Patent Grant
9174207
This application is the United States national phase of PCT/EP2009/062896, filed Oct. 5, 2009, and designating the United States (published in the French language on Apr. 29, 2010, as WO 2010/046226 A1; the title and abstract were also published in English) and claims priority under 35 U.S.C. §119 of FR 0805821, filed Oct. 21, 2008, each hereby expressly incorporated by reference in its entirety and each assigned to the assignee hereof.
The present invention relates to a process for producing compounds comprising at least one nitrile function by hydrocyanation of a compound comprising at least one non-conjugated unsaturation.
It relates more particularly to a production process implementing the reaction of hydrogen cyanide with an organic compound comprising a non-conjugated unsaturation in the presence of a catalytic system comprising nickel having the oxidation state of zero (hereinafter referred to as Ni(0)) with at least one organophosphorus ligand and a cocatalyst belonging to the Lewis acid family.
Such processes have been known for many years and are exploited industrially, in particular for the production of a major chemical intermediate, adiponitrile. This compound is in particular used in the production of hexamethylenediamine, which is an important monomer for the production of polyamides and also an intermediate in the synthesis of diisocyanate compounds.
Thus, the company DU PONT DE NEMOURS has developed and exploited a process for producing adiponitrile by double hydrocyanation of butadiene. This reaction is generally catalysed by a catalytic system comprising a complex of nickel(0) with organophosphorus ligands. This system also comprises a cocatalyst, in particular in the second hydrocyanation step, i.e. hydrocyanation of unsaturated compounds comprising a nitrile function, such as pentenenitriles to dinitrile compounds.
Many cocatalysts have been proposed in patents and are generally compounds belonging to the Lewis acid family. One of the roles of this cocatalyst or promoter is to limit the production of by-products and therefore to promote the formation of linear dinitrile compounds compared with the formation of branched dinitriles.
Thus, many metal halides, such as zinc chloride, zinc bromide, stannous chloride or stannous bromide, have already been proposed, for example in U.S. Pat. No. 3,496,217. Zinc chloride is the preferred cocatalyst.
Organic boron compounds such as triphenyl boron or compounds comprising two boron atoms, as described in U.S. Pat. Nos. 3,864,380 and 3,496,218, or organic tin compounds as in U.S. Pat. No. 4,874,884, have also been proposed.
These cocatalysts have different properties and make it possible to obtain selectivities for different linear dinitriles such as adiponitrile. Some of these cocatalysts have drawbacks associated with the difficulty in extracting them from the reaction medium or with the possibility and ease of extracting the catalytic system or the nickel(0) ligand in the presence of this cocatalyst, in order to recycle it.
There still exists a need to find new cocatalysts for obtaining selectivities for linear dinitriles that are of acceptable levels and easy to use.
One of the aims of the present invention is to provide a new family of compatible cocatalysts which give adiponitrile-selectivity levels that are suitable in the pentenenitrile hydrocyanation reaction.
To this effect, the invention provides a process for producing compounds comprising at least one nitrile function by hydrocyanation of an organic compound comprising at least one non-conjugated unsaturation, comprising from 2 to 20 carbon atoms, by reaction with hydrogen cyanide in the presence of a catalytic system comprising a complex of nickel having the oxidation state of zero with at least one organophosphorus ligand chosen from the group comprising organophosphites, organophosphonites, organophosphinites and organosphosphines and a cocatalyst, characterized in that the cocatalyst is an organometallic compound corresponding to general formula I:
[(R)a—(X)y—]nM—M1[—(X)z—(R1)a1]n1
Advantageously, R and R1, which may be identical or different, represent an aromatic, aliphatic or cycloaliphatic radical, which is substituted or unsubstituted, and which may or may not be bridged, or a halide radical.
In the formula above, the bond between the elements M and M1 is symbolized by a covalent bond. However, said bond may be multiple, depending on the nature of the elements M and M1.
In the formula above, a is equal to the valency of the element X reduced by 1 if y is equal to 1, and a is equal to 1 if y is equal to 0. Similarly, a1 is equal to the valency of the element X reduced by 1 is z is equal to 1, and a1 is equal to 1 if z is equal to 0.
In the formula above, the R radicals may be identical or different. Similarly the R1 radicals may be identical or different.
According to one preferred characteristic of the invention, the cocatalyst is advantageously chosen from the group of the following compounds:
The cocatalysts of the invention are compounds which are described in the literature, as is the process for producing them. The registration number RN CAS is given solely for information purposes. Most of these compounds are commercially available.
In one preferred embodiment of the invention, the catalytic system of the invention contains a cocatalyst in accordance with the invention in a molar ratio of cocatalyst relative to the number of nickel atoms of between 0.01 and 50, and preferably between 0.1 and 10.
The catalytic system of the invention comprises a complex of nickel(0) with at least one organophosphorus compound, preferably a monodentate compound such as triphenylphosphite or tritolylphosphite, described for example in U.S. Pat. No. 3,496,215, DE19953058, FR1529134, FR2069411, U.S. Pat. Nos. 3,631,191, 3,766,231 or FR2523974, or a bidentate compound such as the organophosphite compounds described in Patents WO9906355, WO9906356, WO9906357, WO9906358, WO9952632, WO9965506, WO9962855, U.S. Pat. No. 5,693,843, WO961182, WO9622968, U.S. Pat. No. 5,981,772, WO0136429, WO9964155, WO0213964 and U.S. Pat. No. 6,127,567.
It is also possible to use complexes of nickel(0) with monodentate or bidentate organophosphine compounds as described in Patents WO02/30854, WO02/053527, WO03/068729, WO04/007435, WO04/007432, FR2845379 and WO2004/060855, and more particularly the trithienylphosphine described in the unpublished French application no. 0800381 and the DPPX described in Patent WO2003/031392.
Similarly, the catalytic system of the invention may comprise a complex of nickel(0) with monodentate or bidentate organophosphorus compounds belonging to the organophosphonite or organophosphinite family.
It is also possible to use the cocatalysts of the invention with a nickel(0) complex obtained with a mixture of organophosphite monodentate ligand and of bidentate ligand chosen from the families of compounds belonging to the organophosphites, organophosphonites, organophosphinites or organophosphines, as described in Patents WO03/011457 and WO2004/065352.
The description of the hydrocyanation process is given in several patents, including those mentioned above, and also in the articles by C. A. Tolman published in the reviews Organometallics 3 (1984) 33, Advances in Catalysis (1985) 33-1 and Journal of Chemical Education (1986) vol 63, no. 3, pages 199-201.
Briefly, the process for producing compounds comprising at least one nitrile function, and more particularly dinitrile compounds such as adiponitrile, consists in reacting, in a first step, a diolefin such as 1,3-butadiene with hydrogen cyanide, generally in the absence of solvent and in the presence of a catalytic system. The reaction is carried out under pressure so as to be in a liquid medium. The unsaturated nitrile compounds are separated by successive distillations. The linear nitrile compounds, such as pentenenitriles, are fed into a second hydrocyanation step.
Advantageously, the nonlinear unsaturated nitriles obtained in the first step are subjected to an isomerization step in order to convert them to linear unsaturated nitriles, which are also introduced into the second hydrocyanation step.
In the second hydrocyanation step, the linear unsaturated nitriles are reacted with hydrogen cyanide in the presence of a catalytic system.
The dinitrile compounds formed are separated by successive distillations after extraction of the catalytic system from the reaction medium. Several processes for extracting the catalytic system are described, for example, in U.S. Pat. No. 3,773,809, 4,082,811, 4,339,395 and 5,847,191. Generally, the catalytic system can be separated from the reaction medium by separation into two phases by settling out, obtained by control of the ratios between the mononitrile compounds and the dinitrile compounds contained in the medium. This separation can be improved by the addition of ammonia. It is also possible to precipitate the catalytic system in order to recover it and recycle it, or to use a nonpolar solvent for extracting the catalytic system and separating it from the nitrile products.
The temperature conditions for these various steps are between 10 and 200° C.
The catalytic systems used in the first and second hydrocyanation steps and also in the isomerization step are generally similar, i.e. they contain an identical nickel(0) complex. However, the ratio between the number of nickel atoms and the number of ligand molecules may be different in each of these steps, and also the concentration of the catalytic system in the medium.
Preferably, the cocatalyst is present only in the catalytic system used for the second hydrocyanation step. However, it may also be present in the isomerization step.
The characteristics and performance levels of the process and therefore of the catalytic system used are determined and illustrated by the degree of conversion (DC) of the compound introduced, in particular of the unsaturated mononitrile introduced in the second step, and by the linearity with respect to linear dinitriles produced, i.e. the number of moles of linear dinitriles relative to the number of moles of dinitriles formed. In the case of the production of adiponitrile, the linearity corresponds to the percentage of moles of adiponitrile (AdN) obtained relative to the numbers of moles of dinitriles formed (AdN+ESN+MGN).
The invention will be illustrated more clearly by means of the examples given below, only by way of indication, relating to the production of adiponitrile by hydrocyanation of 3-pentenenitrile. In these examples, the 3-pentenenitrile used is a compound marketed by Aldrich.
In these examples, the following abbreviations are used:
The compounds of formula I used in the examples below are commercially available.
The general procedure used is the following:
The following are loaded successively, under an argon atmosphere, into a 60 ml glass tube of Schott type, equipped with a septum stopper:
The mixture is brought to 70° C. with stirring. Acetone cyanohydrin, an HCN generator, is injected into the reaction medium via a syringe driver with a flow rate of 0.45 ml per hour. After injecting for 3 hours, the syringe driver is stopped. The mixture is cooled to ambient temperature, diluted with acetone and analysed by gas chromatography.
The cocatalysts used in the examples are listed below:
The results are given in Table I below.
| Number | Date | Country | Kind |
|---|---|---|---|
| 08 05821 | Oct 2008 | FR | national |
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/EP2009/062896 | 10/5/2009 | WO | 00 | 9/15/2011 |
| Publishing Document | Publishing Date | Country | Kind |
|---|---|---|---|
| WO2010/046226 | 4/29/2010 | WO | A |
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| 3496217 | Drinkard et al. | Feb 1970 | A |
| 3496218 | Drinkard, Jr. et al. | Feb 1970 | A |
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| 3655723 | Drinkard, Jr. | Apr 1972 | A |
| 3694485 | Drinkard, Jr. et al. | Sep 1972 | A |
| 3766231 | Gosser et al. | Oct 1973 | A |
| 3766237 | Chia et al. | Oct 1973 | A |
| 3773809 | Walter | Nov 1973 | A |
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| 5512696 | Kreutzer et al. | Apr 1996 | A |
| 5693843 | Breikss et al. | Dec 1997 | A |
| 5847191 | Bunel et al. | Dec 1998 | A |
| 5981772 | Foo et al. | Nov 1999 | A |
| 6048996 | Clarkson et al. | Apr 2000 | A |
| 6127567 | Garner et al. | Oct 2000 | A |
| 6153758 | Sannicolo et al. | Nov 2000 | A |
| 6521778 | Fischer et al. | Feb 2003 | B1 |
| 6770770 | Baumann et al. | Aug 2004 | B1 |
| 7084293 | Rosier et al. | Aug 2006 | B2 |
| 7098358 | Burattin et al. | Aug 2006 | B2 |
| 7105696 | Burattin et al. | Sep 2006 | B2 |
| 7442825 | Galland et al. | Oct 2008 | B2 |
| 7470805 | Rosier et al. | Dec 2008 | B2 |
| 7485741 | Bourgeois et al. | Feb 2009 | B2 |
| 7550407 | Bartsch et al. | Jun 2009 | B2 |
| 7612223 | Rosier et al. | Nov 2009 | B2 |
| 7777068 | Bartsch et al. | Aug 2010 | B2 |
| 8697902 | Mastroianni | Apr 2014 | B2 |
| 20040116713 | Beller et al. | Jun 2004 | A1 |
| 20060258874 | Bartsch et al. | Nov 2006 | A1 |
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| 20110118499 | Mastroianni | May 2011 | A1 |
| 20110166376 | Mastroianni | Jul 2011 | A1 |
| 20110288327 | Mastroianni | Nov 2011 | A1 |
| Number | Date | Country |
|---|---|---|
| 199 53 058 | May 2001 | DE |
| 103 14 761 | Oct 2004 | DE |
| 0336314 | Oct 1989 | EP |
| 1 529 134 | May 1968 | FR |
| 2 069 411 | Sep 1971 | FR |
| 2 523 974 | Sep 1983 | FR |
| 2 830 530 | Apr 2003 | FR |
| 2 849 027 | Jun 2004 | FR |
| 2 854 892 | Nov 2004 | FR |
| 2 845 379 | Apr 2009 | FR |
| WO 9622968 | Aug 1996 | WO |
| WO 9906355 | Feb 1999 | WO |
| WO 9906356 | Feb 1999 | WO |
| WO 9906357 | Feb 1999 | WO |
| WO 9952632 | Oct 1999 | WO |
| WO 9962855 | Dec 1999 | WO |
| WO 9964155 | Dec 1999 | WO |
| WO 9965506 | Dec 1999 | WO |
| WO 0136429 | May 2001 | WO |
| WO 0213964 | Feb 2002 | WO |
| WO 0230854 | Apr 2002 | WO |
| WO 02053527 | Jul 2002 | WO |
| WO 03011457 | Feb 2003 | WO |
| WO 03031392 | Apr 2003 | WO |
| WO 03068729 | Aug 2003 | WO |
| WO 2004007432 | Jan 2004 | WO |
| WO 2004007434 | Jan 2004 | WO |
| WO 2004060855 | Jul 2004 | WO |
| WO 2004065352 | Aug 2004 | WO |
| WO 2004087314 | Oct 2004 | WO |
| WO 2009092639 | Jul 2009 | WO |
| Entry |
|---|
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