MULTIDENTATE PHOSPHITE LIGANDS, CATALYTIC COMPOSITIONS CONTAINING SUCH LIGANDS AND CATALYTIC PROCESSES UTILIZING SUCH CATALYTIC COMPOSITIONS

Abstract: Hydrocyanation reactions employing multidentate phosphite ligands and multidentate phosphite ligands are disclosed. The ligands have phenyl containing substituents attached to the ortho position of the terminal phenol group and/or attached to the ortho position of the bridging group. Catalyst compositions having such ligands achieve 97 % or greater distribution in hydrocyanation.

Description: MULTIDENTATE PHOSPHITE LIGANDS, CATALYTIC COMPOSITIONS CONTAINING SUCH LIGANDS AND CATALYTIC PROCESSES UTILIZING SUCH CATALYTIC COMPOSITIONS FTFT T) OF THE INVENTION The invention relates to certain multidentate phosphite ligands, the catalyst compositions made therefrom and a catalytic hydrocyanation process which employs such multidentate phosphite ligands. In particular, the ligands have phenyl containing substituents attached to the ortho position of the terminal phenol group and/or attached to the ortho position of the backbone. TECHNICAL BACKGROUND OF THE INVENTION uuα j jiiϋi us iii j c i o u t uuiCjuUuuo ui Lαiαiy Ms αιιι_ι αi t ι»ι.u ivji α uuiiiu i y i commercially important chemical transformations. Phosphorus ligands commonly encountered in catalysis include phosphines (A), and phosphites (B), shown below. In these representations, R can be virtually any organic group. Monophosphine and onophosphite ligands are compounds which contain a single phosphorus atom which serves as a donor to a metal. Bisphosphine, bisphosphite, and bis(phosphorus) ligands in general, contain two phosphorus donor atoms and normally form cyclic chelate structures with transition metals. P. OR I I R R RO OR A B There are several industrially important catalytic processes employing phosphorus ligands. For example, U.S. Patent No. 5,910,600 to Urata, et al. discloses that bisphosphite compounds can be used as a constituting element of a homogeneous metal catalyst for various reactions such as hydrogenation, hydroformylation, hydrocyanation, hydrocarboxylation, hydroamidation, hydroesterification and aldol condensation. Some of these catalytic processes are used in the commercial production of polymers, solvents, plasticizers and other commodity chemicals. Consequently, due to the extremely large worldwide chemical commodity market, even small .iicremc-.-.-i advances in yield or selectivity in any oi tnese commercially important reactions are highly desirable. Furthermore, the discovery of certain ligands that may be useful for applications across a range of these commercially important reactions is also highly desirable not only for the commercial benefit, but also to enable consolidation and focusing of research and development efforts to a particular group of compounds. U.S. Patent No. 5,512,696 to Kreutzer,et al. discloses a hydrocyanation process using a multidentate phosphite ligand, and the patents and publications referenced therein describe hydrocyanation catalyst systems pertaining to the hydrocyanation of ethylenically unsaturated compounds. U.S. Patent Nos. 5,723,641, 5,663,369, 5,688,986 and 5,847,191 disclose processes and catalyst compositions for the hydrocyanation of monoethylenically unsaturated compounds using zero-valent nickel and multidentate phosphite ligands, and Lewis acid promoters. U.S. Patent No. 5,821,378 to Foo, et al. discloses a liquid phase process for the hydrocyanation of diolefinic compounds to produce nonconjugated acyclic nitriles as well as a liquid phase process for the isomerization of those nitriles to 3- and or 4-monoalkene linear nitriles where the reactions are carried out in the presence of zero-valent nickel and a multidentate phosphite ligand. Other catalytic processes for the hydrocyanation of olefins and the isomerization of monoalkene nitriles are described in the patents and publications referenced therein. Commonly assigned, published PCT Application WO99/06357 discloses multidentate phosphite ligands having alkyl ether substituents on the carbon attached to the ortho position of the terminal phenol group for use in a liquid phase process for the hydrocyanation of diolefinic compounds to produce nonconjugated acyclic nitriles as well as a liquid phase process for the isomerization of those nitriles to 3- and/or 4-monoalkene linear nitriles. The use of multidentate phosphite ligands having binaphthalene and/or biphenyl bridging groups for hydroformylation reactions is disclosed in U.S. Patent Nos. 5,235,113, 5,874,641, 5,710,344 and published PCT Application WO 97/33854 w iuie the cataiyst systems described above may represent commercially viable catalysts, it always remains desirable to provide even more effective, higher performing catalyst precursor compositions, catalytic compositions and catalytic processes to achieve full commercial potential for a desired reaction. The effectiveness and/or performance may be achieved in any or all of rapidity, selectivity, efficiency or stability, depending on the reaction performed. It is also desirable to provide such improved catalyst systems and/or processes which may be optimized for a commercially important reaction such hydrocyanation or isomerization. Other objects and advantages of the present invention will become apparent to those skilled in the art upon reference to the detailed description which hereinafter follows. SUMMARY OF THE INVENTION The invention provides for a hydrocyanation process comprising reacting an acyclic, aliphatic, monoethylenically unsaturated compound in which the ethylenic double bond is not conjugated to any other otefinic group in the molecule with a source of HCN in the presence of a catalyst composition comprising a Lewis acid, a zero-valent nickel and at least one multidentate phosphite ligand selected from the group represented by the following formulae I II or III , in which all like reference characters have the same meaning, except as further explicitly limited. Formula I Formula II wherein R 1 is independently Ci to Cig primary or secondary alkyl, R 2 is independently aryl or substituted aryl, R J is independently aryl or substituted aryl, R 4 is independently Ci to Cι« primary alkyl, R 5 is hydrogen, R 6 is independently aryl or substituted aryl, R 7 is independently Ci to d 8 primary or secondary alkyl, R s is independently Ci to Ci primary or secondary alkyl; and R 9 is independently Ci to Cι 8 primary or secondary alkyl, wherein other positions on the aromatic rings may also be substituted with alkyl, ether or ester groups, or combinations of two or more thereof The invention also provides for a multidentate phosphite ligand having the structure represented by the following Formula I, II or III in which all like reference characters have the same meaning, except as further explicitly limited Formula II wherein R 1 is independently Ci to Cι 8 primary or secondary alkyl; R 2 is independently aryl or substituted aryl, R J is independently aryl or substituted aryl; R 4 is independently Ci to Cι 8 primary alkyl; R 5 is hydrogen; R 6 is independently aryl or substituted aryl; R 7 is independently Ci to C 18 primary or secondary alkyl; R* is independently Ci to C ϊg primary or secondary alkyl; and R 9 is independently Ci to C 18 primary or secondary alkyl; wherein other positions on the aromatic rings may also be substituted with alkyl, ether or ester groups, or combinations of two or more thereof. DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The invention provides for certain multidentate phosphite ligands, improved catalyst systems employing such ligands, and the use of such multidentate phosphite ligands in hydrocyanation reactions. The catalyst compositions useful in the invention preferably are comprised of a multidentate phosphite ligand of formula I, II, and III and a transition metal. Formula I Formula II Formula III wherein R ! is independently Ci to Cm primary alkyl; R 2 is independently aryl or substituted aryl, R J is independently aryl or substituted aryl, R 4 is independently to Cι 8 primary alkyl; R R 55 is hydrogen; R 6 is independently aryl or substituted aryl; R 7 is independently d to Cι 8 primary or secondary alkyl; R 8 is independently Ci to Cι 8 primary or secondary alkyl; and R y is independently Ci to Cj 8 primary or secondary alkyl; wherein other positions on the aromatic rings may also be substituted with alkyl, ether or ester groups, or combinations of two or more thereof. The divalent bridging compounds used in tne ngands descπbed in formulae I, II, and III may be prepared by a variety of methods known in the art. For example, 3,3',5,5'-tetramethyl-2,2'-biphenol can be prepared according to J. Org. Chem., 1963, 28, 1063 and 3,3',5,5',6,6'-Hexamethyl-2,2'-biphenol can be prepared according to JP 85-216749. The 3,3'-diaryi-substituted l,l'-2-naphthols can be obtained according to J. Org. Chem., 1998, 63, 7536. Phosphorochloridite may be prepared by a variety of methods known in the art, for example, see descriptions in Polymer, 1992, 33, 161; Inorganic Synthesis, 1966, 8, 68;.U.S. 5,210,260; Z. Anorg. Allg. Chem., 1986, 535, 221. With ortho- substituted phenols, phosphorochloridites can be prepared in situ from PCI3 and the phenol. Also, phosphorochloridites of 1-naphthols can be prepared in situ from PCI 3 and 1-naphthols in the presence of a base like triethylamine. Another process for preparing the phosphochlorodite comprises treatment of N,N-dialkyl diarylphosphoramidite with HO. ClP(OMe) 2 has been prepared in this manner, see Z Naturforsch, 1972, 27B, 1429. Phosphorochloridites derived from substituted phenols have been prepared using this procedure as described in commonly assigned U.S. Patent No. 5,821,378. By contacting the thus obtained (OAr) 2 PCl , wherein Ar is a substituted aryl, with a divalent bridging compound, for example by the method described in U.S. Patent No. 5,235, 1 13, a bidentate phosphite ligand is obtained which can be used in the process according to the invention. The transition metal may be any transition metal capable of carrying out catalytic transformations and may additionally contain labile ligands which are either displaced during the catalytic reaction, or take an active part in the catalytic transformation. Any of the transition metals may be considered in this regard. The preferred metals are those comprising group VIII of the Periodic Table. The preferred metals for hydroformylation are rhodium, cobalt, iridium, ruthenium, palladium and platinum. The preferred metals for hydrocyanation and/or isomerization are nickel, cobalt, and palladium, and nickel is especially preferred for hydrocyanation. The catalyst compositions of the invention are comprised of at least one multidentate phosphite ligand according to any one of formulae I, II and III and a transition metal. In embodiments of the invention, catalyst comj υsitions useful for processes such as hydroformylation may have Group VTJI compounds such as can be prepared or generated according to techniques well known in the art, as described, for example, WO 95 30680, U.S. 3,907,847, and J. Amer. Chem. Hoc., 1993, 115, 2066. Examples of such suitable Group VHI metals are ruthenium, rhodium, and iridium. Suitable Group VIII metal compounds are hydrides, halides, organic acid salts, acetylacetonates, inorganic acid salts, oxides, carbonyl compounds and amine compounds of these metals. Examples of suitable Group VIII metal compounds are, for example, Ru3(CO)ι 2 , Ru(NO 3 ) 2 , RuCl 3 (Ph 3 P)3, Ru(acac) 3 , Ir 4 (CO) 12 , IrSO 4 , RhCl 3 , Rh(NO 3 ) 3 , Rh(OAc) 3 , Rh 2 O 3 , Rh(acac)(CO) 2 , [Rh(OAc)(COD)] 2 , Rh^CO)-^, Rh6(CO)ι 6 , RhH(CO)(Ph 3 P)3, [Rh(OAc)(CO) 2 ] 2 , and [RhCl(COD)] 2 (wherein "acac" is an acetylacetonate group; "OAc" is an acetyl group; "COD" is 1,5-cyclooctadiene; and "Ph" is a phenyl group). However, it should be noted that the Group VIII metal compounds are not necessarily limited to the above listed compounds. The Group VIII metal is preferably rhodium. Rhodium compounds that contain ligands which can be displaced by the multidentate phosphites are a preferred source of rhodium. Examples of such preferred rhodium compounds are Rh(CO) 2 (acetylacetonate), Rh(CO) 2 (C 4 H 9 COCHCO-t-C 4 H 9 ), Rh 2 O3, Rh^COJu, RhβCCO)*, Rh(O 2 CCH 3 ) 2 , and Rh(2-ethylhexanoate). Rhodium supported on carbon may also be used in this respect. Nickel compounds can be prepared or generated according to techniques well known in the art, as described, for example, in U.S. Patents 3,496,217; 3,631,191; 3,846,461; 3,847,959; and 3,903,120, which are incorporated herein by reference. Zero-valent nickel compounds that contain ligands which can be displaced by the organophosphorus ligand are a preferred source of nickel. Two such preferred zero-valent nickel compounds are Ni(COD)2 (COD is 1,5-cyclooctadiene) and Ni{P(O-o-C 6 H 4 CH 3 )3} 2 (C2H 4 ), both of which are known in the art. Alternatively, divalent nickel compounds may be combined with a reducing agent, to serve as a source of nickel in the reaction. Suitable divalent nickel compounds include compounds of the formula NiY 2 where Y is halide, carboxylate, or acetylacetonate. Suitable reducing agents include metal borohydrides, metal aluminum hydrides, metal alkyls, Zn, Fe, Al, Na, or h^ Elemental nickel, preferably nickel powder, when combined with a halogenated catalyst, as described in U.S. Patent 3,903,120, is also a suitable source of zero- valent nickel. Depending upon the desired reaction to be performed, the catalyst composition of this invention may also include the presence of one or more Lewis acid promoters, which affect both the activity and the selectivity of the catalyst system. The promoter may be an inorganic or organometallic compound in which the at least one of the elements of said inorganic or organometallic compound is selected from scandium, titanium, vanadium, chromium, manganese, iron, cobalt, copper, zinc, boron, aluminum, yttrium, zirconium, niobium, molybdenum, cadmium, rhenium and tin. Examples include ZnBr 2 , Znl 2 , ZnCl 2 , ZnSO 4 , CuCl2, CuCl, Cu(O 3 SCF 3 )2, CoCl , C0I2, Fel 2 , FeCl , FeCl 2 , FeCl 2 (THF) 2 , TiCi4(THF) 2 , T1CI4, T.CI3, ClTi(OiPr) 3 , MnCl 2 , ScCl 3 , AICI3, (CgHi7)AlCl2, (C8Hi7) 2 AlCl, (iso-C 4 H 9 ) 2 AlCl, Ph 2 AlCl, PhAlCl 2 , ReCl 5 , ZrCLi, NbCl 5 , VCI3, CrCI , M0CI5, YCI3, CdCl 2 , LaCl 3 , Er(O 3 SCF )3, Yb(O 2 CCF 3 ) 3 , SmCl 3 , B(C 6 H 5 ) 3 , TaCls. Suitable promoters are further described in U.S. Patents 3,496,217; 3,496,218; and 4,774,353. These include metal salts (such as ZnCh, C0I2, and SnCh), and organometallic compounds (such as RAICI 2 , R3SnO3SCF3, and R 3 B, where R is an alkyl or aryl group). U.S. Patent 4,874,884 describes how synergistic combinations of promoters can be chosen to increase the catalytic activity of the catalyst system. Preferred promoters include CdCl2, FeCl 2 , ZnCl 2 , B(C 6 H 5 ) 3 , and (CβHstøSnX, where X = CF 3 SO3, CH3C6H5SO3, or (CeHs^BCN. The mole ratio of promoter to nickel present in the reaction can be within the range of about 1 : 16 to about 50:1. HYDROCYANATION OF MONOOLEFINIC COMPOUNDS The present invention provides for a process of hydrocyanation, comprising reacting an unsaturated compound with a source of hydrogen cyanide in the presence of a catalyst composition comprising a transition metal selected from Ni, Co, and Pd, and a Lewis acid compound, and at least one ligand selected from the group represented by formulae I , II, or III. Representative ethylenically unsaturated compounds which are useful in the hydrocyanation process of this invention are shown in Formulae IV or V, and the corresponding terminal nitrile compounds produced are illustrated by Formulae IV or VI, respectively, wherein like reference characters have same meaning. catalyst composition CH 3 — (CH2) -CK=CH— (C - R 22 Nc (Cf-y χ+ y + 3 _ R 22 1 r\ promoter, HCN Formula IV Formula V catalyst composition CH =CH-(CH 2 )τ-R 22 NC (CH 2 ) x+2 R < promoter, HCN Formula VI Formula VII wherein R 22 is H, CN, CO 2 R 23 , or perfluoroalkyl; y is an integer of 0 to 12; x is an integer of 0 to 12 when R 22 is H, CO 2 R 23 or perfluoroalkyl; x is an integer of 1 to 12 when R 22 is CN; and R 23 is Ci to C 12 alkyl, or aryl. The nonconjugated acyclic, aliphatic, monoethylenically unsaturated starting materials useful in this invention include unsaturated organic compounds containing from 2 to approximately 30 carbon atoms. Suitable unsaturated compounds include unsubstituted hydrocarbons as well as hydrocarbons substituted with groups which do not attack the catalyst, such as cyano. Examples of these monoethylenically unsaturated compounds include ethylene, propylene, 1- butene, 2-pentene, 2-hexene, etc., nonconjugated diethylenically unsaturated compounds such as allene, substituted compounds such as 3-pentenenitrile, 4-pentenenitrile, methyl pent-3-enoate, and ethylenically unsaturated compounds having perfluoroalkyl substituents such as, for example, C z F 2z+ ι, where z is an integer of up to 20. The monoethylenically unsaturated compounds may also be conjugated to an ester group such as methyl pent-2-enoate. Preferred are nonconjugated linear alkenes, nonconjugated linear Allen-nitriles, nonconjugated linear alkenoates, linear alk-2-enoates and perfluoroalkyl ethylenes. Most preferred substrates include 3- and 4-pentenenitrile, alkyl 2-, 3-, and 4-pentenoaιes, and C z F2 Z+ ιCH=CH 2 (where z is 1 to 12). 3-Pentenenitriie and 4-pentenenitriie are especially preferred As a practical matter, when the nonconjugated acyclic aliphatic monoethylenically unsaturated compounds are used in accordance with this invention, up to about 10% by weight of the monoethylenically unsaturated compound may be present in the form of a conjugated isomer, which itself may undergo hydrocyanation For example, when 3-pentenenitrile is used, as much as 10% by weight thereof may be 2-pentenenitrile (As used herein, the term "pentenenitrile' '' is intended to be identical with "cyanobutene") The preferred products are terminal alkanenitriles, linear dicyanoalkyienes, linear aliphatic cyanoesters, and 3 -(perfluoroalkyl) propionitrile Most preferred products are adiponitrile, alkyl 5-cyanovalerate, and C z F2z + lCH 2 CH2C , where z is 1 to 12. The present hydrocyanation process may be carried out, for example, by charging a reactor with the reactants, catalyst composition, and solvent, if any, but preferably, the hydrogen cyanide is added slowly to the mixture of the other components of the reaction Hydrogen cyanide may be delivered as a liquid or as a vapor to the reaction Another suitable technique is to charge the reactor with the catalyst and the solvent to be used, and feed both the unsaturated compound and the HCN slowly to the reaction mixture The molar ratio of unsaturated compound to catalyst can be varied from about 10 1 to about 2000 1 Preferably, the reaction medium is agitated, for example, by stirring or shaking The reaction product can be recovered by conventional techniques such as, for example, by distillation. The reaction may be run either batchwise or in a continuous manner The hydrocyanation reaction can be carried out with or without a solvent The solvent, if used, should be liquid at the reaction temperature and pressure and inert towards the unsaturated compound and the catalyst. Suitable solvents include hydrocarbons, such as benzene or xylene, and nitriles, such as acetonitrile or benzonitrile In some cases, the unsaturated compound to be hydrocyanated may itself serve as the solvent The exact temperature is dependent to a certain extent on the particular catalyst being used, the particular unsaturated compound being used and the desired rate Normally, temperatures of from -25°C to 200°C can be used, the range of 0°C to 150°C being preferred Atmospheric pressure is satisfactory for carrying out the present invention and hence pressures of from about 0 05 to 10 atmospheres (50 6 to 1013 kPa) are preferred Higher pressures, up to 10,000 kPa or more, can be used, if desired, but any benefit that may be obtained thereby would probably not justify the increased cost of such operations HCN can be introduced to the reaction as a vapor or liquid As an alternative, a cyanohydrin can be used as the source of HCN See, for example, U S Patent 3,655,723 The process of this invention is carried out in the presence of one or more Lewis acid promoters which affect both the activity and the selectivity of the catalyst system The promoter may be an inorganic or organometallic compound in which the in which the at least one of the elements of said inorganic or organometallic compound is selected from scandium, titanium, vanadium, chromium, manganese, iron, cobalt, copper, zinc, boron, aluminum, yttrium, zirconium, niobium, molybdenum, cadmium, rhenium and tin. Examples include ZnBr 2 , Znl 2 , ZnCl 2 , ZnSO 4 , CuCl 2 , CuCl, Cu(O 3 SCF 3 )2, CoCl 2 , CoI 2 , Fel 2 , FeCl 3 , FeCl 2 , FeCl 2 (THF) 2 , TiCl 4 (THF) 2 , TiCl , TiCl 3 , ClTi(OiPr)3, MnCl , ScCl , A1C1 3 , (C 8 Hi 7 )AlCl 2 , (C 8 Hi7) 2 AlCl, (iso-C 4 H 9 ) 2 AlCl, Ph 2 AlCl, PhAlCb, ReCl 5 , ZrCLi, NbCl 5 , VCI3, CrCl , M0CI5, YCI3, CdCl 2 , LaCl 3 , Er(O3SCF 3 )3, Yb(O2CCF 3 ) , SmCl3, B(C 6 H 5 ) 3 , TaC Suitable promoters are further described in U S Patents 3,496,217, 3,496,218, and 4,774,353 These include metal salts (such as ZnCl2, C0I 2 , and SnCl 2 ), and organometallic compounds (such as RAICI2, R3Snθ 3 SCF 3 , and R3B, where R is an alkyl or aryl group) U S Patent 4,874,884 describes how synergistic combinations of promoters can be chosen to increase the catalytic activity of the catalyst system. Preferred promoters include CdCl 2 , FeCl 2 , ZnCl 2 , B(C 6 H5)3, and (CόHsbSnX, where X = CF3SO3, CH3C 6 H 5 SO 3 , or (C 6 H5)3BCN The mole ratio of promoter to nickel present in the reaction can be within the range of about 1 16 to about 50 1 The invention will now be illustrated Dy the following non-limiting examples of certain embodiments thereof, wherein all parts, proportions, and percentages are by weight, unless otherwise indicated The following definitions are applicable wherever the defined terms appear in this specification The term "hydrocarbyl" designates a hydrocarbon molecule from which one hydrogen atom has been removed Such molecules can contain single, double or triple bonds 3PN 3-pentenenitrile 2PN 2-pentenenitrile 4PN 4-pentenenitrile 2M3 2-methyl-3-butenenitrile VN valeronitrile ESN ethylsuccinonitrile MGN 2-methylglutaronitrile 5FVN 5-formylvaleronitrile M3P methyl 3-pentenoate BD 1,3 -butadiene COD 1 , 5 -cy clooctadiene Et 3 N triethylamine PC phosphorus trichloride THF tetrahydrofiiran The protocol for calculating certain reaction results for hydrocyanation reactions and isomerization reactions follows For step 1 hydrocyanation reactions the % useful pentenenitriles (PN's) and the 3PN/2M3 ratio is reported The product distribution is analyzed by gas chromatograph using valeronitrile as an internal standard. The % useful PN's is the molar ratio of the sum of 3PN(cis and trans) and 2M3 divided by the amount of HCN The 3PN/2M3 ratio is the ratio of cis and trans 3PN to 2M3 For step 2 hydrocyanation reactions the selectivity to adiponitrile (ADN) is ADN/(ESN + MGN + ADN) The 3PN and 4PN conversion is calculated using 2- ethoxyethylether (EEE) as an internal standard The total conversion of pentenenitriles (PN's) to dinitriles (DN's), based on the assumption that all material is accounted for, is calculated as (sum (mol DN's)/sum (PN's + BN's + DN's)) (BN's are butenenitriles) The conversion based on HCN is calculated by dividing the total conversion of PN's to DN's by the HCN/PN ratio in the original feed, i.e , (mol DN/mol PN at start)/(mol HCN/mol PN at start) Example 1 2 , -Ethoxyl-l,l'-biphenyl-2-ol was prepared by modifying the procedure reported in J. Org. Chem 1981, 46, 4988 In 50 mL of acetone was added lOg of 2,2'-biphenol and 9 4 g of potassium carbonate After stirring at room temperature for one hour, a solution of iodoethane (9 2 g in 10 mL of acetone) was added slowly dropwise The rriixture was filtered, washed with acetone, and solvent removed by rotary evaporation The residue was flashed chromatographed to give 5 1 g of the 2'-ethoxyl- 1 , 1 '-biphenyl-2-ol as a colorless oil ! H NMR (C 6 D 6 ) 7 20 (m, 3H), 7 10 (m, 1H), 7 05 ( , 1H),6 85 (m, 2H), 6 55 (m, 1H), 3 38 (q, 2H), 0 81 (t, 3H). In a nitrogen purged glove box, the above phenol (0 73g, 3 40 mmol) was dissolved in 10 mL ether, and cooled to -30 °C To this was added cold (-30 °C) 1M phosphorous trichloride solution (1 7 mL), followed by dropwise addition of 1M triethylamine solution (4.0 mL) The solution was stirred at room temperature for 5 minutes, then kept at -30 °C for two hours The reaction mixture was filtered through a pad of Celite and concentrated to yield 0 67 g of the corresponding phosphorous chloridite 31 P NMR (toluene) 160 4 (78%), 126 (22%) The phosphorous chlorodite was reacted with 1, l'-bi-2-naphthol in the presence of triethylamine to yield ligand II 31 P NMR (toluene) 131 3 (major), 130.2. 2,2'-dihydroxy-l, 1 '-binaphthalene-3,3'-bis(diphenylether) was prepared according to literature procedure reported in J. Org. Chem. 1998, 63, 7536). Under an atmosphere of nitrogen, a 250 mL two- necked Schlenk flask equipped with a reflux condenser was charged with 3,3'-bis(dihydroxyborane)-2,2'- dimethoxy-l,l'-binaphthyl (2.250 g, 5.60 mmol), Pd(PPh 2 ) 4 (0.360 g, 0.42 mmol), Ba(OH) 2 (5.25 g, 30.6 mmol), 4-bromo-diphenylether (4.47 g, 17.9 mmol), 1,4-dioxane (36 mL) and H 2 O (12 mL). The reaction mixture was refluxed for 24 hours. Upon cooling to room temperature, the mixture was diluted with CH 2 C1 2 (150 mL) and washed with 1 N HC1 (2x75 mL) and brine (2x75 mL). The solution was dried over MgSO 4 . Removal of the solvent gave a brown oil, which was diluted in dry CH 2 C1 2 (125 mL) and cooled - 40 °C. Over a period of 10 rnin, BBr 3 (3 mL) was slowly added and the reaction mixture was stirred at room temperature overnight. The resulting red-brown solution was cooled to 0 °C, and H 2 O (300 mL) was carefully added. The organic layer was separated and then washed with H 2 O (2x300mL), 1 N HC1 (300 mL) and brine (300 mL). The resulting solution was dried over MgSO 4 and concentrated. The resulting red oil was chromatographed on silica to give 2,2'-dihydroxy-l,l '-binaphthalene-3,3'- bis(diphenylether) as a white crystalline solid ( 0.80 g, 23 %). 1H NMR (C 6 D 6 ): 7.80 (s, 2H), 7.64 (d, J = 8.2 Hz, 2H), 7.53 (d, J - 8.7 Hz, 4H), 7.22 (d, J = 8.3 Hz, 2H), 7.12 (m, 4H) 7.05- 6.96 (m, 14 H), 5.03 (s, 2H). Under an atmosphere of nitrogen, a cold (-35 °C) anhydrous diethyl ether solution (20 mL) of 2,2'-dihydroxy-l,l '-binaphthalene-3,3'-bis(diphenylether) (0.405 g, 0.65 mmol) was added to the phosphochlorodite of 5,6,7,8-tetrahydro-l- naphthol (0.588 g, 1.63 mmol) dissolved in diethyl ether (10 mL). While maintaining this temperature, triethylamine (0.23 mL, 1.63 mmol) was added dropwise to the above mixture resulting in the formation of a white precipitate. After stirring at room temperature for three hours, the reaction mixture was filtered through a pad of basic alumina and Celite . The filtrate was evaporated to yield the desired diphosphite as a white powder (0.537 g, 65 %). 31 P (Η) NMR (202.4 MHz, C 6 D 6 ): 132.75 ppm. Example 3 Under an atmosphere of nitrogen, a cold (-35 °C) anhydrous diethyl ether solution (5 mL) of 2,2'-dihydroxy-l,l '-binaphthalene-3,3'-bis(diphenyl) (0.050 g, yj. ja mmol) was added to the phosphochlorodite of 5,6,7,8-tetrahydro-l-naphthol (0.076 g, 0.21 mmol) dissolved in diethyl ether (5 mL). While maintaining this temperature, triethylamine (0.03 mL, 0.21 mmol) was added dropwise to the above mixture resulting in the formation of a white precipitate. After stirring at room temperature for three hours, the reaction mixture was filtered through a pad of basic alumina and Celite . The filtrate was evaporated to yield the desired diphosphite as a white powder (0.043 g, 58 %). 3I P {Η} NMR (202.4 MHz, C 6 D 6 ) 127.83, 132.14, 132.60 (major), 133.66, 141.51, 143.99 ppm. Hydrocyanation Results For The Ligand of Example 2 Preparation of catalyst: A catalyst solution was prepared by adding 0.0039 g of Ni(COD) 2 (0.014 mmol) in 0.320 ml toluene to 0.062 g of the ligand of Example 2 (0.049 mmol) in 0.200 mL toluene Hydrocyanation of 3, 4 Pentenenitrile (3, 4 PN) : 116 μl of the above catalyst solution (0.0031 mmol Ni), and 13 μl of a solution of ZnCl 2 in 3PN (0.0067 mmol ZnCl 2 ) were added to a vial fitted with a septum cap. The vial was cooled to -20°C and 125 μl of a solution of HCN, t-3PN, and 2-ethoxyethyl ether (0.396 mmol HCN, 0.99 mmol t-3PN) was added. The vial was sealed and set aside for 24 hours at room temperature. The reaction rnixture was diluted with ethyl ether and the product distribution analyzed by GC using 2-ethoxyethyl ether as an internal standard. Analysis showed that 22.7% of the starting pentenenitriles had been converted to dinitrile product ( 62.8% yield based on HCN.) The selectivity to the linear ADN isomer was 97.4%. ±ivurocyanaxion Results For The Ligand of Example 3 Preparation of catalyst: A catalyst solution was prepared by adding 0 0039 g of Ni(COD) 2 (0 014 mmol) in 0 320 ml toluene to 0 025 g of the ligand of Example 3 (0 020 mmol) in 0 200 mL toluene Hydrocyanation of 3, 4 Pentene itrile (3, 4 PN) : 116 μl of the above catalyst solution (0 0031 mmol Ni), and 13 μl of a solution of ZnCl 2 in 3PN (0 0067 mmol ZnCl 2 ) were added to a vial fitted with a septum cap The vial was cooled to -20°C and 125 μl of a solution of HCN, t-3PN, and 2-ethoxyethyl ether (0 396 mmol HCN, 0 99 mmol t-3PN) was added The vial was sealed and set aside for 24 hours at room temperature The reaction mixture was diluted with ethyl ether and the product distribution analyzed by GC using 2-ethoxyethyl ether as an internal standard Analysis showed that 9 2% of the starting pentenenitriles had been converted to dinitrile product ( 25 4% yield based on HCN ) The selectivity to the linear ADN isomer was 97 5%

Claims: What is claimed is: 1. A hydrocyanation process comprising; reacting an acyclic, aliphatic, monoethylenically unsaturated compound in which the ethylenic double bond is not conjugated to any other olefinic group in the molecule with a source of HCN in the presence of a catalyst composition comprising a Lewis acid, a zero-valent nickel and at least one multidentate phosphite ligand selected from the group represented by the following formulae I II or HI , in which all like reference characters have the same meaning, except as further explicitly limited: Formula I Formula II wherein R ! is independently Ci to Cig primary or secondary alkyl; R 2 is independently aryl or substituted aryl; R 3 is independently aryl or substituted aryl; R is independently i w s~→\$ primary alkyl; R 5 is hydrogen; R 6 is independently aryl or substituted aryl; R is independently Ci to Cig primary or secondary alkyl; R 8 is independently Q to Cι 8 primary or secondary alkyl; R 9 is independently Cito Cis primary or secondary alkyl; and wherein other positions on the aromatic rings may also be substituted with alkyl, ether or ester groups, or combinations of two or more thereof. 2. The process of Claim 1 wherein the starting ethylenically unsaturated compound is selected from the group consisting of 3-pentenenitrile, 4-pentene- nitrile; alkyl 2-, 3-, and 4-pentenoates, and C z F 2Z+ ιCH=CH 2 , wherein z is an integer of 1 to 12. 3. The process of Claim 2 wherein the starting ethylenically unsaturated compound is 3-pentenenitrile or 4-pentenenitrile. 4. The process of Claim 1 which is carried out at a temperature of -25°C to 200°C and at a pressure of 50.6 to 1013 kPa. 5. The process of Claim 4 which is carried out at atmospheric pressure and at a temperature of 0°C to 150°C. 6. The process of Claim 1 wherein the Lewis acid is selected from the group consisting of inorganic or organometallic compounds in which the cation is selected from scandium, titanium, vanadium, chromium, manganese, iron, cobalt, copper, zinc, boron, aluminum, yttrium, zirconium, niobium, molybdenum, cadmium, rhenium and tin. 7. The process of Claim 6 wherein the Lewis acid is selected from the group consisting of ZnBr 2 , Z11I 2 , ZnC^, ZnSO 4 , CuCb, CuCl, Cu(O3SCF3)2, C0CI2, C0I2, Fel2, FeC , FeCl2(tetrahydrofuran)2, TiCi4(tetrahydrofuran)2, TiCU, T1CI3, ClTi(OiPr)3, MnCl 2 , ScCl 3 , AIC13, (iso-C 4 H 9 ) 2 AlCl, (phenyl) 2 AlCl, phenylAlCl 2 , ReCl 5 , ZrCU, NbCl 5 , VCI3, CrCb, M0CI5, YCI3, CdCl 2 , LaCl 3 , Er(O 3 SCF 3 ) 3 , Yb(O 2 CCF 3 ) 3 , SmCl 3 , TaCl 5 , CdCl 2 , B(C 6 H 5 ) 3 , and (C 6 H 5 ) 3 SnX, wherein X = CF3SO 3 , CH3C 6 H5SO3, or (C 6 H 5 ) 3 BCN 8 The process of claim 1 wherein the ligand has the structure of formula II, R 2 is substituted aryl and R 4 is cycloalkyl 9 The process of claim 1 wherein the ligand has the structure of formula I and R 3 is unsubstituted phenyl 10 The process of claim 9 wherein R , R and R are methyl 11 The process of claim 9 wherein R 1 , R 8 and R 9 are methyl 12 The process of claim 1 having a distribution of at least about 97% 13 A multidentate phosphite ligand of the formulae I II or III Formula I Formula II wherein R 1 is independently Ci to Cι 8 primary or secondary alkyl; R 2 is independently aryl or substituted aryl, R 3 is independently aryl or substituted aryl, R 4 is independently Ci to Cig primary alkyl, is hydrogen; R 6 is independently aryl or substituted aryl, R 7 is independently Ci to Cι primary or secondary alkyl, R 8 is independently Ci to Cι 8 primary or secondary alkyl, R 9 is independently Ci to C ]8 primary or secondary alkyl, and wherein other positions on the aromatic rings may also be substituted with alkyl, ether or ester groups, or combinations of two or more thereof 14 The ligand of claim 13 wherein the ligand has the structure of formula II and R 2 is substituted aryl 15 The ligand of claim 14 wherein R 4 is cycloalkyl 16 The ligand of claim 13 having the structure of formula I wherein R is unsubstituted phenyl 17 The ligand of claim 16 wherein R 1 , R 7 and R 9 are methyl 18 The ligand of claim 16 wherein R 1 , R 8 and R 9 are methyl o

Inventors: LU HELEN S M, RADU NORA S, LU, HELEN, S., M., RADU, NORA, S.
Applicants: DU PONT, E.I. DU PONT DE NEMOURS AND COMPANY
Application year: 2000
Main classification: C07C253
IPC codes: B01J31, C07B61, C07C253, C07C255, C07F9