The main goal of this work was to develop a strategy that enables tuning of recombinant gene expression relative to the metabolic capacity of the host cell synthesis machinery. In the past, strong expression systems have been developed in order to maximize recombinant gene expression. However, these systems exert an extremely high metabolic burden onto the host cell, which may even lead to cell death. Hence, the period of recombinant gene expression is significantly reduced, and therefore, maximal yield cannot be attained. To extend the production phase and to achieve optimal yields, adjustment of recombinant gene expression by modulation of the transcription rate is required. To control transcription, we designed a feed regime, which continuously supplies limiting amounts of inducer in a constant ratio to biomass. For the accurate determination of appropriate amounts of inducer, a time shifted exponential substrate and inducer feed strategy has been developed. The potential of this metabolic and engineering integrated approach was proven in fed-batch cultivation experiments using E. coli HMS174(DE3)(pET11ahSOD) as model system. Furthermore, our strategy enables the use of lactose as inducer, since its consumption can be compensated by appropriate feed profiles. The attained results fully comply with all requirements of industrial large scale cultivation and improve the applicability of strong expression systems.