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Title:
NEW PROCESS
Document Type and Number:
WIPO Patent Application WO/2012/035017
Kind Code:
A1
Abstract:
A process for the preparation of a compound of formula (I) which are useful as intermediates in the preparation of pharmaceutically active compounds.

Inventors:
HARNETT, Gerard, John (39 College Green, Ennis County Clare, IE)
HAYES, John (12 Victoria Court, Ennis County Clare, IE)
REENTS, Reinhard (Drosselstrasse 3, Muenchenstein, CH-4142, CH)
SMITH, Dennis, A. (29 Silvergrove, Ballybeg, Ennis County Clare, IE)
WALSH, Andrew (Clondrinagh, Lissycasey County Clare, IE)
Application Number:
EP2011/065860
Publication Date:
March 22, 2012
Filing Date:
September 13, 2011
Export Citation:
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Assignee:
F. HOFFMANN-LA ROCHE AG (Grenzacherstrasse 124, Basel, CH-4070, CH)
HARNETT, Gerard, John (39 College Green, Ennis County Clare, IE)
HAYES, John (12 Victoria Court, Ennis County Clare, IE)
REENTS, Reinhard (Drosselstrasse 3, Muenchenstein, CH-4142, CH)
SMITH, Dennis, A. (29 Silvergrove, Ballybeg, Ennis County Clare, IE)
WALSH, Andrew (Clondrinagh, Lissycasey County Clare, IE)
International Classes:
C07C253/30; C07C51/06; C07C51/08; C07C51/60; C07C61/08; C07C255/46; C07C319/06; C07C319/22; C07C321/28; C07C327/06
Attorney, Agent or Firm:
SALUD, Carlos (Grenzacherstrasse 124, Basel, CH-4070, CH)
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Claims:
Claims

1. A process for the preparation of the compound of a cyclohexanecarbonitrile derivative of formula (I):

wherein R1 is (Ci-Cs)alkyl, preferably pent-3-yl, comprising adding a Grignard reagent to cyclohexanecarbonitrile of formula (II)

in the presence of an alkylating agent.

2. A process according to claim 1, wherein the coupling reaction is carried out in the presence of a secondary amine.

3. A process according to claim 1, for the preparation of the compound of a

cyclohexanecarbonitrile derivative of formula (I):

wherein R1 is (Ci-Cs)alkyl, comprising adding a Grignard reagent to a solution or mixture comprising

cyclohexanecarbonitrile of formula (II) according to claim 1, secondary amine and an alkylating agent.

4. A process according to anyone of claims 1 to 3 further comprising the preparation of a cyclohexanecarboxylic acid derivative of formula (IV):

wherein R1 is as defined in claim 1, comprising:

a) hydro ly sing a cyclohexanecarbonitrile derivative of formula (I):

to obtain a cyclohexanecarboxylic acid amide derivative of formula (III);

b) further hydrolysing compound of formula (III) to obtain the compound of formula (IV).

5. A process according to claim 4 additionally comprising the step of reacting a halogenating agent in the presence of a tri-(Ci-C5)alkylamine with compound of formula (IV) as defined in claim 3, to obtain compound of formula (V), wherein X is I, Br, CI or F:

(V)

6. The process according to claim 5, further comprising the step of acylating a compound of the formula VF

with a compound of formula (V) to obtain a compound of formula VI:

wherein R is as defined in claim 1.

7. The process according to claim 6 further comprising the step of reducing the compound of formula VI with a reducing agent to obtain a compound of formula VII :

(VII)

8. The process according to claim 7 further comprising the step of acylating the compound of formula VII with R4C(0)X', wherei ' is I, Br, CI or F, to obtain a compound of formula VIII:

(VI II)

wherein R4 is (Ci-Cs)alkyl and R1 is as defined in claim 1.

9. A process according to any one of claims 1, 2 or 3, wherein the coupling reaction is followed by a mineral acid quenching, such as hydrofluoric acid, hydrochloric acid, boric acid, acetic acid, formic acid, nitric acid, phosphoric acid or sulfuric acid.

10. A process according to any one of claims 1, 2, 3 or 9, wherein the coupling reaction is followed by a hydrochloric acid quenching.

1 1. A process according to any one of claims 1, 2, 3, 9 or 10, wherein a nonprotic solvent is present.

12. A process according to claim 1 1, wherein the nonprotic solvent is tetrahydrofuran.

13. A process according to any one of claims 1 to 12, wherein the alkylating agent is 1-halo- CH2R1 or a sulfonate ester wherein R1 is defined in claim 1.

14. A process according to any one of claims 1 to 13, wherein the alkylating agent is l-halo-2- ethylbutane.

15. A process according to any one of claims 1 to 14, wherein the alkylating agent is 2-ethyl-l- butanol. 16. A process according to any one of claims 1 to 15, wherein the alkylating agent is l-bromo-2- ethylbutane.

17. A process according to any one of claims 1 to 16, wherein the Grignard reagent is (Ci- C6)alkyl-magnesium-halide, phenyl-magnesium-halide, heteroaryl-magnesium-halide or (C3- C6)cycloakyl-magnesium-halide 18. A process according to any one of claims 1 to 17, wherein the Grignard reagent is methylmagnesiumchloride.

19. A process according to any one of claims 1 to 18, wherein the secondary amine is diethylamine or diisopropylamine.

20. A process according to any one of claims 1 to 19, wherein the secondary amine is diethylamine.

21. A process according to any one of claims 1 to 20, wherein the secondary amine is in catalytic amount.

22. A process according to any one of claims 1 to 21, wherein 0.01 to 0.5 equivalents of the secondary amine with respect to cyclohexanecarbonitrile is used. 23. A process according to any of claims 1 to 22, wherein the process is semi-continuous or continuous, particularly continuous.

24. A process for the preparation of S-[2-([[l-(2-ethylbutyl)-cyclohexyl]- carbonyl]amino)phenyl]2-methylpropanethioate comprising the formation of a compound of formula (Γ):

comprising adding a Grignard reagent to a solution or a mixture of cyclohexanecarbonitrile of formula (II), a secondary amine or in the presence of an alkylating agent.

25. The invention as hereinbefore described.

Description:
NEW PROCESS

The present invention relates to a process for the preparation of a cyclohexanecarboxylic acid derivative which is useful as an intermediate in the preparation of pharmaceutically active compounds.

In a first embodiment, the present invention provides a process for the preparation of the compound of a cyclohexanecarbonitrile derivative of formula (I):

wherein R 1 is (Ci-Cs)alkyl, preferably pent-3-yl, comprising adding a Grignard reagent, such as (Ci-C6)alkyl-magnesium-halide, phenyl-magnesium-halide, heteroaryl-magnesium-halide or (C 3 - C6)cycloakyl-magnesium-halide to cyclohexanecarbonitrile of formula (II)

in the presence of an alkylating agent such as a l-halo-CH^R 1 , preferably l-halo-2-ethylbutane, or a sulfonate ester of R^H^-OH, preferably of 2-ethyl-l-butanol, wherein R^s as defined above.

In particular, the above mentioned coupling reaction is carried out in the presence of a secondary amine. In particular, the above mentioned coupling reaction is followed by a mineral acid quenching, such as hydrofluoric acid, hydrochloric acid, boric acid, acetic acid, formic acid, nitric acid, phosphoric acid or sulfuric acid, most preferably by hydrochloric acid.

Contrary to expectation it was surprisingly found that adding the Grignard reagent to a mixture of the cyclohexanecarbonitrile and the alkylating agent, instead of first combining the Grignard reagent and the cyclohexanecarbonitrile before coupling with the alkylating agent, led to improved yields and a reduction in the formation of by-products. It is most surprising that the reaction is not complicated by reaction between the Grignard reagent and the alkylating agent.

The compound of formula (I) may be used as intermediate in the synthesis of valuable pharmaceutical compounds. For example l-(2-ethylbutyl)cyclohexanecarbonitrile may be used in the synthesis of the ones as described in EP 1,020, 439 based on the intermediate process disclosed in WO 2009121788.

Unless otherwise stated, the following terms used in the specification and claims have the meanings given below:

The term "halo" means fluoro, chloro, bromo or iodo, preferably chloro or bromo.

"alkali metal" or "alkali" refers to lithium, sodium, potassium, rubidium and caesium. Preferable alkali metal is lithium or sodium. Of these, sodium is most preferred.

"(Ci-C8)alkyl" refers to a branched or straight hydrocarbon chain of one to eight carbon atoms, such as methyl, ethyl, n-propyl, isopropyl, n-butyl, isobutyl, sec-butyl, t-butyl, pentyl, hexyl and heptyl. (Ci-C 6 )alkyl is preferred.

"(Ci-C6)alkoxy" means a moiety of the formula -OR ab , wherein R ab is an (Ci-C 6 )alkyl moiety as defined herein. Examples of alkoxy moieties include, but are not limited to, methoxy, ethoxy, isopropoxy, and the like.

"(Ci-C6)alkylene" means a linear saturated divalent hydrocarbon moiety of one to six carbon atoms or a branched saturated divalent hydrocarbon moiety of three to six carbon atoms, e.g., methylene, ethylene, 2,2-dimethylethylene, propylene, 2-methylpropylene, butylene, pentylene, and the like.

"halo-(Ci-Cs)alkyl " refers to an alkyl, as defined above, substituted with one or more halogen atoms, preferably with one to three halogen atoms. More preferred halo-(Ci-Cs)alkyl is the chloro- and fluoro-(Ci-C8)alkyl.

"halo-(Ci-Ce)alkoxy " refers to an alkoxy, as defined above, substituted with one or more halogen atoms, preferably with one to three halogen atoms. More preferred halo-(Ci-Ce)alkoxy are the chloro- and fluoro-(Ci-C8)alkoxy.

"(C3-C6)cycloalkyl" refers to a single saturated carbocyclic ring of thee to six ring carbons, such as cyclopropyl, cyclobutyl, cyclopentyl and cyclohexyl. Cycloalkyl may optionally be substituted with one or more substituents, preferably one, two or three, substituents. Preferably, cycloalkyl substituent is selected from the group consisting of (Ci-Ce)alkyl, hydroxy, (Ci- C 6 )alkoxy, halo(Ci-Ce)alkyl, halo(Ci-Ce)alkoxy, halo, amino, mono- and di(Ci-C 6 )alkylamino, hetero(Ci-Ce)alkyl, acyl, aryl and heteroaryl. "Secondary amine" refers to an amine of formula HNR 2 R 3 wherein R 2 and R 3 may be the same or different and are independently selected from (Ci-C 6 )alkyl or (C3-Ce)cycloalkyl, or R 2 and R 3 taken together with the nitrogen atom to which they are attached, form a (C 4 -C 8 )

heterocycloalkane optionally containing an additional heteroatom selected from O or N.

Representative examples include, but are not limited to, piperidine, 4-methyl-piperidine, piperazine, pyrrolidine, morpholine, dimethylamine, diethylamine, diisopropylamine, dicyclohexylamine, ethylmethylamine, ethylpropyl amine and methylpropylamine. Preferably, the secondary amine is chosen from diethylamine, diisopropylamine, dicyclohexylamine, ethylmethylamine, ethylpropylamine, methylpropylamine and morpholine. The more preferred secondary amine is diethylamine or diisopropylamine, most preferred diethylamine. "(C4-C 8 )heterocycloalkane" refers to a saturated non-aromatic cyclic compound of 4 to 8 ring atoms in which one or two ring atoms are heteroatoms selected from N or O, and the

heterocycloalkane may be optionally substituted with one or more (Ci-C3)alkyl, preferably one (Ci-C 3 )alkyl.

"Acyl" means a group of the formula -C(0)-R ag , -C(0)-OR ag ' , -C(0)-OC(0)R ag or -C(O)- R ag R ah wherein R ag is hydrogen, (Ci-C 6 )alkyl, halo(Ci-C 6 )alkyl, heteroalkyl or amino as defined herein, and R ah is hydrogen or (Ci-C 6 )alkyl as defined herein.

"Amino" means a group - R R wherein R and R each independently is hydrogen or (Ci- C 6 )alkyl.

"Aryl" means a monovalent monocyclic or bicyclic aromatic hydrocarbon moiety which is optionally substituted with one or more, preferably one, two or three, substituents, each of which is preferably selected from the group consisting of (Ci-C 6 )alkyl, hydroxy, (Ci-C 6 )alkoxy, halo(Ci-Ce)alkyl, halo(Ci-Ce)alkoxy, halo, nitro, cyano, amino, mono- and di(Ci-C 6 )alkylamino, methylenedioxy, ethylenedioxy, acyl, hetero(Ci-Ce)alkyl, aryl, optionally substituted heteroaryl, optionally substituted aralkyl, and optionally substituted heteroaralkyl. A particularly preferred aryl substituent is halide. More specifically the term aryl includes, but is not limited to, phenyl, 1-naphthyl, 2-naphthyl, and the like, each of which can be substituted or unsubstituted. "Aralkyl" refers to a moiety of the formula -R bc -R bd where R bd is aryl and R bc is (Ci-C 6 )alkylene as defined herein.

"Heteroaryl" means a monovalent monocyclic or bicyclic moiety of 5 to 12 ring atoms having at least one aromatic ring containing one, two, or three ring heteroatoms selected from N, O, or S (preferably N or O), the remaining ring atoms being C, with the understanding that the attachment point of the heteroaryl moiety will be on an aromatic ring. The heteroaryl ring is optionally substituted independently with one or more substituents, preferably one, two or three substituents, each of which is independently selected from (Ci-C6)alkyl, halo(Ci-Ce)alkyl, hydroxy, (Ci-C 6 )alkoxy, halo, nitro and cyano. More specifically the term heteroaryl includes, but is not limited to, pyridyl, furanyl, thienyl, thiazolyl, isothiazolyl, triazolyl, imidazolyl, isoxazolyl, pyrrolyl, pyrazolyl, pyrimidinyl, benzofuranyl, tetrahydrobenzofuranyl,

isobenzofuranyl, benzothiazolyl, benzoisothiazolyl, benzotriazolyl, indolyl, isoindolyl, benzoxazolyl, quinolyl, tetrahydroquinolinyl, isoquinolyl, benzimidazolyl, benzisoxazolyl or benzothienyl, imidazo[l,2-a]-pyridinyl, imidazo[2,l-b]thiazolyl, and the derivatives thereof. "nitrosylating agent"comprises nitrosylsulfuric acid, sodium nitrite or a mixture thereof. Most preferably, the nirtosylating agent is nitrosylsulfuric acid.

"sulfonate ester" of R^F^-OH" or (R ca )(R cb )CH-OH refers to a substituted or an unsubstituted phenyl-sulfonate, an unsubstituted naphthalene-sulfonate or a (Ci-Ce)alkylsulfonate ester derivative of R^H^-OH or (R ca )(R cb )CH-OH, respectively, wherein substituted phenyl and the (Ci-C 6 )alkyl chain, R 1 , R ca , R cb are as defined herein. Representative examples include, but are not limited to, benzenesulfonic acid 2-ethyl-butyl ester, 1-naphthalenesulfonic acid 2-ethyl-butyl ester, 2-naphthalenesulfonic acid 2-ethyl-butyl ester, toluene-4-sulfonic acid 2-ethyl-butyl ester, 4-nitro-benzenesulfonic acid 2-ethyl-butyl ester, 2,4,6-trimethyl-benzenesulfonic acid 2-ethyl- butyl ester, ethanesulfonic acid 2-ethyl-butyl ester, methanesulfonic acid 2-ethyl-butyl ester and butanesulfonic acid 2-ethyl-butyl ester.

"strong acid" refers to an acid that dissociates completely in an aqueous solution with a pH < 2. The strong acids include, but are not limited to: sulphuric acid (H 2 SO 4 ), hydrohalogenic acid (i.e. HX" wherein X" is I, Br, CI or F), nitric acid (HN0 3 ), phosphoric acid (H 3 PO 4 ) and

combinations thereof. Preferably, the strong acid is H 2 SO 4 or hydrohalogenic acid, wherein X" is Br or CI. Most preferably, the strong acid is H 2 SO 4 . Preferably the concentration of H 2 SO 4 in water is in the range of 75% to 90 %, more preferably 78 to 83 %, most preferably 82.5 %. "aqueous base" refers to a solution comprising a base and water. Numerous bases which readily dissolve in water are known in the art, such as NaOH, KOH, Ca(OH) 2 , Mg(OH) 2 , preferably NaOH or KOH. More preferably the aqueous base has a pH of 12 to 14. Accordingly, in another embodiment the present invention provides a process comprising the synthetic steps represented in the following scheme 1 :

Scheme 1.

(VI I I) wherein X is I, Br, CI or F, R 1 is as defined above and R 4 is (Ci-C8)alkyl. In particular, the process comprises hydrolysing cyclohexanecarbonitrile derivative of formula (I) to obtain a cyclohexanecarboxylic acid amide derivative of formula (III) with for example H 2 0 in the presence of a strong acid, or with an aqueous base. The process further comprises reacting the said cyclohexanecarboxylic acid amide derivative with a nitrosyla

ting agent, to obtain the compound of formula (IV). the process comprises reacting a

cyclohexanecarboxylic acid derivative of formula (IV) with a halogenating agent, such as PX 3 , PX 5 , SOX 2 or NCX, to obtain the acyl halide of formula (V). The halogenating step is preferably carried out in the presence of tri-(Ci-C5)alkylamine. Furthermore, the process comprises reacting acyl halide with bis(2-aminophenyl)disulfide to acylate the amino groups of the bis(2- aminophenyl)disulfide, reducing the amino-acylated disulfide product with a reducing agent such as triphenylphosphine, zinc or sodium borohydride to yield the thiol product, and acylating the thiol group in the thiol product with R 4 C(0)X', wherein X' is I, Br, CI or F.

The additional steps may be performed, e.g., according to the procedures described in Shinkai et al, J. Med. Chem. 43 :3566-3572 (2000), WO 2007/051714, WO2009121788.

Preferably the halogenating agent is chosen from thionyl chloride, phosphorus pentachloride, oxalyl chloride, phosphorus tribromide and cyanuric fluoride, most preferably thionyl chloride. The acyl halide of formula (V) wherein X is CI is most preferred.

In the thiol acylation step, preferably the acylating agent is R 4 C(0)X', wherein X' is CI. Most preferably R 4 is isopropyl.

Unless otherwise stated, organic solvent referred herein comprises ether like solvent (e.g.

tetrahydrofuran, methyltetrahydrofuran, diisopropyl ether, t-butylmethyl ether or dibutyl ether, ethyl acetate, butyl acetate), alcohol solvent (e.g. methanol or ethanol), aliphatic hydrocarbon solvent (e.g. hexane, heptane or pentane), saturated alicyclic hydrocarbon solvent (e.g.

cyclohexane or cyclopentane) or aromatic solvent (e.g. toluene or t-butyl-benzene) In a further embodiment, the present invention provides processes as described above wherein nitrosylating agent is generated in situ e.g. mixing H 2 SO 4 and nitrous acid (HNO 2 ) or

H2S0 3 /HN0 3 or N2O3/H2SO4 or HNO3/SO2 to obtain nitrosulfuric acic (NOHSO4).

In another embodiment the invention provides a process for the preparation of the compound of a cyclohexanecarbonitrile derivative of formula (I):

wherein R 1 is (Ci-Cs)alkyl, preferably pent-3-yl, comprising adding a Grignard reagent, such as (Ci-C6)alkyl-magnesium-halide, phenyl-magnesium-halide, heteroaryl-magnesium-halide or (C3- C6)cycloakyl-magnesium-halide to a solution or mixture comprising cyclohexanecarbonitrile of formula (II), secondary amine and an alkylating agent such as a l-halo-CH 2 R 1 , preferably 1- halo-2-ethylbutane, or a sulfonate ester of R 1 CH 2 -OH, preferably of 2-ethyl-l-butanol, wherein R^s as defined above.

Within the processes defined above, preferably the halide of Grignard reagent is chosen from chloride, bromide and iodide, more preferably chloride or bromide, most preferably chloride. The preferred alkyl of the Grignard reagent is (C1-C3) alkyl, more preferably methyl. The most preferred Grignard reagent is methylmagnesiumchloride.

The preferred alkylating agent is l-halo-2-ethylbutane, most preferably l-bromo-2-ethylbutane.

Preferably the alkylation is performed in the presence of a catalytic amount of secondary amine, such as 0.01 to 0.5 equivalent of secondary amine with respect to

cyclohexanecarbonitrile, most preferably 0.05 eq. The dosing time of the Grignard reagent, is preferably 0.5 to 4h, most preferably 1.5h. This addition can be carried out at temperature between 50 to 80C, in particular between 60 to 75°C. After the addition of the Grignard reagent the reaction mixture can be stirred at reflux for a time, in particular for one hour. A nonprotic organic solvent is the preferred solvent during the alkylation, such as

tetrahydrofuran, alone or in combination with another nonprotic solvent, e.g. from the group of the apolar solvents hexane, heptane, methyl tetrahydrofurane, toluene and t-butyl-benzene, more preferably hexane, heptane, toluene and t-butyl-benzene. Most preferably the nonprotic solvent is tetrahydrofuran. Preferably the hydro lysing agent of the cyclohexanecarbonitrile derivative of formula (I) is a strong acid. The most preferred strong acid is sulphuric acid. The hydrolysis step is either carried out by dosing compound of formula (I) to sulphuric acid at a temperature of 80 °C to 120°C or both compound of formula (I) and sulphuric acid are heated as a mixture to a temperature of 80 °C to 120 °C. More preferably the temperature in both modes of addition is 95 to 110 °C, most preferably 105 to 110 °C. 1.5 to 4 equivalents of sulphuric acid with respect to compound of formula (I) is preferably used. More preferably 1.9 to 3.6 equivalents are used. Most preferably 2 equivalents are used. The hydrolysis is carried out with excess water, preferably 5 to 25 eq. of water with respect to the compound of formula (I), more preferably 10 to 20 eq. Most preferably, 14 to 16 eq. of water is used with respect to the compound of formula (I). For the hydrolysis of the amide of formula (III), preferably 1.1 to 1.4 equivalents of

nitrosylsulfuric acid is used, most preferably 1.2 to 1.4 equivalent. Either nitrosylsulfuric acid is added first and followed by water or the water is first added and followed by addition of nitrosylsulfuric acid. The second addition mode is preferred. Preferably, the dosing temperature is at 20 to 65°C, most preferably 60 to 65°C. According to the present invention the "basic aqueous solution" for the extraction step (c) is preferably chosen from inorganic bases or organic bases, a mixture thereof, or from commonly known buffering solutions of suitable pH. The preferred inorganic base is an alkali base, such as alkali carbonate, alkali bicarbonate, alkali borate, alkali phosphate, alkali-hydroxide. A more preferred basic aqueous solution is chosen from solution of potassium bicarbonate, sodium bicarbonate, potassium carbonate, sodium carbonate, sodium borate, sodium hydroxide, or a mixture thereof. The most preferred basic aqueous solution is a solution of sodium bicarbonate, sodium hydroxide or a mixture thereof.

In a further embodiment the present invention provides a process for the preparation of [2-([[l- (2-ethylbutyl)-cyclohexyl]-carbonyl]amino)phenyl]2-methylpro panethioate comprising the formation of a compound of formula (I) obtained by any of the processes and conditions mentioned previously.

The starting materials and reagents, which do not have their synthetic route explicitly disclosed herein, are generally available from commercial sources or are readily prepared using methods well known to the person skilled in the art. For instance, compound of formula (II) is commercially available or can be prepared by procedures known to the skilled person.

The methods of the present invention may be carried out as semi-continuous or continuous processes, more preferably as continuous processes.

The following examples are provided for the purpose of further illustration and are not intended to limit the scope of the claimed invention.

The following abbreviations and definitions are used: br (broad); BuLi (butyllithium); CDC1 3 (deuterated chloroform); eq. (equivalent); g (gram); GC (gas chromatography); h (hour); HC1 (hydrochloric acid); H 2 0 (water); HPLC (High-Performance Liquid Chromatography); ISP (Isotopic Spin Population); KOH (Potassium Hydroxide); LDA (Lithium Diisopropylamide ); M (Molar); m (multiplet); MS (Mass Spectroscopy); mL (milliliter); NaOH (Sodium hydroxide); MR (nuclear magnetic resonance); s (singlet); sec (second); t (triplet); THF (tetrahydrofuran);

Example 1 : l-(2-Ethyl-butyl)-cyclohexanecarbonitrile

Under argon 50.0 g cyclohexane carbonitrile (458 mmol), 1.68g (2.39 mL) diethylamine (22.9 mmol, 0.05 eq.), 76.4 g (64.7 mL) 2-ethylbutyl bromide (463 mmol, 1.01 eq) and 101 g (114 mL) THF are added at 25°C. Then at a temperature of 70 °C using an infusion pump within 4 hours, 173 g methylmagnesiumchloride solution (3M) in THF (22.2% (m/m), 513 mmol, 1.12 eq.) are added. The reaction is stirred for lh at reflux temperature (73°C). A conversion control sample shows <0.1 % (red. area) cyclohexanecarbonitrile. After reaction completion the temperature of the reaction mixture is reduced to 66°C. 232g (232 mL) water 24.8 g (20.6 mL) HC1 37% (251 mmol, 0.55 eq) and 62 g (91.2 mL) heptane are charged under stirring at 25°C . The above hot reaction mixture (55°C) is transferred from the reactor into the flask (25- 60 ) within 15 minutes. The reactor is washed with 20g (23 mL) THF and the wash solvent is also transferred into the Erlenmeyer flask. The biphasic mixture is stirred for 10 minutes. The two clear phases are separated and the lower aqueous phase is removed. The upper organic phase containing product is washed with 154 g water and concentrated at 50°C / <20 mbar. The residue is degassed at 50°C/ <20mbar. Obtained are 89.4 g l-(2-ethyl-butyl)-cyclohexanecarbonitrile crude (Assay: 93.8%, 434 mmol, yield: 94.2%) as an yellow to light brown oil. The product is transferred to a distillation flask. First the pressure in the distillation flask is reduced to 7 mbar, then l-(2-ethyl-butyl)-cyclohexanecarbonitrile crude heated slowly to 116°C .Collected are 6.56 g 1 st cut (1.75g, assay: 78.8%, 2% yield) and 2 nd cut 4.81g, assay: 93.9%, yield 5%) as a colorless to light yellow liquid at 109-116°C ) and then further cuts at 116-117°C ) to give 73.6 g l-(2-ethyl-butyl)-cyclohexanecarbonitrile distilled (assay: 98.5%, yield 82%) as a colorless liquid. Discarded are 2.0 g distillation residue as a brown liquid.

Example 2 : l-(2-Ethyl-butyl)-cyclohexanecarboxylic acid

Under argon 21.1 g (11.6 ml) sulfuric acid (96%) (207 mmol, 2.0 eq, contains 0.84 g water (47 mmol, 0.46 eq)) and 1.96 g water (109 mmol, 1.05 eq) is heated to 105 °C Ti.

20.0 g l-(2-ethyl-butyl)-cyclohexanecarbonitrile (103 mmol, 1.0 eq) is added within 15min at 105°C Ti and the reaction mixture is stirred 2h. A conversion control sample shows l-(2-ethyl- butyl)-cyclohexanecarbonitrile <0.1%. The reaction mixture is cooled to 50°C Ti. Then 28.0 g water (1.55 mol, 15 eq) is added within 5 minutes at 51°C Ti (exotherm). The reaction mixture temperature is adjusted to 61 °C Ti and with vigorous stirring 36.2 g (19 mL) nitrosyl sulfuric acid (40%)) in sulfuric acid (114 mmol, 1.1 eq) is added constantly within 75 minutes at 60°C Ti . The reaction mixture is stirred for 45 minutes at 64 °C Ti. A conversion control sample shows 0.2 norm%> l-(2-ethyl-butyl)-cyclohexanecarboxylic acid amide ). To the biphasic mixture at 64 °C 20 g water is added and 13 g aq. HNO x is evaporated at 131-137 °C and 1000 mbar. 20 g water is added and 20 g aq. FINO x is evaporated at 131-137 °C and 1000 mbar. In the residue <50 ppm nitrite/nitrate are found. The reaction mixture is cooled to 20 °C 20.0 g (29.4 mL) Heptane are added and the biphasic mixture is stirred for 5 minutes. The lower aqueous phase is separated and discarded. To the organic phase 20.0 g water is added and the biphasic mixture is stirred for 10 minutes. The lower aqueous phase is separated and discarded. l-(2-ethyl-butyl)-cyclohexanecarboxylic acid in heptane is filtered using a paper filter and stored. The product containing organic phase is distilled in a Dean- Stark-apparatus at 1 12°C and 1000 mbar until no water can be removed in the water separator.

The organic phase is concentrated at 1 12°C and 1000 mbar to final a volume of 40 mL (27.2g) clear heptane phase. 10 g (14.7 mL) heptane are added. Obtained are 36.56 g l-(2-ethyl-butyl)- cyclohexanecarboxylic acid in heptane (91.3 mmol, assay 53.01%, contained weight: 19.38 g 1- (2-Ethyl-butyl)-cyclohexanecarboxylic acid, yield 88.2%) as light yellow to orange solution. Example 3 : l-(2-Ethyl-butyl)-cyclohexanecarbonitrile

To a 1-litre jacketed flask fitted with a stirrer, thermometer, condenser and pressure-equalised dropping funnel and purged with nitrogen were added cyclohexanecarbonitrile (21.8 g, 200 mmol), diethylamine (1.46 g, 20 mmol), 2-ethylbutybromide (33.3 g, 202 mmol) and tetrahydrofuran (44.0 g). The resulting clear solution was heated to 45 °C and stirred under a continuous stream of nitrogen. Methylmagnesium chloride in tetrahydrofuran (83 g of a 22% solution, 0.246 mmol) was added over one hour while maintaining the temperature of the reaction mixture between 45.3 and 61.4 °C. The mixture was then refluxed between 67.4 and 70.2 °C for 75 minutes. Analysis of the reaction mixture by GLC showed 98.1%> l-(2-ethyl- butyl)-cyclohexanecarbonitrile, 0.9% ethylbutylbromide, 0.0%> cyclohexanecarbonitrile and 0.2% acetylcyclohexane. The mixture was cooled to 48.7 °C then transferred over 25 minutes into a stirred mixture of deionised water (101 g), hydrochloric acid (37%, 10.8 g) and n-heptane (27 g) which had been precooled to 15 °C. The temperature was kept between 15 and 60 °C during the addition. The reaction flask was rinsed with tetrahydrofuran (8.9 g) into the quenched mixture which was then cooled and agitated at between 15 and 30 °C for 20 minutes. After settling for 10 minutes the lower aqueous layer was split off. The remaining organic layer was washed with deionised water (68 g) before being concentrated under reduced pressure on the rotary evaporator at up to 60 °C until no further solvent distilled over. The product was further degassed under high vacuum at 80 °C to leave 38.3 g of pale yellow oil. The w/w assay of the product as determined by internal standard GLC was 95.8%, giving a contained yield of l-(2- ethyl-butyl)-cyclohexanecarbonitrile of 36.7 g or 95.0% of theory. Area normalised assay by GLC showed l-(2-ethyl-butyl)-cyclohexanecarbonitrile 99.1%>, ethylbutyl bromide 0.2%, acetylcyclohexane 0.2% and others 0.5%.

Example 4 : l-(2-Ethyl-butyl)-cyclohexanecarbonitrile To a 1-litre jacketed flask fitted with a stirrer, thermometer, condenser and pressure-equalised dropping funnel and purged with nitrogen were added cyclohexanecarbonitrile (21.8 g, 200 mmol), diethylamine (0.37 g, 20 mmol), 2-ethylbutyl bromide (33.3 g, 202 mmol) and tetrahydrofuran (44.0 g). The resulting clear solution was heated to 45 to 50 °C and stirred under a continuous stream of nitrogen. Methylmagnesium chloride in tetrahydrofuran (83 g of a 22% solution, 0.246 mmol) was added over 65 minutes while maintaining the temperature of the reaction mixture between 46.0 and 55.2 °C. The mixture was then refluxed between 67.5 and 70.2 °C for 100 minutes. Analysis of the reaction mixture by gas liquid chromatography (GLC) showed 96.6%l-(2-ethyl-butyl)-cyclohexanecarbonitrile, 2.0% ethylbutylbromide, 0.0% cyclohexanecarbonitrile and 0.9% acetylcyclohexane. The mixture was cooled to around 50 °C then transferred over 15 minutes into a stirred mixture of deionised water (101 g), hydrochloric acid (37%), 10.8 g) and n- heptane (27 g) which had been precooled to 15 °C. The temperature was kept between 15 and 60 °C during the addition. The reaction flask was rinsed with tetrahydrofuran (8.9 g) into the biphasic mixture which was then cooled and agitated at between 15 and 30 °C for 20 minutes. After settling for 10 minutes the lower aqueous layer was split off. The remaining organic layer was washed with deionised water (68 g) before being concentrated under reduced pressure on the rotary evaporator at up to 50 °C until no further solvent distilled over. The product was further degassed under high vacuum at 80 °C to leave 37.7 g of pale yellow oil. The w/w assay of the product as determined by internal standard gas liquid chromatography (GLC) was 96.9%, giving a contained yield of l-(2-ethyl-butyl)- cyclohexanecarbonitrile of 36.5 g or 94.6% of theory. Area normalised assay by GLC showed 1- (2-ethyl-butyl)-cyclohexanecarbonitrile 97.9%, ethylbutyl bromide 0.8%, acetylcyclohexane 1.1% and others 0.2%.