomerization of 1.5 to 10, trimethylolpropane and pentaerythritol. Glycerin is preferably used. Accordingly, the preferred products obtainable by the process according to the invention thus represent fatty acid glycerides, in particular industrial mixtures of mono- and diglycerides. Lithium salts
Als Lithiumsalze kommen neben Lithiumhydroxid auch Lithium¬ seifen, also Salze des Lithiums mit gegebenenfalls hydroxy- funktionalisierten Fettsäuren mit 6 bis 22 Kohlenstoffatomen und 0, 1, 2 oder 3 Doppelbindungen in Betracht. Typische Bei¬ spiele sind die Lithiumsalze der Capronsäure, Caprylsäure, Caprinsäure Laurinsäure, Myristinsäure, Palmitinsäure, Pal- mitoleinsäure, Stearinsäure, Ölsäure, Elaidinsäure, Petrose- linsäure, Linolsäure, Linolensäure, 12-Hydroxystearinsäure, Ricinolsäure, Arachinsäure, Gadoleinsäure, Behensäure oder Erucasäure. Die Lithiumsalze können in Form wäßriger oder alkoholischer Lösung zum Einsatz gelangen. Wegen ihrer leichten Dosierbarkeit werden vorzugsweise die ohnehin flüs¬ sigen Lithiumsalze ungesättigter Fettsäuren eingesetzt. Die Lithiumseifen können der Reaktionsmischung direkt zugesetzt werden; sie können sich jedoch auch in situ bilden, bei¬ spielsweise aus Lithiumhydroxid und einem Fettsäureester.In addition to lithium hydroxide, lithium salts are also suitable as lithium salts, that is to say salts of lithium with optionally hydroxy-functionalized fatty acids having 6 to 22 carbon atoms and 0, 1, 2 or 3 double bonds. Typical examples are the lithium salts of caproic acid, caprylic acid, capric acid, lauric acid, myristic acid, palmitic acid, palmitoleic acid, stearic acid, oleic acid, elaidic acid, petroseline acid, linoleic acid, linolenic acid, 12-hydroxystearic acid, ricinoleic acid, arachic acid, eradic acid, gadolic acid . The lithium salts can be used in the form of an aqueous or alcoholic solution. Because of their ease of metering, the lithium salts of unsaturated fatty acids, which are in any case liquid, are preferably used. The lithium soaps can be added directly to the reaction mixture; however, they can also form in situ, for example from lithium hydroxide and a fatty acid ester.
Die Einsatzmenge der Lithiumsalze kann 0,001 bis 0,1, vor¬ zugsweise 0,002 bis 0,05 und insbesondere 0,004 bis 0,01 Gew.-% - bezogen auf die Einsatzstoffe - betragen. Da Li¬ thiumionen mit den in Gläsern enthaltenen Alkaliionen aus¬ tauschen können, was zu einer Verringerung der Konzentration an Lithiumionen führen kann, empfiehlt es sich, das Verfahren in Geräten aus Stahl oder ähnlich inerten Materialien durch¬ zuführen. Die Verwendung von Lithiumcarbonat zusammen mit Aluminiumoxid für die Eigenkondensation von Glycerin ist aus JP Patent Abstract .13, 372 (C-627)(3270) 17 bekannt. Veresterung bzw. Umesterung und BleicheThe amount of lithium salts used can be 0.001 to 0.1, preferably 0.002 to 0.05 and in particular 0.004 to 0.01% by weight, based on the starting materials. Since lithium ions can exchange with the alkali ions contained in glasses, which can lead to a reduction in the concentration of lithium ions, it is advisable to carry out the process in devices made of steel or similarly inert materials. The use of lithium carbonate together with aluminum oxide for the self-condensation of glycerol is known from JP Patent Abstract .13, 372 (C-627) (3270) 17. Esterification or transesterification and bleaching
Das molare Verhältnis zwischen Fettsäuren bzw. Fettsäuregly- cerinestern und Polyolen kann 10 : 1 bis 1 : 10, vorzugsweise 3 : 1 bis 1 : 3 betragen. Die Veresterung bzw. Umesterung kann in an sich bekannter Weise im Temperaturbereich von 100 bis 250°C durchgeführt werden. Die Veresterung bzw. Umeste¬ rung kann vollständig, d. h. unter Absättigung aller zur Ver¬ fügung stehender Hydroxylgruppen erfolgen. In einer bevorzug¬ ten Ausführungsform der Erfindung wird jedoch nur eine par¬ tielle Veresterung bzw. Umesterung angestrebt. Unter partiell ist hierbei ein Veresterungsgrad von 10 bis 95, vorzugsweise 25 bis 75 % der zur Verfügung stehenden Hydroxylgruppen zu verstehen. Es sei darauf hingewiesen, daß der Fachmann in der Lage ist, den Grad der Veresterung über das Einsatzverhältnis der Ausgangsstoffe zu steuern, ohne hierzu erfinderisch tätig werden zu müssen.The molar ratio between fatty acids or fatty acid glycerol esters and polyols can be 10: 1 to 1:10, preferably 3: 1 to 1: 3. The esterification or transesterification can be carried out in a manner known per se in the temperature range from 100 to 250 ° C. The esterification or transesterification can be complete, i. H. with saturation of all available hydroxyl groups. In a preferred embodiment of the invention, however, only partial esterification or transesterification is desired. Partial here means a degree of esterification of 10 to 95, preferably 25 to 75% of the available hydroxyl groups. It should be pointed out that the person skilled in the art is able to control the degree of esterification via the use ratio of the starting materials without having to be inventive.
Die Bleiche kann ebenfalls in an sich bekannter Weise durch¬ geführt werden, indem man die Polyolester beispielsweise mit 0,3 bis 1, vorzugsweise 0,2 bis 1 Gew.-% - bezogen auf die Polyolester - Hypochlorit oder vorzugsweise Wasserstoffper¬ oxid versetzt und 0,5 bis 2 h rührt.The bleaching can also be carried out in a manner known per se by adding 0.3 to 1, preferably 0.2 to 1% by weight, based on the polyol esters, of hypochlorite or preferably hydrogen peroxide to the polyol esters and Stirring for 0.5 to 2 hours.
Ein weiterer Gegenstand der Erfindung betrifft hellfarbige Polyolester, die man dadurch erhält, daß man Fettsäuren bzw. Fettsäureglycerinester in Gegenwart von 0,001 bis 0,1 Gew.-% - bezogen auf die Fettstoffe - Lithiumsalzen mit Polyolen einer Veresterung bzw. Umesterung unterwirft und die resul¬ tierenden Polyolester anschließend in an sich bekannter Weise mit Bleichmitteln behandelt. Gewerbliche AnwendbarkeitAnother object of the invention relates to light-colored polyol esters, which are obtained by subjecting fatty acids or fatty acid glycerol esters in the presence of 0.001 to 0.1% by weight, based on the fatty substances, of lithium salts with polyols to an esterification or transesterification and the resul ¬ tating polyol ester then treated in a manner known per se with bleaching agents. Industrial applicability
Die nach dem erfindungsgemäßen Verfahren erhältlichen hell¬ farbigen Polyolester verbessern das Gleitverhalten bei der Herstellung von Polymeren, eignen sich zur antistatischen Ausrüstung von Kunststoffen und weisen gegenüber UV-Strahlung eine farbstabilisierende Wirkung auf.The light-colored polyol esters obtainable by the process according to the invention improve the sliding behavior in the production of polymers, are suitable for the antistatic finishing of plastics and have a color-stabilizing effect against UV radiation.
Ein weiterer Gegenstand der Erfindung betrifft daher die Ver¬ wendung der nach dem erfindungsgemäßen Verfahren erhältlichen hellfarbigen Polyolester als Kunststoffhilfsmittel, in denen sie zu 0,1 bis 5, vorzugsweise 0,5 bis 1,5 Gew.-% - bezogen auf 100 Teile Kunststoff - enthalten sein können.Another object of the invention therefore relates to the use of the light-colored polyol esters obtainable by the process according to the invention as plastic auxiliaries, in which they contain 0.1 to 5, preferably 0.5 to 1.5% by weight, based on 100 parts of plastic - May be included.
Typische Beispiele für Hilfsmittel der genannten Art sind Gleitmittel, Antistatika und UV-Stabilisatoren. In diesem Zusammenhang können die hellfarbigen Polyolester gemeinsam mit weiteren üblichen Einsatzstoffen verwendet werden, als da beispielsweise sind : Metallseifen, gegebenenfalls oxo- oder hydroxysubstituierte Fettsäuren, gegebenenfalls chemisch mo¬ difizierte Hydrotalcite, Alkylphosphate, Alkylphosphite, Di- ketone, epoxidierte Fettsäureniedrigalkyleεter bzw. -glyce- rinester und dergleichen. Geeignete Kunststoffe sind insbe¬ sondere PVC und Polycarbonat.Typical examples of auxiliaries of the type mentioned are lubricants, antistatic agents and UV stabilizers. In this context, the light-colored polyol esters can be used together with other customary starting materials, for example: metal soaps, optionally oxo or hydroxy-substituted fatty acids, optionally chemically modified hydrotalcites, alkyl phosphates, alkyl phosphites, dipetones, epoxidized fatty acid lower alkyl esters or glycates - rinester and the like. Suitable plastics are in particular PVC and polycarbonate.
Die folgenden Beispiele sollen den Gegenstand der Erfindung näher erläutern, ohne ihn darauf einzuschränken. BeispieleThe following examples are intended to explain the subject matter of the invention in more detail without restricting it. Examples
Beispiel 1;Example 1;
a) Umesterung. In einem 1-1-Vierhalsrundkolben mit Rührer, Thermometer und hochangesetztem, absteigenden Kühler wur¬ den 475,3 g (0,5 mol) Rüböl neuer Züchtung (ca. 60 Gew.-% Ölsäureanteil) und 27,3 g (0,3 mol) Glycerin vorgelegt. Zum Start der Umesterungsreaktion wurden der Mischung weitere 4,0 g (0,04 mol) Glycerin und 12 g (0,04 mol) technische Ölsäure (Edenor(R) Ti05, Fa.Henkel KGaA, Düsseldorf/FRG) sowie als Katalysator 0,02 g Lithiumhy¬ droxid - entsprechend 0,004 Gew.-% bezogen auf das Tri- glycerid - zugegeben. Die Reaktionsmischung wurde unter Rühren auf 200°C erhitzt und das Reaktionswasser unter Anlegen eines schwachen Vakuums kontinuierlich entfernt. Nach einer Reaktionszeit von 4 h betrug der Gehalt an freiem Glycerin in der Mischung noch ca. 1 Gew.-%. Das rohe Reaktionsprodukt wurde auf 90°C abgekühlt, mit 0,5 Gew.-% - bezogen auf das Reaktionsprodukt - Bleicherde versetzt und filtriert.a) transesterification. 475.3 g (0.5 mol) of new cultivated rapeseed oil (approx. 60% by weight oleic acid fraction) and 27.3 g (0.05%) were placed in a 1 l four-necked round bottom flask with stirrer, thermometer and high-set, descending cooler. 3 mol) glycerol submitted. At the start of the transesterification reaction, a further 4.0 g (0.04 mol) of glycerol and 12 g (0.04 mol) of technical oleic acid (Edenor ( R ) Ti05, from Henkel KGaA, Düsseldorf / FRG) and the catalyst were added to the mixture , 02 g of lithium hydroxide - corresponding to 0.004% by weight based on the triglyceride - added. The reaction mixture was heated to 200 ° C. with stirring and the water of reaction was continuously removed by applying a weak vacuum. After a reaction time of 4 hours, the free glycerol content in the mixture was still approximately 1% by weight. The crude reaction product was cooled to 90 ° C., 0.5% by weight, based on the reaction product, of bleaching earth was added and the mixture was filtered.
Das resultierende blanke, hellgelbe Öl zeigte eine Lovi- bond-Farbzahl (1 Zoll Küvette) von gelb 5,8 und rot 1,8. b) Bleiche. Ein Teil dieses Öles wurde mit 0,5 Gew.-% - be¬ zogen auf das Öl - wäßrigem Wasserstoffperoxid (35 gew.- %ig) versetzt und über einen Zeitraum von 30 min bei 90°C gerührt. Anschließend wurde ein schwaches Vakuum ange¬ legt, die Mischung über einen Zeitraum von 90 min auf 105°C erhitzt und das Wasser entfernt. Das resultierende blanke, deutlich aufgehellte Öl zeigte eine Lovibond- Farbzahl (1 Zoll Küvette) von gelb 3,3 und rot 0,3.The resulting bright, light yellow oil showed a Lovibond color number (1 inch cuvette) of yellow 5.8 and red 1.8. b) bleach. A portion of this oil was mixed with 0.5% by weight, based on the oil, of aqueous hydrogen peroxide (35% by weight) and stirred at 90 ° C. for 30 minutes. A slight vacuum was then applied, the mixture was heated to 105 ° C. over a period of 90 min and the water was removed. The resulting bare, clearly lightened oil showed a Lovibond color number (1 inch cuvette) of yellow 3.3 and red 0.3.
Vergleichsbeispiel VI:Comparative Example VI:
a) Umesterung. Beispiel 1 wurde unter Einsatz von 475,3 g neuem Rüböl, 31,3 g Glycerin und 12 g Ölsäure wiederholt. Als Katalysator wurde jedoch anstelle des Lithiumsalzes 0,1 g Zinnoxalat - entsprechend 0,02 Gew.-% bezogen auf das Triglycerid - eingesetzt. Den Grenzwert des Glyce- rinrestgehaltes von ca. 1 Gew.-% wurde hier jedoch erst nach einer Reaktionszeit von 13 h erreicht.a) transesterification. Example 1 was repeated using 475.3 g of new beet oil, 31.3 g of glycerin and 12 g of oleic acid. However, 0.1 g of tin oxalate - corresponding to 0.02% by weight, based on the triglyceride - was used as the catalyst instead of the lithium salt. However, the limit value of the residual glycerol content of approx. 1% by weight was only reached after a reaction time of 13 h.
b) Bleiche. Anlog Beispiel 1 wurde ein Teil des Öles mit Wasserstoffperoxid gebleicht. Das resultierende blanke, jedoch wenig aufgehellte öl zeigte eine Lovibond-Farbzahl (1 Zoll Küvette) von gelb 3,4 und rot 1,0. b) bleach. As in Example 1, part of the oil was bleached with hydrogen peroxide. The resulting bare, but little brightened oil showed a Lovibond color number (1 inch cuvette) of yellow 3.4 and red 1.0.

Claims

Patentansprüche Claims
1. Verfahren zur Herstellung von hellfarbigen Polyolestem, bei dem man Fettsäuren bzw. Fettsaureglycerinester in Gegenwart von 0,001 bis 0,1 Gew.-% - bezogen auf die Fettstoffe - Lithiumsalzen mit Polyolen einer Veresterung bzw. umesterung unterwirft und die resultierenden Poly¬ olester anschließend in an sich bekannter Weise mit Bleichmitteln behandelt.1. Process for the preparation of light-colored polyol esters, in which fatty acids or fatty acid glycerol esters in the presence of 0.001 to 0.1% by weight, based on the fatty substances, of lithium salts with polyols are subjected to an esterification or transesterification and the resulting polyesters are subsequently subjected treated in a manner known per se with bleaching agents.
2. Verfahren nach Anspruch 1, dadurch gekennzeichnet, daß man Fettsäuren der Formel (I) einsetzt,2. The method according to claim 1, characterized in that fatty acids of the formula (I) are used,
RiCO-OH (I)RiCO-OH (I)
in der R^CO für einen linearen oder verzweigten alipha- tischen, gegebenenfalls hydroxysubstituierten Acylrest mit 6 bis 22 Kohlenstoffatomen und 0 oder 1 bis 5 Dop¬ pelbindungen steht.in which R ^ CO stands for a linear or branched aliphatic, optionally hydroxy-substituted acyl radical having 6 to 22 carbon atoms and 0 or 1 to 5 double bonds.
3. Verfahren nach Anspruch 1, dadurch gekennzeichnet, daß man Fettsaureglycerinester der Formel (II) einsetzt,3. The method according to claim 1, characterized in that fatty acid glycerol esters of the formula (II) are used,
CH 0-CO-R2 CH 0-CO-R 2
II.
CH-O-CO-R3 (II)CH-O-CO-R 3 (II)
I CH2O-CO-R4 I CH2O-CO-R 4
in der R^CO, R CO und R^CO unabhängig voneinander für li¬ neare oder verzweigte aliphatische, gegebenenfalls hydroxysubstituierte Acylreste mit 6 bis 22 Kohlenstoff¬ atomen und 0 oder 1 bis 5 Doppelbindungen stehen.in which R ^ CO, R CO and R ^ CO independently of one another for linear or branched aliphatic, optionally are hydroxy-substituted acyl radicals having 6 to 22 carbon atoms and 0 or 1 to 5 double bonds.
4. Verfahren nach den Ansprüchen 1 bis 3, dadurch gekenn¬ zeichnet, daß man Polyole einsetzt, die ausgewählt sind aus der Gruppe, die von Glycerin, Oligoglycerinen, Tri- methylolpropan und Pentaerythrit gebildet wird.4. Process according to claims 1 to 3, characterized gekenn¬ characterized in that polyols are used which are selected from the group formed by glycerol, oligoglycerols, trimethylolpropane and pentaerythritol.
5. Verfahren nach den Ansprüchen 1 bis 4, dadurch gekenn¬ zeichnet, daß man die Fettsäuren bzw. Fettsaureglycerin¬ ester und die Polyole im molaren Verhältnis 10 : 1 bis 1 : 10 einsetzt.5. Process according to Claims 1 to 4, characterized in that the fatty acids or fatty acid glycerol esters and the polyols are used in a molar ratio of 10: 1 to 1:10.
6. Verfahren nach den Ansprüchen 1 bis 5, dadurch gekenn¬ zeichnet, daß man als Lithiumsalz Lithiumhydroxid ein¬ setzt.6. The method according to claims 1 to 5, characterized gekenn¬ characterized in that one uses lithium hydroxide as a lithium hydroxide.
7. Verfahren nach den Ansprüchen 1 bis 5, dadurch gekenn¬ zeichnet, daß man als Lithiumsalze Lithiumseifen von ge¬ gebenenfalls hydroxysubstituierten Fettsäuren mit 6 bis 22 Kohlenstoffatomen und 0, 1, 2 oder 3 Doppelbindungen einsetzt.7. The method according to claims 1 to 5, characterized gekenn¬ characterized in that the lithium salts lithium soaps of optionally hydroxy substituted fatty acids with 6 to 22 carbon atoms and 0, 1, 2 or 3 double bonds are used.
8. Verfahren nach den Ansprüchen 1 bis 7, dadurch gekenn¬ zeichnet, daß man die Veresterung bzw. Umesterung im Temperaturbereich von 100 bis 250°C durchführt.8. The method according to claims 1 to 7, characterized gekenn¬ characterized in that one carries out the esterification or transesterification in the temperature range from 100 to 250 ° C.
9. Verfahren nach den Ansprüchen 1 bis 8, dadurch gekenn¬ zeichnet, daß man die Polyolester mit Wasserstoffperoxid behandelt. 9. The method according to claims 1 to 8, characterized gekenn¬ characterized in that the polyol ester is treated with hydrogen peroxide.
10. Hellfarbige Polyolester, dadurch erhältlicht, daß man Fettsäuren bzw. Fettsaureglycerinester in Gegenwart von 0,001 bis 0,1 Gew.-% - bezogen auf die Fettstoffe - Li¬ thiumsalzen mit Polyolen einer Veresterung bzw. Umeste¬ rung unterwirft und die resultierenden Polyolester an¬ schließend in an sich bekannter Weise mit Bleichmitteln behandelt.10. Light-colored polyol esters, obtained by subjecting fatty acids or fatty acid glycerol esters to an esterification or transesterification in the presence of 0.001 to 0.1% by weight, based on the fatty substances, of polyol and the resulting polyol esters ¬ finally treated in a manner known per se with bleaching agents.
11. Verwendung von hellfarbigen Polyolestem nach dem Verfah¬ ren nach den Ansprüchen 1 bis 9 als Kunststoffhilfsmit¬ tel. 11. Use of light-colored polyol esters according to the process according to claims 1 to 9 as plastic auxiliary.
EP94907513A 1993-02-15 1994-02-07 Process for producing light-coloured polyolesters Withdrawn EP0683763A1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
DE4304468 1993-02-15
DE19934304468 DE4304468A1 (en) 1993-02-15 1993-02-15 Process for the production of light colored polyol esters
PCT/EP1994/000345 WO1994018153A1 (en) 1993-02-15 1994-02-07 Process for producing light-coloured polyolesters

Publications (1)

Publication Number Publication Date
EP0683763A1 true EP0683763A1 (en) 1995-11-29

Family

ID=6480455

Family Applications (1)

Application Number Title Priority Date Filing Date
EP94907513A Withdrawn EP0683763A1 (en) 1993-02-15 1994-02-07 Process for producing light-coloured polyolesters

Country Status (4)

Country Link
EP (1) EP0683763A1 (en)
CA (1) CA2156155A1 (en)
DE (1) DE4304468A1 (en)
WO (1) WO1994018153A1 (en)

Families Citing this family (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FI95367C (en) * 1994-09-07 1996-01-25 Raision Tehtaat Oy Ab Method for preparing a synthetic ester from vegetable oil
DE19614722A1 (en) * 1996-04-15 1997-10-16 Henkel Kgaa Low-temperature lubricant and fuel additive
ES2177171T3 (en) * 1998-06-30 2002-12-01 Dhw Deutsche Hydrierwerke Gmbh PROCESS FOR THE TREATMENT OF ACID NATURAL FATS.
DE19903715C2 (en) 1999-01-30 2002-12-05 Cognis Deutschland Gmbh Use of fatty acid alkanolamine esters as internal antistatic agents for thermoplastics
US7538236B2 (en) 2006-01-04 2009-05-26 Suresh Narine Bioplastics, monomers thereof, and processes for the preparation thereof from agricultural feedstocks
DE102009048771A1 (en) 2009-10-08 2011-04-21 Oxea Deutschland Gmbh Process for the preparation of polyol esters
DE102009048773A1 (en) 2009-10-08 2011-04-21 Oxea Deutschland Gmbh Process for the color lightening of polyol esters
DE102009048772A1 (en) 2009-10-08 2011-04-21 Oxea Deutschland Gmbh Process for the preparation of polyol esters
DE102009048774A1 (en) 2009-10-08 2011-04-28 Oxea Deutschland Gmbh Process for the color lightening of polyol esters
DE102009048775A1 (en) * 2009-10-08 2011-04-21 Oxea Deutschland Gmbh Process for the preparation of polyol esters
ES2437749T3 (en) 2009-12-03 2014-01-14 Dow Global Technologies Llc Polyol Fading
EP2513276A4 (en) * 2009-12-17 2016-09-07 Npc Indústrias Químicas Ltda Process for modifying vegetable oils and primary plasticizer for vinyl polymers
GB201001345D0 (en) 2010-01-27 2010-03-17 Equateq Ltd Process for preparing and purifying fatty acids
DE102010033035A1 (en) * 2010-08-02 2012-02-02 Emery Oleochemicals Gmbh Lubricant combination for the processing of thermoplastics
CN109232241A (en) * 2018-09-21 2019-01-18 浙江皇马科技股份有限公司 A kind of preparation method of trihydroxymethylpropanyl ester

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3623371A1 (en) * 1986-07-11 1988-01-21 Huels Chemische Werke Ag CARBOHYDRATE FATTY ACID ESTER AND A METHOD FOR THE PRODUCTION THEREOF
DE4124665A1 (en) * 1991-07-25 1993-01-28 Henkel Kgaa METHOD FOR PRODUCING POLYOL COMPOUNDS

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See references of WO9418153A1 *

Also Published As

Publication number Publication date
WO1994018153A1 (en) 1994-08-18
CA2156155A1 (en) 1994-08-18
DE4304468A1 (en) 1994-08-18

Similar Documents

Publication Publication Date Title
EP0797563B1 (en) Synthetic esters from alcohols and fatty acid mixtures of vegetable oils high in oleic acid and low in stearic acid
EP0683763A1 (en) Process for producing light-coloured polyolesters
DE1156788B (en) Process for the conversion of fatty acid esters of monohydric alcohols with isolated double bonds (íÀIsolenfettsaeureesterníÂ) into fatty acid esters with conjugated double bonds (íÀkonjuenfettsaeureesteríÂ)
DE69005501T2 (en) Process for the preparation of lower alkyl fatty acid monoesters.
DE3107318A1 (en) Process for the preparation of high-quality fatty acid esters
EP0600958B1 (en) Epoxy-ring opening products and method of producing
EP0769042A1 (en) Unsaturated fatty substances with improved cold behaviour
EP0595942B1 (en) Method of preparing polyol compounds
DE4332292A1 (en) Process for the direct hydroxylation of unsaturated carboxylic acids
DE19600025A1 (en) Preparation of fatty acids with low acid values, useful as precursors for esterification reactions
WO2003004591A1 (en) Method for transesterification of fats and/or oils by means of alcoholysis
EP0173941A2 (en) Process for the regulation of the content of di-salts in apha-sulpho fatty-acid esters tensides
WO1992022627A1 (en) Fatty acid glycerin esters having improved rheological properties
EP0728176B1 (en) Method of producing lower-alkyl esters of fatty acids
EP1197559A2 (en) Enzymatic preparation of hydroxyfatty acid esters of polyhydric alcohols being solid at room temperature
DE4125031C1 (en) Prepn. of hydroxylated fatty acid, used to form polymer - comprises hydrolysing epoxidised fatty acid with oxirane rings in presence of activated catalyst e.g. alumina
DE4018293A1 (en) STABILIZERS CONTAINING KETOFENE ACID GLYCERIDES FOR CA / ZN-STABILIZED PVC MOLDING
DE19519887C1 (en) Process for the epoxidation of olefinically unsaturated compounds
DE3916356A1 (en) METHOD FOR THE PRODUCTION OF MIXTURES FROM FATTY ACIDEDIALKYLENE DIAMIDS, FATTY ACID ESTERS AND, IF NECESSARY, METAL SOAPS, MIXTURES OBTAINED THEREOF AND THEIR USE AS A PLASTIC ADDITIVE
DE2214120A1 (en)
EP1075460A1 (en) Method for producing polyolesters
WO2001000549A2 (en) Branched largely insatured fatty alcohols
DE19741913C1 (en) Production of fatty acid ester with low heavy metal content
DE2214179A1 (en)
DE4232167A1 (en) New poly:hydroxy cpds for polymer, esp polyurethane, prodn - obtd by epoxide ring opening of vernol acid contg fatty acid ester(s) with nucleophile(s) which can be hydrogen@, water, alcohol(s) or carboxylic acids

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

17P Request for examination filed

Effective date: 19950809

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): DE FR GB IT NL

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE APPLICATION HAS BEEN WITHDRAWN

18W Application withdrawn

Withdrawal date: 19961010