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10/1211998 16:03 9165350207 <br /> APEX ENViROTECH <br /> field. Regenesis has since gathered evidence that supports the concept that in a mixed <br /> contaminant system BTEX is consumed preferentially to MTBE. This is not a competitive <br /> inhibition—In that different enzyme systems are responsible for the metabolism of each <br /> compound—but rather is a pattern of preferential consumption (BTEX> MTBE). It can be clearly seen <br /> in Figures 2 and 3 that there is a lag in degradation of MTBE relative to BTEX. In Figure 1, where <br /> BTEX is almost non-existent, MTBE is readily degraded from the outset, <br /> Follow-up laboratory experiments further clarified the issue. using microbial isolates that use <br /> MTBE as a sola carbon source, Regenesis has shown the metabolism of MBE can be largely <br /> inhibited by the addition of STEX - causing it to fall behind in the preferential sequence of <br /> degradation, Furthermore, MTBE metabolism can be predictably modulated by the BTEX, such that <br /> when BTEX is removed from the culture MTBE degradation resumes. <br /> Regenesis is now in the process of funding more involved column bioreactor studies which will <br /> elucidate the inhibition of MTBE by background hydrocarbons. More importantly, this work will <br /> establish a mass balance for the process and identify other important co-factors that may be <br /> operating In the system. The First experiments will correlate an increase in CO2 with a decrease <br /> In MTBE to establish that bioremediation is the primary mechanism of removal. Subsequent <br /> experiments will employ radioactively labeled MTBE and follow the appearance of various <br /> intermediates. <br /> Figure 1 <br /> Reduction of MTBE in an ORC Well <br /> ,CA Sft WWM vd lour STEX lovils <br /> 111Fx <br /> 75 --------------------------------------- 4 m <br /> 0 3 1e <br /> 4 <br /> - - ---------------------- <br /> Q <br /> -- -- --- ----- <br /> 2 <br /> aL <br /> 25 - ------.- -------------------- t f <br /> � a <br /> a o <br /> 0 20 40 68 '80 400 1120 -140 <br /> Qat <br /> Figure 2 <br />