METALLOPROTEASES 233
(Inouye, 1992; Murakami et al., 1996), systems with water-miscible organic solvents
(Lee et al., 1992; Kühn et al., 2002), biphasic systems (Hirata et al., 1997; Murakami
and Hirata, 1997; Murakami et al., 1998; Miyanaga et al., 2000b), solid-to-solid
synthesis (Erbeldinger et al., 1998a, b; Erbeldinger et al., 2001) and low-water
solvent systems (Nakanishi et al., 1985). For syntheses in aqueous/organic biphasic
systems (Murakami and Hirata, 1997; Hirata et al., 1997), in low-water solvent
systems with immobilized thermolysin (Nakanishi et al., 1985, 1990) or in
membrane systems (Iacobucci et al., 1994), continuous operation has been used
successfully.
Yields in pure aqueous systems are usually very low. The activity of thermolysin
and, accordingly, the reaction rates in aqueous systems have been found to be
enhanced by the addition of sodium and potassium salts (Inouye, 1992). However,
the pH increase due to salt addition may result in non-enzymatic hydrolysis of the
reactants, a problem which is avoided in reactions at low pH. High yields (95%)
have been achieved by insoluble salt formation between the product and excess Phe-
OMe or unreacted enantiomer D-Phe-OMe followed by subsequent removal of the
precipitate from the aqueous solution (Ager et al., 1998). This method is used in the
commercial aspartame precursor production process of TOSOH (Japan) performed
at Holland Sweetener (The Netherlands) (Fig. 5). Addition of a water-immiscible
solvent like toluene or 4-methylpentan-2-one after the start of formation of the
precipitate was found to permit the process to be run continuously. In the presence
of water-miscible organic solvents (e.g. dimethylsulfoxide) reaction rates were also
enhanced by the addition of salts (Kühn et al., 2002), though yields decreased with
increasing salt concentrations. Yields could be markedly improved by the addition of
alcohols (methanol, 2-propanol) to aqueous systems even though reaction rates were
reduced due to inhibitory effects on thermolysin (Kühn et al., 2002). In biphasic
organic solvent systems, ethyl acetate, tert.-amyl alcohol (Miyanaga et al., 2000b),
n-butyl acetate (Murakami and Hirata, 1997), tributylphosphate and 1-butanol (in
the synthesis of N-formyl-Asp-Phe-OMe – Murakami et al., 2000a) and ionic liquids
(e.g. 1-butyl-3-methylimidazolium hexafluorophosphate – Erbeldinger et al., 2000)
have all been used as solvents. In the solid-to-solid system the pH adjusted by basic
inorganic salt addition played an important role (Erbeldinger et al., 2001). In low-
water solvent systems the water is usually provided by the carrier materials that are
used for adsorptive binding of the enzyme. Polyacrylic ester resins such as XAD-7
(ICN Biomedicals Inc., USA) in ethyl acetate and tert.-amyl alcohol (Miyanaga
et al., 2000a, b), Celite R-640 (FLUKA) in combination with toluene as solvent
(de Martin et al., 2001) or molecularly imprinted polymers (methacrylate-ethylene
glycol dimethacrylate-copolymers) in ethyl acetate (Ye et al., 1999) have all been
used as carrier materials. A considerable increase in thermolysin activity in non-
aqueous media has been achieved by lyophilisation in the presence of KCl or other
inorganic salts (Bedell et al., 1998). Activity could be further improved by the use
of molecular imprinting in combination with activation by salts (Rich et al., 2002).
Cross-linked enzyme crystals (CLECs) of thermolysin which have been used