Higher aqueous-organic biphasic system

In the hydroformylation of alkenes, the major differences between the [RhH(CO)(PPh3)3], and [RhH(CO)(TPPTS)3] catalysts are the lower activity and higher selectivity of the water-soluble complex in aqueous/organic biphasic systems. Lower activity is not unexpected, since alkenes have limited solubility in water (see 4.1.1.1, Table 3). On the other hand, the higher selectivity towards formation of the linear product deserves more scrutiny. 

Higher olefins have negligible solubility in water therefore their hydrocarboxylation in aqueous/organic biphasic systems needs co-solvents or phase transfer agents. With the aid of various PT catalysts 1-octene and 1-dodecene were successfully carbonylated to the corresponding carboxylic acids with good yields (< 85 %) and up to 87 % selectivity towards the formation of the linear add with a [Co2(CO)g] catalyst precursor under forcing conditions (150 °C, 200 bar CO) [57],... 

A recent and exciting area of research is the solubilization of enzymes in nonaqueous solvents. One way solubilization is achieved is through noncovalent complexes of lipid (surfactant) and protein, to be referred to here as enzyme-lipid aggregates, or ELAs. Such complexes are reported to be highly active and stable. Moreover, the activity of ELAs can be significantly higher than free, suspended enzyme (in the absence or presence of surfactant), enzymes solubilized in aqueous-organic biphasic systems, or reverse micellar solutions, and can approach catalytic rates in... 

In conclusion it can be said, that micellar effects offer useful possibilities to tune the reactivity and separation characteristics of aqueous/organic biphasic hydroformylations. Nevertheless, the added sensitivity of the systems to small changes in process variables and the added cost of surfactants and/or specially synthetized ligands have to be justified by high added value products or on grounds of process cost savings. Whether this will happen on industrial scale (perhaps in the hydroformylation of higher olefins) remains to be seen. 

Reactions with these compounds suffer from very low substrate concentrations due to the low solubility of hydrophobic ketone substrates in aqueous media, which leads to unsatisfactory volumetric productivities. To achieve higher substrate concentrations, a biphasic reaction medium was introduced. The system water/ n-heptane (4 1) proved to be the most suitable system with regard to stability of the examined enzymes. The large-scale available (S)-specific ADH from R. erythropolis as well as FDH from C. boidinii are stable for long periods of time in this aqueous-organic solvent system. Preparative conversions with a variety of aromatic ketone substrates were carried out with this reaction medium. For example, p-chloroacetophenone was converted into the corresponding (S )-alcohol with >99% ee and 69% conversion. The obvious increase in volumetric productivity is due to the higher substrate concentrations. The reduction of p-chloroacetophenone... 

There have been many approaches to overcome the problem of low space-time yields in biphasic reaction systems with rhodium and other metals, such as the Ruhrchemie/Rhone-Poulenc process. Concerning two-phase hydroformylation of higher alkenes in an aqueous-organic reaction system, the different approaches can be categorized as follows ... 

The most severe dra wback in homogeneous catalysis is the separation of the catalyst from the reaction mixture. The industrial success of the aqueous two-phase hydroformylation ofpropene to n-butanal [1] in Ruhrchemie AG in 1984 represents the considerable progress in this field. However, aqueous/organic biphasic catalysis has its limitations when the water solubility of the starting materials proves too low, as in hydroformylation of higher olefins (see Chapter 1). To solve this issue, a variety of approaches have been attempted. Additions of co-solvents [2] or surfactants [3, 4] to the system or application of tenside ligands [5, 6] and amphiphilic phosphines [7, 8] are ways to increase the reaction rates. Other approaches such as fluorous biphase system (FBS see Chapter 4) [9], supported aqueous phase catalysis (SAPC see Section 2.6) [10], supercritical CO2 (cf. Chapter 6) [11] and ionic liquids (cf Chapter 5) [12] have also been introduced to deal with this problem. 

Multiply substituted and higher olefins could be successfully hydroformy-lated in PEG-containing organic-organic biphasic systems using the [Rh(PEG)J catalyst precursor. This compoiuid is also active in aqueous-organic systems, and its properties are discussed in the subsection on Hydroformylation under Aqueous-Organic Biphasic Catalysis. 

Rhodium catalysts generated from the sulfonated phosphine 23 (Table 2) were effective in the hydrogenation of olefins in an aqueous/organic or in a homogeneous methanol system, substantially higher rates being observed in the latter system.131 For example, the TOF observed in the hydrogenation of 1-hexene in the biphasic system was 220 h 1 compared to 7860 h 1 in methanol.131... 

Biphasic systems proved to be advantageous as well in the biocatalytic synthesis of (-)-l-trimethylsilylethanol which was performed by asymmetric reduction of acetyltrimethylsilane with an isolate from Rhodotorula sp. AS2.2241 [144]. Immobilized cells were employed due to the easy separation of the product as well as the improved tolerance against unfavorable factors. In an aqueous/organic solvent biphasic system higher product yield and enantiomeric excess were achieved as compared to an aqueous monophasic system. Several organic solvents were examined, and isooctane was found to be the most suitable organic phase for the reaction. 

---