DE102012105879A1 - Process for the preparation of isononyl derivatives - Google Patents

Abstract

The present invention relates to a process for the preparation of isononyl derivatives from fermentatively produced isobutene, the higher purity of which improves the process and the properties of the isononyl derivatives produced.

Description

The present invention relates to a process for the preparation of isononyl derivatives, in particular isononanol (3,5,5-trimethylhexanol as main component), isononyl vinyl ether (3,5,5-trimethylhexyl-1-vinyl ether as main component), isononanal (3,5, 5-trimethylhexanal as the main component), isononanoic acids (3,5,5-trimethylhexanoic acid or 2,2,4,4-tetramethylpentic acid as main components), the glycidyl ester of 3,5,5-trimethylhexanoic acid or 2,2,4, 4-tetramethylpentanoic acid and isononylamine (3,5,5-trimethylhexylamine as main component), preferably from renewable raw material sources.

Such isononyl compounds are important industrial products, especially the isononyl vinyl ethers, i.a. as copolymers for dispersion coatings, isononanol has significance as an alcohol component for plasticizers. Isononanal has due to the reactive aldehyde as an intermediate product of some technical importance and can be converted, for example, by oxidation in isononanoic acid or by reductive amination in isononylamine and in secondary and tertiary amines containing the isononyl. Esters of isononanoic acid are used as lubricants and isononylamines find application in anticorrosive formulations.

Processes for the preparation of isononyl derivatives have been known for some time and, inter alia, in Ullmann's Encyclopedia of Industrial Chemistry, 6th. Ed., Wiley-VCH, 2003, Vol. 6, pp. 497-498; 502-503; and Vol. 2, page 33 described. In most cases this is based on the dimer of the isobutene, which is converted into the corresponding isononanal in the presence of transition metal catalysts by means of the oxo reaction or hydroformylation reaction with a mixture of carbon monoxide and hydrogen, also called synthesis gas ( Hydrocarbon Processing, April 1973, pages 171-173 ; Ullmann's Encyclopedia of Industrial Chemistry, 6th. Ed. Wiley-VCH, 2003, Vol. 2, page 75 ). Isononanal is then oxidized, for example, to isononanoic acid, hydrogenated to isononanol, aminated to isononylamine or isononanol reacted to Isononylvinylethern. However, due to the immense importance of such isononyl derivatives in engineering chemistry, there is a constant search for further improvements in alternative processes and alternative sources of raw materials for the production of isononyl derivatives.

The use of renewable raw materials as starting materials for the production of organic chemicals on an industrial scale is becoming increasingly important. On the one hand, the resources based on crude oil, natural gas and coal are to be spared and, on the other, carbon dioxide is bound with renewable raw materials in a technically usable carbon source, which is in principle cost-effective and available in large quantities. Examples of the use of renewable raw materials for the industrial production of organic chemicals include u.a. the production of citric acid, 1,3-propanediol, L-lysine, succinic acid, lactic acid and itaconic acid.

Renewable resources are not used for the production of isononyl derivatives. Thus, the object is to provide an alternative improved process for the preparation of isononyl derivatives, preferably from renewable raw material sources available. It is of particular importance with regard to the use of isononyl derivatives that as isomeric isobutene is preferably used for the production of isononyl derivatives.

• a) fermentative Herstellung von Isobuten
• b) Dimerisierung von Isobuten zu Diisobuten
• c) Aufreinigung des Diisobutens
• d) Verlängerung um ein Kohlenstoffatom, um ein Isononylderivat zu erhalten
• e) ggf. weitere Derivatisierungen

This object is achieved by a process for the preparation of isononyl derivatives, comprising the steps:

• a) fermentative production of isobutene
• b) Dimerization of isobutene to diisobutene
• c) Purification of the diisobutene
• d) extension by one carbon atom to obtain an isononyl derivative
• e) possibly further derivatizations

It has surprisingly been found that isobutene produced by fermentation is of such high purity with respect to linear butene isomers that subsequent acid-catalyzed dimerization provides diisobutene in high purity and yield. This in turn means that in step d) the isononyl derivative also arises in high purity.

In the prior art, processes are known in which isobutene is produced biochemically on a laboratory scale in high purity. For example, starting from the direct precursor 3-hydroxyisovalerate (3-hydroxy-3-methylbutyrate), Gogerty, DS and Bobik, TA 2010, Applied and Environmental Microbiology, Page 8004-8010 the fermentative-enzymatic synthesis of isobutene, which according to GC no major amounts of n-butene isomers in the desired product were identified.

The term "isononyl derivative" is understood to mean structurally isomeric compounds having at least one C 9 -alkyl radical, in particular a predominant proportion of 3,5,5-trimethylhexyl radical, again in particular 3,5,5-trimethylhexanol and ether, 3,5,5-trimethylhexyl vinyl ether, 3,5,5-trimethylhexanal, 3,5,5-trimethylhexanoic acid and its glycidyl ester and 3,5,5-trimethylhexylamine; and secondary and tertiary amines having at least one 3,5,5-trimethylhexyl radical. In addition, those C9 compounds are also meant, which have the 2,2,4,4-tetramethylpentyl skeleton as the predominant proportion.

The by-product carbon dioxide formed in the fermentation and optionally further inerts may optionally be removed in a conventional manner by suitable separation methods. In most embodiments of the invention, the conversion of isobutene to diisobutene can be carried out even without further purification of the isobutene, which is thus a preferred embodiment of the invention. In this embodiment of the invention, the fermentative process according to the invention makes use of the high selectivity to isobutene as the C ₄ olefin. On the other hand, carbon dioxide and other inerts do not interfere with the dimerization of isobutene to diisobutene. In special cases, however, it may prove expedient to first separate carbon dioxide and other inerts from the isobutene.

• – mittels Mikroorganismen, bevorzugt aus nachwachsenden Rohstoffen und/oder
• – in einem zellfreien enzymatischen Verfahren, ebenfalls bevorzugt aus nachwachsenden Rohstoffen

gewonnen wird.By "fermentative production" of isobutene is meant in particular that isobutene either

• By means of microorganisms, preferably from renewable raw materials and / or
• - In a cell-free enzymatic process, also preferably from renewable resources

is won.

• I) Aceton zu 3-Hydroxyisovaleriat und
• II) 3-Hydroxyisovaleriat zu Isobuten und Kohlendioxid

beschreiben.Isobutene is - as far as is known - not a natural product in the sense that it arises in metabolic processes in organisms in such quantities that an industrial use appears appropriate. However, isobutene is produced in very small amounts by naturally occurring microorganisms ( US4698304 ; Fukuda, H. 1984 et al, From Agricultural and Biological Chemistry (1984), 48 (6), pp. 1679-82 ). Thus, in the previously known embodiments of the invention, the fermentative production of isobutene by means of modified, non-natural microorganisms or the correspondingly modified enzymes. Such microorganisms are from the US 2011165644 (A1) known in Example 13, the synthesis of isobutene from glucose in suitable microorganisms is treated. In WO2012052427 and WO2011032934 describe further enzymatic reactions involving the formation of isobutene as a sequence of sequential enzymatic syntheses of

• I) acetone to 3-hydroxyisovalerate and
• II) 3-hydroxyisovalerate to isobutene and carbon dioxide

describe.

The enzymatically catalyzed decomposition of 3-hydroxyisovalerate to isobutene and carbon dioxide is also known in Gogerty, DS and Bobik, TA 2010, Applied and Environmental Microbiology, p. 8004-8010 treated. According to GC, no larger amounts of n-butene isomers were reported in the desired product. Even in aqueous, non-enzymatically catalyzed systems, spontaneous carbon dioxide cleavage from 3-hydroxyisovalerate is observed with the formation of isobutene, which reacts further with the water present in an equilibrium reaction to give tert-butanol ( Pressman, D. and Lucas, HJ 1940, Journal of the American Chemical Society, pages 2069-2081 ).

If this sequence of enzymatic syntheses described in I and II is included in a suitable microbial host organism capable of synthesizing acetone from metabolic precursors or transporting externally supplied acetone via the cell wall into the cell interior via passive or active transport, this can not be achieved -natural microorganism Isobutene can be produced with a fermentative process in good yield. Microorganisms that synthesize acetone from various carbohydrates have long been known and are used, inter alia, in Jones, TD and Woods, DR 1986, Microb. Reviews, pages 484-524 - described. In - Taylor, DG et al 1980, Journal of General Microbiology, 118, pages 159-170 - describe microorganisms that use acetone as the sole carbon source and thus are able to transport acetone through the cell wall into the cell interior.

• I) Pyruvat zu 2-Acetolactat
• II) 2-Acetolactat zu 2,3-Dihydroxyisovaleriat
• III) 2,3-Dihydroxyisovaleriat zu 2-Oxoisovaleriat
• IV) 2-Oxoisovaleriat zu Isobutyraldehyd
• V) Isobutyraldehyd zu iso-Butanol und
• VI) iso-Butanol zu Isobuten

und ist u.a. in der WO2011076689 und WO2011076691 beschrieben.Another possible metabolic pathway is via the reaction sequence:

• I) pyruvate to 2-acetolactate
• II) 2-acetolactate to 2,3-dihydroxyisovalerate
• III) 2,3-dihydroxyisovalerate to 2-oxoisovalerate
• IV) 2-oxoisovalerate to isobutyraldehyde
• V) isobutyraldehyde to iso-butanol and
• VI) iso-butanol to isobutene

and is among others in the WO2011076689 and WO2011076691 described.

As already described, "diisobutene" is understood to mean 2,4,4-trimethyl-1-pentene, 2,4,4-trimethyl-2-pentene as main components and any desired mixtures of these two compounds.

• – Destillationsverfahren (welche aber dadurch erschwert sind, dass die Abtrennung im Gesamtprozess auftretender linearer Butenisomere einen hohen Aufwand erfordert, da die Siedepunkte der Isomere sehr nahe beieinander liegen, vgl. Kirk-Othmer Encyclopedia of Chemical Technology 3. Auflage 1978, Vol 4, John Wiley & Sons Inc., Seiten 358–360 ).
• – Aufreinigungs bzw. Trennungsverfahren, bei denen Isobuten aufgrund der erhöhten chemischen Reaktivität mittels einer chemischen Reaktion abgetrennt und anschließend wieder in Isobuten umgewandelt wird. Hierzu zählen u.a. Verfahren, wie reversible protonenkatalysierte Wasseranlagerung zum tertiär-Butanol oder die Methanolanlagerung zum Methyl-tertiär-butylether (vgl. EP1489062 ). Aus diesen Additionsprodukten wird dann durch Rückspaltung Isobuten zurückgewonnen (vgl. Weissermel, Arpe, Industrielle Organische Chemie, VCH Verlagsgesellschaft, 3. Auflage, 1988, S. 74–79 ).
• – Aufreinigungs- bzw. Trennungsverfahren, bei denen Isobuten aufgrund der kompakteren räumlichen Molekülstruktur, mittels geeigneter physikalischer Größenausschlussverfahren z.B. mittels Molekularsiebe mit geeigneter Porengröße, von linearen Butenisomeren getrennt wird (vgl. WO2012040859 , Weissermel, Arpe, Industrielle Organische Chemie, VCH Verlagsgesellschaft, 3. Auflage, 1988, S.74 ).
• – Aufreinigungs- bzw. Trennverfahren, die zur Entfernung von Kohlendioxid geeignet sind.

According to a preferred embodiment of the invention, there is no purification of the isobutene between step a) and b), in particular no purification for the removal of linear butene isomers and optionally of inerts such as carbon dioxide and / or nitrogen. By "purification", the following processes are understood in particular (but not limited to):

• - Distillation method (which, however, are complicated by the fact that the separation in the overall process of occurring linear butene isomers requires a lot of effort, since the boiling points of the isomers are very close to each other, see. Kirk-Othmer Encyclopedia of Chemical Technology 3rd Edition 1978, Vol 4, John Wiley & Sons Inc., pp. 358-360 ).
• - Purification or separation process in which isobutene is separated due to the increased chemical reactivity by means of a chemical reaction and then converted back into isobutene. These include, inter alia, processes such as reversible proton-catalyzed addition of water to the tertiary butanol or the methanol addition to methyl tertiary-butyl ether (see. EP1489062 ). Isobutene is then recovered from these addition products by cleavage (cf. Weissermel, Arpe, Industrial Organic Chemistry, VCH Verlagsgesellschaft, 3rd edition, 1988, pp. 74-79 ).
• - Purification or separation process in which isobutene is due to the more compact molecular structure, by means of suitable physical size exclusion process, for example by means of molecular sieves with a suitable pore size, separated from linear butene isomers (see. WO2012040859 . Weissermel, Arpe, Industrial Organic Chemistry, VCH Verlagsgesellschaft, 3rd edition, 1988, p.74 ).
• - Purification or separation processes, which are suitable for the removal of carbon dioxide.

• – aus dem Aufschluss und der Depolymerisation von Zellulose und Hemizellulose mittels geeigneter Methoden;
• – direkt aus Pflanzen mit hohem Zuckergehalt wie Zuckerrübe, Zuckerrohr, Zuckerpalme, Zuckerahorn, Zuckerhirse, Silber-Dattelpalme, Honigpalme, Palmyrapalme und Agaven mittels Extraktion;
• – aus der Depolymerisation von pflanzlicher Stärke durch Hydrolyse;
• – aus der Depolymerisation von tierischem Glycogen durch Hydrolyse;
• – direkt aus in der Milchwirtschaft gewonnener Milch.

According to a preferred embodiment of the invention, the isobutene in step a) is obtained from trisaccharides, disaccharides, monosaccharides, acetone or mixtures thereof. The tri- and disaccharides used are, in particular, raffinose, cellobiose, lactose, isomaltose, maltose and sucrose. The monosaccharides used are, in particular, D-glucose, D-fructose, D-galactose, D-mannose, DL-arabinose and DL-xylose. The tri-, di- and monosaccharides are among others (but not limited to)

• - from the digestion and depolymerization of cellulose and hemicellulose by appropriate methods;
• - directly from plants with high sugar content such as sugar beet, sugar cane, sugar palm, sugar maple, sugar millet, silver date palm, honey palm, palm blossom and agave by extraction;
• From the depolymerization of vegetable starch by hydrolysis;
• From the depolymerization of animal glycogen by hydrolysis;
• - directly from milk produced in the dairy industry.

In a further preferred embodiment of the invention, exclusively renewable raw materials are used for the fermentative production of isobutene. If desired, the origin of the carbon atoms may be from renewable resources. through the in ASTM D6866 described test method can be determined. The ratio of the C ¹⁴ to C ¹² carbon isotopes is determined and compared with the isotope ratio of a reference substance whose carbon atoms come to 100% from renewable raw material sources. This test method is also known in a modified form as the radiocarbon method and is used inter alia in Olsson, IU 1991, Euro Courses: Advanced Scientific Techniques, Volume 1, Issue Sci. Dating Methods, pages 15-35 - described.

According to a preferred embodiment of the invention, the fermentation process is carried out at temperatures of ≥ 20 ° C to ≤ 45 ° C and under atmospheric pressure and releases isobutene as a gaseous product. This embodiment has the advantage that the isobutene thus obtained can be used further immediately or after separation of inerts.

Alternatively, according to an equally preferred embodiment of the invention, the fermentation process is carried out at temperatures of ≥ 20 ° C to ≤ 45 ° C and under pressure between 1 to 30 bar. In this case, isobutene can be obtained as a liquid compound and separated by phase separation directly from the fermentation medium. The separation of inerts can be greatly facilitated in this preferred embodiment.

According to a preferred embodiment, step b) is carried out under acid catalysis. In this case, for example, sulfuric acid or acidic ion exchangers come into consideration, as in, inter alia Weissermel, Arpe, Industrial Organic Chemistry, VCH Verlagsgesellschaft, 3rd edition, 1988, p. 77 ; Hydrocarbon Processing, April 1973, p. 171-173 are described. Alternatively, the in US2004 / 0054246 . US4100220 (A) . US4447668 (A) and US5877372 (A) described methods are used.

• c) Aufreinigung des Diisobutens, bevorzugt durch Destillation

The method comprises a further step c), which is carried out according to b):

• c) purification of the diisobutene, preferably by distillation

Step c) is preferably carried out so that the unreacted volatile components are separated from the diisobutene and the resulting diisobutene is purified by distillation from the optionally formed in small amounts tri-isobutene and higher isobutene oligomers. Tri-isobutene thus obtained and the higher isobutene oligomers thus obtained can likewise be refined to give valuable secondary products.

Step d) is carried out in a preferred embodiment of the present invention by reaction in a hydroformylation reaction / oxo reaction to isononanal. The reaction is discussed further below:
This reaction is preferably carried out in such a way that isononyladehyde is obtained by reacting diisobutene with synthesis gas, preferably using cobalt or rhodium catalysts. Most of these contain predominantly 3,5,5-trimethylhexanal.

According to step e) optionally another derivatization can take place. In the event that isononanal is formed in step d), oxidation or reduction will often occur.

Depending on the application, the reduction of isononanal can take place by means of hydrogenation in the gas or liquid phase on the metal contact. Preferred catalysts are nickel or copper catalysts.

The oxidation of isononanal is preferably carried out with oxygen at moderately elevated temperatures and leads to isononanoic acid with 3,5,5-trimethylhexanoic acid as the main constituent ( Weissermel, Arpe, Industrial Organic Chemistry, VCH Verlagsgesellschaft, 3rd edition, 1988, pp. 143-145 ; Ullmanns Encyclopedia of Industrial Chemistry, 4th edition, 1983, Verlag Chemie, Volume 9, pages 144 ; EP 1854778 A1 ).

The reductive amination of isononanal is preferably carried out with ammonia, a primary or a secondary amine with hydrogen, particularly preferably in the presence of a catalyst, for example a nickel or cobalt catalyst. In this case, primary, secondary or tertiary Isononylamine form depending on the ratio of isononanal to the nitrogen-containing compound.

Isononanol can also be converted into the isononylamines by ammonolysis. The reaction preferably also takes place in the presence of hydrogen, preferably on a nickel or cobalt contact, although no hydrogen is consumed in this reaction.

After that, further derivatizations can take place. Particularly preferred is the vinylations to Isononylvinylethern.

This reaction can be carried out according to a preferred embodiment of the present invention by reacting the isononanol with acetylene, preferably in the presence of alkali metal oxides, at temperatures of 150-180 ° C ( Ullmann's Encyclopedia of Industrial Chemistry, 6th. Ed., Wiley-VCH, 2003, Vol. 38, pages 79-81 ).

wobei R gleich 3,5,5-Trimethylhexyl ist und R¹ häufig Methyl oder Ethyl bedeutet, so dass als Transvinylierungsreagenz beispielsweise Vinylacetat oder Vinylpropionat verwendet wird. ( Ullmanns Encyklopädie der technischen Chemie, 4. Auflage, 1983, Verlag Chemie, Band 23, Seiten 606–607 ). Um das chemische Gleichgewicht in Richtung des gewünschten Vinylethers zu drängen, verwendet man häufig einen Überschuss an dem Transvinylierungsreagenz R¹-C(O)O-CH=CH₂ und/oder entfernt die gebildete Carbonsäure aus dem Reaktionsgemisch. Die kontinuierliche oder semi-kontinuierliche Verfahrensführung kann beispielsweise als Reaktivdestillation ausgestaltet werden ( EP 0 497 340 A2 ) oder als Blasensäule mit aufgesetzter Säule, der noch zusätzlich eine Rektifikationssäule und eine Stripp-Säule nachgeschaltet sind ( WO 2011/139360 A1 und WO 2011/139361 A1 ). Es ist aber auch möglich, die Transvinylierungsreaktion ohne Entzug eines Reaktionspartners durchzuführen und das erhaltene Reaktionsgemisch in einem separaten Aufarbeitungsteil in die einzelnen Komponenten aufzuspalten ( DE 10 2012 002282.4 , DE 10 2012 002274.3 ). Als Transvinylierungskatalysatoren eignen sich beispielsweise Ruthenium- oder Palladiumverbindungen, die unmodifiziert oder modifiziert mit ein- oder mehrzähnigen stickstoff- oder phosphorhaltigen Liganden, wie 2,2´-Bipyridyl oder 1,10-Phenanthrolin, eingesetzt werden. Die als Koppelprodukt erhaltene zum Transvinylierungsreagenz korrespondierende Carbonsäure kann im Verbund weiter derivatisiert werden oder direkt als Wertprodukt genutzt werden. Beispielsweise kann die korrespondierende Carbonsäure in den Vinylester überführt werden, der dann wieder als Transvinylierungsreagenz für Isononanol verwendet wird, oder die korrespondierende Carbonsäure kann in einen Carbonsäureester, ein Carbonsäureanhydrid, ein Carbonsäurehalogenid, ein Carbonsäureamid oder in den entsprechenden Alkohol nach an sich bekannten Verfahren umgewandelt werden. In an alternative but equally preferred embodiment, isononanol undergoes a so-called transvinylation reaction with a vinyl ester of another carboxylic acid

wherein R is 3,5,5-trimethylhexyl and R ^{1 is} often methyl or ethyl, so that, for example, vinyl acetate or vinyl propionate is used as Transvinylierungsreagenz. ( Ullmann's Encyclopedia of Industrial Chemistry, 4th Edition, 1983, Verlag Chemie, Volume 23, pages 606-607 ). In order to force the chemical equilibrium towards the desired vinyl ether, an excess of the transvinylation reagent R ¹ -C (O) O-CH =CH ₂ is often used and / or the carboxylic acid formed is removed from the reaction mixture. The continuous or semi-continuous process can be configured, for example, as a reactive distillation ( EP 0 497 340 A2 ) or as a bubble column with attached column, which are additionally followed by a rectification column and a stripping column ( WO 2011/139360 A1 and WO 2011/139361 A1 ). However, it is also possible to carry out the transvinylation reaction without removal of a reaction partner and to split the resulting reaction mixture into the individual components in a separate work-up section ( DE 10 2012 002282.4 . DE 10 2012 002274.3 ). Suitable transvinylation catalysts are, for example, ruthenium or palladium compounds which are used unmodified or modified with mono- or polydentate nitrogen- or phosphorus-containing ligands, such as 2,2'-bipyridyl or 1,10-phenanthroline. The carboxylic acid corresponding to the transvinylation reagent obtained as by-product can be further derivatized in the composite or used directly as a product of value. For example, the corresponding carboxylic acid can be converted to the vinyl ester, which is then used again as a transvinylation reagent for isononanol, or the corresponding carboxylic acid can be converted to a carboxylic acid ester, a carboxylic acid anhydride, a carboxylic acid halide, a carboxylic acid amide or into the corresponding alcohol by methods known per se ,

According to an alternative but also preferred embodiment, the transvinylation reaction of the isononanol with a vinyl ether is carried out as a transvinylation reagent, so that mutatis mutandis the reaction conditions described above are used. Preferably, inexpensive vinyl ethers, such as methyl vinyl ether ( GB1105956 . JEMCKeon, P.Fitton, Tetrahedron 1972, 28 (2), 233 ).

According to an alternative but equally preferred embodiment, 3,5,5-trimethylhexanoic acid is derivatized into the glycidyl ester by methods known per se, for example by reaction with epichlorohydrin, which can be used to modify alkyd resins ( Weissermel, Arpe, Industrial Organic Chemistry, VCH Verlagsgesellschaft, 3rd edition, 1988, page 152 ; US6433217 )

Another option is the construction of the i-nonyl skeleton by acid-catalyzed carbonylation of the diisobutene in the sense of a Koch reaction (cf. Arpe, Industrial Organic Chemistry, 6th edition, 2007, page 154 et seq ). This essentially produces 2,2,4,4-tetramethylpentanoic acid. In analogy to the above statements, further derivatives are derived therefrom, such as the corresponding glycidyl ester or the vinyl ester of 2,2,4,4-tetramethylpentanoic acid.

The above-mentioned and the claimed synthesis steps to be used according to the invention described in the exemplary embodiments are not subject to special exceptions in their technical conception, so that the selection criteria known in the field of application can be used without restriction.

The individual combinations of the components and the features of the already mentioned embodiments are exemplary; the exchange and substitution of these teachings with other teachings contained in this document with the references cited are also expressly contemplated. Those skilled in the art will recognize that variations, modifications and other implementations described herein may also occur without departing from the spirit and scope of the invention. Accordingly, the above description is illustrative and not restrictive. The word "comprising" used in the claims does not exclude other ingredients or steps. The indefinite article "a" does not exclude the meaning of a plural. The mere fact that certain measures are recited in mutually different claims does not make it clear that a combination of these dimensions can not be used to advantage. The scope of the invention is defined in the following claims and the associated equivalents.

QUOTES INCLUDE IN THE DESCRIPTION

This list of the documents listed by the applicant has been generated automatically and is included solely for the better information of the reader. The list is not part of the German patent or utility model application. The DPMA assumes no liability for any errors or omissions.

Cited patent literature

• US 4698304 [0012]
• US 2011165644 A1 [0012]
• WO 2012052427 [0012]
• WO 2011032934 [0012]
• WO 2011076689 [0015]
• WO 2011076691 [0015]
• EP 1489062 [0017]
• WO 2012040859 [0017]
• US 2004/0054246 [0022]
• US 4100220 A [0022]
• US 4447668 A [0022]
• US 5877372 A [0022]
• EP 1854778 A1 [0028]
• EP 0497340 A2 [0033]
• WO 2011/139360 A1 [0033]
• WO 2011/139361 A1 [0033]
• DE 102012002282 [0033]
• DE 102012002274 [0033]
• GB 1105956 [0034]
• US 6433217 [0035]

Cited non-patent literature

• Ullmann's Encyclopedia of Industrial Chemistry, 6th. Ed., Wiley-VCH, 2003, Vol. 6, pp. 497-498; 502-503; and Vol. 2, page 33 [0003]
• Hydrocarbon Processing, April 1973, pages 171-173 [0003]
• Ullmann's Encyclopedia of Industrial Chemistry, 6th. Ed. Wiley-VCH, 2003, Vol. 2, page 75 [0003]
• Gogerty, DS and Bobik, TA 2010, Applied and Environmental Microbiology, p. 8004-8010 [0008]
• Fukuda, H., 1984 et al, From Agricultural and Biological Chemistry (1984), 48 (6), pp. 1679-82 [0012]
• Gogerty, DS and Bobik, TA 2010, Applied and Environmental Microbiology, page 8004-8010 [0013]
• Pressman, D. and Lucas, HJ 1940, Journal of the American Chemical Society, pages 2069-2081 [0013]
• Jones, TD and Woods, DR 1986, Microb. Reviews, pages 484-524 [0014]
• Taylor, DG et al 1980, Journal of General Microbiology, 118, pages 159-170. [0014]
• Kirk-Othmer Encyclopedia of Chemical Technology 3rd Edition 1978, Vol 4, John Wiley & Sons Inc., pp. 358-360 [0017]
• Weissermel, Arpe, Industrial Organic Chemistry, VCH Verlagsgesellschaft, 3rd edition, 1988, pp. 74-79 [0017]
• Weissermel, Arpe, Industrial Organic Chemistry, VCH Verlagsgesellschaft, 3rd edition, 1988, p.74 [0017]
• ASTM D6866 [0019]
• Olsson, IU 1991, Euro Courses: Advanced Scientific Techniques, Volume 1, Issue Sci. Dating Methods, pages 15-35 [0019]
• Weissermel, Arpe, Industrial Organic Chemistry, VCH Verlagsgesellschaft, 3rd edition, 1988, p. 77 [0022]
• Hydrocarbon Processing, April 1973, p. 171-173 [0022]
• Weissermel, Arpe, Industrial Organic Chemistry, VCH Verlagsgesellschaft, 3rd edition, 1988, pp. 143-145 [0028]
• Ullmanns Encyclopedia of Industrial Chemistry, 4th Edition, 1983, Verlag Chemie, Volume 9, pages 144 [0028]
• Ullmann's Encyclopedia of Industrial Chemistry, 6th. Ed., Wiley-VCH, 2003, Vol. 38, pp. 79-81 [0032]
• Ullmann's Encyclopedia of Industrial Chemistry, 4th Edition, 1983, Verlag Chemie, Volume 23, pages 606-607 [0033]
• JEMCKeon, P.Fitton, Tetrahedron 1972, 28 (2), 233 [0034]
• Weissermel, Arpe, Industrial Organic Chemistry, VCH Verlagsgesellschaft, 3rd edition, 1988, page 152 [0035]
• Arpe, Industrial Organic Chemistry, 6th Edition, 2007, page 154 ff. [0036]

Claims (12)

Process for the preparation of isononyl derivatives, comprising the steps a) fermentative production of isobutene b) Dimerization of isobutene to diisobutene c) Purification of the diisobutene d) extension by one carbon atom to obtain an isononyl derivative e) possibly further derivatizations The method of claim 1, wherein between step a) and b) no purification of the isobutene. Process according to claim 1 or 2, wherein the isobutene in step a) is obtained from trisaccharides, disaccharides, monosaccharides, acetone or mixtures thereof. Process according to claim 1 or 2, wherein renewable raw materials are used for the fermentative production of isobutene. Method according to one of claims 1 to 4, wherein the fermentation process at temperatures of ≥ 20 ° C to ≤ 45 ° C and carried out under atmospheric pressure and isobutene is released as a gaseous product. Method according to one of claims 1 to 4, wherein the fermentation process at temperatures of ≥ 20 ° C to ≤ 45 ° C and under pressure between 1 to 30 bar is performed. Method according to one of claims 1 to 6, wherein step b) is carried out under acid catalysis. Method according to one of claims 1 to 7, wherein step c) is carried out by distillation. Method according to one of claims 1 to 8, wherein step d) is carried out in the sense of a hydroformylation / oxo reaction. A process according to any one of claims 1 to 9, wherein step e) involves oxidation, reduction or amination. Method according to one of claims 1 to 8, wherein step d) leads by acid-catalyzed hydroxycarbonylation in the sense of a Koch reaction to 2,2,4,4-tetramethylpentanoic acid as a main component. Method according to one of claims 1 to 11, wherein step e) includes a reaction with acetylene, with epichlorohydrin, with a vinyl carboxylate and / or with a vinyl ether.