Author/Authors :
Guerrero، L نويسنده Department of Chemical and Environmental Engineering , , Vasquez، M نويسنده Department of Chemical and Environmental Engineering , , Barahona، A نويسنده Department of Chemical and Environmental Engineering , , Montalvo، S نويسنده Department of Chemical Engineering , , Borja، R نويسنده Instituto de la Grasa (CSIC) ,
Abstract :
The general objective of this study was to develop a highly efficient, economical and
integrated technology for the removal of nitrogen compounds through denitrification via nitrite. To
achieve this, a modified UASB reactor was designed, set-up and operated using Chilean zeolite as
microbial support. The results were compared to a conventional UASB reactor used as control. The
volume of each reactor was 2 L. The reactors operated with synthetic wastewater under the same
operating conditions (with superficial velocities, vs, of up to 1 m/h) in the first part of the experiment.
Later, during the second part of the experiment, only the modified UASB was used, with vs of up to
5.5 m/h. In the first part of the experiment, a higher velocity of denitrification in the reactor with
zeolite was obtained. Nitrogen removal at the end of this experimental set for both reactors, with a vs
lower than 1 m/h, was 87%. In the second stage, the modified UASB reactor operated at vs of
between 1.5 and 5.5 m/h. Here, it was observed that the removal of nitrite increased significantly.
Specifically, at vs values of 2.5, 4.0 and 5.5 m/h, a value of the nitrogen loading rate (NLR) of 1.22 kg
N-NO2
-/m3/d was kept constant, achieving nitrogen removal efficiencies of 50%, 65% and 95.5%
respectively. This last value proves how highly effective the modified UASB reactor is when operating
with vs as high as 5.5 m/h.