This study sought to develop a cost-effective biological catalysis process for S-adenosyl-L-methionine (SAM) production. During the process, a mixture of D-methionine (D-Met) and L-methionine (L-Met), namely DL-Met, was used as substrate to replace the conventional but expensive pure L-Met. The concentration of DL-Met in substrate was optimized. When 80 g/L of DL-Met was added in a 5 L-scale bioreactor, 13.74 g/L of SAM was produced with an L-Met conversion rate of 32.15%. The fermentation process was then scaled up to meet the requirements of realistic industrial SAM production. In a 300 L-scale fermentation process, 10.45 g/L of SAM was achieved, with an L-Met conversion rate of 32.61%. Moreover, the proportion of D-Met remaining in broth increased from 50% at the beginning to 76.89% at the end of fermentation. The fermentation process is generally appropriate for commercial SAM production.