S. J. C. Taylor et al. / Bioorg. Med. Chem. 7 (1999) 2163±2168
2165
was used. Regulation of enzyme expression was not
particularly well controlled and the fermentation did
not require induction. A 500 L, 4 day fermentation yiel-
�
1
ded approximately 100 g L (wet weight) of cell paste
�
1
and 3000 units g cell paste, sucient to resolve about
tonnes of racemic substrate.
5
Having optimised the fermentation, we focused on
recovering the lactamase in a form suitable for use in
the biotransformation. The goal was a simple process
that gave suciently pure lactamase such that the pro-
tein content did not cause emulsions during isolation of
the lactam. After lysis of the cells with a combination of
lysozyme and Triton-X100, the bulk of nucleic acids
and cell debris were removed by polyethyleneimine pre-
cipitation and centrifugation. The lactamase was pre-
cipitated from the ®ltrate by standard ammonium
sulfate precipitation, before recovery by centrifugation.
The pellet was ®nally redissolved in Tris±HCl buer,
sterile ®ltered ready for use. This was achieved in an
overall yield of about 70%.
With a readily available supply of semi-puri®ed recom-
binant lactamase available, a much improved process
was quickly developed. The biotransformation was
optimised with respect to substrate concentration,
enzyme loading, pH, buer and temperature. This
Figure 2. Ninhydrin stain of ®lter paper colony transfer. Genomic
library of Comamonas acidovorans in E. coli screened for (+)-g-lacta-
mase acitivity by incubation of adsorbed colonies on (+)-lactam
impregnated ®lter discs. Brown halo apparent around single, central
colony indicating the conversion of lactam to amino acid product.
� 1
highlighted 500 g L substrate, 100 mM Tris±HCl at pH
ꢀ
has been much improved (Scheme 2). Volume eciency
7.5, 25 C to be optimal. The new (� )-lactam process then
�
1
is much higher where the enzyme tolerates 500 g L input
of lactam, a 5-fold increase. Since a clean concentrated
enzyme is used, the isolation was greatly simpli®ed where
direct dichloromethane solvent extraction of the lactam
can be achieved, avoiding the carbon adsorption step, and
associated problems of low volume eciency, handling
and safety issues. The ®nal step is a recrystallisation of the
product from the solvent concentrate.
upstream lac promoter of pUC19, and translates to a
protein of 575 residues (61 kDa). The deduced amino
acid sequence of the translated ORF showed >65%
homology to the acetamidase from Mycobacterium
8
smegmatis and Methylophilus methylotrophus. These
enzymes have been shown to hydrolyse short chain fatty
8
acylamides.
From the cloned gene sequence the N-terminal sequence
was identi®ed. The lactamase was found to have an
extra 31 amino acids upstream of the N-terminus, which
arose by a fortuitous ligation of a short piece of DNA
during the cloning. However, experiments showed that
enzyme expression was good, and subsequent manip-
ulation of the gene to remove these gave no added ben-
e®t. Final modi®cation of the recombinant plasmid was
the insertion of the cer element responsible for multi-
meric resolution and stable inheritance of the wild type
Conclusion
Cloning an enzyme has the obvious bene®t of reducing
the cost of the biocatalyst through over-expression.
However, what can be equally important is the dramatic
impact that use of a cloned enzyme can have on the
overall design of a process, where product recovery in
particular becomes much easier. By carefully planning
the screening strategy, a cloning process can be stream-
lined, as we have shown for the lactamase. The impreg-
nated ®lter paper assay should be applicable for any
soluble substrate/product where a selective staining
method exists.
6
E. coli plasmid ColE I. The cer element was transferred
6
from construct pKS492. The ®nal construct and
expression vector were designated pPET1 (Fig. 4). The
vector was transformed into E. coli MC1061 the desig-
nated recombinant lactamase host. The level of recom-
binant protein was signi®cant to be visualised on
Coomassie SDS-PAGE under induced growth.
Experimental
De®nition of units
The fermentation of the recombinant E. coli was based
on a complex media/feed with glycerol as the carbon
source and peptone/casein as a source of amino acids,
peptides and nitrogen. Initial growth was in a batch
mode after which a continuous feed containing glycerol
For our purpose 1 unit is de®ned as the amount of bio-
catalyst required to produce 1 g of product per hour.
�
1
This may be expressed in units mL for fermentation
�
1
broth or units g for puri®ed protein.