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Environmental Technologies and Eco-innovation in the Czech ...

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The oxidation of ammonia nitrogen to<br />

nitric nitrogen <strong>in</strong> activation is ensured by<br />

nitrification bacteria. However, <strong>the</strong>ir share<br />

<strong>in</strong> activated sludge ranges only from 1 to 3%.<br />

Such low concentrations are given by <strong>the</strong><br />

lower growth rate of nitrification bacteria<br />

compared to o<strong>the</strong>r bacteria. The most widespread<br />

manner of compensat<strong>in</strong>g for <strong>the</strong>ir<br />

low growth speed is <strong>in</strong>creas<strong>in</strong>g <strong>the</strong> sludge<br />

age 13 , which, however, leads to reduc<strong>in</strong>g<br />

<strong>the</strong> bacteria activity <strong>and</strong> to <strong>the</strong> need of<br />

larger activation tanks. An alternative to<br />

<strong>in</strong>crease <strong>the</strong> nitrification bacteria share<br />

<strong>in</strong> <strong>the</strong> activated sludge is <strong>the</strong> <strong>in</strong>clusion of<br />

<strong>in</strong> situ nitrification bioaugmentation,<br />

dur<strong>in</strong>g which nitrification bacteria<br />

cultivation takes place <strong>in</strong> a detached part of<br />

<strong>the</strong> regeneration tank, <strong>in</strong>to which a source<br />

is lead conta<strong>in</strong><strong>in</strong>g substances with nitrogen<br />

present, preferably <strong>the</strong> water from activated<br />

sludge dewater<strong>in</strong>g. The grown nitrification<br />

bacteria are <strong>in</strong>troduced back <strong>in</strong>to <strong>the</strong><br />

system <strong>in</strong> order to <strong>in</strong>crease <strong>the</strong> nitrification<br />

bacteria concentration <strong>in</strong> <strong>the</strong> activation<br />

tank to <strong>in</strong>crease <strong>the</strong> nitrification efficiency.<br />

This method was successfully applied <strong>in</strong><br />

Prague’s Central WWTP <strong>and</strong> <strong>in</strong> <strong>the</strong> Ústí<br />

nad Labem WWTP. By <strong>in</strong>troduc<strong>in</strong>g this<br />

technology, a significant <strong>in</strong>crease <strong>in</strong> <strong>the</strong><br />

efficiency of nitrogen removal was reached.<br />

With <strong>the</strong> correct WWTP design with <strong>in</strong> situ<br />

nitrification bioaugmentation <strong>in</strong> place, <strong>the</strong><br />

required activation tank sizes are reduced<br />

by as much as 40% <strong>and</strong>, at <strong>the</strong> same time,<br />

this br<strong>in</strong>gs an operat<strong>in</strong>g cost sav<strong>in</strong>gs by as<br />

much as 10%.<br />

6.4 | New methods of activated sludge separation 13<br />

One of <strong>the</strong> essential phases of biological waste water treatment is <strong>the</strong> separation of<br />

activated sludge from treated waste water. Bad separation can lead to leakage of <strong>the</strong><br />

activated sludge <strong>in</strong>to <strong>the</strong> discharge, which significantly <strong>in</strong>creases <strong>the</strong> concentrations of<br />

<strong>the</strong> discharge <strong>in</strong>dicators <strong>and</strong> deteriorates <strong>the</strong> overall treatment. In <strong>the</strong> waste treatment<br />

practice, <strong>the</strong> classical f<strong>in</strong>al settl<strong>in</strong>g tanks are be<strong>in</strong>g more <strong>and</strong> more often replaced<br />

with membrane filters 14 that are ei<strong>the</strong>r submerged directly <strong>in</strong>to <strong>the</strong> activation tank<br />

or outside <strong>the</strong> activation tank, or <strong>the</strong>y are located <strong>in</strong> a separate tank. Air is supplied<br />

<strong>in</strong>to <strong>the</strong> system for biodegradation needs <strong>and</strong> for clean<strong>in</strong>g <strong>the</strong> membranes. The driv<strong>in</strong>g<br />

power of <strong>the</strong> treated water discharge is <strong>the</strong> difference of hydrostatic pressures 15 <strong>in</strong><br />

front of <strong>and</strong> beh<strong>in</strong>d <strong>the</strong> membrane. The membrane modules elim<strong>in</strong>ate <strong>the</strong> difficulties<br />

connected with activated sludge separation <strong>in</strong> <strong>the</strong> f<strong>in</strong>al settl<strong>in</strong>g tanks; it is also possible<br />

to operate <strong>the</strong> system at much higher activated sludge concentrations. Inasmuch as<br />

<strong>the</strong> membrane technologies usually range from microfiltration to ultrafiltration areas,<br />

<strong>the</strong> disposal of all undissolved substances, bacteria <strong>and</strong> viruses occurs dur<strong>in</strong>g<br />

13 sludge age – <strong>the</strong> average time that bacteria rema<strong>in</strong> <strong>in</strong> <strong>the</strong> system<br />

14 membrane filter – a filter made of plastic materials that serves as a sieve for separat<strong>in</strong>g <strong>the</strong> two phases<br />

15 hydrostatic pressure – <strong>the</strong> pressure <strong>in</strong> a liquid that is caused by its weight

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