A hydroformylation

Ruthenium. Ruthenium, as a hydroformylation catalyst (14), has an activity signiftcandy lower than that of rhodium and even cobalt (22). Monomeric mthenium carbonyl triphenylphosphine species (23) yield only modest normal to branched regioselectivities under relatively forcing conditions. For example, after 22 hours at 120°C, 10 MPa (1450 psi) of carbon monoxide and hydrogen, biscarbonyltristriphenylphosphine mthenium [61647-76-5] ... 

Betzemeier et al. (1998) have used f-BuOOH, in the presence of a Pd(II) catalyst bearing perfluorinated ligands using a biphasic system of benzene and bromo perfluoro octane to convert a variety of olefins, such as styrene, p-substituted styrenes, vinyl naphthalene, 1-decene etc. to the corresponding ketone via a Wacker type process. Xia and Fell (1997) have used the Li salt of triphenylphosphine monosulphonic acid, which can be solubilized with methanol. A hydroformylation reaction is conducted and catalyst recovery is facilitated by removal of methanol when filtration or extraction with water can be practised. The aqueous solution can be evaporated and the solid salt can be dissolved in methanol and recycled. 

With the excephon of methanol and ethanol, most alcohols are produced from olefins, either through hydration [10] or via a hydroformylation-hydrogenation sequence (Scheme 4-1) [11]. 

The first stage of the process is a hydroformylation (oxo) reaction from which the main product is n-butyraldehyde. The feeds to this reactor are synthesis gas (CO/H2 mixture) and propylene in the molar ratio 2 1, and the recycled products of isobutyraldehyde cracking. The reactor operates at 130°C and 350 bar, using cobalt carbonyl as catalyst in solution. The main reaction products are n- and isobutyraldehyde in the ratio of 4 1, the former being the required product for subsequent conversion to 2-ethylhexanol. In addition, 3 per cent of the propylene feed is converted to propane whilst some does not react. 

A variant of the BISBI ligand system is the NAPHOS ligand, which as expected gives similar levels of n-selectivity in the course of the hydroformylation of terminal alkenes. Interesting is a hydroformylation in the presence of secondary amines which allows a mild and selective one-pot hydroformy-lation/enamine formation (Scheme 13) [58]. 

Internal acetals are found in several biological active natural products such as di-hydroclerodin [209] and aflatoxins as 6/2-70 [210]. An efficient formation of this functionality was described by Eilbracht and coworkers [211], using a hydroformylation of an enediol as 6/2-71 to give the tetrahydrofurobenzofurans 6/2-72 (Scheme 6/2.15). 

The same group also developed an efficient entry to indoles using a combination of a hydroformylation and a Fischer indole synthesis [212]. Under optimized condi-... 

The existence of two different rhodium species co-existing on the silica support can be used as an advantage by controlling their relative amount. Under standard hydroformylation conditions, the cationic species and the neutral hydride complex are both present in significant amounts. Hence hydroformylation and hydrogenation will both proceed under a CO/H2 atmosphere. Indeed a clean one-pot reaction of 1-octene to 1-nonanol was performed, using the supported catalyst for a hydroformylation-hydrogenation cascade reaction. 98 % of the 1-octene was converted in the... 

Horvath performed experiments using substrates with different solubilities in water and showed that, under optimal conditions, this solubility did not influence the activity [67]. These experiments clearly support the fact that the reaction takes place at the organic-water interphase. Furthermore, he performed a hydroformylation reaction in a continuous system and even under reaction conditions no leaching of rhodium complex was detected. Water obviously leaches if the SAPC is used in a continuous flow system, which in a practical application should be compensated for by using water-saturated organic solvents. 

In the early 1970 s, Bayer et al. reported the first use of soluble polymers as supports for the homogeneous catalysts. [52] They used non-crosslinked linear polystyrene (Mw ca. 100 000), which was chloromethylated and converted by treatment with potassium diphenylphosphide into soluble polydiphenyl(styrylmethyl)phosphines. Soluble macromolecular metal complexes were prepared by addition of various metal precursors e.g. [Rh(PPh3)Cl] and [RhH(CO)(PPh3)3]. The first complex was used in the hydrogenation reaction of 1-pentene at 22°C and 1 atm. H2. After 24 h (50% conversion in 3 h) the reaction solution was filtered through a polyamide membrane [53] and the catalysts could be retained quantitatively in the membrane filtration cell. [54] The catalyst was recycled 5 times. Using the second complex, a hydroformylation reaction of 1-pentene was carried out. After 72 h the reaction mixture was filtered through a polyamide membrane and recycled twice. 

After a hydroformylation run, the reaction solution was subjected to ultrafiltration using an asymmetric polyethersulfone membrane (MWCO 50 kDa) supplied by Sartorius. A retention of 99.8% was found. When the catalyst solution was recycled, virtually the same catalytic activity was observed again (165 TO h 1). Repetitive recycling experiments resulted in 2-7% loss of rhodium, which was subscribed to partial oxidation of the phosphine ligand. 

Figure 9.2. Ligand used for supporting a hydroformylation catalyst on a solid support. Leaching of rhodium under the reaction conditions is insignificant.

A method for observing intermediates directly in the reaction cycle is in situ IR spectroscopy under reaction conditions. As early as 1975, Penninger published a contribution concerning in situ IR spectroscopic studies of cobalt carbonyl modified by tri-u-butylphosphine as a hydroformylation catalyst [58] at relatively low catalyst concentrations of 2 mmoll-1. The observed carbonyl... 

Cyclic a-amino acids with an enamine pattern can be obtained upon enantioselective hydrogenation followed by a hydroformylation/cyclization sequence in a single-pot version Rh(I)-DuPHOS acts as a catalyst for both steps, the enantioselective hydrogenation of prochiral dienamides and the hydroformylation of the resulting homoallylic amines (Scheme 13) [52,53]. 

The thermodynamically favoured product of a hydroformylation reaction is not the aldehyde but the alkane. Yet the product is the aldehyde because kinetic control occurs. 

The tppts process has been commercialised by Ruhrchemie (now Celanese), after the initial work conducted by workers at Rhone-Poulenc, for the production of butanal from propene. Since 1995 Hoechst (now Celanese) also operates a hydroformylation plant for 1-butene. The partly isomerised, unconverted butenes are not recycled but sent to a reactor containing a cobalt catalyst. The two-phase process is not suited for higher alkenes because of the... 

Hydroaminomethylation is a simple, efficient and atom-economic method to synthesize various amines. This one-pot reaction consists of three consecutive steps in the first step a hydroformylation of an olefin is performed followed by the reaction of the resulting aldehyde with a primary or secondary amine to give the corresponding enamine or imine. Lastly, this intermediate is hydrogenated to the desired secondary or tertiary amine (Fig. 11) [33-39]. In most cases rhodium salts or complexes are used as the homogeneous catalyst in the hydroaminomethylation. 

The rhodium complex with bis(diphenylphosphino)phenoxazine was immobilized on silica using the sol-gel technique or by a direct grafting to commercially available silica [127]. Under standard hydroformylation conditions (CO/H2 atmosphere), a neutral hydridic complex (57) and cationic species (58) (Scheme 4.35) coexist on the support and act as a hydroformylation/hydrogenation sequence catalyst, giving selectively 1-nonanol from 1-octene 98% of 1-octene were converted to mainly linear nonanal which was subsequently hydrogenated to 1-nonanol. The... 

Figure 4.3. Scheme of a hydroformylation process with recovery of the catalyst based on phase separation induced by the addition of water to the cataiyst-containig polar phase (N-... 

Bohnen et report a hydroformylation method to convert olefins or olefinically unsaturated compounds in the presence of at least one rhodium compound and sulfonated arylphosphines in ILs based on a quaternary ammonium ion or the equivalent of a multiply charged ammonium ion and organic sulfonates or sulfates. 

The hydrolytic decomposition of a potential fluorophosphite ligand would generate free fluoride ions which would be expected to be detrimental to the activity of a hydroformylation catalyst. The patent literature contains abundant references to the detrimental effects of halogens (6) on hydroformylation catalysts, and based on the patent information, one could not reasonably expect a halophosphite to be a successful hydroformylation ligand. However, a second publication by Klender (7) shows that exposure of / and other fluorophosphites to moisture at temperatures of 250°C to 350°C does not generate fluoride, even at part per million levels. 

Symmetric alkenediols undergo a hydroformylation reaction to give perhydrofuro[2,3-, ]pyrans in the presence of a rhodium catalyst. The reaction proceeds in high yields, except in the case of the l,6-diphenyl-3-hexene-l,6-diol (40%) (Equation 19) <2002OL289>. 

Cyanide-containing cobalt catalysts, particularly potassium pentacyanocobalta-te(II) K3[Co(CN)5], are used in the reduction of activated alkenes (conjugated dienes).26,31 [Co(CO)4]2 is best known as a hydroformylation catalyst, but hydrogenation is also possible under specific conditions. Phosphine-substituted analogs are more successful. 

The complex [Rh(nbd)(amphos)2]3+, which contains the water-soluble ligand amphos (33), has been prepared. In a two-phase system this complex acted as a hydroformylation catalyst for 1-hexene.133 Isomerization of the alkene occurred to a limited extent. In the presence of H2 and CO the dicarbonyl [Rh(CO)2(amphos)2]3+ was thought to be formed. 

The reaction of alkenes (and alkynes) with synthesis gas (CO + H2) to produce aldehydes, catalyzed by a number of transition metal complexes, is most often referred to as a hydroformylation reaction or the oxo process. The discovery was made using a cobalt catalyst, and although rhodium-based catalysts have received increased attention because of their increased selectivity under mild reaction conditions, cobalt is still the most used catalyst on an industrial basis. The most industrially important hydrocarbonylation reaction is the synthesis of n-butanal from propene (equation 3). Some of the butanal is hydrogenated to butanol, but most is converted to 2-ethylhexanol via aldol and hydrogenation sequences. 

For monosubstituted ethylenes chiral products arise only when the hydrogen of the catalyst binds to the unsubstituted unsaturated carbon atom of the substrate. Since this product is, in general, the minor one, from the enantiomeric excess no prediction can be made of the face of the substrate preferentially attacked but only the face of the substituted unsaturated carbon atom preferentially formylated to form the chiral product can be established. Indications about all 4 transition states can be obtained using either labelled 2-(2H]-olefins or carrying out a deuterio-formylation instead of a hydroformylation (see Sect. 2.1.5.). 

The reactions of ethyl acrylate and ethyl crotonate were studied (117) in the presence of ethyl orthoformate using 1 1 CO/H2 and 250 and 200 atm pressure. For ethyl acrylate, the distribution of products corresponded to j3-hydroformylation 78.2%, (y,y-diethoxybutyrate and j3-formylpropionic acid), and a-hydroformylation 21.7%, (a-methyl-j8-ethoxyacrylate and -methyl-j3,/3-diethoxypropionate). For ethyl crotonate, y-hydroformyla-tion occurred to the extent of 67-73% (8,8-diethoxyvalerate and y-formyl-butyrate) and a-hydroformylation to the extent of only 13.6% (a-ethyl-/ -ethoxyacrylate and j3-ethyl-j8-diethoxypropionate). 

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