Patent Grant
8299284
The present invention in general relates to compounds and compositions capable of splitting dihydrogen, and in particular to compounds and compositions dissociating dihydrogen and use of said compounds in metal-free hydrogenation. These species are also capable of transfer hydrogenation.
The generation and use of molecular hydrogen (H2) are important processes to fundamental chemical transformations and biological functions. The overwhelming majority of systems known to either liberate or react with H2 involve reaction at a transition metal center. Hydrogenase enzymes, as well as a plethora of synthetic stoichiometric and catalytic reagents for hydrogenation reactions, are based on the processes of oxidative addition and reductive elimination of H2 at a metal center. Metal-free systems that either react with or liberate H2 are rare. A unique metal-free hydrogenase from methanogenic archaeas has been shown to catalyze reactions with H2, and theoretical studies suggest the role of a folate-like cofactor in the reversible activation/liberation of H2. Several metal-free systems have been shown to activate H2. For example, main group element-H2 reactions in low temperature matrices are also known.
Hydrogenation is the addition of hydrogen to unsaturated organic compounds. Such reactions are used for the production of a myriad of chemical products worldwide, from large-scale operations including the upgrading of crude oil and the production of bulk commodity materials to the synthesis of a variety of fine chemicals used in the food, agricultural, and pharmaceutical industries. The process of hydrogen addition to unsaturated precursors is mediated by either homogeneous or heterogeneous transition metal based catalysts. In the 1960s, the advent of organometallic chemistry gave rise to homogeneous transition metal based hydrogenation catalysts for a variety of substrates. The operation of these catalysts hinges on the key step of oxidative addition of hydrogen. More recently, transition metal, systems that effect heterolytic cleavage of hydrogen at a metal center have been uncovered. In these cases, a metal hydride is formed with concurrent protonation of an amido ligand.
Non-transition metal catalysts for hydrogenation reactions are all but unknown. KOtBu has been shown to act as a catalyst effecting the addition of H2 to benzophenone under forcing conditions of 200° C. and greater than 100 bar H2. Organocatalysts have been developed for hydrogenations of enones and imines; however, such systems do not employ H2 directly but rather a surrogate such as a Hantzsch ester as the stoichiometric source of hydrogen. The development of nonmetal hydrogenation catalysts hinges on the discovery of systems that react cleanly with H2, but few are known. Power and coworkers reported the hydrogenation of Ge2-alkyne analogues to give a mixture of Ge2 and primary germane products. J. W. Yang. M. T. Hechavarria Fonseca, B. List, Angew. Chem. 2004, 116, 6829; Angew. Chem. Int. Ed. 2004, 43, 6660. G. H. Spikes. J. C. Fettinger. P. P. Power, J. Am. Chem. Soc. 2005, 127, 12 232. It should be noted that non-transition metal systems have been shown to effect hydrogenation under more forcing conditions. For example. DeWitt. Ramp and Trapasso demonstrated hydrogenation with iPr3B under 67 atm (1000 psi) H2 at 220° C. E. J. DeWitt, F. L. Ramp, L. E. Trapasso, J. Am. Chem. Soc. 1961, 83, 4672-4672; F. L. Ramp, E. J. DeWitt, L. E. Trapasso, Org. Chem. 1962, 27, 4368-4372). Similarly. Haenel and coworkers (E. Osthaus, M. W. Haenel, in Coal Science and Technology, Vol. 11 Elsevier, Amsterdam, 1987, pp. 765-768 (Proc. 1987 Intern. Conf. Coal Sci., Eds.: J. A. Moulijn, K. A. Nater, H. A. G. Chermin),; M. Yalpani, R. Köster, M. W. Haenel, Erdoel Kohle, Erdgas. Petrochem. 1990, 43, 344-347; M. W. Haenel, J. Narangerel, U.-B. Richter, A. Rufinska, Angew. Chem. 2006, 118, 1077-1082; Angew. Chem. Int. Ed. 2006, 45, 1061-1066; M. W. Haenel, J. Narangerel, U.-B. Richter, A. Rufinska, Prep. Pap. Am. Chem. Soc, Div. Fuel Chem. 2006, 51(2), 741-742) among others showed hydrogenation of coal under almost 15 MPa and 280-350° C. using BI3 or alkyl boranes. M. Yalpani, T. Lunow, R. Köster, Chem. Bar. 1989, 122, 687-693; (b) M. Yalpani, R. Köster, Chem. Per. 1990, 123, 719-724. As well, superacid systems have also been shown to effect hydrogenation of alkenes using H2 pressures of at least 35 atm. M. Siskin, J. Am, Chem. Soc. 1974, 96, 3641; (b) J. Wristers, J. Am. Chem. Soc. 1975, 97, 4312.
The ability to dissociate dihydrogen represents a reaction of considerable importance in fields including hydrogenation of ethenically unsaturated feed stocks, chemical fuel storage, hydrogen purification, and hydrogen getters that prevent hydrogen levels from building beyond a preselected threshold. Traditionally, dihydrogen dissociation has involved the use of metal catalysts and in particular palladium. Conventional catalysts inclusive of metal have a number of limitations that include high material cost, high density, the heterogeneous nature of such catalysts relative to liquid phase reactants, and contamination of resultant products with metal catalysts.
Thus, there exists a need for a hydrogen dissociation catalyst that is independent of metal. Additionally, a catalyst capable of operating as a homogeneous catalyst would afford considerable operational advantages. Further, these hydrogen catalysts operate efficiently at lower or comparable temperatures to those used for existing metal based hydrogenation catalysts.
A compound is provided that is operative as a hydrogenation catalyst. The compound is capable of homogenous liquid phase catalysis exclusive of a noble metal. A compound has the formula:
where each of R1, R2, R3 and R4 is independently C6-C18 is aryl-, C5-C8 cycloalkyl-, C6-C18 aryl having at least one C1-C20 alkyl substituent, C5-C8 cycloalkyl having at least one C1-C20 alkyl substituent, C4-C20 branched alkyl-, C16-C30 linear alkyl-, RO—, —NRR′, —PRR′, —SR, fluoro substituted forms thereof, and perfluoro forms thereof; and R5 is C6-C18 is aryl-, C5-C8 cycloalkyl-, C6-C18 aryl having at least one C1-C20 alkyl substituent, C5-C8 cycloalkyl having at least one C1-C20 alkyl substituent, C3-C20 branched alkyl-, C2-C30 linear alkyl-, RO—, —NRR′, —PRR′, —SR, fluoro substituted forms thereof, and perfluoro forms thereof; where R and R′ are each independently C6-C18 aryl-, C5-C8 cycloalkyl-, C6-C18 aryl having at least one C1-C20 alkyl substituent. C5-C8 cycloalkyl having at least one C1-C20 alkyl substituent, C4-C20 branched alkyl-, C2-C30 linear alkyl-, fluoro substituted forms thereof, and perfluoro forms thereof; A is N, P, S, or O with the proviso that when A is S or O, R2 is a nullity; and M is B, Al, Ga or In.
A composition operative as a hydrogenation catalyst includes a compound having the formula:
where each of R1 and R2 is independently C6-C18 aryl-, C5-C8 cycloalkyl-, C6-C18 aryl having at least one C1-C20 alkyl substituent, C5-C8 cycloalkyl having at least one C1-C20 alkyl substituent. C4-C20 branched alkyl-, C16-C30 linear alkyl-, RO—, —NRR′, —PRR′, —SR, fluoro substituted forms thereof, and perfluoro forms thereof; R6 is C1-C30 alkyl-, C6-C18 aryl-, C5-C8 cycloalkyl-, RO—, —NRR′, —PRR′, —SR, a fluoro substituted form thereof, a perfluoro substituted form thereof, H or F; where R and R′ are each independently C6-C18 aryl-, C5-C8 cycloalkyl-, C6-C18 aryl having at least one C1-C20 alkyl substituent, C5-C8 cycloalkyl having at least one C1-C20 alkyl substituent, C4-C20 branched alkyl-, C2-C30 linear alkyl-, fluoro substituted forms thereof, and perfluoro forms thereof; A is N, P, S, or O with the proviso that when A is S or O, R2 is a nullity; in fluid communication with a composition having the formula:
where each of R4, R5 and R7 is independently C6-C18 aryl-, C5-C8 cycloalkyl-, C6-C18 aryl having at least one C1-C20 alkyl substituent, C5-C8 cycloalkyl having at least one C1-C20 alkyl substituent, C4-C20 branched alkyl-, C16-C30 linear alkyl-, RO—, —NRR′, —PRR′, —SR, fluoro substituted forms (hereof and perfluoro forms thereof; where R and R′ are each independently C6-C18 aryl-, C5-C8 cycloalkyl-, C6-C18 aryl having at least one C1-C20 alkyl substituent, C5-C8 cycloalkyl having at least one C1-C20 alkyl substituent, C4-C20 branched alkyl-, C2-C30 linear alkyl-, fluoro substituted forms thereof, and perfluoro forms thereof; and M is B, Al, Ga or In; or a composition of the formula:
where M1 is Ti, Zr or Hf; each of R8, R9 and R10 is independently C6-C18 aryl-, C5-C8 cycloalkyl-, C6-C18 aryl having at least one C1-C20 alkyl substituent, C5-C8 cycloalkyl having at least one C1-C20 alkyl substituent, C4-C20 branched alkyl-, amide, alkoxide, phenoxide, phosphinimide, cyclopentadienyl, indenyl, fluorenyl derivatives, RO—, —NRR′, —PRR′, —SR, fluoro substituted forms thereof, and perfluoro forms thereof; where R and R′ are each independently C6-C18 aryl-, C5-C8 cycloalkyl-, C6-C18 aryl having at least one C1-C20 alkyl substituent, C5-C8 cycloalkyl having at least one C1-C20 alkyl substituent, C4-C20 branched alkyl-, C2-C30 linear alkyl-, fluoro substituted forms thereof, and perfluoro forms thereof; and R11 is C1-C20 alkyl linear or branched with the proviso that R11 is a better leaving group than any of R8, R9 or R10 under nucleophic attack by a hydrogen or other alkyl abstracting agents to yield a cationic M1 species.
A compound is also provided that is an addition reaction product of a compound of formula I and dihydrogen (H2). The compound has the formula:
where each of R1, R2, R3 and R4 is independently C6-C18 aryl-, C5-C8 cycloalkyl-, C6-C18 aryl having at least one C1-C20 alkyl substituent, C5-C8 cycloalkyl having at least one C1-C20 alkyl substituent, C4-C20 branched alkyl-, C16-C30 linear alkyl-, RO—, —NRR′, —PRR′, —SR, fluoro substituted forms thereof, and perfluoro forms thereof; and R5 is C6-C18 aryl-, C5-C8 cycloalkyl-, C6-C18 aryl having at least one C1-C20 alkyl substituent, C5-C8 cycloalkyl having at least one C1-C20 alkyl substituent, C3-C20 branched alkyl-, C2-C30 linear alkyl-, fluoro substituted forms thereof and perfluoro forms thereof; where R and R′ are each independently C6-C18 aryl-, C5-C8 cycloalkyl-, C6-C18 aryl having at least one C1-C20 alkyl substituent, C5-C8 cycloalkyl having at least one C1-C20 alkyl substituent, C4-C20 branched alkyl-, C2-C30 linear alkyl-, fluoro substituted forms thereof, and perfluoro forms thereof; A is N, P, S, or O with the proviso that when A is S, R2 is a nullity; and M is B, Al, Ga or In.
A process of catalytic hydrogenation of a substrate comprising: independently compound I, a mixture of II and III, compound III, a mixture of II, III-V, compound IV, or compound VI together with dihydrogen and solvent form a catalyst whereby hydrogenation of a substrate is effected.
The present invention has utility as compounds and compositions capable of dissociating dihydrogen and reversibly binding hydrogen atoms. In addition to dihydrogen dissociation, a sacrificial dihydrogen source such as primary or secondary amines, primary or secondary phosphines, alcohols and thiols are also is operative according to the present invention to reduce substrates. According to the present invention, a compound is provided that is the reaction product of a sterically hindered Lewis acid with a sterically hindered Lewis base via an intermediate linker group therebetween. The prototypical form of an inventive compound I is a reaction product of linker separated sterically hindered phosphine and a sterically hindered borane. An inventive compound has the formula:
where each of R1, R2, R3 and R4 is independently C6-C18 aryl-, C5-C8 cycloalkyl-, C6-C18 aryl having at least one C1-C20 alkyl substituent, C5-C8 cycloalkyl having at least one C1-C20 alkyl substituent, C4-C20 branched alkyl-, C16-C30 linear alkyl-, RO—, —NRR′, —PRR′, —SR, fluoro substituted forms thereof, and perfluoro forms thereof; and R5 is C6-C18 aryl-, C5-C8 cycloalkyl-, C6-C18 aryl having at least one C1-C20 alkyl substituent, C5-C8 cycloalkyl having at least one C1-C20 alkyl substituent, C3-C20 branched alkyl-, C2-C30 linear alkyl-, RO—, —NRR′, —PRR′, —SR, fluoro substituted forms thereof, and perfluoro forms thereof; where R and R′ are each independently C6-C18 aryl-, C5-C8 cycloalkyl-, C6-C18 aryl having at least one C1-C20 alkyl substituent, C5-C8 cycloalkyl having at least one C1-C20 alkyl substituent, C4-C20 branched alkyl-, C2-C30 linear alkyl-, fluoro substituted forms thereof, and perfluoro forms thereof; A is N, P, S, or O with the proviso that when A is S or O, R2 is a nullity; and M is B, AT Ga or In.
A bimolecular composition according to the present invention capable of dissociating hydrogen and reversibly binding hydrogen atoms includes in a mixture of a phosphine and a borane incapable of reaction owing to steric hindrance. Sterically hindered phosphine is readily replaced with a nitrogen, oxygen, or sulfur analog as shown in formula II. Sterically hindered borane is readily replaced with an aluminum, gallium, or indium analog as shown in formula III. Lesser sterically hindered systems exhibit reactivity at temperatures dependent on the nature of the compounds. The mixture of sterically hindered Lewis base and Lewis acid compounds operative herein have the formulae II and III, respectively:
where each of R1 and R2 is independently C6-C18 is aryl-, C5-C8 cycloalkyl-, C6-C18 aryl having at least one C1-C20 alkyl substituent, C5-C8 cycloalkyl having at least one C1-C20 alkyl substituent, C4-C20 branched alkyl-, C16-C30 linear alkyl-, RO—, —NRR′, —PRR′, —SR, fluoro substituted forms thereof, and perfluoro forms thereof; R6 is C1-C30 alkyl-, C6-C18 aryl-, C5-C8 cycloalkyl-, RO—, —NRR′, —PRR′, —SR, a fluoro substituted form thereof, a perfluoro substituted form thereof, H or F; where R and R′ are each independently C6-C18 aryl-, C5-C8 cycloalkyl-, C6-C18 aryl having at least one C1-C20 alkyl substituent, C5-C8 cycloalkyl having at least one C1-C20 alkyl substituent, C4-C20 branched alkyl-, C2-C30 linear alkyl-, fluoro substituted forms thereof, and perfluoro forms thereof; A is N, P, S, or O with the proviso that when A is S or O, R2 is a nullity.
where each of R4, R5 and R7 is independently C6-C18 aryl-, C5-C8 cycloalkyl-, C6-C18 aryl having at least one C1-C20 alkyl substituent, C5-C8 cycloalkyl having at least one C1-C20 alkyl substituent, C4-C20 branched alkyl-, C16-C30 linear alkyl-, RO—, —NRR′, —PRR′, —SR, fluoro substituted forms thereof, and perfluoro forms thereof; where R and R′ are each independently C6-C18 aryl-, C5-C8 cycloalkyl-, C6-C18 aryl having at least one C1-C20 alkyl substituent, C5-C8 cycloalkyl having at least one C1-C20 alkyl substituent, C4-C20 branched alkyl-, C2-C30 linear alkyl-, fluoro substituted forms thereof, and perfluoro forms thereof; and M is B, Al, Ga or In. In a particular embodiment a sterically hindered perfluorinated composition of formula III has hydrogen catalytic activity independent of the presence of a compound of formula II.
A compound of the formula is also provided that is reversibly converted into the compound of formula I through loss of two hydrogen atoms. The compound has the formula:
where each of R1, R2, R3 and R4 is independently C6-C18 aryl-, C5-C8 cycloalkyl-, C6-C18 aryl having at least one C1-C20 alkyl substituent, C5-C8 cycloalkyl having at least one C1-C20 alkyl substituent, C4-C20 branched alkyl-, C16-C30 linear alkyl-, RO—, —NRR′, —PRR′, —SR, fluoro substituted forms thereof, and perfluoro forms thereof; and R5 is C6-C18 aryl-, C5-C8 cycloalkyl-, C3-C20 branched alkyl-, C2-C30 linear alkyl-, fluoro substituted forms thereof, and perfluoro forms thereof; where R and R′ are each independently C6-C18 aryl-, C5-C8 cycloalkyl-, C6-C18 aryl having at least one C1-C20 alkyl substituent, C5-C8 cycloalkyl having at least one C1-C20 alkyl substituent, C4-C20 branched alkyl-, C2-C30 linear alkyl-, fluoro substituted forms thereof, and perfluoro forms thereof; A is N, P, S, or O with the proviso that when A is S, R2 is a nullity; and M is B, Al, Ga or In.
In an alternate embodiment, hydrogenation occurs through the interaction of a composition of formula II with a transition metal cation of Ti, Zr, or Hf when A is P or N. The transition metal cation is generated in situ by alkyl group abstraction from an organometallic composition of the formula:
where M1 is Ti, Zr or Hf; each of R8, R9 and R10 is independently C6-C18 aryl-, C5-C8 cycloalkyl-, C6-C18 aryl having at least one C1-C20 alkyl substituent, C5-C8 cycloalkyl having at least one C1-C20 alkyl substituent, C4-C20 branched alkyl-, amide, alkoxide, phenoxide, phosphinimide, cyclopentadienyl, indenyl, fluorenyl derivatives, RO—, —NRR′, —PRR′, —SR, fluoro substituted forms thereof, and perfluoro forms thereof; where R and R′ are each independently C6-C18 aryl-, C5-C8 cycloalkyl-, C6-C18 aryl having at least one C1-C20 alkyl substituent, C5-C8 cycloalkyl having at least one C1-C20 alkyl substituent, C4-C20 branched alkyl-, C2-C30 linear alkyl-, fluoro substituted forms thereof, and perfluoro forms thereof; and R11 is C1-C20 alkyl linear or branched with the proviso that R11 is a better leaving group than any of R8, R9 or R10 under nucleophic attack by a hydrogen or other alkyl abstracting agents to yield a cationic M1 species.
The present invention compounds and mixtures of compounds are effective as hydrogenation catalysts for performing reactions illustratively including those provided in Table 1. The compositions and compounds of formulae I-V are operative in hydrogenation catalysis in a neat liquid substrate, in a solution containing substrate, or applied as coating on an inert support.
The present invention is further detailed with respect to the following nonlimiting examples.
The catalyst (0.1-20 mol %) is weighed into a 50 ml round bottomed Schlenk flask and slurried in toluene (2 ml). The reaction is charged with H2. The slurry is then allowed to equilibrate at the desired temperature under an atmosphere of H2 with rapid stirring. A solution of substrate (1.0 mmol) in toluene (2 ml) is added via syringe. Reaction time and temperature vary with substrate. In all cases, the crude mixtures of the completed reactions are pure to the limits of NMR spectroscopy. The product is purified by all volatiles being removed in vacuo trap to trap vacuum distillation or filtration, through a small plug of silica to remove residual catalyst.
In a glove box, tBu2PH—C6F4—BH(C6F5)2 (0.033 g, 0.05 mmol) is weighed into a 50 ml round bottomed Schlenk flask equipped with a small stir bar and slurried in toluene (2 ml). The reaction is attached to a vacuum/H2 line and freeze-pump-thaw cycled three times. The slurry is then allowed to equilibrate at 80° C. under an atmosphere of H2 with rapid (500 rpm) stirring. A solution of N-benzylidine-tert-butyl amine (0.161 g, 1.0 mmol) in toluene (2 ml) is added via syringe. The reaction is periodically monitored by thin layer chromatography (silica, eluent: 1:5 ethyl acetate/hexanes) and 1H NMR spectroscopy and is complete in 1 hour. The solvent is removed in vacuo and the product benzyl-tert-butylamine is purified by trap to trap vacuum distillation. Isolated yield 0.128 g (79%).
The catalyst (0.01-0.20 mmol) and substrate (1 mmol) are weighed into a 100 ml round bottomed glass flask equipped with a Kontes valve. Solvent (4 ml) is added, the reaction transferred to a vacuum/H2 line and the mixture is freeze-pump-thaw cycled three times. The mixture is cooled to −196° C. (liquid N2) and 1 atm. H2 is introduced. The flask is sealed, the reaction is placed in a preheated bath and rapidly stirred. Reaction time and temperature vary with substrate. In all cases, the crude reaction mixtures are of the completed reactions are pure to the limits of NMR spectroscopy. The product is purified by removal of all volatiles in vacuo and trap to trap vacuum distillation or nitration through a small plug of silica to remove residual catalyst.
In a glove box, tBu2PH(C6F4)BH(C6F5)2 (0.33 g, 0.05 mmol) and cis-1.2.3-triphenylaziridine (0.271 g, 1.0 mmol) were weighed into a 100 ml round bottomed glass flask equipped with a Kontes valve and a magnetic stirbar. Toluene (4 ml) is added, the reaction transferred to a vacuum/H2 line and the mixture is freeze-pump-thaw cycled three times. The mixture is cooled to −196° C. (liquid N2) and 1 atm. H2 is introduced. The flask is sealed, the reaction is placed in a 120° C. preheated bath and rapidly (500 rpm) stirred. The reaction is periodically monitored by 1H NMR spectroscopy and is complete in 2 hours. The reaction mixture is poured onto a small plug of silica and eluted with 2:1 hexanes/ethyl acetate (50 ml). The solvent is removed in vacuo and the product N-1,2-diphenylethyl-N-phenyl amine isolated. Yield: 0.269 g (98%)
In the glovebox, a substrate (1 mmol) per Table 2, B(C6F5)3 (26 mg, 0.05 mmol, 5 mol %) and dry toluene (4 ml) are weighed into a 100 ml round bottomed flask equipped with a scalable Teflon tap and small magnetic stirbar. The reaction is then attached to a double manifold H2/vacuum line and degassed (freeze-pump-thaw cycle×3). The reaction is cooled to −196° C. (liquid N2) and 1 atm. H2 is introduced. The flask is sealed and warmed to room temperature. The reaction is then placed in an oil bath heated to the desired temperature and stirred at 500 rpm. At 120° C., the H2 pressure is ˜5 atm. Aliquots are obtained at periodic intervals by rapidly cooling the reaction in a water bath and venting the H2 pressure. Samples are taken by pipette in the glove box. The reaction is re-pressurized using the above procedure. Upon full conversion, the reaction is poured onto a 10 cm plug of silica (200 mesh) and eluted with 2:1 hexanes/ethyl acetate (200 ml). If the amine is not fully soluble in the reaction mixture or the hexanes/ethyl acetate solvent, CH2Cl2 (3×5 ml) is used to wash the reaction vessel. The collected solvent is removed in vacuo to obtain the product in the time and yield shown in Table 2.
aconditions, 1 atm. H2, 80° C.
In the glovebox, a substrate (1 mmol) per Table 3, is reacted in the presence of P(2,4,6-Me3C6H2)3 (19 mg 0.05 mmol, 5 mol %) or PtBu3, (10 mg, 0.05 mmol, 5 mol %) according to the procedure of the Comparative Example. As shown in Table 3, more efficient reaction with the sterically hindered phosphine (formula II) is noted for the imine PhCH(N)SO2Ph and MeCN—B(C6F5)3 reacts when no reductive catalysis is noted absent the phosphine (formula II).
In a glove box, a 100 ml glass bomb equipped with a small stir bar and a Teflon screw tap is charged with imine (1 mmol), catalyst (0.05 mmol, 5 mol %), and dry toluene (4 ml). The reaction is transferred to the vacuum/H2 line and is degassed three times with a freeze-pump-thaw cycle. The reaction flask is cooled to −196° C., 1 atm of H2 is introduced, and the flask then sealed and warmed to room temperature. The reaction is placed in a preheated oil bath and stirred at 500 rpm; at 120° C. this gave an H2 pressure of about 5 atm. To take aliquots, the reaction is cooled rapidly in an ice bath, vented to release the H2 pressure, and taken into a glove box. For the catalyst (2,4,6-Me3C6H2)2 PH(C6H4) BH(C6F5)2 (denoted as compound 1) and (tert-butyl)2 PH(C6H4) BH(C6F5)2 (denoted as compound 2), the following products are obtained in the time and yield shown in Table 4.
These compounds are prepared in a similar fashion. A clear yellow solution of B(C6F5)3 (0.500 g, 0.98 mmol) and i-Pr3P (0.156 g, 0.98 mmol) or molar equivalent of (C6H11)3P, (t-Bu)3P, or (2,4,6-Me3C6H2)3P in toluene (20 mL) is allowed to stir for 12 h at 25° C. during which time a white precipitate formed. Pentane (10 mL) is added, the mixture filtered and dried in vacuo for 1 h. In the instance of (2,4,6-Me3C6H2)3P stirring took place in refluxing toluene. The product is collected as a white solid.
To a solution of compound 3 (0.400 g, 0.600 mmol) or a molar equivalent of compounds 4, 5 or 6 dissolved in CH2Cl2 (10 mL) is added (CH3)2SiHCl (0.66 mL, 6.00 mmol) via syringe. The reaction is allowed to stir 12 h, during which time a precipitate forms. All volatiles are removed in vacuo to give the product as a white solid.
An orange solution of [Ph3C][B(C6F5)4] (0.420 g, 0.456 mmol) in CH2Cl2 (2 mL) is added to a slurry of compound 7 (0.300 g, 0.457 mmol) or molar equivalent of 8, 9, or 10 in CH2Cl2 (5 mL) to give a faint yellow solution. The reaction is allowed to stir for 30 min and the volatiles are removed in vacuo. Pentane (5 mL) is added and the mixture filtered and washed with toluene (2 mL) and pentane (3×2 mL) to give an off white solid.
A 20 mL vial is charged with compound 5 (0.099 g, 0.150 mmol) or a molar equivalent of composition 6, toluene (10 mL) and diethyl ether (1 mL), forming a white slurry. The mixture is cooled to −35° C. and 3.0 M MeMgBr in diethyl ether (0.060 mL, 0.180 mmol) is added via syringe. Immediate formation of a clear yellow solution is observed. The reaction is allowed to warm to room temperature and stirred for 12 h. All volatiles are removed in vacuo and the product extracted with hexanes (3×5 mL) and filtered through celite. The solvent is removed in vacuo to give a yellow solid.
In a glovebox, cis-1,2,3-triphenylaziridine (1 mmol), B(C6F5)3 (6.05 mmol) and (2,4,6-Me3C6H2)3P (0.05 mmol) are reacted according to the procedure of the Comparative Example to yield N-1,2-diphenylethyl-N-phenyl amine.
Patent documents and publications mentioned in the specification are indicative of the levels of those skilled in the art to which the invention pertains. These documents and publications are incorporated herein by reference to the same extent as if each individual document or publication was specifically and individually incorporated herein by reference.
The foregoing description, is illustrative of particular embodiments of the invention, but is not meant to be a limitation upon the practice thereof. The following claims, including all equivalents thereof, are intended to define the scope of the invention.
This application claims priority benefit of U.S. Provisional Applications 60/865,684 filed Nov. 14, 2006; and 60/896,557 filed Mar. 23, 2007 the contents of which are hereby incorporated by reference.
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/IB2007/004577 | 11/14/2007 | WO | 00 | 5/14/2009 |
| Publishing Document | Publishing Date | Country | Kind |
|---|---|---|---|
| WO2008/125911 | 10/23/2008 | WO | A |
| Number | Name | Date | Kind |
|---|---|---|---|
| 20010049331 | Chang | Dec 2001 | A1 |
| Number | Date | Country |
|---|---|---|
| 2004113351 | Dec 2004 | WO |
| Number | Date | Country | |
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| 20100048949 A1 | Feb 2010 | US |
| Number | Date | Country | |
|---|---|---|---|
| 60865684 | Nov 2006 | US | |
| 60896557 | Mar 2007 | US |
