The microbial degradation of thiodiglycol, the primary hydrolysis product of sulfur mustard, by a pure culture of Alcaligenes xylosoxydans ssp. xylosoxydans (SH91) was accomplished in laboratory scale stirred tank reactors. This is a major component of the overall biodegradation process proposed for the complete mineralization of sulfur mustard. Several configurations were evaluated for degradation efficiency including batch, repeated batch, continuous stirred tank reactor (CSTR), and two-stage series CSTR. The repeated batch reactor provided the highest degradation rate of thiodiglycol. Further, this method degraded thiodiglycol in the liquid broth to below the detection limits (0.03 mM). Both batch and repeated batch experiments were simulated by an unstructured mathematical model. Simulation results were in agreement with the experimental data, particularly at low TDG concentration (around 30 mM). This study demonstrates the degradation of thiodiglycol using bioreactors and, more generally, is an experimental study of bioreactor designs for the degradation of growth-inhibitory substances.
A Gram-negative bacterium, Alcaligenes xylosoxydans ssp. xylosoxydans (SH91), consumed thiodiglycol (TDG), the nontoxic hydrolysis product of sulfur mustard, as a primary carbon source and transformed TDG to commercially relevant chemical precursors, [(2-hydroxyethyl)thio]acetic acid (HETA) and thiodiglycolic acid (TDGA). Aerobic fed batch and repeated batch experiments were run to compare the molar yields of HETA and TDGA that result under different operating policies. In repeated batch experiments, 35% of the TDG was converted to HETA. Under the conventional batch process and a repeated fed batch process, the HETA yields were reduced (21% and 18%, respectively), while the yield of TDGA was increased (47% and 31%,respectively). This work demonstrated that cell growth associated biocatalytic transformations were manipulated to achieve a desired byproducts profile through an understanding of the specific reaction and cell growth kinetics and by altering the reaction operating policy accordingly.
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