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GPS-X Technical Reference

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Suspended Growth Models 140<br />

3. Anoxic hydrolysis: This hydrolysis process is active under anoxic<br />

conditions. The oxygen saturation term in aerobic hydrolysis rate expression<br />

is replaced with an oxygen inhibition term. A NO X (NO 2-N+NO 3-N)<br />

saturation term is added to the rate expression. The specific hydrolysis rate is<br />

reduced by anoxic hydrolysis reduction factor (η nox).<br />

4. Anaerobic hydrolysis: This hydrolysis process is active only under<br />

anaerobic conditions. The rate expression contains oxygen and NO X<br />

inhibition terms. The specific hydrolysis rate is reduced by anaerobic<br />

hydrolysis reduction factor (η anaer).<br />

5. Ammonification: The ammonification process converts soluble organic<br />

nitrogen to ammonia nitrogen. Both the ordinary heterotrophic organism and<br />

fermentative organism are considered to participate in the ammonification<br />

process. The kinetics of ammonification is similar to that provided in ASM1.<br />

6. Growth on fermentable substrate (ss) using O 2 as electron acceptor: The<br />

process of heterotrophic growth takes place under aerobic conditions. The<br />

reaction rate for this process is formulated considering the concept of multi<br />

substrate kinetics outlined in ASM2d model. The growth rate is considered<br />

proportional to the ratio of fermentable substrate to total soluble substrate<br />

(ss+sac+spro) available to heterotrophic biomass. The main difference in the<br />

growth stoichiometry of different biomass is the uptake of N and P, Ca, Mg,<br />

K, anion and cation during the biomass growth. In this implementation, it is<br />

assumed that concentration of Ca, Mg and K is non-limiting during growth.<br />

If required, the saturation terms for each micronutrient can be added easily in<br />

the model equations. The growth kinetics does not use the alkalinity<br />

saturation function as it is planned to add a pH inhibition term in the growth<br />

kinetics at a later date.<br />

7. Growth on acetate (sac) using O 2 as electron acceptor: The process of<br />

aerobic heterotrophic growth on acetate is similar to the process #6, except<br />

that the growth rate is proportional to the ratio of acetate concentration to the<br />

total soluble substrate (ss+sac+spro) available to heterotrophic biomass.<br />

8. Growth on propionate (spro) using O 2 as electron acceptor: The process of<br />

aerobic heterotrophic growth on acetate is similar to the process #6, except<br />

that the growth rate is proportional to the ratio of propionate concentration to<br />

the total soluble substrate (ss+sac+spro) available to heterotrophic biomass.<br />

<strong>GPS</strong>-X <strong>Technical</strong> <strong>Reference</strong>

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