In this study, a non‐sterile (open) continuous fermentation (OCF) process with no‐carbon loss was developed to improve lactic acid (LA) productivity and operational stability from the co‐utilization of lignocellulose‐derived sugars by thermophilic Enterococcus faecium QU 50. The effects of different sugar mixtures on LA production were firstly investigated in conventional OCF at 50°C, pH 6.5 and a dilution rate of 0.20 hr−1. The xylose consumption ratio was greatly lower than that of glucose in fermentations with glucose/xylose mixtures, indicating apparent carbon catabolite repression (CCR). However, CCR could be efficiently eliminated by feeding solutions containing the cellobiose/xylose mixture. In OCF at a dilution rate ca. 0.10 hr−1, strain QU 50 produced 42.6 g L−1 of l‐LA with a yield of 0.912 g g−1‐consumed sugars, LA yield of 0.655 g g−1 based on mixed sugar‐loaded, and a productivity of 4.31 g L−1 hr−1 from simulated energy cane hydrolyzate. In OCF with high cell density by cell recycling, simultaneous and complete co‐utilization of sugars was achieved with stable LA production at 60.1 ± 3.25 g L−1 with LA yield of 0.944 g g−1‐consumed sugar and LA productivity of 6.49 ± 0.357 g L−1 hr−1. Besides this, a dramatic increase in LA yield of 0.927 g g−1 based on mixed sugar‐loaded with prolonged operational stability for at least 500 hr (>20 days) was established. This robust system demonstrates an initial green step with a no‐carbon loss under energy‐saving toward the feasibility of sustainable LA production from lignocellulosic sugars.