The heterologous production of epothilone D in Myxococcus xanthus was improved by 140-fold from an initial titer of 0.16 mg/L with the incorporation of an adsorber resin, the identification of a suitable carbon source, and the implementation of a fed-batch process. To reduce the degradation of epothilone D in the basal medium, XAD-16 (20 g/L) was added to stabilize the secreted product. This greatly facilitated its recovery and enhanced the yield by three-fold. The potential of using oils as a carbon source for cell growth and product formation was also evaluated. From a screen of various oils, methyl oleate was shown to have the greatest impact. At the optimal concentration of 7 mL/L in a batch process, the maximum cell density was increased from 0.4 g dry cell weight (DCW)/L to 2 g DCW/L. Product yield, however, depended on the presence of trace elements in the production medium. With an exogenous supplement of trace metals to the basal medium, the peak epothilone D titer was enhanced eight-fold. This finding demonstrates the significant role of metal ions in cell metabolism and in epothilone biosynthesis. To further increase the product yield, a continuous fed-batch process was used to promote a higher cell density and to maintain an extended production period. The optimized fed-batch cultures consistently yielded a cell density of 7 g DCW/L and an average production titer of 23 mg/L.

Development of natural products for therapeutic use is often hindered by limited availability of material from producing organisms. The speed at which current technologies enable the cloning, sequencing, and manipulation of secondary metabolite genes for production of novel compounds has made it impractical to optimize each new organism by conventional strain improvement procedures. We have exploited the overproduction properties of two industrial organisms- Saccharopolyspora erythraea and Streptomyces fradiae, previously improved for erythromycin and tylosin production, respectively-to enhance titers of polyketides produced by genetically modified polyketide synthases (PKSs). An efficient method for delivering large PKS expression vectors into S. erythraea was achieved by insertion of a chromosomal attachment site ( attB) for phiC31-based integrating vectors. For both strains, it was discovered that only the native PKS-associated promoter was capable of sustaining high polyketide titers in that strain. Expression of PKS genes cloned from wild-type organisms in the overproduction strains resulted in high polyketide titers whereas expression of the PKS gene from the S. erythraea overproducer in heterologous hosts resulted in only normal titers. This demonstrated that the overproduction characteristics are primarily due to mutations in non-PKS genes and should therefore operate on other PKSs. Expression of genetically engineered erythromycin PKS genes resulted in production of erythromycin analogs in greatly superior quantity than obtained from previously used hosts. Further development of these hosts could bypass tedious mutagenesis and screening approaches to strain improvement and expedite development of compounds from this valuable class of natural products.

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Polyketides, a large family of bioactive natural products, are synthesized from building blocks derived from alpha-carboxylated Coenzyme A thioesters such as malonyl-CoA and (2S)-methylmalonyl-CoA. The productivity of polyketide fermentation processes in natural and heterologous hosts is frequently limited by the availability of these precursors in vivo. We describe a metabolic engineering strategy to enhance both the yield and volumetric productivity of polyketide biosynthesis. The genes matB and matC from Rhizobium trifolii encode a malonyl-CoA synthetase and a putative dicarboxylate transport protein, respectively. These proteins can directly convert exogenous malonate and methylmalonate into their corresponding CoA thioesters with an ATP requirement of 2 mol per mol of acyl-CoA produced. Heterologous expression of matBC in a recombinant strain of Streptomyces coelicolor that produces the macrolactone 6-deoxyerythronolide B results in a 300% enhancement of macrolactone titers. The unusual efficiency of the bioconversion is illustrated by the fact that approximately one-third of the methylmalonate units added to the fermentation medium are converted into macrolactones. The direct conversion of inexpensive feedstocks such as malonate and methylmalonate into polyketides represents the most carbon- and energy-efficient route to these high value natural products and has implications for cost-effective fermentation of numerous commercial and development-stage small molecules.

A fermentation process employing precursor-directed biosynthesis is being developed for the manufacture of 6-deoxyerythronolide B (6-dEB) analogues. Through a plasmid-based system in Streptomyces coelicolor, 6-dEB synthesis is catalyzed by 6-dEB synthase (DEBS). 6-dEB synthesis is abolished by inactivation of the ketosynthase (KS) 1 domain of DEBS but can be restored by providing synthetic activated diketides. Because of its inherent catalytic flexibility, the KS1-deficient DEBS is capable of utilizing unnatural diketides to form various 13-substituted 6-dEBs. Here we characterize process variables associated with diketide feeding in shake-flask experiments. 13-R-6-dEB production was found to depend strongly on diketide feed concentrations, on the growth phase of cultures at feeding time, and on the R-group present in the diketide moiety. In all cases a major portion of the fed diketides was degraded by the cells.