“…For example, expression levels of a recombinant hyperthermophilic T. maritima 6-phosphogluconate dehydrogenase in E. coli have been increased by ~500-fold by optimization of codon usage, expression plasmid and host, inducer type, concentration, and adding time, and so on [65]. Typical values of recombinant enzyme yield based on sugar (Y P/S ) may be up to 0.2 g of protein/g of sugar consumed [35], based on several well-known facts of (i) cell mass yield based on sugar in aerobic fermentation (Y X/S ) = ~0.5-0.6 g cell mass/g sugar [33,36,71], (ii) high intracellular cellular protein content = ~0.5-0.6 g protein/g cell mass [72], and (iii) high recombinant enzyme percentage in a total cellular protein = 50-70% [63,65,66,73]. Based on the rule of thumb of industrial fermentations, it is estimated that the production cost of recombinant protein may be $4.50-7.5/kg of protein = $0.30/kg sugar/(0.2 g protein/g sugar) × 3-5 (a cost adjustment coefficient due to other nutrient costs, labor, etc.…”